Merge pull request #1 from titusquah/titus_changes

summer_2020_changes_titus
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titusquah 5 years ago committed by GitHub
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@ -1,3 +1,60 @@
# parameter-estimation
# REEPS
LLEPE (Liquid-Liquid Extraction Parameter Estimator) is a toolkit for estimating standard thermodynamic parameters for Gibbs minimization.
Extend a methodology for estimating standard thermodynamic parameters for Gibbs minimization in multiphase, multicomponent separations systems
## Installation
To install llepe, clone the repository with the command
```
$ git clone https://xgitlab.cels.anl.gov/summer-2020/parameter-estimation.git
```
Navigate into the parameter-estimation folder with
```
cd parameter-estimation
```
and run the command below in your terminal
```
$ pip install -e.
```
For docs and tests, run
```
$ pip install -e .[docs,tests]
```
### Dependencies
llepe uses packages: cantera (https://cantera.org/), pandas, numpy, scipy, xml, seaborn, and matplotlib
## Usage
Check out examples in docs/examples
Readthedocs documentation are in docs/build/html/index.html
```python
from llepe import LLEPE
opt_dict = {'Nd(H(A)2)3(org)_h0': {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': 'Nd(H(A)2)3(org)',
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'input_value': -4.7e6}}
searcher_parameters = {'exp_data': 'Nd_exp_data.csv',
'phases_xml_filename': 'twophase.xml',
'opt_dict': opt_dict,
'phase_names': ['HCl_electrolyte', 'PC88A_liquid'],
'aq_solvent_name': 'H2O(L)',
'extractant_name': '(HA)2(org)',
'diluant_name': 'dodecane',
'complex_names': ['Nd(H(A)2)3(org)'],
'extracted_species_ion_names': ['Nd+++'],
'aq_solvent_rho': 1000.0,
'extractant_rho': 960.0,
'diluant_rho': 750.0}
searcher = LLEPE(**searcher_parameters)
est_enthalpy = searcher.fit()
searcher.update_xml(est_enthalpy)
searcher.parity_plot(print_r_squared=True)
```

@ -0,0 +1,6 @@
HI(m),Heq,ZI(m),Zeq,REI,REeq(m),D(m)
0.01,0.08830357,1,0.92169643,0.05000119,0.0239,1.0921
0.01,0.10509409,1,0.90490591,0.09999803,0.0683,0.4641
0.01,0.1090171,1,0.9009829,0.1500057,0.117,0.2821
0.01,0.106012,1,0.903988,0.200004,0.168,0.1905
0.01,0.11893447,1,0.89106553,0.30001149,0.2637,0.1377
1 HI(m) Heq ZI(m) Zeq REI REeq(m) D(m)
2 0.01 0.08830357 1 0.92169643 0.05000119 0.0239 1.0921
3 0.01 0.10509409 1 0.90490591 0.09999803 0.0683 0.4641
4 0.01 0.1090171 1 0.9009829 0.1500057 0.117 0.2821
5 0.01 0.106012 1 0.903988 0.200004 0.168 0.1905
6 0.01 0.11893447 1 0.89106553 0.30001149 0.2637 0.1377

@ -0,0 +1,216 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Nd[M],Xaq Nd,D Nd,Feed Pr[M],Xaq Pr,D Pr,Feed Ce[M],Xaq Ce,D Ce,Feed La[M],Xaq La,D La,Feed Dy[M],Xaq Dy,D Dy,Feed Sm[M],Xaq Sm,D Sm,Feed Y[M],Xaq Y,D Y
Formiga (2016),0.316227766,0.316227766,1,1,0.038824182,0.036106489,0.075268817,0.011354951,0.010673654,0.063829787,0.104199378,0.102323789,0.018329939,0.046794403,0.046466843,0.007049345,0,0,0,0,0,0,0,0,0
Formiga (2016),0.1,0.1,1,1,0.038824182,0.023294509,0.666666667,0.011354951,0.007153619,0.587301587,0.104199378,0.087527477,0.19047619,0.046794403,0.044454683,0.052631579,0,0,0,0,0,0,0,0,0
Formiga (2016),0.01,0.01,1,1,0.038824182,0.011647255,2.333333333,0.011354951,0.003860683,1.941176471,0.104199378,0.065645608,0.587301587,0.046794403,0.040711131,0.149425287,0,0,0,0,0,0,0,0,0
Lyon (2016),0.02,0.02,1,1,0.048530227,0.029263727,0.658374793,0.04967791,0.035072604,0.416430595,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.048530227,0.032127011,0.510574018,0.04967791,0.037506822,0.324503311,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.048530227,0.039018303,0.243781095,0.04967791,0.043070748,0.153402537,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.048530227,0.046443428,0.044932079,0.04967791,0.048535318,0.023541453,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.259983361,0.197587354,0.315789474,0.088710553,0.071855548,0.234567901,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.259983361,0.207986689,0.25,0.088710553,0.07540397,0.176470588,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.259983361,0.21578619,0.204819277,0.088710553,0.077178181,0.149425287,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.259983361,0.244384359,0.063829787,0.088710553,0.08338792,0.063829787,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.017097653,0.33,0.008303308,0.006642646,0.25,0,0,0,0.054425491,0.050393973,0.08,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.013298174,0.71,0.008303308,0.005462702,0.52,0,0,0,0.054425491,0.048594188,0.12,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010932634,1.08,0.008303308,0.004537327,0.83,0,0,0,0.054425491,0.048164151,0.13,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.009396644,1.42,0.008303308,0.003972875,1.09,0,0,0,0.054425491,0.047326514,0.15,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.008209342,1.77,0.008303308,0.002997584,1.77,0,0,0,0.054425491,0.045735706,0.19,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.018928042,0.201385664,0.008303308,0.007354823,0.128960943,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.014333115,0.586527247,0.008303308,0.005999476,0.384005473,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010952454,1.076235839,0.008303308,0.004805359,0.727926764,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.008786058,1.588177405,0.008303308,0.003974007,1.089404412,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.00700602,2.245762712,0.008303308,0.00322327,1.576050934,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.1,0.1,0.009359401,0.007999488,0.17,0.003371001,0.003064546,0.1,0.038539496,0.037783819,0.02,0.022461314,0.022020896,0.02,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.3,0.3,0.009359401,0.006881912,0.36,0.003371001,0.002763116,0.22,0.038539496,0.035357336,0.09,0.022461314,0.021597417,0.04,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.5,0.5,0.009359401,0.005813293,0.61,0.003371001,0.002340973,0.44,0.038539496,0.032386131,0.19,0.022461314,0.02060671,0.09,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.7,0.7,0.009359401,0.005638193,0.66,0.003371001,0.002147134,0.57,0.038539496,0.03034606,0.27,0.022461314,0.019877269,0.13,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,1,1,0.009359401,0.005005027,0.87,0.003371001,0.001862432,0.81,0.038539496,0.028547775,0.35,0.022461314,0.019702907,0.14,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,2,2,0.009359401,0.003109436,2.01,0.003371001,0.001404584,1.4,0.038539496,0.021059834,0.83,0.022461314,0.018261231,0.23,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.0508008,0.0305,0.6656,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.09999878,0.0763,0.3106,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.15009456,0.1232,0.2183,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.2000068,0.1708,0.171,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.30001216,0.2672,0.1228,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.0499975,0.035,0.4285,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.10000115,0.0785,0.2739,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.1500032,0.128,0.1719,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.20000832,0.1752,0.1416,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.29999816,0.2728,0.0997,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.05010115,0.0355,0.4113,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.10000382,0.0826,0.2107,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.1499967,0.1305,0.1494,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.2000008,0.178,0.1236,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.05,0.04,0.25,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.10029675,0.0865,0.1595,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.15000153,0.1351,0.1103,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.20054418,0.1838,0.0911,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.29999441,0.2753,0.0897,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.29998992,0.2811,0.0672,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.10000029,0.0221,3.5249,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000025,0.0575,1.6087,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999582,0.1037,0.9286,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.25000596,0.1494,0.6734,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30000931,0.1997,0.5023,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.0500002,0.0106,3.717,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.09999641,0.0409,1.4449,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.14999806,0.0802,0.8703,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999448,0.1252,0.5974,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.29999394,0.2206,0.3599,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.04999904,0.0221,1.2624,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.09999996,0.0573,0.7452,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000096,0.0984,0.5244,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999616,0.1414,0.4144,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30001016,0.2369,0.2664,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.04799855,0.0313,0.5335,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.1000035,0.071,0.4085,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000453,0.1131,0.3263,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19980428,0.1586,0.2598,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30000123,0.2517,0.1919,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.04999962,0.0363,0.3774,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.09999712,0.0844,0.1848,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.1499944,0.1345,0.1152,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.19999665,0.1835,0.0899,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.24999486,0.2329,0.0734,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.29998637,0.2833,0.0589,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.0499991,0.0395,0.2658,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.10000231,0.0881,0.1351,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.15000091,0.1367,0.0973,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.20009536,0.1856,0.0781,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.40540686,0.3846,0.0541,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.09999756,0.0897,0.1148,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.15000544,0.1391,0.0784,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.19999343,0.1883,0.0621,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.29999853,0.2881,0.0413,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.05030076,0.0444,0.1329,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.09999639,0.0919,0.0881,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.15000408,0.1413,0.0616,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.20049903,0.1917,0.0459,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.29948604,0.2883,0.0388,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.08666112,0.05352756,0.619,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.08666112,0.060900295,0.423,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.08666112,0.067916239,0.276,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.08666112,0.084878668,0.021,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0.08666112,0.08666112,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.042983916,0.015124531,1.842,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.042983916,0.020410216,1.106,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.042983916,0.026354332,0.631,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.042983916,0.039290599,0.094,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0.042983916,0.042983916,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.005546312,3.16E-05,174.668,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.005546312,0.000451912,11.273,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.005546312,0.001558828,2.558,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.005546312,0.005400498,0.027,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0.005546312,0.005546312,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,1,1,0.1,0.087622932,0.141253754,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,1.5,1.5,0.1,0.07955199,0.257039578,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,2,2,0.1,0.074253556,0.34673685,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,2.5,2.5,0.1,0.071525275,0.398107171,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,3,3,0.1,0.066613942,0.501187234,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,1,1,0.1,0.075124079,0.331131121,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,1,1,0.1,0.065582051,0.52480746,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,1,1,0.1,0.059662917,0.676082975,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.262,0.26,2,2,0.1,0.079923999,0.251188643,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,2,2,0.1,0.061313682,0.630957344,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,2,2,0.1,0.051151089,0.954992586,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,2,2,0.1,0.044837645,1.230268771,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0114,0.01,2,2,0.1,0.041450132,1.412537545,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.262,0.26,3,3,0.1,0.074253556,0.34673685,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,3,3,0.1,0.048273748,1.071519305,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,3,3,0.1,0.040337083,1.479108388,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,3,3,0.1,0.033900091,1.9498446,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0114,0.01,3,3,0.1,0.030387123,2.290867653,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.05000119,0.0239,1.0921,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.09999803,0.0683,0.4641,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.1500057,0.117,0.2821,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.200004,0.168,0.1905,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.30001149,0.2637,0.1377,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.03453582,0.0201,0.7182,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.09996185,0.0757,0.3205,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.19999308,0.1722,0.1614,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.04999817,0.0389,0.2853,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.1499974,0.133,0.1278,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.19999876,0.1807,0.1068,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.2500032,0.232,0.0776,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.30001216,0.2807,0.0688,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.01996974,0.0189,0.0566,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.04997968,0.0478,0.0456,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.15000144,0.1464,0.0246,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.29998765,0.2957,0.0145,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.04999786,0.0482,0.0373,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.10000096,0.0976,0.0246,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.20000784,0.1968,0.0163,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.03,0.03,1,1,0,0,0,0.09296866,0.06556323,0.418,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.09296866,0.066835844,0.391,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.09296866,0.080076365,0.161,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.09296866,0.091957131,0.011,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0,0,0,0.09296866,0.09296866,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.03,0.03,1,1,0,0,0,0.047548856,0.02373882,1.003,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.047548856,0.025646632,0.854,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.047548856,0.034988121,0.359,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.047548856,0.045371046,0.048,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0,0,0,0.047548856,0.047548856,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0,0,0,0.00638716,5.54E-05,114.332,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.00638716,0.000669233,8.544,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.00638716,0.002264147,1.821,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.00638716,0.006323921,0.01,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0,0,0,0.00638716,0.00638716,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.04999995,0.0259,0.9305,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.09999925,0.0725,0.3793,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.20000715,0.1673,0.1955,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.29999192,0.2648,0.1329,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.05000109,0.0307,0.6287,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.10009624,0.0776,0.2899,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.20000456,0.1736,0.1521,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.2999997,0.273,0.0989,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.05002915,0.0349,0.4335,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.09997622,0.0809,0.2358,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.14999553,0.1299,0.1547,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.25001088,0.2272,0.1004,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.04999995,0.0385,0.2987,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.09999936,0.0864,0.1574,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.14998624,0.1343,0.1168,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.24999474,0.2334,0.0711,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.0499992,0.0415,0.2048,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.10000199,0.0901,0.1099,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.1999998,0.189,0.0582,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.30000544,0.2888,0.0388,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0500503,0.0115,3.3522,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0999792,0.048,1.0829,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1500016,0.0944,0.589,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.24999968,0.1864,0.3412,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30000263,0.2371,0.2653,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.05032248,0.0156,2.2258,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.10000216,0.0556,0.7986,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000255,0.1035,0.4493,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30392343,0.1997,0.5219,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30000411,0.2471,0.2141,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.04999989,0.0219,1.2831,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999773,0.0623,0.6051,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000375,0.1105,0.3575,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.2500038,0.2073,0.206,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30061536,0.2572,0.1688,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0502452,0.0408,0.2315,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999592,0.0842,0.1876,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.14999496,0.1334,0.1244,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1999935,0.1814,0.1025,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30001088,0.2782,0.0784,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1500005,0.047,2.1915
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999809,0.0857,1.3337
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.2999996,0.1772,0.693
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.05,0.016,2.125
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1000004,0.0445,1.2472
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000048,0.0828,0.8116
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999436,0.1214,0.6474
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.29999366,0.2083,0.4402
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.04999995,0.0333,0.5015
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999846,0.0694,0.4409
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000104,0.1108,0.3538
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999756,0.1526,0.3106
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.29999472,0.2416,0.2417
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.25000384,0.1984,0.2601
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0500013,0.0405,0.2346
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999854,0.0838,0.1933
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999977,0.1753,0.1409
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999804,0.0908,0.1013
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19992651,0.1851,0.0801
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30001335,0.2821,0.0635
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Nd[M] Xaq Nd D Nd Feed Pr[M] Xaq Pr D Pr Feed Ce[M] Xaq Ce D Ce Feed La[M] Xaq La D La Feed Dy[M] Xaq Dy D Dy Feed Sm[M] Xaq Sm D Sm Feed Y[M] Xaq Y D Y
2 Formiga (2016) 0.316227766 0.316227766 1 1 0.038824182 0.036106489 0.075268817 0.011354951 0.010673654 0.063829787 0.104199378 0.102323789 0.018329939 0.046794403 0.046466843 0.007049345 0 0 0 0 0 0 0 0 0
3 Formiga (2016) 0.1 0.1 1 1 0.038824182 0.023294509 0.666666667 0.011354951 0.007153619 0.587301587 0.104199378 0.087527477 0.19047619 0.046794403 0.044454683 0.052631579 0 0 0 0 0 0 0 0 0
4 Formiga (2016) 0.01 0.01 1 1 0.038824182 0.011647255 2.333333333 0.011354951 0.003860683 1.941176471 0.104199378 0.065645608 0.587301587 0.046794403 0.040711131 0.149425287 0 0 0 0 0 0 0 0 0
5 Lyon (2016) 0.02 0.02 1 1 0.048530227 0.029263727 0.658374793 0.04967791 0.035072604 0.416430595 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
6 Lyon (2016) 0.05 0.05 1 1 0.048530227 0.032127011 0.510574018 0.04967791 0.037506822 0.324503311 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
7 Lyon (2016) 0.1 0.1 1 1 0.048530227 0.039018303 0.243781095 0.04967791 0.043070748 0.153402537 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
8 Lyon (2016) 0.3 0.3 1 1 0.048530227 0.046443428 0.044932079 0.04967791 0.048535318 0.023541453 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
9 Lyon (2016) 0.01 0.01 1 1 0.259983361 0.197587354 0.315789474 0.088710553 0.071855548 0.234567901 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
10 Lyon (2016) 0.05 0.05 1 1 0.259983361 0.207986689 0.25 0.088710553 0.07540397 0.176470588 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
11 Lyon (2016) 0.1 0.1 1 1 0.259983361 0.21578619 0.204819277 0.088710553 0.077178181 0.149425287 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
12 Lyon (2016) 0.3 0.3 1 1 0.259983361 0.244384359 0.063829787 0.088710553 0.08338792 0.063829787 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
13 Banda (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.017097653 0.33 0.008303308 0.006642646 0.25 0 0 0 0.054425491 0.050393973 0.08 0 0 0 0 0 0 0 0 0
14 Banda (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.013298174 0.71 0.008303308 0.005462702 0.52 0 0 0 0.054425491 0.048594188 0.12 0 0 0 0 0 0 0 0 0
15 Banda (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010932634 1.08 0.008303308 0.004537327 0.83 0 0 0 0.054425491 0.048164151 0.13 0 0 0 0 0 0 0 0 0
16 Banda (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.009396644 1.42 0.008303308 0.003972875 1.09 0 0 0 0.054425491 0.047326514 0.15 0 0 0 0 0 0 0 0 0
17 Banda (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.008209342 1.77 0.008303308 0.002997584 1.77 0 0 0 0.054425491 0.045735706 0.19 0 0 0 0 0 0 0 0 0
18 Liu (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.018928042 0.201385664 0.008303308 0.007354823 0.128960943 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
19 Liu (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.014333115 0.586527247 0.008303308 0.005999476 0.384005473 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
20 Liu (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010952454 1.076235839 0.008303308 0.004805359 0.727926764 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
21 Liu (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.008786058 1.588177405 0.008303308 0.003974007 1.089404412 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
22 Liu (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.00700602 2.245762712 0.008303308 0.00322327 1.576050934 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
23 Kim (2012) 0.01023293 0.01023293 0.1 0.1 0.009359401 0.007999488 0.17 0.003371001 0.003064546 0.1 0.038539496 0.037783819 0.02 0.022461314 0.022020896 0.02 0 0 0 0 0 0 0 0 0
24 Kim (2012) 0.01023293 0.01023293 0.3 0.3 0.009359401 0.006881912 0.36 0.003371001 0.002763116 0.22 0.038539496 0.035357336 0.09 0.022461314 0.021597417 0.04 0 0 0 0 0 0 0 0 0
25 Kim (2012) 0.01023293 0.01023293 0.5 0.5 0.009359401 0.005813293 0.61 0.003371001 0.002340973 0.44 0.038539496 0.032386131 0.19 0.022461314 0.02060671 0.09 0 0 0 0 0 0 0 0 0
26 Kim (2012) 0.01023293 0.01023293 0.7 0.7 0.009359401 0.005638193 0.66 0.003371001 0.002147134 0.57 0.038539496 0.03034606 0.27 0.022461314 0.019877269 0.13 0 0 0 0 0 0 0 0 0
27 Kim (2012) 0.01023293 0.01023293 1 1 0.009359401 0.005005027 0.87 0.003371001 0.001862432 0.81 0.038539496 0.028547775 0.35 0.022461314 0.019702907 0.14 0 0 0 0 0 0 0 0 0
28 Kim (2012) 0.01023293 0.01023293 2 2 0.009359401 0.003109436 2.01 0.003371001 0.001404584 1.4 0.038539496 0.021059834 0.83 0.022461314 0.018261231 0.23 0 0 0 0 0 0 0 0 0
29 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.0508008 0.0305 0.6656 0 0 0 0 0 0 0 0 0 0 0 0
30 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.09999878 0.0763 0.3106 0 0 0 0 0 0 0 0 0 0 0 0
31 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.15009456 0.1232 0.2183 0 0 0 0 0 0 0 0 0 0 0 0
32 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.2000068 0.1708 0.171 0 0 0 0 0 0 0 0 0 0 0 0
33 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.30001216 0.2672 0.1228 0 0 0 0 0 0 0 0 0 0 0 0
34 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.0499975 0.035 0.4285 0 0 0 0 0 0 0 0 0 0 0 0
35 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.10000115 0.0785 0.2739 0 0 0 0 0 0 0 0 0 0 0 0
36 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.1500032 0.128 0.1719 0 0 0 0 0 0 0 0 0 0 0 0
37 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.20000832 0.1752 0.1416 0 0 0 0 0 0 0 0 0 0 0 0
38 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.29999816 0.2728 0.0997 0 0 0 0 0 0 0 0 0 0 0 0
39 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.05010115 0.0355 0.4113 0 0 0 0 0 0 0 0 0 0 0 0
40 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.10000382 0.0826 0.2107 0 0 0 0 0 0 0 0 0 0 0 0
41 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.1499967 0.1305 0.1494 0 0 0 0 0 0 0 0 0 0 0 0
42 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.2000008 0.178 0.1236 0 0 0 0 0 0 0 0 0 0 0 0
43 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.05 0.04 0.25 0 0 0 0 0 0 0 0 0 0 0 0
44 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.10029675 0.0865 0.1595 0 0 0 0 0 0 0 0 0 0 0 0
45 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.15000153 0.1351 0.1103 0 0 0 0 0 0 0 0 0 0 0 0
46 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.20054418 0.1838 0.0911 0 0 0 0 0 0 0 0 0 0 0 0
47 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.29999441 0.2753 0.0897 0 0 0 0 0 0 0 0 0 0 0 0
48 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.29998992 0.2811 0.0672 0 0 0 0 0 0 0 0 0 0 0 0
49 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.10000029 0.0221 3.5249 0 0 0 0 0 0
50 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000025 0.0575 1.6087 0 0 0 0 0 0
51 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999582 0.1037 0.9286 0 0 0 0 0 0
52 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.25000596 0.1494 0.6734 0 0 0 0 0 0
53 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30000931 0.1997 0.5023 0 0 0 0 0 0
54 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.0500002 0.0106 3.717 0 0 0 0 0 0
55 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.09999641 0.0409 1.4449 0 0 0 0 0 0
56 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.14999806 0.0802 0.8703 0 0 0 0 0 0
57 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999448 0.1252 0.5974 0 0 0 0 0 0
58 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.29999394 0.2206 0.3599 0 0 0 0 0 0
59 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.04999904 0.0221 1.2624 0 0 0 0 0 0
60 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.09999996 0.0573 0.7452 0 0 0 0 0 0
61 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000096 0.0984 0.5244 0 0 0 0 0 0
62 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999616 0.1414 0.4144 0 0 0 0 0 0
63 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30001016 0.2369 0.2664 0 0 0 0 0 0
64 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.04799855 0.0313 0.5335 0 0 0 0 0 0
65 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.1000035 0.071 0.4085 0 0 0 0 0 0
66 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000453 0.1131 0.3263 0 0 0 0 0 0
67 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19980428 0.1586 0.2598 0 0 0 0 0 0
68 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30000123 0.2517 0.1919 0 0 0 0 0 0
69 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.04999962 0.0363 0.3774 0 0 0 0 0 0 0 0 0
70 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.09999712 0.0844 0.1848 0 0 0 0 0 0 0 0 0
71 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.1499944 0.1345 0.1152 0 0 0 0 0 0 0 0 0
72 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.19999665 0.1835 0.0899 0 0 0 0 0 0 0 0 0
73 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.24999486 0.2329 0.0734 0 0 0 0 0 0 0 0 0
74 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.29998637 0.2833 0.0589 0 0 0 0 0 0 0 0 0
75 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.0499991 0.0395 0.2658 0 0 0 0 0 0 0 0 0
76 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.10000231 0.0881 0.1351 0 0 0 0 0 0 0 0 0
77 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.15000091 0.1367 0.0973 0 0 0 0 0 0 0 0 0
78 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.20009536 0.1856 0.0781 0 0 0 0 0 0 0 0 0
79 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.40540686 0.3846 0.0541 0 0 0 0 0 0 0 0 0
80 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.09999756 0.0897 0.1148 0 0 0 0 0 0 0 0 0
81 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.15000544 0.1391 0.0784 0 0 0 0 0 0 0 0 0
82 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.19999343 0.1883 0.0621 0 0 0 0 0 0 0 0 0
83 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.29999853 0.2881 0.0413 0 0 0 0 0 0 0 0 0
84 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.05030076 0.0444 0.1329 0 0 0 0 0 0 0 0 0
85 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.09999639 0.0919 0.0881 0 0 0 0 0 0 0 0 0
86 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.15000408 0.1413 0.0616 0 0 0 0 0 0 0 0 0
87 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.20049903 0.1917 0.0459 0 0 0 0 0 0 0 0 0
88 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.29948604 0.2883 0.0388 0 0 0 0 0 0 0 0 0
89 Lyon (2016) 0.01 0.01 1 1 0.08666112 0.05352756 0.619 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
90 Lyon (2016) 0.05 0.05 1 1 0.08666112 0.060900295 0.423 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
91 Lyon (2016) 0.1 0.1 1 1 0.08666112 0.067916239 0.276 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
92 Lyon (2016) 0.3 0.3 1 1 0.08666112 0.084878668 0.021 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
93 Lyon (2016) 0.5 0.5 1 1 0.08666112 0.08666112 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
94 Lyon (2016) 0.01 0.01 1 1 0.042983916 0.015124531 1.842 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
95 Lyon (2016) 0.05 0.05 1 1 0.042983916 0.020410216 1.106 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
96 Lyon (2016) 0.1 0.1 1 1 0.042983916 0.026354332 0.631 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
97 Lyon (2016) 0.3 0.3 1 1 0.042983916 0.039290599 0.094 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
98 Lyon (2016) 0.5 0.5 1 1 0.042983916 0.042983916 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
99 Lyon (2016) 0.01 0.01 1 1 0.005546312 3.16E-05 174.668 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
100 Lyon (2016) 0.05 0.05 1 1 0.005546312 0.000451912 11.273 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
101 Lyon (2016) 0.1 0.1 1 1 0.005546312 0.001558828 2.558 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
102 Lyon (2016) 0.3 0.3 1 1 0.005546312 0.005400498 0.027 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
103 Lyon (2016) 0.5 0.5 1 1 0.005546312 0.005546312 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
104 Lee (2005) 0.251 0.25 1 1 0.1 0.087622932 0.141253754 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
105 Lee (2005) 0.251 0.25 1.5 1.5 0.1 0.07955199 0.257039578 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
106 Lee (2005) 0.251 0.25 2 2 0.1 0.074253556 0.34673685 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
107 Lee (2005) 0.251 0.25 2.5 2.5 0.1 0.071525275 0.398107171 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
108 Lee (2005) 0.251 0.25 3 3 0.1 0.066613942 0.501187234 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
109 Lee (2005) 0.134 0.13 1 1 0.1 0.075124079 0.331131121 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
110 Lee (2005) 0.0835 0.08 1 1 0.1 0.065582051 0.52480746 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
111 Lee (2005) 0.0285 0.03 1 1 0.1 0.059662917 0.676082975 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
112 Lee (2005) 0.262 0.26 2 2 0.1 0.079923999 0.251188643 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
113 Lee (2005) 0.134 0.13 2 2 0.1 0.061313682 0.630957344 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
114 Lee (2005) 0.0835 0.08 2 2 0.1 0.051151089 0.954992586 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
115 Lee (2005) 0.0285 0.03 2 2 0.1 0.044837645 1.230268771 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
116 Lee (2005) 0.0114 0.01 2 2 0.1 0.041450132 1.412537545 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
117 Lee (2005) 0.262 0.26 3 3 0.1 0.074253556 0.34673685 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
118 Lee (2005) 0.134 0.13 3 3 0.1 0.048273748 1.071519305 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
119 Lee (2005) 0.0835 0.08 3 3 0.1 0.040337083 1.479108388 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
120 Lee (2005) 0.0285 0.03 3 3 0.1 0.033900091 1.9498446 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
121 Lee (2005) 0.0114 0.01 3 3 0.1 0.030387123 2.290867653 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
122 Li (1987) 0.01 0.01 1 1 0.05000119 0.0239 1.0921 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
123 Li (1987) 0.01 0.01 1 1 0.09999803 0.0683 0.4641 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
124 Li (1987) 0.01 0.01 1 1 0.1500057 0.117 0.2821 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
125 Li (1987) 0.01 0.01 1 1 0.200004 0.168 0.1905 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
126 Li (1987) 0.01 0.01 1 1 0.30001149 0.2637 0.1377 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
127 Li (1987) 0.05 0.05 1 1 0.03453582 0.0201 0.7182 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
128 Li (1987) 0.05 0.05 1 1 0.09996185 0.0757 0.3205 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
129 Li (1987) 0.05 0.05 1 1 0.19999308 0.1722 0.1614 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
130 Li (1987) 0.1 0.1 1 1 0.04999817 0.0389 0.2853 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
131 Li (1987) 0.1 0.1 1 1 0.1499974 0.133 0.1278 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
132 Li (1987) 0.1 0.1 1 1 0.19999876 0.1807 0.1068 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
133 Li (1987) 0.1 0.1 1 1 0.2500032 0.232 0.0776 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
134 Li (1987) 0.1 0.1 1 1 0.30001216 0.2807 0.0688 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
135 Li (1987) 0.3 0.3 1 1 0.01996974 0.0189 0.0566 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
136 Li (1987) 0.3 0.3 1 1 0.04997968 0.0478 0.0456 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
137 Li (1987) 0.3 0.3 1 1 0.15000144 0.1464 0.0246 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
138 Li (1987) 0.3 0.3 1 1 0.29998765 0.2957 0.0145 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
139 Li (1987) 0.5 0.5 1 1 0.04999786 0.0482 0.0373 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
140 Li (1987) 0.5 0.5 1 1 0.10000096 0.0976 0.0246 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
141 Li (1987) 0.5 0.5 1 1 0.20000784 0.1968 0.0163 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
142 Lyon (2016) 0.03 0.03 1 1 0 0 0 0.09296866 0.06556323 0.418 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
143 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.09296866 0.066835844 0.391 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
144 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.09296866 0.080076365 0.161 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
145 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.09296866 0.091957131 0.011 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
146 Lyon (2016) 0.5 0.5 1 1 0 0 0 0.09296866 0.09296866 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
147 Lyon (2016) 0.03 0.03 1 1 0 0 0 0.047548856 0.02373882 1.003 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
148 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.047548856 0.025646632 0.854 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
149 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.047548856 0.034988121 0.359 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
150 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.047548856 0.045371046 0.048 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
151 Lyon (2016) 0.5 0.5 1 1 0 0 0 0.047548856 0.047548856 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
152 Lyon (2016) 0.01 0.01 1 1 0 0 0 0.00638716 5.54E-05 114.332 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
153 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.00638716 0.000669233 8.544 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
154 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.00638716 0.002264147 1.821 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
155 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.00638716 0.006323921 0.01 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
156 Lyon (2016) 0.5 0.5 1 1 0 0 0 0.00638716 0.00638716 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
157 Li (1987) 0.01 0.01 1 1 0 0 0 0.04999995 0.0259 0.9305 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
158 Li (1987) 0.01 0.01 1 1 0 0 0 0.09999925 0.0725 0.3793 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
159 Li (1987) 0.01 0.01 1 1 0 0 0 0.20000715 0.1673 0.1955 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
160 Li (1987) 0.01 0.01 1 1 0 0 0 0.29999192 0.2648 0.1329 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
161 Li (1987) 0.03 0.03 1 1 0 0 0 0.05000109 0.0307 0.6287 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
162 Li (1987) 0.03 0.03 1 1 0 0 0 0.10009624 0.0776 0.2899 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
163 Li (1987) 0.03 0.03 1 1 0 0 0 0.20000456 0.1736 0.1521 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
164 Li (1987) 0.03 0.03 1 1 0 0 0 0.2999997 0.273 0.0989 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
165 Li (1987) 0.05 0.05 1 1 0 0 0 0.05002915 0.0349 0.4335 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
166 Li (1987) 0.05 0.05 1 1 0 0 0 0.09997622 0.0809 0.2358 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
167 Li (1987) 0.05 0.05 1 1 0 0 0 0.14999553 0.1299 0.1547 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
168 Li (1987) 0.05 0.05 1 1 0 0 0 0.25001088 0.2272 0.1004 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
169 Li (1987) 0.07 0.07 1 1 0 0 0 0.04999995 0.0385 0.2987 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
170 Li (1987) 0.07 0.07 1 1 0 0 0 0.09999936 0.0864 0.1574 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
171 Li (1987) 0.07 0.07 1 1 0 0 0 0.14998624 0.1343 0.1168 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
172 Li (1987) 0.07 0.07 1 1 0 0 0 0.24999474 0.2334 0.0711 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
173 Li (1987) 0.1 0.1 1 1 0 0 0 0.0499992 0.0415 0.2048 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
174 Li (1987) 0.1 0.1 1 1 0 0 0 0.10000199 0.0901 0.1099 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
175 Li (1987) 0.1 0.1 1 1 0 0 0 0.1999998 0.189 0.0582 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
176 Li (1987) 0.1 0.1 1 1 0 0 0 0.30000544 0.2888 0.0388 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
177 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0500503 0.0115 3.3522 0 0 0
178 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0999792 0.048 1.0829 0 0 0
179 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1500016 0.0944 0.589 0 0 0
180 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.24999968 0.1864 0.3412 0 0 0
181 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30000263 0.2371 0.2653 0 0 0
182 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.05032248 0.0156 2.2258 0 0 0
183 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.10000216 0.0556 0.7986 0 0 0
184 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000255 0.1035 0.4493 0 0 0
185 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30392343 0.1997 0.5219 0 0 0
186 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30000411 0.2471 0.2141 0 0 0
187 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.04999989 0.0219 1.2831 0 0 0
188 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999773 0.0623 0.6051 0 0 0
189 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000375 0.1105 0.3575 0 0 0
190 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.2500038 0.2073 0.206 0 0 0
191 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30061536 0.2572 0.1688 0 0 0
192 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0502452 0.0408 0.2315 0 0 0
193 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999592 0.0842 0.1876 0 0 0
194 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.14999496 0.1334 0.1244 0 0 0
195 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1999935 0.1814 0.1025 0 0 0
196 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30001088 0.2782 0.0784 0 0 0
197 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1500005 0.047 2.1915
198 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999809 0.0857 1.3337
199 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.2999996 0.1772 0.693
200 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.05 0.016 2.125
201 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1000004 0.0445 1.2472
202 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000048 0.0828 0.8116
203 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999436 0.1214 0.6474
204 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.29999366 0.2083 0.4402
205 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.04999995 0.0333 0.5015
206 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999846 0.0694 0.4409
207 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000104 0.1108 0.3538
208 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999756 0.1526 0.3106
209 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.29999472 0.2416 0.2417
210 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.25000384 0.1984 0.2601
211 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0500013 0.0405 0.2346
212 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999854 0.0838 0.1933
213 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999977 0.1753 0.1409
214 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999804 0.0908 0.1013
215 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19992651 0.1851 0.0801
216 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30001335 0.2821 0.0635

@ -0,0 +1,6 @@
HI(m),REeq(m),D(m),ZI(m),Zeq,Heq,REI
0.01,0.0239,1.0921,1,0.92169643,0.08830357,0.05000119
0.01,0.0683,0.4641,1,0.90490591,0.10509409,0.09999803
0.01,0.117,0.2821,1,0.9009829,0.1090171,0.1500057
0.01,0.168,0.1905,1,0.903988,0.106012,0.200004
0.01,0.2637,0.1377,1,0.89106553,0.11893447,0.30001149
1 HI(m) REeq(m) D(m) ZI(m) Zeq Heq REI
2 0.01 0.0239 1.0921 1 0.92169643 0.08830357 0.05000119
3 0.01 0.0683 0.4641 1 0.90490591 0.10509409 0.09999803
4 0.01 0.117 0.2821 1 0.9009829 0.1090171 0.1500057
5 0.01 0.168 0.1905 1 0.903988 0.106012 0.200004
6 0.01 0.2637 0.1377 1 0.89106553 0.11893447 0.30001149

@ -0,0 +1,21 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Ce[M],Xaq Ce,D Ce
Li (1987) Ce,0.01,0.01,1,1,0.05080080000000001,0.0305,0.6656
Li (1987) Ce,0.01,0.01,1,1,0.09999878,0.0763,0.3106
Li (1987) Ce,0.01,0.01,1,1,0.15009456,0.1232,0.2183
Li (1987) Ce,0.01,0.01,1,1,0.20000679999999998,0.1708,0.171
Li (1987) Ce,0.01,0.01,1,1,0.30001216,0.2672,0.1228
Li (1987) Ce,0.03,0.03,1,1,0.0499975,0.035,0.4285
Li (1987) Ce,0.03,0.03,1,1,0.10000115,0.0785,0.2739
Li (1987) Ce,0.03,0.03,1,1,0.1500032,0.128,0.1719
Li (1987) Ce,0.03,0.03,1,1,0.20000832,0.1752,0.1416
Li (1987) Ce,0.03,0.03,1,1,0.29999816,0.2728,0.0997
Li (1987) Ce,0.05,0.05,1,1,0.05010115,0.0355,0.4113
Li (1987) Ce,0.05,0.05,1,1,0.10000382,0.0826,0.2107
Li (1987) Ce,0.05,0.05,1,1,0.1499967,0.1305,0.1494
Li (1987) Ce,0.05,0.05,1,1,0.20000079999999998,0.17800000000000002,0.1236
Li (1987) Ce,0.07,0.07,1,1,0.05,0.04,0.25
Li (1987) Ce,0.07,0.07,1,1,0.10029675,0.0865,0.1595
Li (1987) Ce,0.07,0.07,1,1,0.15000153,0.1351,0.1103
Li (1987) Ce,0.07,0.07,1,1,0.20054418,0.1838,0.0911
Li (1987) Ce,0.07,0.07,1,1,0.29999441,0.2753,0.0897
Li (1987) Ce,0.07,0.07,1,1,0.29998992,0.2811,0.0672
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Ce[M] Xaq Ce D Ce
2 Li (1987) Ce 0.01 0.01 1 1 0.05080080000000001 0.0305 0.6656
3 Li (1987) Ce 0.01 0.01 1 1 0.09999878 0.0763 0.3106
4 Li (1987) Ce 0.01 0.01 1 1 0.15009456 0.1232 0.2183
5 Li (1987) Ce 0.01 0.01 1 1 0.20000679999999998 0.1708 0.171
6 Li (1987) Ce 0.01 0.01 1 1 0.30001216 0.2672 0.1228
7 Li (1987) Ce 0.03 0.03 1 1 0.0499975 0.035 0.4285
8 Li (1987) Ce 0.03 0.03 1 1 0.10000115 0.0785 0.2739
9 Li (1987) Ce 0.03 0.03 1 1 0.1500032 0.128 0.1719
10 Li (1987) Ce 0.03 0.03 1 1 0.20000832 0.1752 0.1416
11 Li (1987) Ce 0.03 0.03 1 1 0.29999816 0.2728 0.0997
12 Li (1987) Ce 0.05 0.05 1 1 0.05010115 0.0355 0.4113
13 Li (1987) Ce 0.05 0.05 1 1 0.10000382 0.0826 0.2107
14 Li (1987) Ce 0.05 0.05 1 1 0.1499967 0.1305 0.1494
15 Li (1987) Ce 0.05 0.05 1 1 0.20000079999999998 0.17800000000000002 0.1236
16 Li (1987) Ce 0.07 0.07 1 1 0.05 0.04 0.25
17 Li (1987) Ce 0.07 0.07 1 1 0.10029675 0.0865 0.1595
18 Li (1987) Ce 0.07 0.07 1 1 0.15000153 0.1351 0.1103
19 Li (1987) Ce 0.07 0.07 1 1 0.20054418 0.1838 0.0911
20 Li (1987) Ce 0.07 0.07 1 1 0.29999441 0.2753 0.0897
21 Li (1987) Ce 0.07 0.07 1 1 0.29998992 0.2811 0.0672

@ -0,0 +1,21 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Dy[M],Xaq Dy,D Dy
Li (1987) Dy,0.1,0.1,1,1,0.10000029,0.0221,3.5249
Li (1987) Dy,0.1,0.1,1,1,0.15000025,0.0575,1.6087
Li (1987) Dy,0.1,0.1,1,1,0.19999582,0.1037,0.9286
Li (1987) Dy,0.1,0.1,1,1,0.25000596,0.1494,0.6734
Li (1987) Dy,0.1,0.1,1,1,0.30000931,0.1997,0.5023
Li (1987) Dy,0.3,0.3,1,1,0.050000199999999995,0.0106,3.717
Li (1987) Dy,0.3,0.3,1,1,0.09999641,0.0409,1.4449
Li (1987) Dy,0.3,0.3,1,1,0.14999806,0.0802,0.8703
Li (1987) Dy,0.3,0.3,1,1,0.19999448,0.1252,0.5974
Li (1987) Dy,0.3,0.3,1,1,0.29999394,0.2206,0.3599
Li (1987) Dy,0.5,0.5,1,1,0.04999904,0.0221,1.2624
Li (1987) Dy,0.5,0.5,1,1,0.09999996,0.0573,0.7452
Li (1987) Dy,0.5,0.5,1,1,0.15000096,0.0984,0.5244
Li (1987) Dy,0.5,0.5,1,1,0.19999616,0.1414,0.4144
Li (1987) Dy,0.5,0.5,1,1,0.30001016,0.2369,0.2664
Li (1987) Dy,0.7,0.7,1,1,0.04799855,0.0313,0.5335
Li (1987) Dy,0.7,0.7,1,1,0.1000035,0.071,0.4085
Li (1987) Dy,0.7,0.7,1,1,0.15000453,0.1131,0.3263
Li (1987) Dy,0.7,0.7,1,1,0.19980428,0.1586,0.2598
Li (1987) Dy,0.7,0.7,1,1,0.30000123,0.2517,0.1919
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Dy[M] Xaq Dy D Dy
2 Li (1987) Dy 0.1 0.1 1 1 0.10000029 0.0221 3.5249
3 Li (1987) Dy 0.1 0.1 1 1 0.15000025 0.0575 1.6087
4 Li (1987) Dy 0.1 0.1 1 1 0.19999582 0.1037 0.9286
5 Li (1987) Dy 0.1 0.1 1 1 0.25000596 0.1494 0.6734
6 Li (1987) Dy 0.1 0.1 1 1 0.30000931 0.1997 0.5023
7 Li (1987) Dy 0.3 0.3 1 1 0.050000199999999995 0.0106 3.717
8 Li (1987) Dy 0.3 0.3 1 1 0.09999641 0.0409 1.4449
9 Li (1987) Dy 0.3 0.3 1 1 0.14999806 0.0802 0.8703
10 Li (1987) Dy 0.3 0.3 1 1 0.19999448 0.1252 0.5974
11 Li (1987) Dy 0.3 0.3 1 1 0.29999394 0.2206 0.3599
12 Li (1987) Dy 0.5 0.5 1 1 0.04999904 0.0221 1.2624
13 Li (1987) Dy 0.5 0.5 1 1 0.09999996 0.0573 0.7452
14 Li (1987) Dy 0.5 0.5 1 1 0.15000096 0.0984 0.5244
15 Li (1987) Dy 0.5 0.5 1 1 0.19999616 0.1414 0.4144
16 Li (1987) Dy 0.5 0.5 1 1 0.30001016 0.2369 0.2664
17 Li (1987) Dy 0.7 0.7 1 1 0.04799855 0.0313 0.5335
18 Li (1987) Dy 0.7 0.7 1 1 0.1000035 0.071 0.4085
19 Li (1987) Dy 0.7 0.7 1 1 0.15000453 0.1131 0.3263
20 Li (1987) Dy 0.7 0.7 1 1 0.19980428 0.1586 0.2598
21 Li (1987) Dy 0.7 0.7 1 1 0.30000123 0.2517 0.1919

@ -0,0 +1,21 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed La[M],Xaq La,D La
Li (1987) La,0.0001,0.0001,1,1,0.04999962,0.0363,0.3774
Li (1987) La,0.0001,0.0001,1,1,0.09999712,0.0844,0.1848
Li (1987) La,0.0001,0.0001,1,1,0.1499944,0.1345,0.1152
Li (1987) La,0.0001,0.0001,1,1,0.19999665,0.1835,0.0899
Li (1987) La,0.0001,0.0001,1,1,0.24999486,0.2329,0.0734
Li (1987) La,0.0001,0.0001,1,1,0.29998637,0.2833,0.0589
Li (1987) La,0.01,0.01,1,1,0.0499991,0.0395,0.2658
Li (1987) La,0.01,0.01,1,1,0.10000231,0.0881,0.1351
Li (1987) La,0.01,0.01,1,1,0.15000091,0.1367,0.0973
Li (1987) La,0.01,0.01,1,1,0.20009536,0.1856,0.0781
Li (1987) La,0.01,0.01,1,1,0.40540686,0.3846,0.0541
Li (1987) La,0.03,0.03,1,1,0.09999756,0.0897,0.1148
Li (1987) La,0.03,0.03,1,1,0.15000544,0.1391,0.0784
Li (1987) La,0.03,0.03,1,1,0.19999343,0.1883,0.0621
Li (1987) La,0.03,0.03,1,1,0.29999853,0.2881,0.0413
Li (1987) La,0.04,0.04,1,1,0.05030076,0.0444,0.1329
Li (1987) La,0.04,0.04,1,1,0.09999639,0.0919,0.0881
Li (1987) La,0.04,0.04,1,1,0.15000408,0.1413,0.0616
Li (1987) La,0.04,0.04,1,1,0.20049903,0.1917,0.0459
Li (1987) La,0.04,0.04,1,1,0.29948604,0.2883,0.0388
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed La[M] Xaq La D La
2 Li (1987) La 0.0001 0.0001 1 1 0.04999962 0.0363 0.3774
3 Li (1987) La 0.0001 0.0001 1 1 0.09999712 0.0844 0.1848
4 Li (1987) La 0.0001 0.0001 1 1 0.1499944 0.1345 0.1152
5 Li (1987) La 0.0001 0.0001 1 1 0.19999665 0.1835 0.0899
6 Li (1987) La 0.0001 0.0001 1 1 0.24999486 0.2329 0.0734
7 Li (1987) La 0.0001 0.0001 1 1 0.29998637 0.2833 0.0589
8 Li (1987) La 0.01 0.01 1 1 0.0499991 0.0395 0.2658
9 Li (1987) La 0.01 0.01 1 1 0.10000231 0.0881 0.1351
10 Li (1987) La 0.01 0.01 1 1 0.15000091 0.1367 0.0973
11 Li (1987) La 0.01 0.01 1 1 0.20009536 0.1856 0.0781
12 Li (1987) La 0.01 0.01 1 1 0.40540686 0.3846 0.0541
13 Li (1987) La 0.03 0.03 1 1 0.09999756 0.0897 0.1148
14 Li (1987) La 0.03 0.03 1 1 0.15000544 0.1391 0.0784
15 Li (1987) La 0.03 0.03 1 1 0.19999343 0.1883 0.0621
16 Li (1987) La 0.03 0.03 1 1 0.29999853 0.2881 0.0413
17 Li (1987) La 0.04 0.04 1 1 0.05030076 0.0444 0.1329
18 Li (1987) La 0.04 0.04 1 1 0.09999639 0.0919 0.0881
19 Li (1987) La 0.04 0.04 1 1 0.15000408 0.1413 0.0616
20 Li (1987) La 0.04 0.04 1 1 0.20049903 0.1917 0.0459
21 Li (1987) La 0.04 0.04 1 1 0.29948604 0.2883 0.0388

@ -0,0 +1,51 @@
label,Feed H+[M],Feed H+[M],PC88A[M],PC88A[M],Feed Nd[M],Xaq Nd,D Nd
Lyon (2016) Nd,0.01,0.01,1,1,0.08666112,0.05352756,0.619
Lyon (2016) Nd,0.05,0.05,1,1,0.08666112,0.060900295,0.423
Lyon (2016) Nd,0.1,0.1,1,1,0.08666112,0.067916239,0.276
Lyon (2016) Nd,0.3,0.3,1,1,0.08666112,0.084878668,0.021
Lyon (2016) Nd,0.01,0.01,1,1,0.042983916,0.015124531,1.842
Lyon (2016) Nd,0.05,0.05,1,1,0.042983916,0.020410216,1.106
Lyon (2016) Nd,0.1,0.1,1,1,0.042983916,0.026354332,0.631
Lyon (2016) Nd,0.3,0.3,1,1,0.042983916,0.039290599,0.094
Lyon (2016) Nd,0.01,0.01,1,1,0.005546312,3.16E-05,174.668
Lyon (2016) Nd,0.05,0.05,1,1,0.005546312,0.000451912,11.273
Lyon (2016) Nd,0.1,0.1,1,1,0.005546312,0.001558828,2.558
Lyon (2016) Nd,0.3,0.3,1,1,0.005546312,0.005400498,0.027
Lee (2005) Nd,0.251,0.25,1,1,0.1,0.087622932,0.141253754
Lee (2005) Nd,0.251,0.25,1.5,1.5,0.1,0.07955199,0.257039578
Lee (2005) Nd,0.251,0.25,2,2,0.1,0.074253556,0.34673685
Lee (2005) Nd,0.251,0.25,2.5,2.5,0.1,0.071525275,0.398107171
Lee (2005) Nd,0.251,0.25,3,3,0.1,0.066613942,0.501187234
Lee (2005) Nd,0.134,0.13,1,1,0.1,0.075124079,0.331131121
Lee (2005) Nd,0.0835,0.08,1,1,0.1,0.065582051,0.52480746
Lee (2005) Nd,0.0285,0.03,1,1,0.1,0.059662917,0.676082975
Lee (2005) Nd,0.262,0.26,2,2,0.1,0.079923999,0.251188643
Lee (2005) Nd,0.134,0.13,2,2,0.1,0.061313682,0.630957344
Lee (2005) Nd,0.0835,0.08,2,2,0.1,0.051151089,0.954992586
Lee (2005) Nd,0.0285,0.03,2,2,0.1,0.044837645,1.230268771
Lee (2005) Nd,0.0114,0.01,2,2,0.1,0.041450132,1.412537545
Lee (2005) Nd,0.262,0.26,3,3,0.1,0.074253556,0.34673685
Lee (2005) Nd,0.134,0.13,3,3,0.1,0.048273748,1.071519305
Lee (2005) Nd,0.0835,0.08,3,3,0.1,0.040337083,1.479108388
Lee (2005) Nd,0.0285,0.03,3,3,0.1,0.033900091,1.9498446
Lee (2005) Nd,0.0114,0.01,3,3,0.1,0.030387123,2.290867653
Li (1987) Nd,0.01,0.01,1,1,0.05000119,0.0239,1.0921
Li (1987) Nd,0.01,0.01,1,1,0.09999803,0.0683,0.4641
Li (1987) Nd,0.01,0.01,1,1,0.1500057,0.117,0.2821
Li (1987) Nd,0.01,0.01,1,1,0.200004,0.168,0.1905
Li (1987) Nd,0.01,0.01,1,1,0.30001149,0.2637,0.1377
Li (1987) Nd,0.05,0.05,1,1,0.03453582,0.0201,0.7182
Li (1987) Nd,0.05,0.05,1,1,0.09996185,0.0757,0.3205
Li (1987) Nd,0.05,0.05,1,1,0.19999308,0.1722,0.1614
Li (1987) Nd,0.1,0.1,1,1,0.04999817,0.0389,0.2853
Li (1987) Nd,0.1,0.1,1,1,0.1499974,0.133,0.1278
Li (1987) Nd,0.1,0.1,1,1,0.19999876,0.1807,0.1068
Li (1987) Nd,0.1,0.1,1,1,0.2500032,0.232,0.0776
Li (1987) Nd,0.1,0.1,1,1,0.30001216,0.2807,0.0688
Li (1987) Nd,0.3,0.3,1,1,0.01996974,0.0189,0.0566
Li (1987) Nd,0.3,0.3,1,1,0.04997968,0.0478,0.0456
Li (1987) Nd,0.3,0.3,1,1,0.15000144,0.1464,0.0246
Li (1987) Nd,0.3,0.3,1,1,0.29998765,0.2957,0.0145
Li (1987) Nd,0.5,0.5,1,1,0.04999786,0.0482,0.0373
Li (1987) Nd,0.5,0.5,1,1,0.10000096,0.0976,0.0246
Li (1987) Nd,0.5,0.5,1,1,0.20000784,0.1968,0.0163
1 label Feed H+[M] Feed H+[M] PC88A[M] PC88A[M] Feed Nd[M] Xaq Nd D Nd
2 Lyon (2016) Nd 0.01 0.01 1 1 0.08666112 0.05352756 0.619
3 Lyon (2016) Nd 0.05 0.05 1 1 0.08666112 0.060900295 0.423
4 Lyon (2016) Nd 0.1 0.1 1 1 0.08666112 0.067916239 0.276
5 Lyon (2016) Nd 0.3 0.3 1 1 0.08666112 0.084878668 0.021
6 Lyon (2016) Nd 0.01 0.01 1 1 0.042983916 0.015124531 1.842
7 Lyon (2016) Nd 0.05 0.05 1 1 0.042983916 0.020410216 1.106
8 Lyon (2016) Nd 0.1 0.1 1 1 0.042983916 0.026354332 0.631
9 Lyon (2016) Nd 0.3 0.3 1 1 0.042983916 0.039290599 0.094
10 Lyon (2016) Nd 0.01 0.01 1 1 0.005546312 3.16E-05 174.668
11 Lyon (2016) Nd 0.05 0.05 1 1 0.005546312 0.000451912 11.273
12 Lyon (2016) Nd 0.1 0.1 1 1 0.005546312 0.001558828 2.558
13 Lyon (2016) Nd 0.3 0.3 1 1 0.005546312 0.005400498 0.027
14 Lee (2005) Nd 0.251 0.25 1 1 0.1 0.087622932 0.141253754
15 Lee (2005) Nd 0.251 0.25 1.5 1.5 0.1 0.07955199 0.257039578
16 Lee (2005) Nd 0.251 0.25 2 2 0.1 0.074253556 0.34673685
17 Lee (2005) Nd 0.251 0.25 2.5 2.5 0.1 0.071525275 0.398107171
18 Lee (2005) Nd 0.251 0.25 3 3 0.1 0.066613942 0.501187234
19 Lee (2005) Nd 0.134 0.13 1 1 0.1 0.075124079 0.331131121
20 Lee (2005) Nd 0.0835 0.08 1 1 0.1 0.065582051 0.52480746
21 Lee (2005) Nd 0.0285 0.03 1 1 0.1 0.059662917 0.676082975
22 Lee (2005) Nd 0.262 0.26 2 2 0.1 0.079923999 0.251188643
23 Lee (2005) Nd 0.134 0.13 2 2 0.1 0.061313682 0.630957344
24 Lee (2005) Nd 0.0835 0.08 2 2 0.1 0.051151089 0.954992586
25 Lee (2005) Nd 0.0285 0.03 2 2 0.1 0.044837645 1.230268771
26 Lee (2005) Nd 0.0114 0.01 2 2 0.1 0.041450132 1.412537545
27 Lee (2005) Nd 0.262 0.26 3 3 0.1 0.074253556 0.34673685
28 Lee (2005) Nd 0.134 0.13 3 3 0.1 0.048273748 1.071519305
29 Lee (2005) Nd 0.0835 0.08 3 3 0.1 0.040337083 1.479108388
30 Lee (2005) Nd 0.0285 0.03 3 3 0.1 0.033900091 1.9498446
31 Lee (2005) Nd 0.0114 0.01 3 3 0.1 0.030387123 2.290867653
32 Li (1987) Nd 0.01 0.01 1 1 0.05000119 0.0239 1.0921
33 Li (1987) Nd 0.01 0.01 1 1 0.09999803 0.0683 0.4641
34 Li (1987) Nd 0.01 0.01 1 1 0.1500057 0.117 0.2821
35 Li (1987) Nd 0.01 0.01 1 1 0.200004 0.168 0.1905
36 Li (1987) Nd 0.01 0.01 1 1 0.30001149 0.2637 0.1377
37 Li (1987) Nd 0.05 0.05 1 1 0.03453582 0.0201 0.7182
38 Li (1987) Nd 0.05 0.05 1 1 0.09996185 0.0757 0.3205
39 Li (1987) Nd 0.05 0.05 1 1 0.19999308 0.1722 0.1614
40 Li (1987) Nd 0.1 0.1 1 1 0.04999817 0.0389 0.2853
41 Li (1987) Nd 0.1 0.1 1 1 0.1499974 0.133 0.1278
42 Li (1987) Nd 0.1 0.1 1 1 0.19999876 0.1807 0.1068
43 Li (1987) Nd 0.1 0.1 1 1 0.2500032 0.232 0.0776
44 Li (1987) Nd 0.1 0.1 1 1 0.30001216 0.2807 0.0688
45 Li (1987) Nd 0.3 0.3 1 1 0.01996974 0.0189 0.0566
46 Li (1987) Nd 0.3 0.3 1 1 0.04997968 0.0478 0.0456
47 Li (1987) Nd 0.3 0.3 1 1 0.15000144 0.1464 0.0246
48 Li (1987) Nd 0.3 0.3 1 1 0.29998765 0.2957 0.0145
49 Li (1987) Nd 0.5 0.5 1 1 0.04999786 0.0482 0.0373
50 Li (1987) Nd 0.5 0.5 1 1 0.10000096 0.0976 0.0246
51 Li (1987) Nd 0.5 0.5 1 1 0.20000784 0.1968 0.0163

@ -0,0 +1,33 @@
label,Feed H+[M],Feed H+[M],PC88A[M],PC88A[M],Feed Pr[M],Xaq Pr,D Pr
Lyon (2016) Pr,0.03,0.03,1,1,0.09296866,0.06556323,0.418
Lyon (2016) Pr,0.05,0.05,1,1,0.09296866,0.066835844,0.391
Lyon (2016) Pr,0.1,0.1,1,1,0.09296866,0.080076365,0.161
Lyon (2016) Pr,0.3,0.3,1,1,0.09296866,0.091957131,0.011
Lyon (2016) Pr,0.03,0.03,1,1,0.047548856,0.02373882,1.003
Lyon (2016) Pr,0.05,0.05,1,1,0.047548856,0.025646632,0.854
Lyon (2016) Pr,0.1,0.1,1,1,0.047548856,0.034988121,0.359
Lyon (2016) Pr,0.3,0.3,1,1,0.047548856,0.045371046,0.048
Lyon (2016) Pr,0.01,0.01,1,1,0.00638716,5.54E-05,114.332
Lyon (2016) Pr,0.05,0.05,1,1,0.00638716,0.000669233,8.544
Lyon (2016) Pr,0.1,0.1,1,1,0.00638716,0.002264147,1.821
Lyon (2016) Pr,0.3,0.3,1,1,0.00638716,0.006323921,0.01
Li (1987) Pr,0.01,0.01,1,1,0.04999995,0.0259,0.9305
Li (1987) Pr,0.01,0.01,1,1,0.09999925,0.0725,0.3793
Li (1987) Pr,0.01,0.01,1,1,0.20000715,0.1673,0.1955
Li (1987) Pr,0.01,0.01,1,1,0.29999192,0.2648,0.1329
Li (1987) Pr,0.03,0.03,1,1,0.05000109,0.0307,0.6287
Li (1987) Pr,0.03,0.03,1,1,0.10009624,0.0776,0.2899
Li (1987) Pr,0.03,0.03,1,1,0.20000456,0.1736,0.1521
Li (1987) Pr,0.03,0.03,1,1,0.2999997,0.273,0.0989
Li (1987) Pr,0.05,0.05,1,1,0.05002915,0.0349,0.4335
Li (1987) Pr,0.05,0.05,1,1,0.09997622,0.0809,0.2358
Li (1987) Pr,0.05,0.05,1,1,0.14999553,0.1299,0.1547
Li (1987) Pr,0.05,0.05,1,1,0.25001088,0.2272,0.1004
Li (1987) Pr,0.07,0.07,1,1,0.04999995,0.0385,0.2987
Li (1987) Pr,0.07,0.07,1,1,0.09999936,0.0864,0.1574
Li (1987) Pr,0.07,0.07,1,1,0.14998624,0.1343,0.1168
Li (1987) Pr,0.07,0.07,1,1,0.24999474,0.2334,0.0711
Li (1987) Pr,0.1,0.1,1,1,0.0499992,0.0415,0.2048
Li (1987) Pr,0.1,0.1,1,1,0.10000199,0.0901,0.1099
Li (1987) Pr,0.1,0.1,1,1,0.1999998,0.189,0.0582
Li (1987) Pr,0.1,0.1,1,1,0.30000544,0.2888,0.0388
1 label Feed H+[M] Feed H+[M] PC88A[M] PC88A[M] Feed Pr[M] Xaq Pr D Pr
2 Lyon (2016) Pr 0.03 0.03 1 1 0.09296866 0.06556323 0.418
3 Lyon (2016) Pr 0.05 0.05 1 1 0.09296866 0.066835844 0.391
4 Lyon (2016) Pr 0.1 0.1 1 1 0.09296866 0.080076365 0.161
5 Lyon (2016) Pr 0.3 0.3 1 1 0.09296866 0.091957131 0.011
6 Lyon (2016) Pr 0.03 0.03 1 1 0.047548856 0.02373882 1.003
7 Lyon (2016) Pr 0.05 0.05 1 1 0.047548856 0.025646632 0.854
8 Lyon (2016) Pr 0.1 0.1 1 1 0.047548856 0.034988121 0.359
9 Lyon (2016) Pr 0.3 0.3 1 1 0.047548856 0.045371046 0.048
10 Lyon (2016) Pr 0.01 0.01 1 1 0.00638716 5.54E-05 114.332
11 Lyon (2016) Pr 0.05 0.05 1 1 0.00638716 0.000669233 8.544
12 Lyon (2016) Pr 0.1 0.1 1 1 0.00638716 0.002264147 1.821
13 Lyon (2016) Pr 0.3 0.3 1 1 0.00638716 0.006323921 0.01
14 Li (1987) Pr 0.01 0.01 1 1 0.04999995 0.0259 0.9305
15 Li (1987) Pr 0.01 0.01 1 1 0.09999925 0.0725 0.3793
16 Li (1987) Pr 0.01 0.01 1 1 0.20000715 0.1673 0.1955
17 Li (1987) Pr 0.01 0.01 1 1 0.29999192 0.2648 0.1329
18 Li (1987) Pr 0.03 0.03 1 1 0.05000109 0.0307 0.6287
19 Li (1987) Pr 0.03 0.03 1 1 0.10009624 0.0776 0.2899
20 Li (1987) Pr 0.03 0.03 1 1 0.20000456 0.1736 0.1521
21 Li (1987) Pr 0.03 0.03 1 1 0.2999997 0.273 0.0989
22 Li (1987) Pr 0.05 0.05 1 1 0.05002915 0.0349 0.4335
23 Li (1987) Pr 0.05 0.05 1 1 0.09997622 0.0809 0.2358
24 Li (1987) Pr 0.05 0.05 1 1 0.14999553 0.1299 0.1547
25 Li (1987) Pr 0.05 0.05 1 1 0.25001088 0.2272 0.1004
26 Li (1987) Pr 0.07 0.07 1 1 0.04999995 0.0385 0.2987
27 Li (1987) Pr 0.07 0.07 1 1 0.09999936 0.0864 0.1574
28 Li (1987) Pr 0.07 0.07 1 1 0.14998624 0.1343 0.1168
29 Li (1987) Pr 0.07 0.07 1 1 0.24999474 0.2334 0.0711
30 Li (1987) Pr 0.1 0.1 1 1 0.0499992 0.0415 0.2048
31 Li (1987) Pr 0.1 0.1 1 1 0.10000199 0.0901 0.1099
32 Li (1987) Pr 0.1 0.1 1 1 0.1999998 0.189 0.0582
33 Li (1987) Pr 0.1 0.1 1 1 0.30000544 0.2888 0.0388

@ -0,0 +1,21 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Sm[M],Xaq Sm,D Sm
Li (1987) Sm,0.01,0.01,1,1,0.050050300000000006,0.0115,3.3522
Li (1987) Sm,0.01,0.01,1,1,0.09997919999999999,0.048,1.0829
Li (1987) Sm,0.01,0.01,1,1,0.1500016,0.0944,0.589
Li (1987) Sm,0.01,0.01,1,1,0.24999968,0.1864,0.3412
Li (1987) Sm,0.01,0.01,1,1,0.30000263,0.2371,0.2653
Li (1987) Sm,0.05,0.05,1,1,0.05032248,0.0156,2.2258
Li (1987) Sm,0.05,0.05,1,1,0.10000216,0.0556,0.7986
Li (1987) Sm,0.05,0.05,1,1,0.15000255,0.1035,0.4493
Li (1987) Sm,0.05,0.05,1,1,0.30392343,0.1997,0.5219
Li (1987) Sm,0.05,0.05,1,1,0.30000411,0.2471,0.2141
Li (1987) Sm,0.1,0.1,1,1,0.04999989,0.0219,1.2831
Li (1987) Sm,0.1,0.1,1,1,0.09999773,0.0623,0.6051
Li (1987) Sm,0.1,0.1,1,1,0.15000375,0.1105,0.3575
Li (1987) Sm,0.1,0.1,1,1,0.2500038,0.2073,0.20600000000000002
Li (1987) Sm,0.1,0.1,1,1,0.30061536,0.2572,0.1688
Li (1987) Sm,0.3,0.3,1,1,0.0502452,0.0408,0.2315
Li (1987) Sm,0.3,0.3,1,1,0.09999592,0.0842,0.1876
Li (1987) Sm,0.3,0.3,1,1,0.14999496,0.1334,0.1244
Li (1987) Sm,0.3,0.3,1,1,0.1999935,0.1814,0.1025
Li (1987) Sm,0.3,0.3,1,1,0.30001088,0.2782,0.0784
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Sm[M] Xaq Sm D Sm
2 Li (1987) Sm 0.01 0.01 1 1 0.050050300000000006 0.0115 3.3522
3 Li (1987) Sm 0.01 0.01 1 1 0.09997919999999999 0.048 1.0829
4 Li (1987) Sm 0.01 0.01 1 1 0.1500016 0.0944 0.589
5 Li (1987) Sm 0.01 0.01 1 1 0.24999968 0.1864 0.3412
6 Li (1987) Sm 0.01 0.01 1 1 0.30000263 0.2371 0.2653
7 Li (1987) Sm 0.05 0.05 1 1 0.05032248 0.0156 2.2258
8 Li (1987) Sm 0.05 0.05 1 1 0.10000216 0.0556 0.7986
9 Li (1987) Sm 0.05 0.05 1 1 0.15000255 0.1035 0.4493
10 Li (1987) Sm 0.05 0.05 1 1 0.30392343 0.1997 0.5219
11 Li (1987) Sm 0.05 0.05 1 1 0.30000411 0.2471 0.2141
12 Li (1987) Sm 0.1 0.1 1 1 0.04999989 0.0219 1.2831
13 Li (1987) Sm 0.1 0.1 1 1 0.09999773 0.0623 0.6051
14 Li (1987) Sm 0.1 0.1 1 1 0.15000375 0.1105 0.3575
15 Li (1987) Sm 0.1 0.1 1 1 0.2500038 0.2073 0.20600000000000002
16 Li (1987) Sm 0.1 0.1 1 1 0.30061536 0.2572 0.1688
17 Li (1987) Sm 0.3 0.3 1 1 0.0502452 0.0408 0.2315
18 Li (1987) Sm 0.3 0.3 1 1 0.09999592 0.0842 0.1876
19 Li (1987) Sm 0.3 0.3 1 1 0.14999496 0.1334 0.1244
20 Li (1987) Sm 0.3 0.3 1 1 0.1999935 0.1814 0.1025
21 Li (1987) Sm 0.3 0.3 1 1 0.30001088 0.2782 0.0784

@ -0,0 +1,21 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Y[M],Xaq Y,D Y
Li (1987) Y,0.1,0.1,1,1,0.1500005,0.047,2.1915
Li (1987) Y,0.1,0.1,1,1,0.19999809,0.0857,1.3337
Li (1987) Y,0.1,0.1,1,1,0.2999996,0.1772,0.693
Li (1987) Y,0.5,0.5,1,1,0.05,0.016,2.125
Li (1987) Y,0.5,0.5,1,1,0.10000039999999999,0.0445,1.2472
Li (1987) Y,0.5,0.5,1,1,0.15000048,0.0828,0.8116
Li (1987) Y,0.5,0.5,1,1,0.19999436,0.1214,0.6474
Li (1987) Y,0.5,0.5,1,1,0.29999366,0.2083,0.4402
Li (1987) Y,1.0,1.0,1,1,0.04999995,0.0333,0.5015
Li (1987) Y,1.0,1.0,1,1,0.09999846,0.0694,0.4409
Li (1987) Y,1.0,1.0,1,1,0.15000104,0.1108,0.3538
Li (1987) Y,1.0,1.0,1,1,0.19999756,0.1526,0.3106
Li (1987) Y,1.0,1.0,1,1,0.29999472,0.2416,0.2417
Li (1987) Y,1.0,1.0,1,1,0.25000384,0.1984,0.2601
Li (1987) Y,1.5,1.5,1,1,0.050001300000000005,0.0405,0.2346
Li (1987) Y,1.5,1.5,1,1,0.09999854,0.0838,0.1933
Li (1987) Y,1.5,1.5,1,1,0.19999977,0.1753,0.1409
Li (1987) Y,2.0,2.0,1,1,0.09999804,0.0908,0.1013
Li (1987) Y,2.0,2.0,1,1,0.19992651,0.1851,0.0801
Li (1987) Y,2.0,2.0,1,1,0.30001335,0.2821,0.0635
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Y[M] Xaq Y D Y
2 Li (1987) Y 0.1 0.1 1 1 0.1500005 0.047 2.1915
3 Li (1987) Y 0.1 0.1 1 1 0.19999809 0.0857 1.3337
4 Li (1987) Y 0.1 0.1 1 1 0.2999996 0.1772 0.693
5 Li (1987) Y 0.5 0.5 1 1 0.05 0.016 2.125
6 Li (1987) Y 0.5 0.5 1 1 0.10000039999999999 0.0445 1.2472
7 Li (1987) Y 0.5 0.5 1 1 0.15000048 0.0828 0.8116
8 Li (1987) Y 0.5 0.5 1 1 0.19999436 0.1214 0.6474
9 Li (1987) Y 0.5 0.5 1 1 0.29999366 0.2083 0.4402
10 Li (1987) Y 1.0 1.0 1 1 0.04999995 0.0333 0.5015
11 Li (1987) Y 1.0 1.0 1 1 0.09999846 0.0694 0.4409
12 Li (1987) Y 1.0 1.0 1 1 0.15000104 0.1108 0.3538
13 Li (1987) Y 1.0 1.0 1 1 0.19999756 0.1526 0.3106
14 Li (1987) Y 1.0 1.0 1 1 0.29999472 0.2416 0.2417
15 Li (1987) Y 1.0 1.0 1 1 0.25000384 0.1984 0.2601
16 Li (1987) Y 1.5 1.5 1 1 0.050001300000000005 0.0405 0.2346
17 Li (1987) Y 1.5 1.5 1 1 0.09999854 0.0838 0.1933
18 Li (1987) Y 1.5 1.5 1 1 0.19999977 0.1753 0.1409
19 Li (1987) Y 2.0 2.0 1 1 0.09999804 0.0908 0.1013
20 Li (1987) Y 2.0 2.0 1 1 0.19992651 0.1851 0.0801
21 Li (1987) Y 2.0 2.0 1 1 0.30001335 0.2821 0.0635

@ -0,0 +1,8 @@
species,beta0,beta1,Cphi
Ce,0.6005,4.91,-0.02619
Dy,0.6129,5.359,-0.0197
La,0.593,5.277,-0.02434
Nd,0.5877,5.206,-0.01969
Pr,0.5879,5.448,-0.02067
Sm,0.5978,5.279,-0.01992
Y,0.6248,5.66,-0.01563
1 species beta0 beta1 Cphi
2 Ce 0.6005 4.91 -0.02619
3 Dy 0.6129 5.359 -0.0197
4 La 0.593 5.277 -0.02434
5 Nd 0.5877 5.206 -0.01969
6 Pr 0.5879 5.448 -0.02067
7 Sm 0.5978 5.279 -0.01992
8 Y 0.6248 5.66 -0.01563

@ -0,0 +1,21 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Nd[M],Xaq Nd,D Nd,Feed Pr[M],Xaq Pr,D Pr,Feed Ce[M],Xaq Ce,D Ce,Feed La[M],Xaq La,D La,Feed Dy[M],Xaq Dy,D Dy,Feed Sm[M],Xaq Sm,D Sm,Feed Y[M],Xaq Y,D Y
Lyon (2016),0.02,0.02,1,1,0.048530227,0.029263727,0.658374793,0.04967791,0.035072604,0.416430595,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.048530227,0.032127011,0.510574018,0.04967791,0.037506822,0.324503311,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.048530227,0.039018303,0.243781095,0.04967791,0.043070748,0.153402537,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.048530227,0.046443428,0.044932079,0.04967791,0.048535318,0.023541453,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.017097653,0.33,0.008303308,0.006642646,0.25,0,0,0,0.054425491,0.050393973,0.08,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.013298174,0.71,0.008303308,0.005462702,0.52,0,0,0,0.054425491,0.048594188,0.12,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010932634,1.08,0.008303308,0.004537327,0.83,0,0,0,0.054425491,0.048164151,0.13,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.009396644,1.42,0.008303308,0.003972875,1.09,0,0,0,0.054425491,0.047326514,0.15,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.008209342,1.77,0.008303308,0.002997584,1.77,0,0,0,0.054425491,0.045735706,0.19,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.018928042,0.201385664,0.008303308,0.007354823,0.128960943,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.014333115,0.586527247,0.008303308,0.005999476,0.384005473,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010952454,1.076235839,0.008303308,0.004805359,0.727926764,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.008786058,1.588177405,0.008303308,0.003974007,1.089404412,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.00700602,2.245762712,0.008303308,0.00322327,1.576050934,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.1,0.1,0.009359401,0.007999488,0.17,0.003371001,0.003064546,0.1,0.038539496,0.037783819,0.02,0.022461314,0.022020896,0.02,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.3,0.3,0.009359401,0.006881912,0.36,0.003371001,0.002763116,0.22,0.038539496,0.035357336,0.09,0.022461314,0.021597417,0.04,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.5,0.5,0.009359401,0.005813293,0.61,0.003371001,0.002340973,0.44,0.038539496,0.032386131,0.19,0.022461314,0.02060671,0.09,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.7,0.7,0.009359401,0.005638193,0.66,0.003371001,0.002147134,0.57,0.038539496,0.03034606,0.27,0.022461314,0.019877269,0.13,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,1,1,0.009359401,0.005005027,0.87,0.003371001,0.001862432,0.81,0.038539496,0.028547775,0.35,0.022461314,0.019702907,0.14,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,2,2,0.009359401,0.003109436,2.01,0.003371001,0.001404584,1.4,0.038539496,0.021059834,0.83,0.022461314,0.018261231,0.23,0,0,0,0,0,0,0,0,0
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Nd[M] Xaq Nd D Nd Feed Pr[M] Xaq Pr D Pr Feed Ce[M] Xaq Ce D Ce Feed La[M] Xaq La D La Feed Dy[M] Xaq Dy D Dy Feed Sm[M] Xaq Sm D Sm Feed Y[M] Xaq Y D Y
2 Lyon (2016) 0.02 0.02 1 1 0.048530227 0.029263727 0.658374793 0.04967791 0.035072604 0.416430595 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
3 Lyon (2016) 0.05 0.05 1 1 0.048530227 0.032127011 0.510574018 0.04967791 0.037506822 0.324503311 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
4 Lyon (2016) 0.1 0.1 1 1 0.048530227 0.039018303 0.243781095 0.04967791 0.043070748 0.153402537 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
5 Lyon (2016) 0.3 0.3 1 1 0.048530227 0.046443428 0.044932079 0.04967791 0.048535318 0.023541453 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
6 Banda (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.017097653 0.33 0.008303308 0.006642646 0.25 0 0 0 0.054425491 0.050393973 0.08 0 0 0 0 0 0 0 0 0
7 Banda (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.013298174 0.71 0.008303308 0.005462702 0.52 0 0 0 0.054425491 0.048594188 0.12 0 0 0 0 0 0 0 0 0
8 Banda (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010932634 1.08 0.008303308 0.004537327 0.83 0 0 0 0.054425491 0.048164151 0.13 0 0 0 0 0 0 0 0 0
9 Banda (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.009396644 1.42 0.008303308 0.003972875 1.09 0 0 0 0.054425491 0.047326514 0.15 0 0 0 0 0 0 0 0 0
10 Banda (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.008209342 1.77 0.008303308 0.002997584 1.77 0 0 0 0.054425491 0.045735706 0.19 0 0 0 0 0 0 0 0 0
11 Liu (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.018928042 0.201385664 0.008303308 0.007354823 0.128960943 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
12 Liu (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.014333115 0.586527247 0.008303308 0.005999476 0.384005473 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
13 Liu (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010952454 1.076235839 0.008303308 0.004805359 0.727926764 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
14 Liu (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.008786058 1.588177405 0.008303308 0.003974007 1.089404412 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
15 Liu (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.00700602 2.245762712 0.008303308 0.00322327 1.576050934 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
16 Kim (2012) 0.01023293 0.01023293 0.1 0.1 0.009359401 0.007999488 0.17 0.003371001 0.003064546 0.1 0.038539496 0.037783819 0.02 0.022461314 0.022020896 0.02 0 0 0 0 0 0 0 0 0
17 Kim (2012) 0.01023293 0.01023293 0.3 0.3 0.009359401 0.006881912 0.36 0.003371001 0.002763116 0.22 0.038539496 0.035357336 0.09 0.022461314 0.021597417 0.04 0 0 0 0 0 0 0 0 0
18 Kim (2012) 0.01023293 0.01023293 0.5 0.5 0.009359401 0.005813293 0.61 0.003371001 0.002340973 0.44 0.038539496 0.032386131 0.19 0.022461314 0.02060671 0.09 0 0 0 0 0 0 0 0 0
19 Kim (2012) 0.01023293 0.01023293 0.7 0.7 0.009359401 0.005638193 0.66 0.003371001 0.002147134 0.57 0.038539496 0.03034606 0.27 0.022461314 0.019877269 0.13 0 0 0 0 0 0 0 0 0
20 Kim (2012) 0.01023293 0.01023293 1 1 0.009359401 0.005005027 0.87 0.003371001 0.001862432 0.81 0.038539496 0.028547775 0.35 0.022461314 0.019702907 0.14 0 0 0 0 0 0 0 0 0
21 Kim (2012) 0.01023293 0.01023293 2 2 0.009359401 0.003109436 2.01 0.003371001 0.001404584 1.4 0.038539496 0.021059834 0.83 0.022461314 0.018261231 0.23 0 0 0 0 0 0 0 0 0

@ -0,0 +1,209 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Nd[M],Xaq Nd,D Nd,Feed Pr[M],Xaq Pr,D Pr,Feed Ce[M],Xaq Ce,D Ce,Feed La[M],Xaq La,D La,Feed Dy[M],Xaq Dy,D Dy,Feed Sm[M],Xaq Sm,D Sm,Feed Y[M],Xaq Y,D Y
Lyon (2016),0.02,0.02,1,1,0.048530227,0.029263727,0.658374793,0.04967791,0.035072604,0.416430595,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.048530227,0.032127011,0.510574018,0.04967791,0.037506822,0.324503311,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.048530227,0.039018303,0.243781095,0.04967791,0.043070748,0.153402537,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.048530227,0.046443428,0.044932079,0.04967791,0.048535318,0.023541453,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.017097653,0.33,0.008303308,0.006642646,0.25,0,0,0,0.054425491,0.050393973,0.08,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.013298174,0.71,0.008303308,0.005462702,0.52,0,0,0,0.054425491,0.048594188,0.12,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010932634,1.08,0.008303308,0.004537327,0.83,0,0,0,0.054425491,0.048164151,0.13,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.009396644,1.42,0.008303308,0.003972875,1.09,0,0,0,0.054425491,0.047326514,0.15,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.008209342,1.77,0.008303308,0.002997584,1.77,0,0,0,0.054425491,0.045735706,0.19,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.018928042,0.201385664,0.008303308,0.007354823,0.128960943,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.014333115,0.586527247,0.008303308,0.005999476,0.384005473,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010952454,1.076235839,0.008303308,0.004805359,0.727926764,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.008786058,1.588177405,0.008303308,0.003974007,1.089404412,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.00700602,2.245762712,0.008303308,0.00322327,1.576050934,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.1,0.1,0.009359401,0.007999488,0.17,0.003371001,0.003064546,0.1,0.038539496,0.037783819,0.02,0.022461314,0.022020896,0.02,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.3,0.3,0.009359401,0.006881912,0.36,0.003371001,0.002763116,0.22,0.038539496,0.035357336,0.09,0.022461314,0.021597417,0.04,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.5,0.5,0.009359401,0.005813293,0.61,0.003371001,0.002340973,0.44,0.038539496,0.032386131,0.19,0.022461314,0.02060671,0.09,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.7,0.7,0.009359401,0.005638193,0.66,0.003371001,0.002147134,0.57,0.038539496,0.03034606,0.27,0.022461314,0.019877269,0.13,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,1,1,0.009359401,0.005005027,0.87,0.003371001,0.001862432,0.81,0.038539496,0.028547775,0.35,0.022461314,0.019702907,0.14,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,2,2,0.009359401,0.003109436,2.01,0.003371001,0.001404584,1.4,0.038539496,0.021059834,0.83,0.022461314,0.018261231,0.23,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.0508008,0.0305,0.6656,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.09999878,0.0763,0.3106,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.15009456,0.1232,0.2183,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.2000068,0.1708,0.171,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.30001216,0.2672,0.1228,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.0499975,0.035,0.4285,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.10000115,0.0785,0.2739,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.1500032,0.128,0.1719,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.20000832,0.1752,0.1416,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.29999816,0.2728,0.0997,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.05010115,0.0355,0.4113,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.10000382,0.0826,0.2107,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.1499967,0.1305,0.1494,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.2000008,0.178,0.1236,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.05,0.04,0.25,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.10029675,0.0865,0.1595,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.15000153,0.1351,0.1103,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.20054418,0.1838,0.0911,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.29999441,0.2753,0.0897,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.29998992,0.2811,0.0672,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.10000029,0.0221,3.5249,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000025,0.0575,1.6087,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999582,0.1037,0.9286,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.25000596,0.1494,0.6734,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30000931,0.1997,0.5023,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.0500002,0.0106,3.717,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.09999641,0.0409,1.4449,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.14999806,0.0802,0.8703,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999448,0.1252,0.5974,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.29999394,0.2206,0.3599,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.04999904,0.0221,1.2624,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.09999996,0.0573,0.7452,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000096,0.0984,0.5244,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999616,0.1414,0.4144,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30001016,0.2369,0.2664,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.04799855,0.0313,0.5335,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.1000035,0.071,0.4085,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000453,0.1131,0.3263,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19980428,0.1586,0.2598,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30000123,0.2517,0.1919,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.04999962,0.0363,0.3774,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.09999712,0.0844,0.1848,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.1499944,0.1345,0.1152,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.19999665,0.1835,0.0899,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.24999486,0.2329,0.0734,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.29998637,0.2833,0.0589,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.0499991,0.0395,0.2658,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.10000231,0.0881,0.1351,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.15000091,0.1367,0.0973,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.20009536,0.1856,0.0781,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.40540686,0.3846,0.0541,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.09999756,0.0897,0.1148,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.15000544,0.1391,0.0784,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.19999343,0.1883,0.0621,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.29999853,0.2881,0.0413,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.05030076,0.0444,0.1329,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.09999639,0.0919,0.0881,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.15000408,0.1413,0.0616,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.20049903,0.1917,0.0459,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.29948604,0.2883,0.0388,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.08666112,0.05352756,0.619,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.08666112,0.060900295,0.423,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.08666112,0.067916239,0.276,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.08666112,0.084878668,0.021,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0.08666112,0.08666112,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.042983916,0.015124531,1.842,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.042983916,0.020410216,1.106,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.042983916,0.026354332,0.631,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.042983916,0.039290599,0.094,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0.042983916,0.042983916,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.005546312,3.16E-05,174.668,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.005546312,0.000451912,11.273,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.005546312,0.001558828,2.558,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.005546312,0.005400498,0.027,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0.005546312,0.005546312,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,1,1,0.1,0.087622932,0.141253754,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,1.5,1.5,0.1,0.07955199,0.257039578,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,2,2,0.1,0.074253556,0.34673685,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,2.5,2.5,0.1,0.071525275,0.398107171,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,3,3,0.1,0.066613942,0.501187234,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,1,1,0.1,0.075124079,0.331131121,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,1,1,0.1,0.065582051,0.52480746,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,1,1,0.1,0.059662917,0.676082975,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.262,0.26,2,2,0.1,0.079923999,0.251188643,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,2,2,0.1,0.061313682,0.630957344,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,2,2,0.1,0.051151089,0.954992586,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,2,2,0.1,0.044837645,1.230268771,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0114,0.01,2,2,0.1,0.041450132,1.412537545,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.262,0.26,3,3,0.1,0.074253556,0.34673685,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,3,3,0.1,0.048273748,1.071519305,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,3,3,0.1,0.040337083,1.479108388,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,3,3,0.1,0.033900091,1.9498446,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0114,0.01,3,3,0.1,0.030387123,2.290867653,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.05000119,0.0239,1.0921,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.09999803,0.0683,0.4641,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.1500057,0.117,0.2821,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.200004,0.168,0.1905,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.30001149,0.2637,0.1377,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.03453582,0.0201,0.7182,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.09996185,0.0757,0.3205,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.19999308,0.1722,0.1614,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.04999817,0.0389,0.2853,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.1499974,0.133,0.1278,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.19999876,0.1807,0.1068,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.2500032,0.232,0.0776,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.30001216,0.2807,0.0688,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.01996974,0.0189,0.0566,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.04997968,0.0478,0.0456,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.15000144,0.1464,0.0246,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.29998765,0.2957,0.0145,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.04999786,0.0482,0.0373,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.10000096,0.0976,0.0246,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.20000784,0.1968,0.0163,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.03,0.03,1,1,0,0,0,0.09296866,0.06556323,0.418,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.09296866,0.066835844,0.391,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.09296866,0.080076365,0.161,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.09296866,0.091957131,0.011,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0,0,0,0.09296866,0.09296866,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.03,0.03,1,1,0,0,0,0.047548856,0.02373882,1.003,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.047548856,0.025646632,0.854,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.047548856,0.034988121,0.359,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.047548856,0.045371046,0.048,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0,0,0,0.047548856,0.047548856,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0,0,0,0.00638716,5.54E-05,114.332,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.00638716,0.000669233,8.544,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.00638716,0.002264147,1.821,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.00638716,0.006323921,0.01,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.5,0.5,1,1,0,0,0,0.00638716,0.00638716,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.04999995,0.0259,0.9305,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.09999925,0.0725,0.3793,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.20000715,0.1673,0.1955,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.29999192,0.2648,0.1329,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.05000109,0.0307,0.6287,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.10009624,0.0776,0.2899,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.20000456,0.1736,0.1521,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.2999997,0.273,0.0989,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.05002915,0.0349,0.4335,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.09997622,0.0809,0.2358,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.14999553,0.1299,0.1547,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.25001088,0.2272,0.1004,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.04999995,0.0385,0.2987,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.09999936,0.0864,0.1574,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.14998624,0.1343,0.1168,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.24999474,0.2334,0.0711,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.0499992,0.0415,0.2048,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.10000199,0.0901,0.1099,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.1999998,0.189,0.0582,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.30000544,0.2888,0.0388,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0500503,0.0115,3.3522,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0999792,0.048,1.0829,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1500016,0.0944,0.589,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.24999968,0.1864,0.3412,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30000263,0.2371,0.2653,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.05032248,0.0156,2.2258,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.10000216,0.0556,0.7986,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000255,0.1035,0.4493,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30392343,0.1997,0.5219,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30000411,0.2471,0.2141,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.04999989,0.0219,1.2831,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999773,0.0623,0.6051,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000375,0.1105,0.3575,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.2500038,0.2073,0.206,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30061536,0.2572,0.1688,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0502452,0.0408,0.2315,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999592,0.0842,0.1876,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.14999496,0.1334,0.1244,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1999935,0.1814,0.1025,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30001088,0.2782,0.0784,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1500005,0.047,2.1915
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999809,0.0857,1.3337
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.2999996,0.1772,0.693
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.05,0.016,2.125
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1000004,0.0445,1.2472
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000048,0.0828,0.8116
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999436,0.1214,0.6474
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.29999366,0.2083,0.4402
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.04999995,0.0333,0.5015
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999846,0.0694,0.4409
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000104,0.1108,0.3538
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999756,0.1526,0.3106
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.29999472,0.2416,0.2417
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.25000384,0.1984,0.2601
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0500013,0.0405,0.2346
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999854,0.0838,0.1933
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999977,0.1753,0.1409
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999804,0.0908,0.1013
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19992651,0.1851,0.0801
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30001335,0.2821,0.0635
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Nd[M] Xaq Nd D Nd Feed Pr[M] Xaq Pr D Pr Feed Ce[M] Xaq Ce D Ce Feed La[M] Xaq La D La Feed Dy[M] Xaq Dy D Dy Feed Sm[M] Xaq Sm D Sm Feed Y[M] Xaq Y D Y
2 Lyon (2016) 0.02 0.02 1 1 0.048530227 0.029263727 0.658374793 0.04967791 0.035072604 0.416430595 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
3 Lyon (2016) 0.05 0.05 1 1 0.048530227 0.032127011 0.510574018 0.04967791 0.037506822 0.324503311 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
4 Lyon (2016) 0.1 0.1 1 1 0.048530227 0.039018303 0.243781095 0.04967791 0.043070748 0.153402537 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
5 Lyon (2016) 0.3 0.3 1 1 0.048530227 0.046443428 0.044932079 0.04967791 0.048535318 0.023541453 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
6 Banda (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.017097653 0.33 0.008303308 0.006642646 0.25 0 0 0 0.054425491 0.050393973 0.08 0 0 0 0 0 0 0 0 0
7 Banda (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.013298174 0.71 0.008303308 0.005462702 0.52 0 0 0 0.054425491 0.048594188 0.12 0 0 0 0 0 0 0 0 0
8 Banda (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010932634 1.08 0.008303308 0.004537327 0.83 0 0 0 0.054425491 0.048164151 0.13 0 0 0 0 0 0 0 0 0
9 Banda (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.009396644 1.42 0.008303308 0.003972875 1.09 0 0 0 0.054425491 0.047326514 0.15 0 0 0 0 0 0 0 0 0
10 Banda (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.008209342 1.77 0.008303308 0.002997584 1.77 0 0 0 0.054425491 0.045735706 0.19 0 0 0 0 0 0 0 0 0
11 Liu (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.018928042 0.201385664 0.008303308 0.007354823 0.128960943 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
12 Liu (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.014333115 0.586527247 0.008303308 0.005999476 0.384005473 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
13 Liu (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010952454 1.076235839 0.008303308 0.004805359 0.727926764 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
14 Liu (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.008786058 1.588177405 0.008303308 0.003974007 1.089404412 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
15 Liu (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.00700602 2.245762712 0.008303308 0.00322327 1.576050934 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
16 Kim (2012) 0.01023293 0.01023293 0.1 0.1 0.009359401 0.007999488 0.17 0.003371001 0.003064546 0.1 0.038539496 0.037783819 0.02 0.022461314 0.022020896 0.02 0 0 0 0 0 0 0 0 0
17 Kim (2012) 0.01023293 0.01023293 0.3 0.3 0.009359401 0.006881912 0.36 0.003371001 0.002763116 0.22 0.038539496 0.035357336 0.09 0.022461314 0.021597417 0.04 0 0 0 0 0 0 0 0 0
18 Kim (2012) 0.01023293 0.01023293 0.5 0.5 0.009359401 0.005813293 0.61 0.003371001 0.002340973 0.44 0.038539496 0.032386131 0.19 0.022461314 0.02060671 0.09 0 0 0 0 0 0 0 0 0
19 Kim (2012) 0.01023293 0.01023293 0.7 0.7 0.009359401 0.005638193 0.66 0.003371001 0.002147134 0.57 0.038539496 0.03034606 0.27 0.022461314 0.019877269 0.13 0 0 0 0 0 0 0 0 0
20 Kim (2012) 0.01023293 0.01023293 1 1 0.009359401 0.005005027 0.87 0.003371001 0.001862432 0.81 0.038539496 0.028547775 0.35 0.022461314 0.019702907 0.14 0 0 0 0 0 0 0 0 0
21 Kim (2012) 0.01023293 0.01023293 2 2 0.009359401 0.003109436 2.01 0.003371001 0.001404584 1.4 0.038539496 0.021059834 0.83 0.022461314 0.018261231 0.23 0 0 0 0 0 0 0 0 0
22 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.0508008 0.0305 0.6656 0 0 0 0 0 0 0 0 0 0 0 0
23 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.09999878 0.0763 0.3106 0 0 0 0 0 0 0 0 0 0 0 0
24 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.15009456 0.1232 0.2183 0 0 0 0 0 0 0 0 0 0 0 0
25 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.2000068 0.1708 0.171 0 0 0 0 0 0 0 0 0 0 0 0
26 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.30001216 0.2672 0.1228 0 0 0 0 0 0 0 0 0 0 0 0
27 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.0499975 0.035 0.4285 0 0 0 0 0 0 0 0 0 0 0 0
28 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.10000115 0.0785 0.2739 0 0 0 0 0 0 0 0 0 0 0 0
29 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.1500032 0.128 0.1719 0 0 0 0 0 0 0 0 0 0 0 0
30 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.20000832 0.1752 0.1416 0 0 0 0 0 0 0 0 0 0 0 0
31 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.29999816 0.2728 0.0997 0 0 0 0 0 0 0 0 0 0 0 0
32 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.05010115 0.0355 0.4113 0 0 0 0 0 0 0 0 0 0 0 0
33 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.10000382 0.0826 0.2107 0 0 0 0 0 0 0 0 0 0 0 0
34 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.1499967 0.1305 0.1494 0 0 0 0 0 0 0 0 0 0 0 0
35 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.2000008 0.178 0.1236 0 0 0 0 0 0 0 0 0 0 0 0
36 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.05 0.04 0.25 0 0 0 0 0 0 0 0 0 0 0 0
37 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.10029675 0.0865 0.1595 0 0 0 0 0 0 0 0 0 0 0 0
38 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.15000153 0.1351 0.1103 0 0 0 0 0 0 0 0 0 0 0 0
39 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.20054418 0.1838 0.0911 0 0 0 0 0 0 0 0 0 0 0 0
40 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.29999441 0.2753 0.0897 0 0 0 0 0 0 0 0 0 0 0 0
41 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.29998992 0.2811 0.0672 0 0 0 0 0 0 0 0 0 0 0 0
42 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.10000029 0.0221 3.5249 0 0 0 0 0 0
43 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000025 0.0575 1.6087 0 0 0 0 0 0
44 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999582 0.1037 0.9286 0 0 0 0 0 0
45 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.25000596 0.1494 0.6734 0 0 0 0 0 0
46 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30000931 0.1997 0.5023 0 0 0 0 0 0
47 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.0500002 0.0106 3.717 0 0 0 0 0 0
48 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.09999641 0.0409 1.4449 0 0 0 0 0 0
49 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.14999806 0.0802 0.8703 0 0 0 0 0 0
50 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999448 0.1252 0.5974 0 0 0 0 0 0
51 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.29999394 0.2206 0.3599 0 0 0 0 0 0
52 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.04999904 0.0221 1.2624 0 0 0 0 0 0
53 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.09999996 0.0573 0.7452 0 0 0 0 0 0
54 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000096 0.0984 0.5244 0 0 0 0 0 0
55 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999616 0.1414 0.4144 0 0 0 0 0 0
56 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30001016 0.2369 0.2664 0 0 0 0 0 0
57 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.04799855 0.0313 0.5335 0 0 0 0 0 0
58 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.1000035 0.071 0.4085 0 0 0 0 0 0
59 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000453 0.1131 0.3263 0 0 0 0 0 0
60 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19980428 0.1586 0.2598 0 0 0 0 0 0
61 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30000123 0.2517 0.1919 0 0 0 0 0 0
62 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.04999962 0.0363 0.3774 0 0 0 0 0 0 0 0 0
63 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.09999712 0.0844 0.1848 0 0 0 0 0 0 0 0 0
64 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.1499944 0.1345 0.1152 0 0 0 0 0 0 0 0 0
65 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.19999665 0.1835 0.0899 0 0 0 0 0 0 0 0 0
66 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.24999486 0.2329 0.0734 0 0 0 0 0 0 0 0 0
67 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.29998637 0.2833 0.0589 0 0 0 0 0 0 0 0 0
68 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.0499991 0.0395 0.2658 0 0 0 0 0 0 0 0 0
69 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.10000231 0.0881 0.1351 0 0 0 0 0 0 0 0 0
70 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.15000091 0.1367 0.0973 0 0 0 0 0 0 0 0 0
71 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.20009536 0.1856 0.0781 0 0 0 0 0 0 0 0 0
72 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.40540686 0.3846 0.0541 0 0 0 0 0 0 0 0 0
73 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.09999756 0.0897 0.1148 0 0 0 0 0 0 0 0 0
74 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.15000544 0.1391 0.0784 0 0 0 0 0 0 0 0 0
75 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.19999343 0.1883 0.0621 0 0 0 0 0 0 0 0 0
76 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.29999853 0.2881 0.0413 0 0 0 0 0 0 0 0 0
77 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.05030076 0.0444 0.1329 0 0 0 0 0 0 0 0 0
78 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.09999639 0.0919 0.0881 0 0 0 0 0 0 0 0 0
79 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.15000408 0.1413 0.0616 0 0 0 0 0 0 0 0 0
80 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.20049903 0.1917 0.0459 0 0 0 0 0 0 0 0 0
81 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.29948604 0.2883 0.0388 0 0 0 0 0 0 0 0 0
82 Lyon (2016) 0.01 0.01 1 1 0.08666112 0.05352756 0.619 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
83 Lyon (2016) 0.05 0.05 1 1 0.08666112 0.060900295 0.423 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
84 Lyon (2016) 0.1 0.1 1 1 0.08666112 0.067916239 0.276 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
85 Lyon (2016) 0.3 0.3 1 1 0.08666112 0.084878668 0.021 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
86 Lyon (2016) 0.5 0.5 1 1 0.08666112 0.08666112 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
87 Lyon (2016) 0.01 0.01 1 1 0.042983916 0.015124531 1.842 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
88 Lyon (2016) 0.05 0.05 1 1 0.042983916 0.020410216 1.106 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
89 Lyon (2016) 0.1 0.1 1 1 0.042983916 0.026354332 0.631 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
90 Lyon (2016) 0.3 0.3 1 1 0.042983916 0.039290599 0.094 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
91 Lyon (2016) 0.5 0.5 1 1 0.042983916 0.042983916 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
92 Lyon (2016) 0.01 0.01 1 1 0.005546312 3.16E-05 174.668 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
93 Lyon (2016) 0.05 0.05 1 1 0.005546312 0.000451912 11.273 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
94 Lyon (2016) 0.1 0.1 1 1 0.005546312 0.001558828 2.558 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
95 Lyon (2016) 0.3 0.3 1 1 0.005546312 0.005400498 0.027 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
96 Lyon (2016) 0.5 0.5 1 1 0.005546312 0.005546312 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
97 Lee (2005) 0.251 0.25 1 1 0.1 0.087622932 0.141253754 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
98 Lee (2005) 0.251 0.25 1.5 1.5 0.1 0.07955199 0.257039578 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
99 Lee (2005) 0.251 0.25 2 2 0.1 0.074253556 0.34673685 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
100 Lee (2005) 0.251 0.25 2.5 2.5 0.1 0.071525275 0.398107171 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
101 Lee (2005) 0.251 0.25 3 3 0.1 0.066613942 0.501187234 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
102 Lee (2005) 0.134 0.13 1 1 0.1 0.075124079 0.331131121 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
103 Lee (2005) 0.0835 0.08 1 1 0.1 0.065582051 0.52480746 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
104 Lee (2005) 0.0285 0.03 1 1 0.1 0.059662917 0.676082975 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
105 Lee (2005) 0.262 0.26 2 2 0.1 0.079923999 0.251188643 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
106 Lee (2005) 0.134 0.13 2 2 0.1 0.061313682 0.630957344 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
107 Lee (2005) 0.0835 0.08 2 2 0.1 0.051151089 0.954992586 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
108 Lee (2005) 0.0285 0.03 2 2 0.1 0.044837645 1.230268771 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
109 Lee (2005) 0.0114 0.01 2 2 0.1 0.041450132 1.412537545 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
110 Lee (2005) 0.262 0.26 3 3 0.1 0.074253556 0.34673685 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
111 Lee (2005) 0.134 0.13 3 3 0.1 0.048273748 1.071519305 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
112 Lee (2005) 0.0835 0.08 3 3 0.1 0.040337083 1.479108388 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
113 Lee (2005) 0.0285 0.03 3 3 0.1 0.033900091 1.9498446 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
114 Lee (2005) 0.0114 0.01 3 3 0.1 0.030387123 2.290867653 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
115 Li (1987) 0.01 0.01 1 1 0.05000119 0.0239 1.0921 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
116 Li (1987) 0.01 0.01 1 1 0.09999803 0.0683 0.4641 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
117 Li (1987) 0.01 0.01 1 1 0.1500057 0.117 0.2821 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
118 Li (1987) 0.01 0.01 1 1 0.200004 0.168 0.1905 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
119 Li (1987) 0.01 0.01 1 1 0.30001149 0.2637 0.1377 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
120 Li (1987) 0.05 0.05 1 1 0.03453582 0.0201 0.7182 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
121 Li (1987) 0.05 0.05 1 1 0.09996185 0.0757 0.3205 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
122 Li (1987) 0.05 0.05 1 1 0.19999308 0.1722 0.1614 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
123 Li (1987) 0.1 0.1 1 1 0.04999817 0.0389 0.2853 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
124 Li (1987) 0.1 0.1 1 1 0.1499974 0.133 0.1278 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
125 Li (1987) 0.1 0.1 1 1 0.19999876 0.1807 0.1068 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
126 Li (1987) 0.1 0.1 1 1 0.2500032 0.232 0.0776 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
127 Li (1987) 0.1 0.1 1 1 0.30001216 0.2807 0.0688 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
128 Li (1987) 0.3 0.3 1 1 0.01996974 0.0189 0.0566 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
129 Li (1987) 0.3 0.3 1 1 0.04997968 0.0478 0.0456 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
130 Li (1987) 0.3 0.3 1 1 0.15000144 0.1464 0.0246 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
131 Li (1987) 0.3 0.3 1 1 0.29998765 0.2957 0.0145 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
132 Li (1987) 0.5 0.5 1 1 0.04999786 0.0482 0.0373 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
133 Li (1987) 0.5 0.5 1 1 0.10000096 0.0976 0.0246 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
134 Li (1987) 0.5 0.5 1 1 0.20000784 0.1968 0.0163 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
135 Lyon (2016) 0.03 0.03 1 1 0 0 0 0.09296866 0.06556323 0.418 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
136 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.09296866 0.066835844 0.391 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
137 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.09296866 0.080076365 0.161 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
138 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.09296866 0.091957131 0.011 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
139 Lyon (2016) 0.5 0.5 1 1 0 0 0 0.09296866 0.09296866 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
140 Lyon (2016) 0.03 0.03 1 1 0 0 0 0.047548856 0.02373882 1.003 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
141 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.047548856 0.025646632 0.854 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
142 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.047548856 0.034988121 0.359 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
143 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.047548856 0.045371046 0.048 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
144 Lyon (2016) 0.5 0.5 1 1 0 0 0 0.047548856 0.047548856 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
145 Lyon (2016) 0.01 0.01 1 1 0 0 0 0.00638716 5.54E-05 114.332 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
146 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.00638716 0.000669233 8.544 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
147 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.00638716 0.002264147 1.821 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
148 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.00638716 0.006323921 0.01 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
149 Lyon (2016) 0.5 0.5 1 1 0 0 0 0.00638716 0.00638716 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
150 Li (1987) 0.01 0.01 1 1 0 0 0 0.04999995 0.0259 0.9305 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
151 Li (1987) 0.01 0.01 1 1 0 0 0 0.09999925 0.0725 0.3793 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
152 Li (1987) 0.01 0.01 1 1 0 0 0 0.20000715 0.1673 0.1955 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
153 Li (1987) 0.01 0.01 1 1 0 0 0 0.29999192 0.2648 0.1329 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
154 Li (1987) 0.03 0.03 1 1 0 0 0 0.05000109 0.0307 0.6287 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
155 Li (1987) 0.03 0.03 1 1 0 0 0 0.10009624 0.0776 0.2899 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
156 Li (1987) 0.03 0.03 1 1 0 0 0 0.20000456 0.1736 0.1521 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
157 Li (1987) 0.03 0.03 1 1 0 0 0 0.2999997 0.273 0.0989 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
158 Li (1987) 0.05 0.05 1 1 0 0 0 0.05002915 0.0349 0.4335 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
159 Li (1987) 0.05 0.05 1 1 0 0 0 0.09997622 0.0809 0.2358 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
160 Li (1987) 0.05 0.05 1 1 0 0 0 0.14999553 0.1299 0.1547 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
161 Li (1987) 0.05 0.05 1 1 0 0 0 0.25001088 0.2272 0.1004 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
162 Li (1987) 0.07 0.07 1 1 0 0 0 0.04999995 0.0385 0.2987 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
163 Li (1987) 0.07 0.07 1 1 0 0 0 0.09999936 0.0864 0.1574 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
164 Li (1987) 0.07 0.07 1 1 0 0 0 0.14998624 0.1343 0.1168 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
165 Li (1987) 0.07 0.07 1 1 0 0 0 0.24999474 0.2334 0.0711 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
166 Li (1987) 0.1 0.1 1 1 0 0 0 0.0499992 0.0415 0.2048 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
167 Li (1987) 0.1 0.1 1 1 0 0 0 0.10000199 0.0901 0.1099 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
168 Li (1987) 0.1 0.1 1 1 0 0 0 0.1999998 0.189 0.0582 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
169 Li (1987) 0.1 0.1 1 1 0 0 0 0.30000544 0.2888 0.0388 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
170 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0500503 0.0115 3.3522 0 0 0
171 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0999792 0.048 1.0829 0 0 0
172 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1500016 0.0944 0.589 0 0 0
173 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.24999968 0.1864 0.3412 0 0 0
174 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30000263 0.2371 0.2653 0 0 0
175 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.05032248 0.0156 2.2258 0 0 0
176 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.10000216 0.0556 0.7986 0 0 0
177 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000255 0.1035 0.4493 0 0 0
178 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30392343 0.1997 0.5219 0 0 0
179 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30000411 0.2471 0.2141 0 0 0
180 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.04999989 0.0219 1.2831 0 0 0
181 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999773 0.0623 0.6051 0 0 0
182 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000375 0.1105 0.3575 0 0 0
183 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.2500038 0.2073 0.206 0 0 0
184 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30061536 0.2572 0.1688 0 0 0
185 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0502452 0.0408 0.2315 0 0 0
186 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999592 0.0842 0.1876 0 0 0
187 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.14999496 0.1334 0.1244 0 0 0
188 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1999935 0.1814 0.1025 0 0 0
189 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30001088 0.2782 0.0784 0 0 0
190 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1500005 0.047 2.1915
191 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999809 0.0857 1.3337
192 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.2999996 0.1772 0.693
193 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.05 0.016 2.125
194 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1000004 0.0445 1.2472
195 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000048 0.0828 0.8116
196 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999436 0.1214 0.6474
197 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.29999366 0.2083 0.4402
198 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.04999995 0.0333 0.5015
199 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999846 0.0694 0.4409
200 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000104 0.1108 0.3538
201 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999756 0.1526 0.3106
202 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.29999472 0.2416 0.2417
203 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.25000384 0.1984 0.2601
204 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0500013 0.0405 0.2346
205 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999854 0.0838 0.1933
206 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999977 0.1753 0.1409
207 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999804 0.0908 0.1013
208 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19992651 0.1851 0.0801
209 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30001335 0.2821 0.0635

@ -0,0 +1,210 @@
label,Feed H+[M],Feed H+[M].1,PC88A[M],PC88A[M].1,Feed Nd[M],Xaq Nd,D Nd,Feed Pr[M],Xaq Pr,D Pr,Feed Ce[M],Xaq Ce,D Ce,Feed La[M],Xaq La,D La,Feed Dy[M],Xaq Dy,D Dy,Feed Sm[M],Xaq Sm,D Sm,Feed Y[M],Xaq Y,D Y
Formiga (2016),0.316227766,0.316227766,1,1,0.038824182,0.036106489,0.075268817,0.011354951,0.010673654,0.063829787,0.104199378,0.102323789,0.018329939,0.046794403,0.046466843,0.007049345,0,0,0,0,0,0,0,0,0
Formiga (2016),0.1,0.1,1,1,0.038824182,0.023294509,0.666666667,0.011354951,0.007153619,0.587301587,0.104199378,0.087527477,0.19047619,0.046794403,0.044454683,0.052631579,0,0,0,0,0,0,0,0,0
Formiga (2016),0.01,0.01,1,1,0.038824182,0.011647255,2.333333333,0.011354951,0.003860683,1.941176471,0.104199378,0.065645608,0.587301587,0.046794403,0.040711131,0.149425287,0,0,0,0,0,0,0,0,0
Lyon (2016),0.02,0.02,1,1,0.048530227,0.029263727,0.658374793,0.04967791,0.035072604,0.416430595,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.048530227,0.032127011,0.510574018,0.04967791,0.037506822,0.324503311,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.048530227,0.039018303,0.243781095,0.04967791,0.043070748,0.153402537,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.048530227,0.046443428,0.044932079,0.04967791,0.048535318,0.023541453,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.259983361,0.197587354,0.315789474,0.088710553,0.071855548,0.234567901,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.259983361,0.207986689,0.25,0.088710553,0.07540397,0.176470588,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.259983361,0.21578619,0.204819277,0.088710553,0.077178181,0.149425287,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.259983361,0.244384359,0.063829787,0.088710553,0.08338792,0.063829787,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.017097653,0.33,0.008303308,0.006642646,0.25,0,0,0,0.054425491,0.050393973,0.08,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.013298174,0.71,0.008303308,0.005462702,0.52,0,0,0,0.054425491,0.048594188,0.12,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010932634,1.08,0.008303308,0.004537327,0.83,0,0,0,0.054425491,0.048164151,0.13,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.009396644,1.42,0.008303308,0.003972875,1.09,0,0,0,0.054425491,0.047326514,0.15,0,0,0,0,0,0,0,0,0
Liu (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.008209342,1.77,0.008303308,0.002997584,1.77,0,0,0,0.054425491,0.045735706,0.19,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.1,0.1,0.022739878,0.018928042,0.201385664,0.008303308,0.007354823,0.128960943,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.3,0.3,0.022739878,0.014333115,0.586527247,0.008303308,0.005999476,0.384005473,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.5,0.5,0.022739878,0.010952454,1.076235839,0.008303308,0.004805359,0.727926764,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.7,0.7,0.022739878,0.008786058,1.588177405,0.008303308,0.003974007,1.089404412,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Banda (2014),1.00E-05,1.00E-05,0.9,0.9,0.022739878,0.00700602,2.245762712,0.008303308,0.00322327,1.576050934,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.1,0.1,0.009359401,0.007999488,0.17,0.003371001,0.003064546,0.1,0.038539496,0.037783819,0.02,0.022461314,0.022020896,0.02,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.3,0.3,0.009359401,0.006881912,0.36,0.003371001,0.002763116,0.22,0.038539496,0.035357336,0.09,0.022461314,0.021597417,0.04,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.5,0.5,0.009359401,0.005813293,0.61,0.003371001,0.002340973,0.44,0.038539496,0.032386131,0.19,0.022461314,0.02060671,0.09,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,0.7,0.7,0.009359401,0.005638193,0.66,0.003371001,0.002147134,0.57,0.038539496,0.03034606,0.27,0.022461314,0.019877269,0.13,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,1,1,0.009359401,0.005005027,0.87,0.003371001,0.001862432,0.81,0.038539496,0.028547775,0.35,0.022461314,0.019702907,0.14,0,0,0,0,0,0,0,0,0
Kim (2012),0.01023293,0.01023293,2,2,0.009359401,0.003109436,2.01,0.003371001,0.001404584,1.4,0.038539496,0.021059834,0.83,0.022461314,0.018261231,0.23,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.0508008,0.0305,0.6656,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.09999878,0.0763,0.3106,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.15009456,0.1232,0.2183,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.2000068,0.1708,0.171,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0.30001216,0.2672,0.1228,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.0499975,0.035,0.4285,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.10000115,0.0785,0.2739,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.1500032,0.128,0.1719,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.20000832,0.1752,0.1416,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0.29999816,0.2728,0.0997,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.05010115,0.0355,0.4113,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.10000382,0.0826,0.2107,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.1499967,0.1305,0.1494,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0.2000008,0.178,0.1236,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.05,0.04,0.25,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.10029675,0.0865,0.1595,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.15000153,0.1351,0.1103,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.20054418,0.1838,0.0911,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.29999441,0.2753,0.0897,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0,0,0,0.29998992,0.2811,0.0672,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.10000029,0.0221,3.5249,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000025,0.0575,1.6087,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999582,0.1037,0.9286,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.25000596,0.1494,0.6734,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30000931,0.1997,0.5023,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.0500002,0.0106,3.717,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.09999641,0.0409,1.4449,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.14999806,0.0802,0.8703,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999448,0.1252,0.5974,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.29999394,0.2206,0.3599,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.04999904,0.0221,1.2624,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.09999996,0.0573,0.7452,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000096,0.0984,0.5244,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19999616,0.1414,0.4144,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30001016,0.2369,0.2664,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.04799855,0.0313,0.5335,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.1000035,0.071,0.4085,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.15000453,0.1131,0.3263,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.19980428,0.1586,0.2598,0,0,0,0,0,0
Li (1987),0.7,0.7,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0.30000123,0.2517,0.1919,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.04999962,0.0363,0.3774,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.09999712,0.0844,0.1848,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.1499944,0.1345,0.1152,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.19999665,0.1835,0.0899,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.24999486,0.2329,0.0734,0,0,0,0,0,0,0,0,0
Li (1987),0.0001,0.0001,1,1,0,0,0,0,0,0,0,0,0,0.29998637,0.2833,0.0589,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.0499991,0.0395,0.2658,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.10000231,0.0881,0.1351,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.15000091,0.1367,0.0973,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.20009536,0.1856,0.0781,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0.40540686,0.3846,0.0541,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.09999756,0.0897,0.1148,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.15000544,0.1391,0.0784,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.19999343,0.1883,0.0621,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0,0,0,0,0,0,0.29999853,0.2881,0.0413,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.05030076,0.0444,0.1329,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.09999639,0.0919,0.0881,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.15000408,0.1413,0.0616,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.20049903,0.1917,0.0459,0,0,0,0,0,0,0,0,0
Li (1987),0.04,0.04,1,1,0,0,0,0,0,0,0,0,0,0.29948604,0.2883,0.0388,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.08666112,0.05352756,0.619,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.08666112,0.060900295,0.423,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.08666112,0.067916239,0.276,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.08666112,0.084878668,0.021,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.042983916,0.015124531,1.842,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.042983916,0.020410216,1.106,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.042983916,0.026354332,0.631,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.042983916,0.039290599,0.094,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0.005546312,3.16E-05,174.668,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0.005546312,0.000451912,11.273,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0.005546312,0.001558828,2.558,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0.005546312,0.005400498,0.027,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,1,1,0.1,0.087622932,0.141253754,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,1.5,1.5,0.1,0.07955199,0.257039578,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,2,2,0.1,0.074253556,0.34673685,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,2.5,2.5,0.1,0.071525275,0.398107171,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.251,0.25,3,3,0.1,0.066613942,0.501187234,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,1,1,0.1,0.075124079,0.331131121,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,1,1,0.1,0.065582051,0.52480746,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,1,1,0.1,0.059662917,0.676082975,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.262,0.26,2,2,0.1,0.079923999,0.251188643,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,2,2,0.1,0.061313682,0.630957344,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,2,2,0.1,0.051151089,0.954992586,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,2,2,0.1,0.044837645,1.230268771,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0114,0.01,2,2,0.1,0.041450132,1.412537545,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.262,0.26,3,3,0.1,0.074253556,0.34673685,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.134,0.13,3,3,0.1,0.048273748,1.071519305,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0835,0.08,3,3,0.1,0.040337083,1.479108388,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0285,0.03,3,3,0.1,0.033900091,1.9498446,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lee (2005),0.0114,0.01,3,3,0.1,0.030387123,2.290867653,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.05000119,0.0239,1.0921,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.09999803,0.0683,0.4641,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.1500057,0.117,0.2821,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.200004,0.168,0.1905,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0.30001149,0.2637,0.1377,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.03453582,0.0201,0.7182,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.09996185,0.0757,0.3205,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0.19999308,0.1722,0.1614,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.04999817,0.0389,0.2853,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.1499974,0.133,0.1278,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.19999876,0.1807,0.1068,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.2500032,0.232,0.0776,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0.30001216,0.2807,0.0688,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.01996974,0.0189,0.0566,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.04997968,0.0478,0.0456,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.15000144,0.1464,0.0246,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.3,0.3,1,1,0.29998765,0.2957,0.0145,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.04999786,0.0482,0.0373,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.10000096,0.0976,0.0246,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.5,0.5,1,1,0.20000784,0.1968,0.0163,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.03,0.03,1,1,0,0,0,0.09296866,0.06556323,0.418,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.09296866,0.066835844,0.391,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.09296866,0.080076365,0.161,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.09296866,0.091957131,0.011,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.03,0.03,1,1,0,0,0,0.047548856,0.02373882,1.003,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.047548856,0.025646632,0.854,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.047548856,0.034988121,0.359,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.047548856,0.045371046,0.048,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.01,0.01,1,1,0,0,0,0.00638716,5.54E-05,114.332,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.05,0.05,1,1,0,0,0,0.00638716,0.000669233,8.544,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.1,0.1,1,1,0,0,0,0.00638716,0.002264147,1.821,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Lyon (2016),0.3,0.3,1,1,0,0,0,0.00638716,0.006323921,0.01,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.04999995,0.0259,0.9305,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.09999925,0.0725,0.3793,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.20000715,0.1673,0.1955,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0.29999192,0.2648,0.1329,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.05000109,0.0307,0.6287,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.10009624,0.0776,0.2899,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.20000456,0.1736,0.1521,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.03,0.03,1,1,0,0,0,0.2999997,0.273,0.0989,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.05002915,0.0349,0.4335,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.09997622,0.0809,0.2358,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.14999553,0.1299,0.1547,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0.25001088,0.2272,0.1004,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.04999995,0.0385,0.2987,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.09999936,0.0864,0.1574,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.14998624,0.1343,0.1168,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.07,0.07,1,1,0,0,0,0.24999474,0.2334,0.0711,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.0499992,0.0415,0.2048,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.10000199,0.0901,0.1099,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.1999998,0.189,0.0582,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0.30000544,0.2888,0.0388,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0500503,0.0115,3.3522,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0999792,0.048,1.0829,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1500016,0.0944,0.589,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.24999968,0.1864,0.3412,0,0,0
Li (1987),0.01,0.01,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30000263,0.2371,0.2653,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.05032248,0.0156,2.2258,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.10000216,0.0556,0.7986,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000255,0.1035,0.4493,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30392343,0.1997,0.5219,0,0,0
Li (1987),0.05,0.05,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30000411,0.2471,0.2141,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.04999989,0.0219,1.2831,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999773,0.0623,0.6051,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000375,0.1105,0.3575,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.2500038,0.2073,0.206,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30061536,0.2572,0.1688,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0502452,0.0408,0.2315,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999592,0.0842,0.1876,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.14999496,0.1334,0.1244,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1999935,0.1814,0.1025,0,0,0
Li (1987),0.3,0.3,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30001088,0.2782,0.0784,0,0,0
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1500005,0.047,2.1915
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999809,0.0857,1.3337
Li (1987),0.1,0.1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.2999996,0.1772,0.693
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.05,0.016,2.125
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.1000004,0.0445,1.2472
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000048,0.0828,0.8116
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999436,0.1214,0.6474
Li (1987),0.5,0.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.29999366,0.2083,0.4402
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.04999995,0.0333,0.5015
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999846,0.0694,0.4409
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.15000104,0.1108,0.3538
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999756,0.1526,0.3106
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.29999472,0.2416,0.2417
Li (1987),1,1,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.25000384,0.1984,0.2601
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.0500013,0.0405,0.2346
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999854,0.0838,0.1933
Li (1987),1.5,1.5,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19999977,0.1753,0.1409
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.09999804,0.0908,0.1013
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.19992651,0.1851,0.0801
Li (1987),2,2,1,1,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0,0.30001335,0.2821,0.0635
1 label Feed H+[M] Feed H+[M].1 PC88A[M] PC88A[M].1 Feed Nd[M] Xaq Nd D Nd Feed Pr[M] Xaq Pr D Pr Feed Ce[M] Xaq Ce D Ce Feed La[M] Xaq La D La Feed Dy[M] Xaq Dy D Dy Feed Sm[M] Xaq Sm D Sm Feed Y[M] Xaq Y D Y
2 Formiga (2016) 0.316227766 0.316227766 1 1 0.038824182 0.036106489 0.075268817 0.011354951 0.010673654 0.063829787 0.104199378 0.102323789 0.018329939 0.046794403 0.046466843 0.007049345 0 0 0 0 0 0 0 0 0
3 Formiga (2016) 0.1 0.1 1 1 0.038824182 0.023294509 0.666666667 0.011354951 0.007153619 0.587301587 0.104199378 0.087527477 0.19047619 0.046794403 0.044454683 0.052631579 0 0 0 0 0 0 0 0 0
4 Formiga (2016) 0.01 0.01 1 1 0.038824182 0.011647255 2.333333333 0.011354951 0.003860683 1.941176471 0.104199378 0.065645608 0.587301587 0.046794403 0.040711131 0.149425287 0 0 0 0 0 0 0 0 0
5 Lyon (2016) 0.02 0.02 1 1 0.048530227 0.029263727 0.658374793 0.04967791 0.035072604 0.416430595 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
6 Lyon (2016) 0.05 0.05 1 1 0.048530227 0.032127011 0.510574018 0.04967791 0.037506822 0.324503311 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
7 Lyon (2016) 0.1 0.1 1 1 0.048530227 0.039018303 0.243781095 0.04967791 0.043070748 0.153402537 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
8 Lyon (2016) 0.3 0.3 1 1 0.048530227 0.046443428 0.044932079 0.04967791 0.048535318 0.023541453 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
9 Lyon (2016) 0.01 0.01 1 1 0.259983361 0.197587354 0.315789474 0.088710553 0.071855548 0.234567901 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
10 Lyon (2016) 0.05 0.05 1 1 0.259983361 0.207986689 0.25 0.088710553 0.07540397 0.176470588 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
11 Lyon (2016) 0.1 0.1 1 1 0.259983361 0.21578619 0.204819277 0.088710553 0.077178181 0.149425287 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
12 Lyon (2016) 0.3 0.3 1 1 0.259983361 0.244384359 0.063829787 0.088710553 0.08338792 0.063829787 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
13 Liu (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.017097653 0.33 0.008303308 0.006642646 0.25 0 0 0 0.054425491 0.050393973 0.08 0 0 0 0 0 0 0 0 0
14 Liu (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.013298174 0.71 0.008303308 0.005462702 0.52 0 0 0 0.054425491 0.048594188 0.12 0 0 0 0 0 0 0 0 0
15 Liu (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010932634 1.08 0.008303308 0.004537327 0.83 0 0 0 0.054425491 0.048164151 0.13 0 0 0 0 0 0 0 0 0
16 Liu (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.009396644 1.42 0.008303308 0.003972875 1.09 0 0 0 0.054425491 0.047326514 0.15 0 0 0 0 0 0 0 0 0
17 Liu (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.008209342 1.77 0.008303308 0.002997584 1.77 0 0 0 0.054425491 0.045735706 0.19 0 0 0 0 0 0 0 0 0
18 Banda (2014) 1.00E-05 1.00E-05 0.1 0.1 0.022739878 0.018928042 0.201385664 0.008303308 0.007354823 0.128960943 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
19 Banda (2014) 1.00E-05 1.00E-05 0.3 0.3 0.022739878 0.014333115 0.586527247 0.008303308 0.005999476 0.384005473 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
20 Banda (2014) 1.00E-05 1.00E-05 0.5 0.5 0.022739878 0.010952454 1.076235839 0.008303308 0.004805359 0.727926764 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
21 Banda (2014) 1.00E-05 1.00E-05 0.7 0.7 0.022739878 0.008786058 1.588177405 0.008303308 0.003974007 1.089404412 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
22 Banda (2014) 1.00E-05 1.00E-05 0.9 0.9 0.022739878 0.00700602 2.245762712 0.008303308 0.00322327 1.576050934 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
23 Kim (2012) 0.01023293 0.01023293 0.1 0.1 0.009359401 0.007999488 0.17 0.003371001 0.003064546 0.1 0.038539496 0.037783819 0.02 0.022461314 0.022020896 0.02 0 0 0 0 0 0 0 0 0
24 Kim (2012) 0.01023293 0.01023293 0.3 0.3 0.009359401 0.006881912 0.36 0.003371001 0.002763116 0.22 0.038539496 0.035357336 0.09 0.022461314 0.021597417 0.04 0 0 0 0 0 0 0 0 0
25 Kim (2012) 0.01023293 0.01023293 0.5 0.5 0.009359401 0.005813293 0.61 0.003371001 0.002340973 0.44 0.038539496 0.032386131 0.19 0.022461314 0.02060671 0.09 0 0 0 0 0 0 0 0 0
26 Kim (2012) 0.01023293 0.01023293 0.7 0.7 0.009359401 0.005638193 0.66 0.003371001 0.002147134 0.57 0.038539496 0.03034606 0.27 0.022461314 0.019877269 0.13 0 0 0 0 0 0 0 0 0
27 Kim (2012) 0.01023293 0.01023293 1 1 0.009359401 0.005005027 0.87 0.003371001 0.001862432 0.81 0.038539496 0.028547775 0.35 0.022461314 0.019702907 0.14 0 0 0 0 0 0 0 0 0
28 Kim (2012) 0.01023293 0.01023293 2 2 0.009359401 0.003109436 2.01 0.003371001 0.001404584 1.4 0.038539496 0.021059834 0.83 0.022461314 0.018261231 0.23 0 0 0 0 0 0 0 0 0
29 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.0508008 0.0305 0.6656 0 0 0 0 0 0 0 0 0 0 0 0
30 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.09999878 0.0763 0.3106 0 0 0 0 0 0 0 0 0 0 0 0
31 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.15009456 0.1232 0.2183 0 0 0 0 0 0 0 0 0 0 0 0
32 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.2000068 0.1708 0.171 0 0 0 0 0 0 0 0 0 0 0 0
33 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0.30001216 0.2672 0.1228 0 0 0 0 0 0 0 0 0 0 0 0
34 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.0499975 0.035 0.4285 0 0 0 0 0 0 0 0 0 0 0 0
35 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.10000115 0.0785 0.2739 0 0 0 0 0 0 0 0 0 0 0 0
36 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.1500032 0.128 0.1719 0 0 0 0 0 0 0 0 0 0 0 0
37 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.20000832 0.1752 0.1416 0 0 0 0 0 0 0 0 0 0 0 0
38 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0.29999816 0.2728 0.0997 0 0 0 0 0 0 0 0 0 0 0 0
39 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.05010115 0.0355 0.4113 0 0 0 0 0 0 0 0 0 0 0 0
40 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.10000382 0.0826 0.2107 0 0 0 0 0 0 0 0 0 0 0 0
41 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.1499967 0.1305 0.1494 0 0 0 0 0 0 0 0 0 0 0 0
42 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0.2000008 0.178 0.1236 0 0 0 0 0 0 0 0 0 0 0 0
43 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.05 0.04 0.25 0 0 0 0 0 0 0 0 0 0 0 0
44 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.10029675 0.0865 0.1595 0 0 0 0 0 0 0 0 0 0 0 0
45 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.15000153 0.1351 0.1103 0 0 0 0 0 0 0 0 0 0 0 0
46 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.20054418 0.1838 0.0911 0 0 0 0 0 0 0 0 0 0 0 0
47 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.29999441 0.2753 0.0897 0 0 0 0 0 0 0 0 0 0 0 0
48 Li (1987) 0.07 0.07 1 1 0 0 0 0 0 0 0.29998992 0.2811 0.0672 0 0 0 0 0 0 0 0 0 0 0 0
49 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.10000029 0.0221 3.5249 0 0 0 0 0 0
50 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000025 0.0575 1.6087 0 0 0 0 0 0
51 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999582 0.1037 0.9286 0 0 0 0 0 0
52 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.25000596 0.1494 0.6734 0 0 0 0 0 0
53 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30000931 0.1997 0.5023 0 0 0 0 0 0
54 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.0500002 0.0106 3.717 0 0 0 0 0 0
55 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.09999641 0.0409 1.4449 0 0 0 0 0 0
56 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.14999806 0.0802 0.8703 0 0 0 0 0 0
57 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999448 0.1252 0.5974 0 0 0 0 0 0
58 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.29999394 0.2206 0.3599 0 0 0 0 0 0
59 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.04999904 0.0221 1.2624 0 0 0 0 0 0
60 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.09999996 0.0573 0.7452 0 0 0 0 0 0
61 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000096 0.0984 0.5244 0 0 0 0 0 0
62 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19999616 0.1414 0.4144 0 0 0 0 0 0
63 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30001016 0.2369 0.2664 0 0 0 0 0 0
64 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.04799855 0.0313 0.5335 0 0 0 0 0 0
65 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.1000035 0.071 0.4085 0 0 0 0 0 0
66 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.15000453 0.1131 0.3263 0 0 0 0 0 0
67 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.19980428 0.1586 0.2598 0 0 0 0 0 0
68 Li (1987) 0.7 0.7 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0.30000123 0.2517 0.1919 0 0 0 0 0 0
69 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.04999962 0.0363 0.3774 0 0 0 0 0 0 0 0 0
70 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.09999712 0.0844 0.1848 0 0 0 0 0 0 0 0 0
71 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.1499944 0.1345 0.1152 0 0 0 0 0 0 0 0 0
72 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.19999665 0.1835 0.0899 0 0 0 0 0 0 0 0 0
73 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.24999486 0.2329 0.0734 0 0 0 0 0 0 0 0 0
74 Li (1987) 0.0001 0.0001 1 1 0 0 0 0 0 0 0 0 0 0.29998637 0.2833 0.0589 0 0 0 0 0 0 0 0 0
75 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.0499991 0.0395 0.2658 0 0 0 0 0 0 0 0 0
76 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.10000231 0.0881 0.1351 0 0 0 0 0 0 0 0 0
77 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.15000091 0.1367 0.0973 0 0 0 0 0 0 0 0 0
78 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.20009536 0.1856 0.0781 0 0 0 0 0 0 0 0 0
79 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0.40540686 0.3846 0.0541 0 0 0 0 0 0 0 0 0
80 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.09999756 0.0897 0.1148 0 0 0 0 0 0 0 0 0
81 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.15000544 0.1391 0.0784 0 0 0 0 0 0 0 0 0
82 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.19999343 0.1883 0.0621 0 0 0 0 0 0 0 0 0
83 Li (1987) 0.03 0.03 1 1 0 0 0 0 0 0 0 0 0 0.29999853 0.2881 0.0413 0 0 0 0 0 0 0 0 0
84 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.05030076 0.0444 0.1329 0 0 0 0 0 0 0 0 0
85 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.09999639 0.0919 0.0881 0 0 0 0 0 0 0 0 0
86 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.15000408 0.1413 0.0616 0 0 0 0 0 0 0 0 0
87 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.20049903 0.1917 0.0459 0 0 0 0 0 0 0 0 0
88 Li (1987) 0.04 0.04 1 1 0 0 0 0 0 0 0 0 0 0.29948604 0.2883 0.0388 0 0 0 0 0 0 0 0 0
89 Lyon (2016) 0.01 0.01 1 1 0.08666112 0.05352756 0.619 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
90 Lyon (2016) 0.05 0.05 1 1 0.08666112 0.060900295 0.423 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
91 Lyon (2016) 0.1 0.1 1 1 0.08666112 0.067916239 0.276 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
92 Lyon (2016) 0.3 0.3 1 1 0.08666112 0.084878668 0.021 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
93 Lyon (2016) 0.01 0.01 1 1 0.042983916 0.015124531 1.842 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
94 Lyon (2016) 0.05 0.05 1 1 0.042983916 0.020410216 1.106 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
95 Lyon (2016) 0.1 0.1 1 1 0.042983916 0.026354332 0.631 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
96 Lyon (2016) 0.3 0.3 1 1 0.042983916 0.039290599 0.094 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
97 Lyon (2016) 0.01 0.01 1 1 0.005546312 3.16E-05 174.668 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
98 Lyon (2016) 0.05 0.05 1 1 0.005546312 0.000451912 11.273 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
99 Lyon (2016) 0.1 0.1 1 1 0.005546312 0.001558828 2.558 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
100 Lyon (2016) 0.3 0.3 1 1 0.005546312 0.005400498 0.027 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
101 Lee (2005) 0.251 0.25 1 1 0.1 0.087622932 0.141253754 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
102 Lee (2005) 0.251 0.25 1.5 1.5 0.1 0.07955199 0.257039578 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
103 Lee (2005) 0.251 0.25 2 2 0.1 0.074253556 0.34673685 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
104 Lee (2005) 0.251 0.25 2.5 2.5 0.1 0.071525275 0.398107171 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
105 Lee (2005) 0.251 0.25 3 3 0.1 0.066613942 0.501187234 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
106 Lee (2005) 0.134 0.13 1 1 0.1 0.075124079 0.331131121 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
107 Lee (2005) 0.0835 0.08 1 1 0.1 0.065582051 0.52480746 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
108 Lee (2005) 0.0285 0.03 1 1 0.1 0.059662917 0.676082975 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
109 Lee (2005) 0.262 0.26 2 2 0.1 0.079923999 0.251188643 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
110 Lee (2005) 0.134 0.13 2 2 0.1 0.061313682 0.630957344 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
111 Lee (2005) 0.0835 0.08 2 2 0.1 0.051151089 0.954992586 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
112 Lee (2005) 0.0285 0.03 2 2 0.1 0.044837645 1.230268771 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
113 Lee (2005) 0.0114 0.01 2 2 0.1 0.041450132 1.412537545 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
114 Lee (2005) 0.262 0.26 3 3 0.1 0.074253556 0.34673685 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
115 Lee (2005) 0.134 0.13 3 3 0.1 0.048273748 1.071519305 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
116 Lee (2005) 0.0835 0.08 3 3 0.1 0.040337083 1.479108388 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
117 Lee (2005) 0.0285 0.03 3 3 0.1 0.033900091 1.9498446 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
118 Lee (2005) 0.0114 0.01 3 3 0.1 0.030387123 2.290867653 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
119 Li (1987) 0.01 0.01 1 1 0.05000119 0.0239 1.0921 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
120 Li (1987) 0.01 0.01 1 1 0.09999803 0.0683 0.4641 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
121 Li (1987) 0.01 0.01 1 1 0.1500057 0.117 0.2821 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
122 Li (1987) 0.01 0.01 1 1 0.200004 0.168 0.1905 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
123 Li (1987) 0.01 0.01 1 1 0.30001149 0.2637 0.1377 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
124 Li (1987) 0.05 0.05 1 1 0.03453582 0.0201 0.7182 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
125 Li (1987) 0.05 0.05 1 1 0.09996185 0.0757 0.3205 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
126 Li (1987) 0.05 0.05 1 1 0.19999308 0.1722 0.1614 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
127 Li (1987) 0.1 0.1 1 1 0.04999817 0.0389 0.2853 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
128 Li (1987) 0.1 0.1 1 1 0.1499974 0.133 0.1278 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
129 Li (1987) 0.1 0.1 1 1 0.19999876 0.1807 0.1068 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
130 Li (1987) 0.1 0.1 1 1 0.2500032 0.232 0.0776 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
131 Li (1987) 0.1 0.1 1 1 0.30001216 0.2807 0.0688 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
132 Li (1987) 0.3 0.3 1 1 0.01996974 0.0189 0.0566 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
133 Li (1987) 0.3 0.3 1 1 0.04997968 0.0478 0.0456 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
134 Li (1987) 0.3 0.3 1 1 0.15000144 0.1464 0.0246 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
135 Li (1987) 0.3 0.3 1 1 0.29998765 0.2957 0.0145 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
136 Li (1987) 0.5 0.5 1 1 0.04999786 0.0482 0.0373 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
137 Li (1987) 0.5 0.5 1 1 0.10000096 0.0976 0.0246 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
138 Li (1987) 0.5 0.5 1 1 0.20000784 0.1968 0.0163 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
139 Lyon (2016) 0.03 0.03 1 1 0 0 0 0.09296866 0.06556323 0.418 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
140 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.09296866 0.066835844 0.391 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
141 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.09296866 0.080076365 0.161 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
142 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.09296866 0.091957131 0.011 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
143 Lyon (2016) 0.03 0.03 1 1 0 0 0 0.047548856 0.02373882 1.003 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
144 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.047548856 0.025646632 0.854 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
145 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.047548856 0.034988121 0.359 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
146 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.047548856 0.045371046 0.048 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
147 Lyon (2016) 0.01 0.01 1 1 0 0 0 0.00638716 5.54E-05 114.332 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
148 Lyon (2016) 0.05 0.05 1 1 0 0 0 0.00638716 0.000669233 8.544 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
149 Lyon (2016) 0.1 0.1 1 1 0 0 0 0.00638716 0.002264147 1.821 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
150 Lyon (2016) 0.3 0.3 1 1 0 0 0 0.00638716 0.006323921 0.01 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
151 Li (1987) 0.01 0.01 1 1 0 0 0 0.04999995 0.0259 0.9305 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
152 Li (1987) 0.01 0.01 1 1 0 0 0 0.09999925 0.0725 0.3793 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
153 Li (1987) 0.01 0.01 1 1 0 0 0 0.20000715 0.1673 0.1955 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
154 Li (1987) 0.01 0.01 1 1 0 0 0 0.29999192 0.2648 0.1329 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
155 Li (1987) 0.03 0.03 1 1 0 0 0 0.05000109 0.0307 0.6287 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
156 Li (1987) 0.03 0.03 1 1 0 0 0 0.10009624 0.0776 0.2899 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
157 Li (1987) 0.03 0.03 1 1 0 0 0 0.20000456 0.1736 0.1521 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
158 Li (1987) 0.03 0.03 1 1 0 0 0 0.2999997 0.273 0.0989 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
159 Li (1987) 0.05 0.05 1 1 0 0 0 0.05002915 0.0349 0.4335 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
160 Li (1987) 0.05 0.05 1 1 0 0 0 0.09997622 0.0809 0.2358 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
161 Li (1987) 0.05 0.05 1 1 0 0 0 0.14999553 0.1299 0.1547 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
162 Li (1987) 0.05 0.05 1 1 0 0 0 0.25001088 0.2272 0.1004 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
163 Li (1987) 0.07 0.07 1 1 0 0 0 0.04999995 0.0385 0.2987 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
164 Li (1987) 0.07 0.07 1 1 0 0 0 0.09999936 0.0864 0.1574 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
165 Li (1987) 0.07 0.07 1 1 0 0 0 0.14998624 0.1343 0.1168 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
166 Li (1987) 0.07 0.07 1 1 0 0 0 0.24999474 0.2334 0.0711 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
167 Li (1987) 0.1 0.1 1 1 0 0 0 0.0499992 0.0415 0.2048 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
168 Li (1987) 0.1 0.1 1 1 0 0 0 0.10000199 0.0901 0.1099 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
169 Li (1987) 0.1 0.1 1 1 0 0 0 0.1999998 0.189 0.0582 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
170 Li (1987) 0.1 0.1 1 1 0 0 0 0.30000544 0.2888 0.0388 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0
171 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0500503 0.0115 3.3522 0 0 0
172 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0999792 0.048 1.0829 0 0 0
173 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1500016 0.0944 0.589 0 0 0
174 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.24999968 0.1864 0.3412 0 0 0
175 Li (1987) 0.01 0.01 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30000263 0.2371 0.2653 0 0 0
176 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.05032248 0.0156 2.2258 0 0 0
177 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.10000216 0.0556 0.7986 0 0 0
178 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000255 0.1035 0.4493 0 0 0
179 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30392343 0.1997 0.5219 0 0 0
180 Li (1987) 0.05 0.05 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30000411 0.2471 0.2141 0 0 0
181 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.04999989 0.0219 1.2831 0 0 0
182 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999773 0.0623 0.6051 0 0 0
183 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000375 0.1105 0.3575 0 0 0
184 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.2500038 0.2073 0.206 0 0 0
185 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30061536 0.2572 0.1688 0 0 0
186 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0502452 0.0408 0.2315 0 0 0
187 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999592 0.0842 0.1876 0 0 0
188 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.14999496 0.1334 0.1244 0 0 0
189 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1999935 0.1814 0.1025 0 0 0
190 Li (1987) 0.3 0.3 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30001088 0.2782 0.0784 0 0 0
191 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1500005 0.047 2.1915
192 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999809 0.0857 1.3337
193 Li (1987) 0.1 0.1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.2999996 0.1772 0.693
194 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.05 0.016 2.125
195 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.1000004 0.0445 1.2472
196 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000048 0.0828 0.8116
197 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999436 0.1214 0.6474
198 Li (1987) 0.5 0.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.29999366 0.2083 0.4402
199 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.04999995 0.0333 0.5015
200 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999846 0.0694 0.4409
201 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.15000104 0.1108 0.3538
202 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999756 0.1526 0.3106
203 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.29999472 0.2416 0.2417
204 Li (1987) 1 1 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.25000384 0.1984 0.2601
205 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.0500013 0.0405 0.2346
206 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999854 0.0838 0.1933
207 Li (1987) 1.5 1.5 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19999977 0.1753 0.1409
208 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.09999804 0.0908 0.1013
209 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.19992651 0.1851 0.0801
210 Li (1987) 2 2 1 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0.30001335 0.2821 0.0635

@ -0,0 +1,8 @@
,species,slope,intercept
0,Nd,3.000419727896623,-795340.4205623841
1,Pr,2.9947634514300585,-812098.2612992612
2,Ce,2.9999638712218615,-797736.0628337285
3,La,2.999891115669218,-796947.1165858557
4,Dy,3.0047799810800417,-797942.4465453301
5,Sm,3.004641443857438,-788584.0264811738
6,Y,3.0034812142034917,-808803.511500664
1 species slope intercept
2 0 Nd 3.000419727896623 -795340.4205623841
3 1 Pr 2.9947634514300585 -812098.2612992612
4 2 Ce 2.9999638712218615 -797736.0628337285
5 3 La 2.999891115669218 -796947.1165858557
6 4 Dy 3.0047799810800417 -797942.4465453301
7 5 Sm 3.004641443857438 -788584.0264811738
8 6 Y 3.0034812142034917 -808803.511500664

@ -0,0 +1 @@
{"(HA)2(org)_h0": {"upper_element_name": "species", "upper_attrib_name": "name", "upper_attrib_value": "(HA)2(org)", "lower_element_name": "h0", "lower_attrib_name": null, "lower_attrib_value": null, "input_format": "{0}", "input_value": -1376877.1544988335}}

File diff suppressed because one or more lines are too long

@ -0,0 +1,324 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Ce dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Ce(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:10 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Ce(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Ce:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:10 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Ce+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H Ce C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,338 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Ce dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Ce(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:15 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Ce(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Ce:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:15 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Ce+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Ce+++">
<beta0 updated="Updated at 16:15 7-31-2020"> 0.6005, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:15 7-31-2020"> 4.91, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:15 7-31-2020"> -0.026189999999999998, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H Ce C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,481 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Dy(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:11 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Dy(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Dy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:11 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Dy+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,495 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Dy(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:18 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Dy(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Dy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:18 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Dy+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Dy+++">
<beta0 updated="Updated at 16:18 7-31-2020"> 0.6129, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:18 7-31-2020"> 5.359, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:18 7-31-2020"> -0.0197, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,324 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P La dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane La(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:10 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="La(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 La:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:10 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- La+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H La C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,339 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P La dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane La(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:16 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="La(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 La:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:16 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- La+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="La+++">
<beta0 updated="Updated at 16:16 7-31-2020"> 0.593, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:16 7-31-2020"> 5.277, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:16 7-31-2020"> -0.02434, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H La C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,325 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:8 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:8 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H Nd C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,606 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org) Pr(H(A)2)3(org) Ce(H(A)2)3(org) La(H(A)2)3(org) Dy(H(A)2)3(org) Sm(H(A)2)3(org) Y(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-1059541.4005512903</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.320974226079</molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-3978649.6160132056</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.973500071223</molarVolume>
</standardState>
</species>
<species name="Pr(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Pr:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-3985038.4367615725</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.979936421078</molarVolume>
</standardState>
</species>
<species name="Ce(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Ce:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-3978119.7710579354</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">1.0060487218</molarVolume>
</standardState>
</species>
<species name="La(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 La:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-3977135.4681356866</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.981485801577</molarVolume>
</standardState>
</species>
<species name="Dy(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Dy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-3985847.427512692</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.961666360676</molarVolume>
</standardState>
</species>
<species name="Y(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Y:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-4001903.249479101</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.958888814485</molarVolume>
</standardState>
</species>
<species name="Sm(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Sm:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 12:9 7-31-2020">-3976184.3569597593</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.9642 </molarVolume>
</standardState>
</species>
<species name="Gd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Gd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="yep">-4829446.858</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume>0.9642</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++ Pr+++ Ce+++ La+++ Dy+++ Sm+++ Y+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,716 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org) Pr(H(A)2)3(org) Ce(H(A)2)3(org) La(H(A)2)3(org) Dy(H(A)2)3(org) Sm(H(A)2)3(org) Y(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-1376877.1544988335</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.320974226079</molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-4926549.797810851</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.973500071223</molarVolume>
</standardState>
</species>
<species name="Pr(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Pr:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-4935519.640701385</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.979936421078</molarVolume>
</standardState>
</species>
<species name="Ce(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Ce:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-4928317.781440989</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">1.0060487218</molarVolume>
</standardState>
</species>
<species name="La(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 La:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-4927428.65973482</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.981485801577</molarVolume>
</standardState>
</species>
<species name="Dy(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Dy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-4935155.356789877</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.961666360676</molarVolume>
</standardState>
</species>
<species name="Y(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Y:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-4944228.17930387</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.958888814485</molarVolume>
</standardState>
</species>
<species name="Sm(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Sm:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:32 7-31-2020">-4925606.187988869</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.9642 </molarVolume>
</standardState>
</species>
<species name="Gd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Gd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="yep">-4829446.858</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume>0.9642</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++ Pr+++ Ce+++ La+++ Dy+++ Sm+++ Y+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Pr+++">
<beta0 updated="Updated at 16:32 7-31-2020"> 0.5879108393945309, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:32 7-31-2020"> 5.4483234694357385, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:32 7-31-2020"> -0.02066999867229882, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Nd+++">
<beta0 updated="Updated at 16:32 7-31-2020"> 0.7459775851223264, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:32 7-31-2020"> 7.68392131299453, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:32 7-31-2020"> -0.01963615126026457, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="La+++">
<beta0 updated="Updated at 16:32 7-31-2020"> 0.5929999713109059, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:32 7-31-2020"> 5.2769992484445485, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:32 7-31-2020"> -0.024339999997603376, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Dy+++">
<beta0 updated="Updated at 16:32 7-31-2020"> 0.612950248542597, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:32 7-31-2020"> 5.3599329374557385, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:32 7-31-2020"> -0.019699989216349984, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Ce+++">
<beta0 updated="Updated at 16:32 7-31-2020"> 0.6005000182766684, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:32 7-31-2020"> 4.910000193972841, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:32 7-31-2020"> -0.02618999999473301, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Y+++">
<beta0 updated="Updated at 16:32 7-31-2020"> 0.9656352678202726, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:32 7-31-2020"> 8.514180603037651, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:32 7-31-2020"> -0.015467323909969704, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Sm+++">
<beta0 updated="Updated at 16:32 7-31-2020"> 0.5977991228263208, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:32 7-31-2020"> 5.278978156246855, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:32 7-31-2020"> -0.019920000110321332, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,341 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:13 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:13 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Nd+++">
<beta0 updated="Updated at 16:13 7-31-2020"> 0.5877, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:13 7-31-2020"> 5.206, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:13 7-31-2020"> -0.01969, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H Nd C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,325 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Pr dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Pr(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:9 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Pr(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Pr:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:9 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Pr+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H Pr C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,341 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Pr dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Pr(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:15 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Pr(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Pr:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:15 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Pr+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="NO3-" cation="H+">
<beta0> 0.123757018, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1> 0.31055417, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> -0.005539018, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
02mar (Table 3)
Marion, G. M. (2002) "A molal-based model for strong acid chemistry at low
temperatures (less than 200 to 298 K)", Geochimica et Cosmochimica Acta, Vol. 66,
No. 14, pp. 2499-2516. These parameters are derived from the mole fraction model of
Clegg and Brimblecombe (1990) but were parameterized by Marion (2002) for the Pitzer
molality-based model.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Pr+++">
<beta0 updated="Updated at 16:15 7-31-2020"> 0.5879, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:15 7-31-2020"> 5.4479999999999995, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:15 7-31-2020"> -0.020669999999999997, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elements.xml"> O H Pr C Fe Si N Na Cl Ca P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<speciesChemFormula> Na+ </speciesChemFormula>
<atomArray> Na:1 </atomArray>
<charge> 1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -62591 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -57433 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 13.96 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.1839 </a1>
<a2 units="cal/gmol"> -228.5 </a2>
<a3 units="cal-K/gmol/bar"> 3.256 </a3>
<a4 units="cal-K/gmol"> -27260 </a4>
<c1 units="cal/gmol/K"> 18.18 </c1>
<c2 units="cal-K/gmol"> -29810 </c2>
<omega_Pr_Tr units="cal/gmol"> 33060 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,483 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Sm(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:11 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Sm(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Sm:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:11 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.9642 </molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Sm+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,498 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Sm(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:19 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Sm(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Sm:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:19 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.9642 </molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Sm+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Sm+++">
<beta0 updated="Updated at 16:19 7-31-2020"> 0.5978, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:19 7-31-2020"> 5.279, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:19 7-31-2020"> -0.01992, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,481 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Y(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:12 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Y(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Y:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 15:12 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Y+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,496 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Y(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:22 7-31-2020">-1460300.0</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.32</molarVolume>
</standardState>
</species>
<species name="Y(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Y:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 16:22 7-31-2020">-5177400.0</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="yep">0.94</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Y+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Y+++">
<beta0 updated="Updated at 16:22 7-31-2020"> 0.6248, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 16:22 7-31-2020"> 5.66, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 16:22 7-31-2020"> -0.01563, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,942 @@
<ctml>
<elementData caseSensitive="no">
<element name="H" atomicWt = "1.00794" atomicNumber = "1">
<entropy298 value = "65.340E3">
<source>
The standard entropy (1/2 H2gas) was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and Chemical Reference
Data, Monograph 9, p. 1310. G_0 = -19.48112E6 J kmol-1
</source>
</entropy298>
</element>
<element name="D" atomicWt = "2.014102" atomicNumber = "1" >
<entropy298 value = "72.480E3">
<source>
The standard entropy (1/2 D2 gas) was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1040.
</source>
</entropy298>
</element>
<element name="Tr" atomicWt = "3.016327" atomicNumber = "1" >
<entropy298>
<source>
There is no reference state thermodynamic data tabulated
for this element.
</source>
</entropy298>
</element>
<element name="He" atomicWt = "4.00260" atomicNumber = "2" >
<entropy298 value = "126.152E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1361.
</source>
</entropy298>
</element>
<element name="Li" atomicWt = "6.941" atomicNumber = "3" >
<entropy298 value = "29.085E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1493.
</source>
</entropy298>
</element>
<element name="Be" atomicWt = "9.012182" atomicNumber = "4" >
<entropy298 value = "9.440E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 361.
</source>
</entropy298>
</element>
<element name="B" atomicWt = "10.811" atomicNumber = "5" >
<entropy298 value = "5.834E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 177.
</source>
</entropy298>
</element>
<element name="C" atomicWt = "12.011" atomicNumber = "6">
<entropy298 value = "5.740E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 550.
</source>
</entropy298>
</element>
<element name="N" atomicWt = "14.00674" atomicNumber = "7" >
<entropy298 value = "95.8045E3">
<source>
The standard entropy (1/2 N2 gas) was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1621.
</source>
</entropy298>
</element>
<element name="O" atomicWt = "15.9994" atomicNumber = "8" >
<entropy298 value = "102.5735E3">
<source>
The standard entropy (1/2 O2 gas) was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1745.
</source>
</entropy298>
</element>
<element name="F" atomicWt = "18.9984032" atomicNumber = "9" >
<entropy298 value = "101.3945E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1099.
</source>
</entropy298>
</element>
<element name="Ne" atomicWt = "20.1797" atomicNumber = "10" >
<entropy298 value = "146.327E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1695.
</source>
</entropy298>
</element>
<element name="Na" atomicWt = "22.98977" atomicNumber = "11" >
<entropy298 value = "51.455E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1637.
</source>
</entropy298>
</element>
<element name="Mg" atomicWt = "24.3050" atomicNumber = "12" >
<entropy298 value = "32.671E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1529.
</source>
</entropy298>
</element>
<element name="Al" atomicWt = "26.98154" atomicNumber = "13" >
<entropy298 value = "28.275E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 59.
</source>
</entropy298>
</element>
<element name="Si" atomicWt = "28.0855" atomicNumber = "14">
<entropy298 value = "18.820E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1881.
</source>
</entropy298>
</element>
<element name="P" atomicWt = "30.97376" atomicNumber = "15" >
<entropy298 value = "41.077E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1817.
</source>
</entropy298>
</element>
<element name="S" atomicWt = "32.066" atomicNumber = "16" >
<entropy298 value = "32.056E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1859.
</source>
</entropy298>
</element>
<element name="Cl" atomicWt = "35.4527" atomicNumber = "17">
<entropy298 value = "111.535E3">
<source>
The standard entropy (1/2 Cl2 gas) was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 811.
</source>
</entropy298>
</element>
<element name="Ar" atomicWt = "39.948" atomicNumber = "18" >
<entropy298 value = "154.845E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 175.
</source>
</entropy298>
</element>
<element name="K" atomicWt = "39.0983" atomicNumber = "19">
<entropy298 value = "64.670E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1465.
</source>
</entropy298>
</element>
<element name="Ca" atomicWt = "40.078" atomicNumber = "20" >
<entropy298 value = "41.588E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 703.
</source>
</entropy298>
</element>
<element name="Sc" atomicWt = "44.95591" atomicNumber = "21" >
<entropy298>
<source>
No reference state data for this element in the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9.
</source>
</entropy298>
</element>
<element name="Ti" atomicWt = "47.88" atomicNumber = "22" >
<entropy298 value = "30.759E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1907.
</source>
</entropy298>
</element>
<element name="V" atomicWt = "50.9415" atomicNumber = "23" >
<entropy298 value = "28.936E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1917.
</source>
</entropy298>
</element>
<element name="Cr" atomicWt = "51.9961" atomicNumber = "24" >
<entropy298 value = "23.618E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 959.
</source>
</entropy298>
</element>
<element name="Mn" atomicWt = "54.9381" atomicNumber = "25" >
<entropy298 value = "32.010E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1571.
</source>
</entropy298>
</element>
<element name="Fe" atomicWt = "55.847" atomicNumber = "26" >
<entropy298 value = "27.321E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1221.
</source>
</entropy298>
</element>
<element name="Co" atomicWt = "58.9332" atomicNumber = "27" >
<entropy298 value = "30.067E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 943.
</source>
</entropy298>
</element>
<element name="Ni" atomicWt = "58.69" atomicNumber = "28" >
<entropy298 value = "29.870E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1697.
</source>
</entropy298>
</element>
<element name="Cu" atomicWt = "63.546" atomicNumber = "29" >
<entropy298 value = "33.164E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1005.
</source>
</entropy298>
</element>
<element name="Zn" atomicWt = "65.38" atomicNumber = "30" >
<entropy298 value = "41.717E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1935.
</source>
</entropy298>
</element>
<element name="Ga" atomicWt = "69.723" atomicNumber = "31" >
<entropy298 value = "40.838E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1253.
</source>
</entropy298>
</element>
<element name="Ge" atomicWt = "72.61" atomicNumber = "32" >
<entropy298 value = "31.09E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 88.
</source>
</entropy298>
</element>
<element name="As" atomicWt = "74.92159" atomicNumber = "33" >
<entropy298 value = "35.69E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 69.
</source>
</entropy298>
</element>
<element name="Se" atomicWt = "78.96" atomicNumber = "34" >
<entropy298 value = "42.27E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 107
</source>
</entropy298>
</element>
<element name="Br" atomicWt = "79.904" atomicNumber = "35" >
<entropy298 value = "76.103E3">
<source>
The standard entropy (1/2 Br2 gas) was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 470.
</source>
</entropy298>
</element>
<element name="Kr" atomicWt = "83.80" atomicNumber = "36" >
<entropy298 value = "164.084E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1491.
</source>
</entropy298>
</element>
<element name="Rb" atomicWt = "85.4678" atomicNumber = "37" >
<entropy298 value = "76.778E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1849.
</source>
</entropy298>
</element>
<element name="Sr" atomicWt = "87.62" atomicNumber = "38" >
<entropy298 value = "55.694E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1891.
</source>
</entropy298>
</element>
<element name="Y" atomicWt = "88.90585" atomicNumber = "39" >
<entropy298>
<source>
No reference state data found for Y.
</source>
</entropy298>
</element>
<element name="Zr" atomicWt = "91.224" atomicNumber = "40" >
<entropy298 value = "38.869E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1943.
</source>
</entropy298>
</element>
<element name="Nb" atomicWt = "92.90638" atomicNumber = "41" >
<entropy298 value = "36.464E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1675.
</source>
</entropy298>
</element>
<element name="Mo" atomicWt = "95.94 " atomicNumber = "42" >
<entropy298 value = "28.605E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1577.
</source>
</entropy298>
</element>
<element name="Tc" atomicWt = "97.9072" atomicNumber = "43" >
<entropy298 value = "32.506E3">
<source>
The standard entropy was taken from the OECD-NEA
handbook (Guillaumont et al., 2003) "UPDATE ON THE
CHEMICAL THERMODYNAMICS OF URANIUM, NEPTUNIUM,
PLUTONIUM, AMERICIUM AND TECHNETIUM", Table 7-1,
p. 127.
</source>
</entropy298>
</element>
<element name="Ru" atomicWt = "101.07" atomicNumber = "44" >
<entropy298 value = "28.53E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 92.
</source>
</entropy298>
</element>
<element name="Rh" atomicWt = "102.9055" atomicNumber = "45" >
<entropy298 value = "31.54E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 90.
</source>
</entropy298>
</element>
<element name="Pd" atomicWt = "106.42" atomicNumber = "46" >
<entropy298 value = "37.82E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 84.
</source>
</entropy298>
</element>
<element name="Ag" atomicWt = "107.8682" atomicNumber = "47" >
<entropy298 value = "42.55E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 67.
</source>
</entropy298>
</element>
<element name="Cd" atomicWt = "112.411" atomicNumber = "48" >
<entropy298 value = "51.80E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 79.
</source>
</entropy298>
</element>
<element name="In" atomicWt = "114.82" atomicNumber = "49" >
<entropy298 value = "57.84E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 64.
</source>
</entropy298>
</element>
<element name="Sn" atomicWt = "118.710" atomicNumber = "50" >
<entropy298 value = "51.18E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 109.
</source>
</entropy298>
</element>
<element name="Sb" atomicWt = "121.75" atomicNumber = "51" >
<entropy298 value = "45.52E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 106.
</source>
</entropy298>
</element>
<element name="Te" atomicWt = "127.6" atomicNumber = "52" >
<entropy298 value = "49.71E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 111.
</source>
</entropy298>
</element>
<element name="I" atomicWt = " 126.90447" atomicNumber = "53" >
<entropy298 value = "58.071E3">
<source>
The standard entropy (1/2 I2) was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1413.
</source>
</entropy298>
</element>
<element name="Xe" atomicWt = "131.29" atomicNumber = "54" >
<entropy298 value = "169.684E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1933.
</source>
</entropy298>
</element>
<element name="Cs" atomicWt = "132.90543" atomicNumber = "55" >
<entropy298 value = "85.147E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 977.
</source>
</entropy298>
</element>
<element name="Ba" atomicWt = "137.327" atomicNumber = "56" >
<entropy298 value = "62.475E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 319.
</source>
</entropy298>
</element>
<element name="La" atomicWt = "138.9055" atomicNumber = "57" >
<entropy298 value = "56.90E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 68.
</source>
</entropy298>
</element>
<element name="Ce" atomicWt = "140.115" atomicNumber = "58" >
<entropy298 value = "72.00E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 80.
</source>
</entropy298>
</element>
<element name="Pr" atomicWt = "140.90765" atomicNumber = "59" >
<entropy298 value = "73.93E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 85.
</source>
</entropy298>
</element>
<element name="Nd" atomicWt = "144.24" atomicNumber = "60" >
<entropy298 value = "71.09E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 77.
</source>
</entropy298>
</element>
<element name="Pm" atomicWt = "144.9127" atomicNumber = "61" >
<entropy298>
<source>
There is no handbook standard state thermodynamic data for
this element. There are estimates for stability constants
of aqueous and solid species in Spahiu and Bruno (1995),
A Selected Thermodynamic Database for REE to be Used in
HLNW Performance Assessment Exercises. SKB Technical
Report 95-35. Stockholm, Sweden: Swedish Nuclear Fuel and
Waste Management Company. The compilation of Konings
et al. list an estimated standard entropy value for Pm
of 158.0 J/K/mol at 298.15 K but with a non-zero enthalpy of
formation which is not indicative of a reference state
form for this element.
</source>
</entropy298>
</element>
<element name="Sm" atomicWt = "150.36 " atomicNumber = "62" >
<entropy298 value = "69.50E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 100.
</source>
</entropy298>
</element>
<element name="Eu" atomicWt = "151.965" atomicNumber = "63" >
<entropy298 value = "80.79E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 52.
</source>
</entropy298>
</element>
<element name="Gd" atomicWt = "157.25" atomicNumber = "64" >
<entropy298 value = "40.83E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 55.
</source>
</entropy298>
</element>
<element name="Tb" atomicWt = "158.92534" atomicNumber = "65" >
<entropy298 value = "73.30E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 104.
</source>
</entropy298>
</element>
<element name="Dy" atomicWt = "162.50" atomicNumber = "66" >
<entropy298 value = "74.89E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 50.
</source>
</entropy298>
</element>
<element name="Ho" atomicWt = "164.93032" atomicNumber = "67" >
<entropy298 value = "75.02E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 62.
</source>
</entropy298>
</element>
<element name="Er" atomicWt = "167.26" atomicNumber = "68" >
<entropy298 value = "73.18E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 51.
</source>
</entropy298>
</element>
<element name="Tm" atomicWt = "168.93421" atomicNumber = "69" >
<entropy298 value = "74.01E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 109.
</source>
</entropy298>
</element>
<element name="Yb" atomicWt = "173.04" atomicNumber = "70" >
<entropy298 value = "59.83E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 115.
</source>
</entropy298>
</element>
<element name="Lu" atomicWt = "174.967" atomicNumber = "71" >
<entropy298 value = "50.96E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 70.
</source>
</entropy298>
</element>
<element name="Hf" atomicWt = "178.49" atomicNumber = "72" >
<entropy298 value = "43.560E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1363.
</source>
</entropy298>
</element>
<element name="Ta" atomicWt = "180.9479" atomicNumber = "73" >
<entropy298 value = "41.471E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1899.
</source>
</entropy298>
</element>
<element name="W" atomicWt = "183.85" atomicNumber = "74" >
<entropy298 value = "32.660E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1925.
</source>
</entropy298>
</element>
<element name="Re" atomicWt = "186.207" atomicNumber = "75" >
<entropy298 value = "36.53E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 89.
</source>
</entropy298>
</element>
<element name="Os" atomicWt = "190.2" atomicNumber = "76" >
<entropy298 value = "32.64E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 81.
</source>
</entropy298>
</element>
<element name="Ir" atomicWt = "192.22" atomicNumber = "77" >
<entropy298 value = "35.48E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1979), Thermodynamic Properties of
Minerals and Related Substances at 298.15 K
and 1 bar (10^5 Pascals) Pressure abd at Higher
Temperatures, USGS Bulletin 1452, p. 65.
</source>
</entropy298>
</element>
<element name="Pt" atomicWt = "195.08" atomicNumber = "78" >
<entropy298 value = "41.63E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 103.
</source>
</entropy298>
</element>
<element name="Au" atomicWt = "196.96654" atomicNumber = "79" >
<entropy298 value = "47.49E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 70.
</source>
</entropy298>
</element>
<element name="Hg" atomicWt = "200.59" atomicNumber = "80" >
<entropy298 value = "76.028E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1373.
</source>
</entropy298>
</element>
<element name="Ti" atomicWt = "204.3833" atomicNumber = "81" >
<entropy298 value = "30.759E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1907.
</source>
</entropy298>
</element>
<element name="Pb" atomicWt = "207.2" atomicNumber = "82" >
<entropy298 value = "64.785E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1835.
</source>
</entropy298>
</element>
<element name="Bi" atomicWt = "208.98037" atomicNumber = "83" >
<entropy298 value = "56.74E3">
<source>
The standard entropy was taken from Robie and
Hemingway (1995), Thermodynamic Properties of
Minerals and Related Substances, USGS Bulletin
2131, p. 74.
</source>
</entropy298>
</element>
<element name="Po" atomicWt = "208.9824" atomicNumber = "84" >
<entropy298>
<source>
No standard state thermodynamic data for this element.
</source>
</entropy298>
</element>
<element name="At" atomicWt = "209.9871" atomicNumber = "85" >
<entropy298>
<source>
No standard state thermodynamic data for this element.
</source>
</entropy298>
</element>
<element name="Rn" atomicWt = "222.0176" atomicNumber = "86" >
<entropy298 value = "176.235E3">
<source>
The standard entropy was taken from the NIST-JANAF
Handbook (Chase 1998), Journal of Physical and
Chemical Reference Data, Monograph 9, p. 1857.
</source>
</entropy298>
</element>
<element name="Fr" atomicWt = "223.0197" atomicNumber = "87" >
<entropy298>
<source>
No standard state thermodynamic data for this element.
</source>
</entropy298>
</element>
<element name="Ra" atomicWt = "226.0254" atomicNumber = "88" >
<entropy298>
<source>
No standard state thermodynamic data for this element.
</source>
</entropy298>
</element>
<element name="Ac" atomicWt = "227.0279" atomicNumber = "89" >
<entropy298>
<source>
No standard state thermodynamic data for this element.
</source>
</entropy298>
</element>
<element name="Th" atomicWt = "232.0381" atomicNumber = "90" >
<entropy298 value = "51.080E3">
<source>
The standard entropy was taken from the OECD-NEA
handbook (Guillaumont et al., 2003) "UPDATE ON THE
CHEMICAL THERMODYNAMICS OF URANIUM, NEPTUNIUM,
PLUTONIUM, AMERICIUM AND TECHNETIUM", Table 8-1,
p. 145.
</source>
</entropy298>
</element>
<element name="Pa" atomicWt = "231.03588" atomicNumber = "91" >
<entropy298>
<source>
No standard state thermodynamic data for this element.
</source>
</entropy298>
</element>
<element name="U" atomicWt = "238.0508" atomicNumber = "92" >
<entropy298 value = "50.20E3">
<source>
The standard entropy was taken from the OECD-NEA
handbook (Guillaumont et al., 2003) "UPDATE ON THE
CHEMICAL THERMODYNAMICS OF URANIUM, NEPTUNIUM,
PLUTONIUM, AMERICIUM AND TECHNETIUM", Table 3-1,
p. 45.
</source>
</entropy298>
</element>
<element name="Np" atomicWt = "237.0482" atomicNumber = "93" >
<entropy298 value = "50.460E3">
<source>
The standard entropy was taken from the OECD-NEA
handbook (Guillaumont et al., 2003) "UPDATE ON THE
CHEMICAL THERMODYNAMICS OF URANIUM, NEPTUNIUM,
PLUTONIUM, AMERICIUM AND TECHNETIUM", Table 4-1,
p. 81.
</source>
</entropy298>
</element>
<element name="Pu" atomicWt = "244.0482" atomicNumber = "94" >
<entropy298 value = "54.460E3">
<source>
The standard entropy was taken from the OECD-NEA
handbook (Guillaumont et al., 2003) "UPDATE ON THE
CHEMICAL THERMODYNAMICS OF URANIUM, NEPTUNIUM,
PLUTONIUM, AMERICIUM AND TECHNETIUM", Table 5-1,
p. 99.
</source>
</entropy298>
</element>
<element name="E" atomicWt = "0.000545" atomicNumber = "0" >
<entropy298 value = "0.0E3">
<source>
The entropy is zero so as not to overcount. The 1/2 H2(g) entropy
is handled elsewhere.
</source>
</entropy298>
</element>
<element name="dummy" atomicWt = "170.335" atomicNumber = "0" >
<entropy298 value = "0.0E3">
<source>
The entropy is zero so as to make the 'dummy' dodecane phase inert.
This phase is used in TBP equilibrium problems as an 'inert' diluent.
The atomicWt is that reported for dodecane.
</source>
</entropy298>
</element>
</elementData>
</ctml>

@ -0,0 +1,734 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org) Pr(H(A)2)3(org) Ce(H(A)2)3(org) La(H(A)2)3(org) Dy(H(A)2)3(org) Sm(H(A)2)3(org) Y(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 101325.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-1375274.5395942358</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.320974226079</molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-4924702.801342797</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.973500071223</molarVolume>
</standardState>
</species>
<species name="Pr(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Pr:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-4933297.85118053</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.979936421078</molarVolume>
</standardState>
</species>
<species name="Ce(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Ce:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-4925793.594958098</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">1.0060487218</molarVolume>
</standardState>
</species>
<species name="La(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 La:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-4921414.408105163</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.981485801577</molarVolume>
</standardState>
</species>
<species name="Dy(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Dy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-4927250.91118887</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.961666360676</molarVolume>
</standardState>
</species>
<species name="Y(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Y:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-4939280.834663128</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.958888814485</molarVolume>
</standardState>
</species>
<species name="Sm(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Sm:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:14 7-28-2020">-4921187.817651384</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.9642 </molarVolume>
</standardState>
</species>
<species name="Gd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Gd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="yep">-4829446.858</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume>0.9642</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++ Pr+++ Ce+++ La+++ Dy+++ Sm+++ Y+++ Na+
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 101325.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Pr+++">
<beta0 updated="Updated at 11:14 7-28-2020"> 0.41211840588454257, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:14 7-28-2020"> 0.5446957279361009, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 11:14 7-28-2020"> -0.02066999867229882, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Nd+++">
<beta0 updated="Updated at 11:14 7-28-2020"> 0.35663172954569944, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:14 7-28-2020"> 2.9004659704748335, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 11:14 7-28-2020"> -0.01963615126026457, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="La+++">
<beta0 updated="Updated at 11:14 7-28-2020"> 0.05797526981415538, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:14 7-28-2020"> 16.763625801929546, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 11:14 7-28-2020"> -0.024339999997603376, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Dy+++">
<beta0 updated="Updated at 11:14 7-28-2020"> 0.5534945060571388, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:14 7-28-2020"> 9.205570263716002, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 11:14 7-28-2020"> -0.019699989216349984, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Ce+++">
<beta0 updated="Updated at 11:14 7-28-2020"> 0.05726405599313575, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:14 7-28-2020"> 2.6992201079308558, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 11:14 7-28-2020"> -0.02618999999473301, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Y+++">
<beta0 updated="Updated at 11:14 7-28-2020"> 0.8866130626375315, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:14 7-28-2020"> 9.867928019371377, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 11:14 7-28-2020"> -0.015467323909969704, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Sm+++">
<beta0 updated="Updated at 11:14 7-28-2020"> 0.5978087854283536, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:14 7-28-2020"> 5.279188087719687, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 11:14 7-28-2020"> -0.019920000110321332, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E Na</elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 E:1</atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 E:1</atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 E:-1</atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 E:-3</atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Na+">
<atomArray> Na:1 E:-1 </atomArray>
<charge> +1 </charge>
<thermo>
<Mu0 Pref="100000.0" Tmax="1000.0" Tmin="200.0">
<H298 units="cal/mol"> 0.0 </H298>
<numPoints> 2 </numPoints>
<floatArray size="2" title="Mu0Values" units="Dimensionless">
-125.5213, -125.5213
</floatArray>
<floatArray size="2" title="Mu0Temperatures">
298.15, 333.15
</floatArray>
</Mu0>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 1.3 </molarVolume>
</standardState>
</species>
</speciesData>
</ctml>

@ -0,0 +1,256 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> -1302518.58 </h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.3214 </molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 14:28 7-27-2020">-4704699.156668724</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 1.0073 </molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,6 @@
{
"cells": [],
"metadata": {},
"nbformat": 4,
"nbformat_minor": 4
}

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@ -0,0 +1,243 @@
import llepe
import pandas as pd
import numpy as np
import json
def mod_lin_param_df(lp_df, input_val, mini_species, mini_lin_param):
new_lp_df = lp_df.copy()
index = new_lp_df.index[new_lp_df['species'] == mini_species].tolist()[0]
new_lp_df.at[index, mini_lin_param] = input_val
return new_lp_df
species_list = 'Nd,Pr,Ce,La,Dy,Sm,Y'.split(',')
pitzer_param_list = ['beta0', 'beta1']
lin_param_list = ['intercept']
meas_pitzer_param_df = pd.read_csv("../../data/csvs/may_pitzer_params.csv")
pitzer_params_filename = "../../data/jsons/min_h0_pitzer_params.txt"
with open(pitzer_params_filename) as file:
pitzer_params_dict = json.load(file)
ext_h0_filename = "../../data/jsons/min_h0_guess_ext_h0.txt"
with open(ext_h0_filename) as file:
ext_h0_dict = json.load(file)
labeled_data = pd.read_csv("../../data/csvs/"
"multicomponent_PC88A_HCL_NdPrCeLaDySmY.csv")
exp_data = labeled_data.drop(labeled_data.columns[0], axis=1)
xml_file = "PC88A_HCL_NdPrCeLaDySmY_w_pitzer.xml"
lin_param_df = pd.read_csv("../../data/csvs"
"/zeroes_removed_min_h0_pitzer_lin_params.csv")
new_lin_param_df = lin_param_df.copy()
for ind, row in lin_param_df.iterrows():
new_lin_param_df.at[ind, 'slope'] = 3
estimator_params = {'exp_data': exp_data,
'phases_xml_filename': xml_file,
'phase_names': ['HCl_electrolyte', 'PC88A_liquid'],
'aq_solvent_name': 'H2O(L)',
'extractant_name': '(HA)2(org)',
'diluant_name': 'dodecane',
'complex_names': ['{0}(H(A)2)3(org)'.format(species)
for species in species_list],
'extracted_species_ion_names': ['{0}+++'.format(species)
for species in
species_list],
'aq_solvent_rho': 1000.0,
'extractant_rho': 960.0,
'diluant_rho': 750.0,
'temp_xml_file_path': 'outputs/temp.xml',
'objective_function': llepe.lmse_perturbed_obj
}
estimator = llepe.LLEPE(**estimator_params)
def ext_to_complex(h0, custom_obj_dict, mini_species):
linear_params = custom_obj_dict['lin_param_df']
row = linear_params[linear_params['species'] == mini_species]
return row['slope'].values[0] * h0[0] + row['intercept'].values[0]
dependant_params_dict = {}
for species, complex_name in zip(species_list,
estimator_params['complex_names']):
inner_dict = {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': complex_name,
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'function': ext_to_complex,
'kwargs': {"mini_species": species},
'independent_params': '(HA)2(org)_h0'}
dependant_params_dict['{0}_h0'.format(complex_name)] = inner_dict
estimator.update_xml(pitzer_params_dict)
estimator.set_custom_objects_dict({'lin_param_df': new_lin_param_df})
estimator.set_dependant_params_dict(dependant_params_dict)
estimator.update_xml(ext_h0_dict,
dependant_params_dict=dependant_params_dict)
eps = 1e-20
mini_eps = 1e-4
pitzer_guess_dict = {'species': [],
'beta0': [],
'beta1': []}
for species in species_list:
pitzer_guess_dict['species'].append(species)
for param in pitzer_param_list:
mini_dict = pitzer_params_dict['{0}_{1}'.format(species, param)]
value = mini_dict['input_value']
pitzer_guess_dict[param].append(value)
pitzer_guess_df = pd.DataFrame(pitzer_guess_dict)
ext_h0_guess = ext_h0_dict['(HA)2(org)_h0']['input_value']
lin_guess_df = new_lin_param_df.copy()
ignore_list = []
optimizer = 'scipy_minimize'
output_dict = {'iter': [0],
'best_obj': [1e20],
'rel_diff': [1e20],
'best_ext_h0': [1e20]}
for species in species_list:
for lin_param in lin_param_list:
output_dict['{0}_{1}'.format(species, lin_param)] = [1e20]
for pitzer_param in pitzer_param_list:
output_dict['{0}_{1}'.format(species, pitzer_param)] = [1e20]
i = 0
rel_diff = 1000
obj_diff1 = 1000
obj_diff2 = 1000
while obj_diff1 > eps or obj_diff2 > eps:
i += 1
print(i)
best_obj = 1e20
best_ext_h0 = 0
output_dict['iter'].append(i)
for species in species_list:
print(species)
lower_species = species.lower()
info_dict = {'(HA)2(org)_h0': {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': '(HA)2(org)',
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'input_value': ext_h0_guess}}
for pitzer_param in pitzer_param_list:
if '{0}_{1}'.format(species, pitzer_param) not in ignore_list:
pitzer_row = pitzer_guess_df[
pitzer_guess_df['species'] == species]
inner_dict = {'upper_element_name': 'binarySaltParameters',
'upper_attrib_name': 'cation',
'upper_attrib_value':
'{0}+++'.format(species),
'lower_element_name': pitzer_param,
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': ' {0}, 0.0, 0.0, 0.0, 0.0 ',
'input_value':
pitzer_row[pitzer_param].values[0]
}
info_dict['{0}_{1}'.format(
species, pitzer_param)] = inner_dict
for lin_param in lin_param_list:
if '{0}_{1}'.format(species, lin_param) not in ignore_list:
lin_row = lin_guess_df[lin_guess_df['species'] == species]
inner_dict = {'custom_object_name': 'lin_param_df',
'function': mod_lin_param_df,
'kwargs': {'mini_species': species,
'mini_lin_param': lin_param},
'input_value': lin_row[lin_param].values[0]
}
info_dict['{0}_{1}'.format(
species, lin_param)] = inner_dict
estimator.set_opt_dict(info_dict)
estimator.update_custom_objects_dict(info_dict)
estimator.update_xml(info_dict)
obj_kwargs = {'species_list': species_list, 'epsilon': 1e-100}
bounds = [(1e-1, 1e1)] * len(info_dict)
optimizer_kwargs = {"method": 'l-bfgs-b',
"bounds": bounds}
opt_dict, obj_value = estimator.fit(
objective_kwargs=obj_kwargs,
optimizer_kwargs=optimizer_kwargs)
if obj_value < best_obj:
best_obj = obj_value
best_ext_h0 = opt_dict['(HA)2(org)_h0']['input_value']
for lin_param in lin_param_list:
if '{0}_{1}'.format(species, lin_param) not in ignore_list:
mini_dict = opt_dict['{0}_{1}'.format(species, lin_param)]
value = mini_dict['input_value']
output_dict['{0}_{1}'.format(species, lin_param)].append(value)
else:
value = output_dict['{0}_{1}'.format(species, lin_param)][-1]
output_dict['{0}_{1}'.format(species, lin_param)].append(value)
for pitzer_param in pitzer_param_list:
if '{0}_{1}'.format(species, pitzer_param) not in ignore_list:
mini_dict = opt_dict['{0}_{1}'.format(species, pitzer_param)]
value = mini_dict['input_value']
output_dict['{0}_{1}'.format(
species, pitzer_param)].append(value)
else:
value = output_dict['{0}_{1}'.format(
species, pitzer_param)][-1]
output_dict['{0}_{1}'.format(
species, pitzer_param)].append(value)
estimator.update_custom_objects_dict(info_dict)
estimator.update_xml(opt_dict)
pitzer_guess_dict = {'species': []}
for pitzer_param in pitzer_param_list:
pitzer_guess_dict[pitzer_param] = []
lin_guess_dict = {'species': []}
for lin_param in lin_param_list:
lin_guess_dict[lin_param] = []
for species in species_list:
pitzer_guess_dict['species'].append(species)
lin_guess_dict['species'].append(species)
for pitzer_param in pitzer_param_list:
pitzer_str = '{0}_{1}'.format(species, pitzer_param)
value_list = output_dict['{0}_{1}'.format(species, pitzer_param)]
value = value_list[-1]
pitzer_guess_dict[pitzer_param].append(value)
if i > 2:
mini_rel_diff1 = np.abs(value_list[-1]
- value_list[-2]) / (
np.abs(value_list[-2]))
mini_rel_diff2 = np.abs(value_list[-2] - value_list[-3]) / (
np.abs(value_list[-3]))
if mini_rel_diff1 < mini_eps and mini_rel_diff2 < mini_eps:
if pitzer_str not in ignore_list:
ignore_list.append(pitzer_str)
for lin_param in lin_param_list:
lin_str = '{0}_{1}'.format(species, lin_param)
value_list = output_dict['{0}_{1}'.format(species, lin_param)]
value = value_list[-1]
lin_guess_dict[lin_param].append(value)
if i > 2:
mini_rel_diff1 = np.abs(value_list[-1]
- value_list[-2]) / (
np.abs(value_list[-2]))
mini_rel_diff2 = np.abs(value_list[-2] - value_list[-3]) / (
np.abs(value_list[-3]))
if mini_rel_diff1 < mini_eps and mini_rel_diff2 < mini_eps:
if lin_str not in ignore_list:
ignore_list.append(lin_str)
pitzer_guess_df = pd.DataFrame(pitzer_guess_dict)
lin_guess_df = pd.DataFrame(lin_guess_dict)
ext_h0_guess = best_ext_h0
output_dict['best_ext_h0'].append(best_ext_h0)
output_dict['best_obj'].append(best_obj)
output_dict['rel_diff'].append(100)
output_df = pd.DataFrame(output_dict)
old_row = output_df.iloc[-2, :].values[4:]
new_row = output_df.iloc[-1, :].values[4:]
rel_diff = np.sum(np.abs(new_row - old_row) / np.abs(old_row))
del(output_dict['rel_diff'][-1])
output_dict['rel_diff'].append(rel_diff)
output_df = pd.DataFrame(output_dict)
output_df.to_csv('outputs/iterative_fitter_output_multicomponent.csv')
obj_diff1 = output_dict['best_obj'][-2]-output_dict['best_obj'][-1]
if i > 2:
obj_diff2 = output_dict['best_obj'][-3] - output_dict['best_obj'][-1]

@ -0,0 +1,275 @@
import llepe
import pandas as pd
import numpy as np
import json
import matplotlib.pyplot as plt
import matplotlib
import re
def set_size(w, h, ax=None):
""" w, h: width, height in inches """
if not ax:
ax = plt.gca()
left = ax.figure.subplotpars.left
right = ax.figure.subplotpars.right
top = ax.figure.subplotpars.top
bottom = ax.figure.subplotpars.bottom
fig_width = float(w) / (right - left)
fig_height = float(h) / (top - bottom)
ax.figure.set_size_inches(fig_width, fig_height)
font = {'family': 'sans serif',
'size': 24}
matplotlib.rc('font', **font)
matplotlib.rc('xtick', labelsize=18)
matplotlib.rc('ytick', labelsize=18)
matplotlib.rcParams['lines.linewidth'] = 4
matplotlib.rcParams['lines.markersize'] = 10
def ext_to_complex(h0, custom_obj_dict, mini_species):
linear_params = custom_obj_dict['lin_param_df']
row = linear_params[linear_params['species'] == mini_species]
return row['slope'].values[0] * h0[0] + row['intercept'].values[0]
def mod_lin_param_df(lp_df, input_val, mini_species, mini_lin_param):
new_lp_df = lp_df.copy()
index = new_lp_df.index[new_lp_df['species'] == mini_species].tolist()[0]
new_lp_df.at[index, mini_lin_param] = input_val
return new_lp_df
info_df = pd.read_csv('outputs/iterative_fitter_output4.csv')
test_row = -1
pitzer_params_filename = "../../data/jsons/min_h0_pitzer_params.txt"
with open(pitzer_params_filename) as file:
pitzer_params_dict = json.load(file)
pitzer_params_df = pd.DataFrame(pitzer_params_dict)
species_list = 'Nd,Pr,Ce,La,Dy,Sm,Y'.split(',')
pitzer_param_list = ['beta0', 'beta1']
labeled_data = pd.read_csv("../../data/csvs/"
"PC88A_HCL_NdPrCeLaDySmY.csv")
labeled_data = labeled_data.sort_values(['Feed Pr[M]', 'Feed Ce[M]'],
ascending=True)
exp_data = labeled_data.drop(labeled_data.columns[0], axis=1)
xml_file = "PC88A_HCL_NdPrCeLaDySmY_w_pitzer.xml"
lin_param_df = pd.read_csv("../../data/csvs"
"/zeroes_removed_min_h0_pitzer_lin_params.csv")
estimator_params = {'exp_data': exp_data,
'phases_xml_filename': xml_file,
'phase_names': ['HCl_electrolyte', 'PC88A_liquid'],
'aq_solvent_name': 'H2O(L)',
'extractant_name': '(HA)2(org)',
'diluant_name': 'dodecane',
'complex_names': ['{0}(H(A)2)3(org)'.format(species)
for species in species_list],
'extracted_species_ion_names': ['{0}+++'.format(species)
for species in
species_list],
'aq_solvent_rho': 1000.0,
'extractant_rho': 960.0,
'diluant_rho': 750.0,
'temp_xml_file_path': 'outputs/temp.xml',
'objective_function': llepe.lmse_perturbed_obj
}
dependant_params_dict = {}
for species, complex_name in zip(species_list,
estimator_params['complex_names']):
inner_dict = {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': complex_name,
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'function': ext_to_complex,
'kwargs': {"mini_species": species},
'independent_params': '(HA)2(org)_h0'}
dependant_params_dict['{0}_h0'.format(complex_name)] = inner_dict
info_dict = {'(HA)2(org)_h0': {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': '(HA)2(org)',
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'input_value':
info_df.iloc[test_row, :]['best_ext_h0']}}
for species in species_list:
for pitzer_param in pitzer_param_list:
pitzer_str = "{0}_{1}".format(species, pitzer_param)
value = info_df.iloc[test_row, :][pitzer_str]
pitzer_params_dict[pitzer_str]['input_value'] = value
lin_str = "{0}_slope".format(species)
inner_dict = {'custom_object_name': 'lin_param_df',
'function': mod_lin_param_df,
'kwargs': {'mini_species': species,
'mini_lin_param': 'slope'},
'input_value': 3
}
info_dict[lin_str] = inner_dict
lin_str = "{0}_intercept".format(species)
value = info_df.iloc[test_row, :][lin_str]
inner_dict = {'custom_object_name': 'lin_param_df',
'function': mod_lin_param_df,
'kwargs': {'mini_species': species,
'mini_lin_param': 'intercept'},
'input_value': value
}
info_dict[lin_str] = inner_dict
info_dict.update(pitzer_params_dict)
estimator = llepe.LLEPE(**estimator_params)
estimator.set_custom_objects_dict({'lin_param_df': lin_param_df})
estimator.update_custom_objects_dict(info_dict)
estimator.update_xml(info_dict,
dependant_params_dict=dependant_params_dict)
compared_value = 'La_org_eq'
plot_title = None
legend = True
predicted_dict = estimator.get_predicted_dict()
exp_df = estimator.get_exp_df()
pred = pd.DataFrame(predicted_dict)[compared_value].fillna(0).values
meas = exp_df[compared_value].fillna(0).values
name_breakdown = re.findall('[^_\W]+', compared_value)
compared_species = name_breakdown[0]
data_labels = list(labeled_data['label'])
if compared_species == 'h':
feed_molarity = exp_df['h_i'].fillna(0).values
elif compared_species == 'z':
feed_molarity = exp_df['z_i'].fillna(0).values
else:
feed_molarity = exp_df[
'{0}_aq_i'.format(compared_species)].fillna(0).values
combined_df = pd.DataFrame({'pred': pred,
'meas': meas,
'label': data_labels,
'feed_molarity': feed_molarity})
combined_df = combined_df[(combined_df['feed_molarity'] != 0)]
meas = combined_df['meas'].values
pred = combined_df['pred'].values
min_data = np.min([pred, meas])
max_data = np.max([pred, meas])
min_max_data = np.array([min_data, max_data])
if compared_species == 'h':
default_title = '$H^+$ eq. conc. (mol/L)'
elif compared_species == 'z':
default_title = '{0} eq. conc. (mol/L)'.format(extractant_name)
else:
phase = name_breakdown[1]
if phase == 'aq':
extracted_species_charge = extracted_species_charges[
extracted_species_list.index(
compared_species)]
default_title = '$%s^{%d+}$ eq. conc. (mol/L)' \
% (compared_species, extracted_species_charge)
elif phase == 'd':
default_title = '{0} distribution ratio'.format(
compared_species)
else:
default_title = '{0} complex eq. conc. (mol/L)'.format(
compared_species)
fig, ax = plt.subplots(figsize=(8, 6))
if isinstance(data_labels, list):
# unique_labels = list(set(data_labels))
unique_labels = ['Li (1987)',
'Kim (2012)',
'Formiga (2016)',
'Banda (2014)',
]
color_list = ['r', 'g', 'b', 'm']
marker_list = ['o', 's', 'P', 'X', ]
for ind, label in enumerate(unique_labels):
filtered_data = combined_df[combined_df['label'] == label]
filtered_meas = filtered_data['meas']
filtered_pred = filtered_data['pred']
if len(filtered_pred) != 0:
ax.scatter(filtered_meas,
filtered_pred,
label=label,
color=color_list[ind],
marker=marker_list[ind])
if legend:
ax.legend(loc=4)
ax.plot(min_max_data, min_max_data, color="b", label="")
ax.text(min_max_data[0],
min_max_data[1] * 0.9,
'$R^2$={0:.2f}'.format(estimator.r_squared(compared_value)))
ax.set(xlabel='Measured', ylabel='Predicted')
if plot_title is None:
ax.set_title(default_title)
set_size(8, 6)
plt.tight_layout()
plt.show()
# exp_data = estimator.get_exp_df()
# feed_cols = []
# for col in exp_data.columns:
# if 'aq_i' in col:
# feed_cols.append(col)
# exp_data['total_re'] = exp_data[feed_cols].sum(axis=1)
# label_list = []
# for index, row in exp_data[feed_cols].iterrows():
# bool_list = list((row > 0).values)
# label = ''
# for species, el in zip(species_list, bool_list):
# if el:
# label = '{0}-{1}'.format(label, species)
# label = label[1:]
# label_list.append(label)
# r2s = ""
# for species in species_list:
# # if species=='La':
# # save_name = 'outputs' \
# # '/parity_iterative_fitter_{0}_org_eq'.format(species)
# save_name = None
# fig, ax = estimator.parity_plot('{0}_org_eq'.format(species),
# c_data=
# exp_data['total_re'].values,
# c_label='Feed total RE '
# 'molarity (mol/L)',
# print_r_squared=False,
# plot_title='')
# ax.plot([0, 0.05], [0, 0.05], c='b')
# ax.text(0.01, 0.04,
# '$R^2$={0:.2f}'.format(estimator.r_squared(
# '{0}_org_eq'.format(species))))
# ax.set_xlim((0, 0.05))
# ax.set_ylim((0, 0.05))
# r2s += str(estimator.r_squared('{0}_org_eq'.format(species))) + ','
#
# # fig, ax = estimator.parity_plot('{0}_org_eq'.format(species),
# # data_labels=list(labeled_data['label']),
# # print_r_squared=True,
# # save_path=save_name)
# # ax.legend(loc=4)
# pred_df = pd.DataFrame(estimator.get_predicted_dict())
# new_cols = []
# for col in pred_df.columns:
# new_cols.append("pred_{0}".format(col))
# pred_df.columns = new_cols
# new_cols = ['label',
# 'h_i',
# 'h_eq',
# 'z_i',
# 'z_eq'
# ]
# for species in species_list:
# new_cols.append("{0}_aq_i".format(species))
# new_cols.append("{0}_aq_eq".format(species))
# new_cols.append("{0}_d_eq".format(species))
# labeled_data.columns = new_cols
# total_df = labeled_data.join(pred_df)
# total_df.to_csv('if_mse_total_df.csv')
# short_info_dict = {}
# for key, value in info_dict.items():
# short_info_dict[key] = value['input_value']
# with open("outputs/iterative_fitter_short_info_dict.txt", 'w') as file:
# json.dump(short_info_dict, file)

@ -0,0 +1,51 @@
import matplotlib.pyplot as plt
import pandas as pd
go = 'y'
parameters = 'slope,intercept,beta0,beta1'.split(',')
# while go == 'y':
# go = input('continue? ')
# if go != 'y':
# break
# plt.close('all')
df = pd.read_csv('outputs/iterative_fitter_output4.csv')
info_cols = {parameter: [] for parameter in parameters}
for col in df.columns:
for parameter in parameters:
if parameter in col:
info_cols[parameter].append(col)
for parameter in parameters:
mini_df = df[info_cols[parameter]]
fig, ax = plt.subplots()
ax.set_title(parameter)
for col in info_cols[parameter]:
ax.plot(df['iter'].values[1:],
df[col].values[1:],
label=col,
linestyle='-',
marker='o')
ax.set_xlabel('iteration')
ax.set_ylabel('Value')
plt.legend()
plt.tight_layout()
plt.savefig('outputs/{0}.png'.format(parameter))
fig, ax = plt.subplots()
ax.set_title('best_obj_value')
ax.plot(df['iter'].values[1:],
df['best_obj'].values[1:],
linestyle='-',
marker='o')
ax.set_xlabel('iteration')
ax.set_ylabel('Value')
plt.tight_layout()
plt.savefig('outputs/best_obj.png')
fig, ax = plt.subplots()
ax.set_title('rel_diff')
ax.plot(df['iter'].values[1:],
df['rel_diff'].values[1:],
linestyle='-',
marker='o')
ax.set_xlabel('iteration')
ax.set_ylabel('Value')
plt.tight_layout()
# plt.savefig('outputs/rel_diff.png')

@ -0,0 +1,274 @@
import llepe
import pandas as pd
import numpy as np
import json
def mod_lin_param_df(lp_df, input_val, mini_species, mini_lin_param):
new_lp_df = lp_df.copy()
index = new_lp_df.index[new_lp_df['species'] == mini_species].tolist()[0]
new_lp_df.at[index, mini_lin_param] = input_val
return new_lp_df
def ext_to_complex(h0, custom_obj_dict, mini_species):
linear_params = custom_obj_dict['lin_param_df']
mini_row = linear_params[linear_params['species'] == mini_species]
val = mini_row['slope'].values[0] * h0[0] + mini_row['intercept'].values[0]
return val
species_list = 'Nd,Pr,Ce,La,Dy,Sm,Y'.split(',')
pitzer_param_list = ['beta0', 'beta1']
lin_param_list = ['intercept']
short_info_filename = 'outputs/iterative_fitter_short_info_dict.txt'
with open(short_info_filename) as file:
short_info_dict = json.load(file)
labeled_data = pd.read_csv("../../data/csvs/"
"zeroes_removed_PC88A_HCL_NdPrCeLaDySmY.csv")
exp_data = labeled_data.drop(labeled_data.columns[0], axis=1)
xml_file = "PC88A_HCL_NdPrCeLaDySmY_w_pitzer.xml"
lin_param_df = pd.read_csv("../../data/csvs"
"/zeroes_removed_min_h0_pitzer_lin_params.csv")
new_lin_param_df = lin_param_df.copy()
for ind, row in lin_param_df.iterrows():
new_lin_param_df.at[ind, 'slope'] = 3
species = row['species']
val = short_info_dict['{0}_intercept'.format(species)]
new_lin_param_df.at[ind, 'intercept'] = val
estimator_params = {'exp_data': exp_data,
'phases_xml_filename': xml_file,
'phase_names': ['HCl_electrolyte', 'PC88A_liquid'],
'aq_solvent_name': 'H2O(L)',
'extractant_name': '(HA)2(org)',
'diluant_name': 'dodecane',
'complex_names': ['{0}(H(A)2)3(org)'.format(species)
for species in species_list],
'extracted_species_ion_names': ['{0}+++'.format(species)
for species in
species_list],
'aq_solvent_rho': 1000.0,
'extractant_rho': 960.0,
'diluant_rho': 750.0,
'temp_xml_file_path': 'outputs/temp1.xml',
'objective_function': llepe.mean_squared_error,
'custom_objects_dict': {'lin_param_df': new_lin_param_df}
}
dependant_params_dict = {}
for species, complex_name in zip(species_list,
estimator_params['complex_names']):
inner_dict = {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': complex_name,
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'function': ext_to_complex,
'kwargs': {"mini_species": species},
'independent_params': '(HA)2(org)_h0',
}
dependant_params_dict['{0}_h0'.format(complex_name)] = inner_dict
info_dict = {'(HA)2(org)_h0': {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': '(HA)2(org)',
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'input_value':
short_info_dict['(HA)2(org)_h0']}}
for species in species_list:
for param in pitzer_param_list:
name = "{0}_{1}".format(species, param)
inner_dict = {'upper_element_name': 'binarySaltParameters',
'upper_attrib_name': 'cation',
'upper_attrib_value': '{0}+++'.format(species),
'lower_element_name': param,
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': ' {0}, 0.0, 0.0, 0.0, 0.0 ',
'input_value':
short_info_dict[name]}
info_dict[name] = inner_dict
for param in lin_param_list:
name = "{0}_{1}".format(species, param)
inner_dict = {'custom_object_name': 'lin_param_df',
'function': mod_lin_param_df,
'kwargs': {'mini_species': species,
'mini_lin_param': param},
'input_value': short_info_dict[name]
}
estimator = llepe.LLEPE(**estimator_params)
estimator.update_xml(info_dict,
dependant_params_dict=dependant_params_dict)
estimator.set_dependant_params_dict(dependant_params_dict)
eps = 1e-20
mini_eps = 1e-4
pitzer_guess_dict = {'species': [],
'beta0': [],
'beta1': []}
for species in species_list:
pitzer_guess_dict['species'].append(species)
for param in pitzer_param_list:
mini_dict = info_dict['{0}_{1}'.format(species, param)]
value = mini_dict['input_value']
pitzer_guess_dict[param].append(value)
pitzer_guess_df = pd.DataFrame(pitzer_guess_dict)
ext_h0_guess = info_dict['(HA)2(org)_h0']['input_value']
lin_guess_df = new_lin_param_df.copy()
ignore_list = []
optimizer = 'scipy_minimize'
output_dict = {'iter': [0],
'best_obj': [1e20],
'rel_diff': [1e20],
'best_ext_h0': [1e20]}
for species in species_list:
for lin_param in lin_param_list:
output_dict['{0}_{1}'.format(species, lin_param)] = [1e20]
for pitzer_param in pitzer_param_list:
output_dict['{0}_{1}'.format(species, pitzer_param)] = [1e20]
i = 0
rel_diff = 1000
obj_diff1 = 1000
obj_diff2 = 1000
while obj_diff1 > eps or obj_diff2 > eps:
i += 1
print(i)
best_obj = 1e20
best_ext_h0 = 0
output_dict['iter'].append(i)
for species in species_list:
print(species)
lower_species = species.lower()
info_dict = {'(HA)2(org)_h0': {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': '(HA)2(org)',
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'input_value': ext_h0_guess}}
for pitzer_param in pitzer_param_list:
if '{0}_{1}'.format(species, pitzer_param) not in ignore_list:
pitzer_row = pitzer_guess_df[
pitzer_guess_df['species'] == species]
inner_dict = {'upper_element_name': 'binarySaltParameters',
'upper_attrib_name': 'cation',
'upper_attrib_value':
'{0}+++'.format(species),
'lower_element_name': pitzer_param,
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': ' {0}, 0.0, 0.0, 0.0, 0.0 ',
'input_value':
pitzer_row[pitzer_param].values[0]
}
info_dict['{0}_{1}'.format(
species, pitzer_param)] = inner_dict
for lin_param in lin_param_list:
if '{0}_{1}'.format(species, lin_param) not in ignore_list:
lin_row = lin_guess_df[lin_guess_df['species'] == species]
inner_dict = {'custom_object_name': 'lin_param_df',
'function': mod_lin_param_df,
'kwargs': {'mini_species': species,
'mini_lin_param': lin_param},
'input_value': lin_row[lin_param].values[0]
}
info_dict['{0}_{1}'.format(
species, lin_param)] = inner_dict
estimator.set_opt_dict(info_dict)
estimator.update_custom_objects_dict(info_dict)
estimator.update_xml(info_dict)
obj_kwargs = {'species_list': species_list}
bounds = [(1e-1, 1e1)] * len(info_dict)
optimizer_kwargs = {"method": 'l-bfgs-b',
"bounds": bounds}
opt_dict, obj_value = estimator.fit(
objective_kwargs=obj_kwargs,
optimizer_kwargs=optimizer_kwargs)
if obj_value < best_obj:
best_obj = obj_value
best_ext_h0 = opt_dict['(HA)2(org)_h0']['input_value']
for lin_param in lin_param_list:
if '{0}_{1}'.format(species, lin_param) not in ignore_list:
mini_dict = opt_dict['{0}_{1}'.format(species, lin_param)]
value = mini_dict['input_value']
output_dict['{0}_{1}'.format(species, lin_param)].append(value)
else:
value = output_dict['{0}_{1}'.format(species, lin_param)][-1]
output_dict['{0}_{1}'.format(species, lin_param)].append(value)
for pitzer_param in pitzer_param_list:
if '{0}_{1}'.format(species, pitzer_param) not in ignore_list:
mini_dict = opt_dict['{0}_{1}'.format(species, pitzer_param)]
value = mini_dict['input_value']
output_dict['{0}_{1}'.format(
species, pitzer_param)].append(value)
else:
value = output_dict['{0}_{1}'.format(
species, pitzer_param)][-1]
output_dict['{0}_{1}'.format(
species, pitzer_param)].append(value)
estimator.update_custom_objects_dict(info_dict)
estimator.update_xml(opt_dict)
pitzer_guess_dict = {'species': []}
for pitzer_param in pitzer_param_list:
pitzer_guess_dict[pitzer_param] = []
lin_guess_dict = {'species': []}
for lin_param in lin_param_list:
lin_guess_dict[lin_param] = []
for species in species_list:
pitzer_guess_dict['species'].append(species)
lin_guess_dict['species'].append(species)
for pitzer_param in pitzer_param_list:
pitzer_str = '{0}_{1}'.format(species, pitzer_param)
value_list = output_dict['{0}_{1}'.format(species, pitzer_param)]
value = value_list[-1]
pitzer_guess_dict[pitzer_param].append(value)
if i > 2:
mini_rel_diff1 = np.abs(value_list[-1]
- value_list[-2]) / (
np.abs(value_list[-2]))
mini_rel_diff2 = np.abs(value_list[-2] - value_list[-3]) / (
np.abs(value_list[-3]))
if mini_rel_diff1 < mini_eps and mini_rel_diff2 < mini_eps:
if pitzer_str not in ignore_list:
ignore_list.append(pitzer_str)
for lin_param in lin_param_list:
lin_str = '{0}_{1}'.format(species, lin_param)
value_list = output_dict['{0}_{1}'.format(species, lin_param)]
value = value_list[-1]
lin_guess_dict[lin_param].append(value)
if i > 2:
mini_rel_diff1 = np.abs(value_list[-1]
- value_list[-2]) / (
np.abs(value_list[-2]))
mini_rel_diff2 = np.abs(value_list[-2] - value_list[-3]) / (
np.abs(value_list[-3]))
if mini_rel_diff1 < mini_eps and mini_rel_diff2 < mini_eps:
if lin_str not in ignore_list:
ignore_list.append(lin_str)
pitzer_guess_df = pd.DataFrame(pitzer_guess_dict)
lin_guess_df = pd.DataFrame(lin_guess_dict)
ext_h0_guess = best_ext_h0
output_dict['best_ext_h0'].append(best_ext_h0)
output_dict['best_obj'].append(best_obj)
output_dict['rel_diff'].append(100)
output_df = pd.DataFrame(output_dict)
old_row = output_df.iloc[-2, :].values[4:]
new_row = output_df.iloc[-1, :].values[4:]
rel_diff = np.sum(np.abs(new_row - old_row) / np.abs(old_row))
del (output_dict['rel_diff'][-1])
output_dict['rel_diff'].append(rel_diff)
output_df = pd.DataFrame(output_dict)
output_df.to_csv('outputs/iterative_fitter_w_mse_output.csv')
obj_diff1 = np.abs(
output_dict['best_obj'][-1] - output_dict['best_obj'][-2])
if i > 2:
obj_diff2 = np.abs(
output_dict['best_obj'][-1] - output_dict['best_obj'][-3])

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@ -0,0 +1 @@
{"(HA)2(org)_h0": {"upper_element_name": "species", "upper_attrib_name": "name", "upper_attrib_value": "(HA)2(org)", "lower_element_name": "h0", "lower_attrib_name": null, "lower_attrib_value": null, "input_format": "{0}", "input_value": -1376882.3191117246}, "Nd_slope": {"custom_object_name": "lin_param_df", "function":

@ -0,0 +1,24 @@
,iter,best_obj,rel_diff,best_ext_h0,Nd_slope,Nd_intercept,Nd_beta0,Nd_beta1,Pr_slope,Pr_intercept,Pr_beta0,Pr_beta1,Ce_slope,Ce_intercept,Ce_beta0,Ce_beta1,La_slope,La_intercept,La_beta0,La_beta1,Dy_slope,Dy_intercept,Dy_beta0,Dy_beta1,Sm_slope,Sm_intercept,Sm_beta0,Sm_beta1,Y_slope,Y_intercept,Y_beta0,Y_beta1
0,0,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20
1,1,0.00016134227249800634,28.000000000000057,-1376877.7655517121,2.997016104344558,-798273.2701355412,0.8974067641732357,9.428749928658126,2.9952636557673946,-812187.4113891785,0.5879108865959323,5.448324456659969,3.000763765252656,-797785.6715641882,0.6005000281672793,4.910000049022438,3.0029250992523053,-797753.1250426786,0.5930012908436624,5.277035454314173,3.005188887840825,-797963.3947393347,0.6129503793970729,5.359935242349485,3.0049141894588356,-788597.673243324,0.5977991609874977,5.278978873136207,3.004211003525449,-808858.5407597149,0.9656358640797775,8.51418935794808
2,2,8.491196928368016e-05,3.753743510814017,-1375785.2564991405,2.9970374674100313,-798274.3744081341,0.8974068120162436,9.42874961145886,2.994978971888568,-812110.2180829814,0.5879107200993189,5.448316407663497,2.9947405016045665,-813706.4008379887,0.45247610268275573,0.4910000049022438,2.9955784444500653,-811485.5788168659,0.9744013695120132,11.536623868407073,3.0051886646689425,-797963.3849246526,0.6129504080166187,5.359935711747232,2.998286291636726,-796410.7377837397,0.6989623741537213,6.874571631031283,2.9980686905189895,-816110.2339357884,0.8864580596701681,9.871827648349246
3,3,8.491196925751041e-05,1.3872557586710772,-1376877.1540548366,2.981636126077384,-815701.8403939944,0.9757586265135513,7.972840020817166,2.9919947944629675,-814690.7699676664,0.6543020425532663,6.401935572967909,2.9912895029379314,-812768.7207378447,0.4524742361735793,0.4909988885665818,2.8816137399778095,-1165713.786906667,0.6673287483674718,11.13954713731451,3.0051888954051678,-797963.3977338726,0.6129504256882,5.359936001703055,2.998286456943957,-796410.7468898736,0.6989623710221783,6.8745716509720465,2.9980701639611307,-816110.3144777927,0.8864580604329536,9.87182766313202
4,4,8.491196864453183e-05,3.124350706237914,-1376877.152537996,3.0030651668677755,-788714.7627699226,0.8876477500590181,7.1795656837403845,2.9492981846969997,-866396.0136278999,0.06543020425532663,14.481702424339913,2.9915899054971504,-812784.8309966518,0.4524742264332296,0.49099888634665106,2.802400719850797,-1217568.8940603866,0.734765523062068,16.501184782487442,3.005188678309654,-797963.3880226224,0.6129504505231561,5.359936408928357,2.9982864229571073,-796410.7471635938,0.6989623610327844,6.874571712665922,2.998069983411216,-816110.5901289525,0.8864580599623918,9.871827432740531
5,5,8.491196857946013e-05,1.1315146871019859,-1376877.1544992805,3.009261826624499,-790493.4807183052,0.8876820541130862,7.180366876068199,2.95493306423167,-941679.8410781198,0.06542242940021062,14.596387046646438,2.9939929242661925,-813370.2300667212,0.4524750816922801,0.49099914533270717,2.7412268066767798,-1181700.5928732348,0.0734765523062068,17.778208795501687,3.0051889032028973,-797963.4006334972,0.6129504699710735,5.359936728023126,2.9982864523758734,-796410.7494542947,0.6989623571542753,6.874571712665922,2.9980699791830183,-816110.5900394547,0.8864580599623918,9.871827432586276
6,6,8.491196857868175e-05,0.8212092953360018,-1376877.1544988493,3.018448578935926,-756591.4774984489,0.8847071856293566,7.127732469249149,2.946746698619443,-914521.2680772808,0.0655303675034554,17.87160024357031,2.9951696006679125,-813508.1242683842,0.45247514275357914,0.4909991719996952,2.8979917114047042,-880424.1009942711,0.07397534024322364,14.445668342341632,3.005188689731846,-797963.3909449822,0.6129504919765936,5.359937088895021,2.998286417872815,-796410.7494542947,0.6989623397580044,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
7,7,8.491196857967895e-05,2.8535135475763593,-1376877.1544988335,2.9803570928818193,-831169.3940393181,2.3855150593783625,0.9943792524787087,2.927591618356134,-906967.4787334907,0.06534292291155007,16.133908724056262,3.0029738570325497,-795932.5448638537,0.4524823795863963,0.4909954629866391,2.9609895390962344,-881255.3332121583,0.07326400481624591,14.648731908806054,3.005188911656549,-797963.4035243823,0.6129505135552498,5.3599374429477535,2.998286452518918,-796410.7494542947,0.6989623360131538,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
8,8,8.491196857967895e-05,0.5074295633771292,-1376877.1544988335,3.046988319365659,-695733.7822299139,2.118879762861775,0.9832916930997248,2.9452585522682813,-902617.5883506279,0.06531634264974066,14.535540289940167,3.001724622774424,-796341.6549504208,0.45078352007925804,0.49034083082370367,2.9722238052604713,-851355.1697072648,0.07317245680858252,14.005551062985573,3.0051886986863527,-797963.3937399577,0.6129505334265856,5.359937768806609,2.998286418340077,-796410.7494542947,0.6989623190362244,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
9,9,8.491196857967895e-05,0.8233569178526139,-1376877.1544988335,2.9825936071777024,-834718.8445277695,2.265417073982851,0.994361984624478,2.960695251829361,-883765.0750479599,0.06535572997952777,14.395940812001363,3.0011755877522677,-797620.9536781705,0.451768694057885,0.4905988771385775,3.01363818781501,-765715.3192727776,0.07374063593564315,19.03231059683384,3.0051889209677576,-797963.4064770396,0.6129505574921508,5.359938163641345,2.998286452651492,-796410.7494542947,0.6989623152735008,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
10,10,8.491196857967895e-05,0.4773109299773383,-1376877.1544988335,3.0188840683355007,-758130.1305298645,2.1690523176501006,0.9984406194127493,2.982890660585592,-840275.2594169229,0.0654841686928967,14.704161508382992,2.997539444125265,-805146.4436967466,0.450156356171543,0.4900762819026168,2.9884659287162063,-823730.0588083962,0.07331458114972399,16.339393531863305,3.0051887064580316,-797963.3965185066,0.6129505756465488,5.359938461354856,2.998286418810594,-796410.7494542947,0.6989622987206754,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
11,11,8.491196857967895e-05,1.3118334901996995,-1376877.1544988335,3.0139001564181234,-777482.0137288059,2.4891695692571334,1.0067452500133052,2.7082813102477377,-1340320.351525344,0.06570193477294409,15.318347397454074,2.9937062166470865,-811848.1861685036,0.3807242781267447,0.4571366236203172,3.0321484162541092,-734038.497344836,0.07278743339509186,15.771531203484976,3.0051889316605727,-797963.4095808832,0.6129506027939315,5.359938906721338,2.9982864527868296,-796410.7494542947,0.6989622949357988,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
12,12,8.491196857967895e-05,0.6176079935219678,-1376877.1544988335,2.9991637169323253,-799348.0533050542,2.0606574395422745,0.9999146041973166,2.645965929040643,-1371545.8507318976,0.06530562967326357,14.087654782739659,2.994388651142047,-812440.2720371439,0.3797153647239341,0.45689994044316656,2.976360040153504,-826947.2829702377,0.0721742508966242,13.950564590026154,3.005188713573002,-797963.3993561977,0.6129506195016742,5.3599391806962355,2.9982864192709067,-796410.7494542947,0.6989622787849055,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
13,13,8.491196857967895e-05,0.447458797489282,-1376877.1544988335,2.9980180983111584,-800782.7580580596,2.384966567099209,1.0089359468087284,2.624593032594632,-1360513.8600727562,0.0652016206426237,13.974111290564698,2.9921196188008023,-811824.6368088808,0.37971475358406565,0.4568995049435289,2.9835754249798847,-836109.188415324,0.07001616810133855,16.854824585869906,3.0051889446809152,-797963.4129476986,0.6129506507011362,5.359939692544431,2.998286452925373,-796410.7494542947,0.6989622749758465,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
14,14,8.491196857967895e-05,0.348360677031186,-1376877.1544988335,2.9982081321172895,-800795.2294772209,2.384966526824247,1.0089359542883563,2.666975566695788,-1499994.1414862953,0.06545352162164432,15.242130244485235,2.9921792830474856,-811827.830457512,0.3797147346864944,0.45689949537118524,3.0165968899178837,-760698.0568963296,0.06972550438458386,17.353271986524845,3.005188720514459,-797963.4023398461,0.6129506661375982,5.359939945648347,2.9982864196902987,-796410.7494542947,0.6989622591872565,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
15,15,8.491196857967895e-05,0.8542573291619304,-1376877.1544988335,2.998712505758874,-802387.4877053623,1.5206330649921567,0.9981622444785841,2.713156877040639,-1478192.0473444732,0.06274057809944926,13.092934019657042,2.994891728361129,-812682.5967323158,0.38018937518269785,0.4567780326119338,3.03009818160027,-757243.0989114699,0.0690109050871497,13.154321394861364,3.005188961745495,-797963.4167757028,0.6129507031227088,5.359940552366342,2.9982864530536806,-796410.7494542947,0.6989622553597238,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
16,16,8.491196857967895e-05,0.9448120605121391,-1376877.1544988335,2.997515876288025,-800762.0931049074,2.371926193409047,1.0392028818516033,2.529014996778218,-1394593.2488741723,0.06362240882017806,15.72054555069271,2.992321826257504,-811985.236014034,0.380188573336472,0.45677745562445643,3.0311603879490625,-757395.5635541482,0.06901090642373163,13.15434949309279,3.0051887279351726,-797963.4056092768,0.6129507173831404,5.359940786171395,2.9982864200995016,-796410.7494542947,0.6989622399197148,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
17,17,8.491196857967895e-05,0.06986866489189483,-1376877.1544988335,2.998185517350526,-800940.9851411111,2.3719292648415435,1.0392030732451656,2.572480079015409,-1398076.7310485386,0.06363412395715484,14.965559296480045,2.9916507242807455,-811803.1343536598,0.3801884696593834,0.4567773926702631,3.029587351548093,-757002.5991619993,0.06901085836588974,13.153841661748762,3.00518898709267,-797963.4214979863,0.6129507639240588,5.359941549628348,2.9982864531810547,-796410.7494542947,0.6989622360690536,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
18,18,8.491196857967895e-05,7.537649140057278,-1376877.1544988335,2.9139186135307895,-903717.07595184,1.1713250218349551,7.8961519078936995,2.551409491193631,-1396607.749248508,0.06364635989520172,15.028103657774764,2.992358699183809,-811883.3497541018,0.38014823465953007,0.45676064010613937,3.0225440094645197,-757527.3282072913,0.06907140877109968,16.557914647062493,3.0051887374402306,-797963.4094522469,0.6129507769959467,5.3599417639476465,2.9982864204802095,-796410.7494542947,0.6989622209402793,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
19,19,8.491196857967895e-05,0.3395564898628593,-1376877.1544988335,2.9206876794423295,-906067.0736166579,1.171453185504549,7.897253707676486,2.542473620212442,-1395291.4660299404,0.06365232727832787,15.064625151652315,2.9913152280569513,-811600.2380135104,0.3801480833041433,0.45676053922619353,3.00948706713011,-770684.9871133575,0.06894408512873036,21.578016654838063,3.0051890362364753,-797963.4285937521,0.6129508452597554,5.359942883786607,2.998286453304157,-796410.7494542947,0.6989622170705244,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
20,20,8.491196857967895e-05,0.27887232716945426,-1376877.1544988335,2.932945093248787,-893472.3867422906,1.2372118357462467,8.367708345062676,2.5681008604924935,-1424501.3718411059,0.06389293355566235,16.006743784511794,2.9915688192964494,-811676.8964187511,0.38001482584768576,0.4566967822701942,2.9966407511121345,-795742.7223232647,0.06891628915899889,21.364797187402115,3.005188756433512,-797963.4149199789,0.6129508568428819,5.359943073668666,2.9982864208411075,-796410.7494542947,0.6989622022429722,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
21,21,8.491196857967895e-05,0.07904486462976254,-1376877.1544988335,2.9192941732704183,-899595.6903217547,1.2289167121597353,8.270591970104478,2.5885541497990276,-1425201.6370605633,0.06406357430240948,16.055658203899945,2.991141414262,-812827.4608356728,0.3798926190405488,0.45663532315631505,2.993009643896257,-802640.8358981846,0.06886889954042703,20.88499046197079,3.0051892653467993,-797963.4540443348,0.6129510889764764,5.359946881486811,2.9982864534278213,-796410.7494542947,0.6989621983540872,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
22,22,8.491196857967895e-05,2.8078518871500875,-1376877.1544988335,2.5130533352916404,-1308478.271342789,2.3685619028157476,1.0600650778914467,2.532808888931495,-1416725.967204896,0.06411203767956787,15.094184412115302,2.990867139013824,-812773.0935418691,0.3798925911718346,0.456635306115862,2.99518346032217,-803786.8612650471,0.06825025926005274,14.294244836372703,3.0051888907116417,-797963.4353105845,0.6129510969272831,5.359947011739686,2.9982864212214833,-796410.7494542947,0.6989621838326963,6.874571712665922,2.9980699785721763,-816110.5900320362,0.8864580599623918,9.871827432559574
1 iter best_obj rel_diff best_ext_h0 Nd_slope Nd_intercept Nd_beta0 Nd_beta1 Pr_slope Pr_intercept Pr_beta0 Pr_beta1 Ce_slope Ce_intercept Ce_beta0 Ce_beta1 La_slope La_intercept La_beta0 La_beta1 Dy_slope Dy_intercept Dy_beta0 Dy_beta1 Sm_slope Sm_intercept Sm_beta0 Sm_beta1 Y_slope Y_intercept Y_beta0 Y_beta1
2 0 0 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20
3 1 1 0.00016134227249800634 28.000000000000057 -1376877.7655517121 2.997016104344558 -798273.2701355412 0.8974067641732357 9.428749928658126 2.9952636557673946 -812187.4113891785 0.5879108865959323 5.448324456659969 3.000763765252656 -797785.6715641882 0.6005000281672793 4.910000049022438 3.0029250992523053 -797753.1250426786 0.5930012908436624 5.277035454314173 3.005188887840825 -797963.3947393347 0.6129503793970729 5.359935242349485 3.0049141894588356 -788597.673243324 0.5977991609874977 5.278978873136207 3.004211003525449 -808858.5407597149 0.9656358640797775 8.51418935794808
4 2 2 8.491196928368016e-05 3.753743510814017 -1375785.2564991405 2.9970374674100313 -798274.3744081341 0.8974068120162436 9.42874961145886 2.994978971888568 -812110.2180829814 0.5879107200993189 5.448316407663497 2.9947405016045665 -813706.4008379887 0.45247610268275573 0.4910000049022438 2.9955784444500653 -811485.5788168659 0.9744013695120132 11.536623868407073 3.0051886646689425 -797963.3849246526 0.6129504080166187 5.359935711747232 2.998286291636726 -796410.7377837397 0.6989623741537213 6.874571631031283 2.9980686905189895 -816110.2339357884 0.8864580596701681 9.871827648349246
5 3 3 8.491196925751041e-05 1.3872557586710772 -1376877.1540548366 2.981636126077384 -815701.8403939944 0.9757586265135513 7.972840020817166 2.9919947944629675 -814690.7699676664 0.6543020425532663 6.401935572967909 2.9912895029379314 -812768.7207378447 0.4524742361735793 0.4909988885665818 2.8816137399778095 -1165713.786906667 0.6673287483674718 11.13954713731451 3.0051888954051678 -797963.3977338726 0.6129504256882 5.359936001703055 2.998286456943957 -796410.7468898736 0.6989623710221783 6.8745716509720465 2.9980701639611307 -816110.3144777927 0.8864580604329536 9.87182766313202
6 4 4 8.491196864453183e-05 3.124350706237914 -1376877.152537996 3.0030651668677755 -788714.7627699226 0.8876477500590181 7.1795656837403845 2.9492981846969997 -866396.0136278999 0.06543020425532663 14.481702424339913 2.9915899054971504 -812784.8309966518 0.4524742264332296 0.49099888634665106 2.802400719850797 -1217568.8940603866 0.734765523062068 16.501184782487442 3.005188678309654 -797963.3880226224 0.6129504505231561 5.359936408928357 2.9982864229571073 -796410.7471635938 0.6989623610327844 6.874571712665922 2.998069983411216 -816110.5901289525 0.8864580599623918 9.871827432740531
7 5 5 8.491196857946013e-05 1.1315146871019859 -1376877.1544992805 3.009261826624499 -790493.4807183052 0.8876820541130862 7.180366876068199 2.95493306423167 -941679.8410781198 0.06542242940021062 14.596387046646438 2.9939929242661925 -813370.2300667212 0.4524750816922801 0.49099914533270717 2.7412268066767798 -1181700.5928732348 0.0734765523062068 17.778208795501687 3.0051889032028973 -797963.4006334972 0.6129504699710735 5.359936728023126 2.9982864523758734 -796410.7494542947 0.6989623571542753 6.874571712665922 2.9980699791830183 -816110.5900394547 0.8864580599623918 9.871827432586276
8 6 6 8.491196857868175e-05 0.8212092953360018 -1376877.1544988493 3.018448578935926 -756591.4774984489 0.8847071856293566 7.127732469249149 2.946746698619443 -914521.2680772808 0.0655303675034554 17.87160024357031 2.9951696006679125 -813508.1242683842 0.45247514275357914 0.4909991719996952 2.8979917114047042 -880424.1009942711 0.07397534024322364 14.445668342341632 3.005188689731846 -797963.3909449822 0.6129504919765936 5.359937088895021 2.998286417872815 -796410.7494542947 0.6989623397580044 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
9 7 7 8.491196857967895e-05 2.8535135475763593 -1376877.1544988335 2.9803570928818193 -831169.3940393181 2.3855150593783625 0.9943792524787087 2.927591618356134 -906967.4787334907 0.06534292291155007 16.133908724056262 3.0029738570325497 -795932.5448638537 0.4524823795863963 0.4909954629866391 2.9609895390962344 -881255.3332121583 0.07326400481624591 14.648731908806054 3.005188911656549 -797963.4035243823 0.6129505135552498 5.3599374429477535 2.998286452518918 -796410.7494542947 0.6989623360131538 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
10 8 8 8.491196857967895e-05 0.5074295633771292 -1376877.1544988335 3.046988319365659 -695733.7822299139 2.118879762861775 0.9832916930997248 2.9452585522682813 -902617.5883506279 0.06531634264974066 14.535540289940167 3.001724622774424 -796341.6549504208 0.45078352007925804 0.49034083082370367 2.9722238052604713 -851355.1697072648 0.07317245680858252 14.005551062985573 3.0051886986863527 -797963.3937399577 0.6129505334265856 5.359937768806609 2.998286418340077 -796410.7494542947 0.6989623190362244 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
11 9 9 8.491196857967895e-05 0.8233569178526139 -1376877.1544988335 2.9825936071777024 -834718.8445277695 2.265417073982851 0.994361984624478 2.960695251829361 -883765.0750479599 0.06535572997952777 14.395940812001363 3.0011755877522677 -797620.9536781705 0.451768694057885 0.4905988771385775 3.01363818781501 -765715.3192727776 0.07374063593564315 19.03231059683384 3.0051889209677576 -797963.4064770396 0.6129505574921508 5.359938163641345 2.998286452651492 -796410.7494542947 0.6989623152735008 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
12 10 10 8.491196857967895e-05 0.4773109299773383 -1376877.1544988335 3.0188840683355007 -758130.1305298645 2.1690523176501006 0.9984406194127493 2.982890660585592 -840275.2594169229 0.0654841686928967 14.704161508382992 2.997539444125265 -805146.4436967466 0.450156356171543 0.4900762819026168 2.9884659287162063 -823730.0588083962 0.07331458114972399 16.339393531863305 3.0051887064580316 -797963.3965185066 0.6129505756465488 5.359938461354856 2.998286418810594 -796410.7494542947 0.6989622987206754 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
13 11 11 8.491196857967895e-05 1.3118334901996995 -1376877.1544988335 3.0139001564181234 -777482.0137288059 2.4891695692571334 1.0067452500133052 2.7082813102477377 -1340320.351525344 0.06570193477294409 15.318347397454074 2.9937062166470865 -811848.1861685036 0.3807242781267447 0.4571366236203172 3.0321484162541092 -734038.497344836 0.07278743339509186 15.771531203484976 3.0051889316605727 -797963.4095808832 0.6129506027939315 5.359938906721338 2.9982864527868296 -796410.7494542947 0.6989622949357988 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
14 12 12 8.491196857967895e-05 0.6176079935219678 -1376877.1544988335 2.9991637169323253 -799348.0533050542 2.0606574395422745 0.9999146041973166 2.645965929040643 -1371545.8507318976 0.06530562967326357 14.087654782739659 2.994388651142047 -812440.2720371439 0.3797153647239341 0.45689994044316656 2.976360040153504 -826947.2829702377 0.0721742508966242 13.950564590026154 3.005188713573002 -797963.3993561977 0.6129506195016742 5.3599391806962355 2.9982864192709067 -796410.7494542947 0.6989622787849055 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
15 13 13 8.491196857967895e-05 0.447458797489282 -1376877.1544988335 2.9980180983111584 -800782.7580580596 2.384966567099209 1.0089359468087284 2.624593032594632 -1360513.8600727562 0.0652016206426237 13.974111290564698 2.9921196188008023 -811824.6368088808 0.37971475358406565 0.4568995049435289 2.9835754249798847 -836109.188415324 0.07001616810133855 16.854824585869906 3.0051889446809152 -797963.4129476986 0.6129506507011362 5.359939692544431 2.998286452925373 -796410.7494542947 0.6989622749758465 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
16 14 14 8.491196857967895e-05 0.348360677031186 -1376877.1544988335 2.9982081321172895 -800795.2294772209 2.384966526824247 1.0089359542883563 2.666975566695788 -1499994.1414862953 0.06545352162164432 15.242130244485235 2.9921792830474856 -811827.830457512 0.3797147346864944 0.45689949537118524 3.0165968899178837 -760698.0568963296 0.06972550438458386 17.353271986524845 3.005188720514459 -797963.4023398461 0.6129506661375982 5.359939945648347 2.9982864196902987 -796410.7494542947 0.6989622591872565 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
17 15 15 8.491196857967895e-05 0.8542573291619304 -1376877.1544988335 2.998712505758874 -802387.4877053623 1.5206330649921567 0.9981622444785841 2.713156877040639 -1478192.0473444732 0.06274057809944926 13.092934019657042 2.994891728361129 -812682.5967323158 0.38018937518269785 0.4567780326119338 3.03009818160027 -757243.0989114699 0.0690109050871497 13.154321394861364 3.005188961745495 -797963.4167757028 0.6129507031227088 5.359940552366342 2.9982864530536806 -796410.7494542947 0.6989622553597238 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
18 16 16 8.491196857967895e-05 0.9448120605121391 -1376877.1544988335 2.997515876288025 -800762.0931049074 2.371926193409047 1.0392028818516033 2.529014996778218 -1394593.2488741723 0.06362240882017806 15.72054555069271 2.992321826257504 -811985.236014034 0.380188573336472 0.45677745562445643 3.0311603879490625 -757395.5635541482 0.06901090642373163 13.15434949309279 3.0051887279351726 -797963.4056092768 0.6129507173831404 5.359940786171395 2.9982864200995016 -796410.7494542947 0.6989622399197148 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
19 17 17 8.491196857967895e-05 0.06986866489189483 -1376877.1544988335 2.998185517350526 -800940.9851411111 2.3719292648415435 1.0392030732451656 2.572480079015409 -1398076.7310485386 0.06363412395715484 14.965559296480045 2.9916507242807455 -811803.1343536598 0.3801884696593834 0.4567773926702631 3.029587351548093 -757002.5991619993 0.06901085836588974 13.153841661748762 3.00518898709267 -797963.4214979863 0.6129507639240588 5.359941549628348 2.9982864531810547 -796410.7494542947 0.6989622360690536 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
20 18 18 8.491196857967895e-05 7.537649140057278 -1376877.1544988335 2.9139186135307895 -903717.07595184 1.1713250218349551 7.8961519078936995 2.551409491193631 -1396607.749248508 0.06364635989520172 15.028103657774764 2.992358699183809 -811883.3497541018 0.38014823465953007 0.45676064010613937 3.0225440094645197 -757527.3282072913 0.06907140877109968 16.557914647062493 3.0051887374402306 -797963.4094522469 0.6129507769959467 5.3599417639476465 2.9982864204802095 -796410.7494542947 0.6989622209402793 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
21 19 19 8.491196857967895e-05 0.3395564898628593 -1376877.1544988335 2.9206876794423295 -906067.0736166579 1.171453185504549 7.897253707676486 2.542473620212442 -1395291.4660299404 0.06365232727832787 15.064625151652315 2.9913152280569513 -811600.2380135104 0.3801480833041433 0.45676053922619353 3.00948706713011 -770684.9871133575 0.06894408512873036 21.578016654838063 3.0051890362364753 -797963.4285937521 0.6129508452597554 5.359942883786607 2.998286453304157 -796410.7494542947 0.6989622170705244 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
22 20 20 8.491196857967895e-05 0.27887232716945426 -1376877.1544988335 2.932945093248787 -893472.3867422906 1.2372118357462467 8.367708345062676 2.5681008604924935 -1424501.3718411059 0.06389293355566235 16.006743784511794 2.9915688192964494 -811676.8964187511 0.38001482584768576 0.4566967822701942 2.9966407511121345 -795742.7223232647 0.06891628915899889 21.364797187402115 3.005188756433512 -797963.4149199789 0.6129508568428819 5.359943073668666 2.9982864208411075 -796410.7494542947 0.6989622022429722 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
23 21 21 8.491196857967895e-05 0.07904486462976254 -1376877.1544988335 2.9192941732704183 -899595.6903217547 1.2289167121597353 8.270591970104478 2.5885541497990276 -1425201.6370605633 0.06406357430240948 16.055658203899945 2.991141414262 -812827.4608356728 0.3798926190405488 0.45663532315631505 2.993009643896257 -802640.8358981846 0.06886889954042703 20.88499046197079 3.0051892653467993 -797963.4540443348 0.6129510889764764 5.359946881486811 2.9982864534278213 -796410.7494542947 0.6989621983540872 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574
24 22 22 8.491196857967895e-05 2.8078518871500875 -1376877.1544988335 2.5130533352916404 -1308478.271342789 2.3685619028157476 1.0600650778914467 2.532808888931495 -1416725.967204896 0.06411203767956787 15.094184412115302 2.990867139013824 -812773.0935418691 0.3798925911718346 0.456635306115862 2.99518346032217 -803786.8612650471 0.06825025926005274 14.294244836372703 3.0051888907116417 -797963.4353105845 0.6129510969272831 5.359947011739686 2.9982864212214833 -796410.7494542947 0.6989621838326963 6.874571712665922 2.9980699785721763 -816110.5900320362 0.8864580599623918 9.871827432559574

@ -0,0 +1,8 @@
,iter,best_obj,rel_diff,best_ext_h0,Nd_intercept,Nd_beta0,Nd_beta1,Pr_intercept,Pr_beta0,Pr_beta1,Ce_intercept,Ce_beta0,Ce_beta1,La_intercept,La_beta0,La_beta1,Dy_intercept,Dy_beta0,Dy_beta1,Sm_intercept,Sm_beta0,Sm_beta1,Y_intercept,Y_beta0,Y_beta1
0,0,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20
1,1,0.00016129407933554554,21.000000000000057,-1376877.152986458,-796238.0142870437,1.437426638616483,5.347609621840506,-807393.2082028955,0.05879108393945309,0.5448323469435737,-793502.5397317475,1.584075553189004,9.71291104987633,-804144.2085745687,0.9975450638457432,0.5276999248444548,-801913.2126520091,0.7646409184903517,7.849312986255907,-795363.8004519838,0.5978071372268503,5.279164697561237,-814653.355406187,0.9657649833215246,8.515799878446009
2,2,0.00010559366199558426,2.7344663371161086,-1376882.3191580868,-796384.0556926059,1.437428165636144,5.347617052258618,-808095.4393259468,0.05879108550298423,0.5448323732068848,-789522.5091359932,0.20352352259320314,21.12029634455721,-803938.2604268632,1.0223150014212676,0.5296310756363933,-801912.5225008891,0.7646405127343534,7.849315503928965,-794049.2354743823,0.6989186480410126,6.87781841947533,-814193.8647533458,0.8852782052211031,9.334631175295913
3,3,0.00010559208431248382,0.871670386095456,-1376882.3191106108,-795019.7041121587,1.0623904260280357,8.59415748006841,-808447.2602100212,0.05879108748614492,0.5448324180244323,-790036.1207336787,0.20352355232601096,21.120499613123066,-803280.4365906577,1.0223156310422086,0.5296310565325039,-801913.2141124238,0.7646397332938777,7.849320590516409,-794050.473416772,0.6989082446227728,6.877882156513195,-814192.7894051562,0.8852798138822874,9.334648695392262
4,4,0.00010559049315627479,0.07015128064420798,-1376882.3191117246,-794658.0175977976,1.1251830517616783,8.514892100389922,-807677.5423918352,0.05879108748614492,0.5448324180244323,-789888.8933961166,0.20352350532323682,21.120426174002823,-803102.8847466783,1.022316535866388,0.5296311209773129,-801913.2141124238,0.7646397332938777,7.849320590516409,-794049.2325867265,0.698908158523472,6.877882600430561,-814193.8242471424,0.8852802073165494,9.334653075341238
5,5,0.00010559143289274391,0.1697956144703469,-1376882.3191117246,-794987.0313159251,1.2137224368583803,7.748229523847203,-807547.2398569525,0.05879108748614492,0.5448324180244323,-789724.873364379,0.20352350532323682,21.120426174002823,-802873.2925607098,1.022316535866388,0.5296311209773129,-801913.2141124238,0.7646397332938777,7.849320590516409,-794049.2325867265,0.698908158523472,6.877882600430561,-814193.8242471424,0.8852802073165494,9.334653075341238
6,6,0.00010559143289274391,0.0002104590846558891,-1376882.3191117246,-794919.3525195834,1.2137222016802447,7.748226963005033,-807602.8883771595,0.05879108748614492,0.5448324180244323,-789740.8658638338,0.20352350532323682,21.120426174002823,-802901.9082448303,1.022316535866388,0.5296311209773129,-801913.2141124238,0.7646397332938777,7.849320590516409,-794049.2325867265,0.698908158523472,6.877882600430561,-814193.8242471424,0.8852802073165494,9.334653075341238
1 iter best_obj rel_diff best_ext_h0 Nd_intercept Nd_beta0 Nd_beta1 Pr_intercept Pr_beta0 Pr_beta1 Ce_intercept Ce_beta0 Ce_beta1 La_intercept La_beta0 La_beta1 Dy_intercept Dy_beta0 Dy_beta1 Sm_intercept Sm_beta0 Sm_beta1 Y_intercept Y_beta0 Y_beta1
2 0 0 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20
3 1 1 0.00016129407933554554 21.000000000000057 -1376877.152986458 -796238.0142870437 1.437426638616483 5.347609621840506 -807393.2082028955 0.05879108393945309 0.5448323469435737 -793502.5397317475 1.584075553189004 9.71291104987633 -804144.2085745687 0.9975450638457432 0.5276999248444548 -801913.2126520091 0.7646409184903517 7.849312986255907 -795363.8004519838 0.5978071372268503 5.279164697561237 -814653.355406187 0.9657649833215246 8.515799878446009
4 2 2 0.00010559366199558426 2.7344663371161086 -1376882.3191580868 -796384.0556926059 1.437428165636144 5.347617052258618 -808095.4393259468 0.05879108550298423 0.5448323732068848 -789522.5091359932 0.20352352259320314 21.12029634455721 -803938.2604268632 1.0223150014212676 0.5296310756363933 -801912.5225008891 0.7646405127343534 7.849315503928965 -794049.2354743823 0.6989186480410126 6.87781841947533 -814193.8647533458 0.8852782052211031 9.334631175295913
5 3 3 0.00010559208431248382 0.871670386095456 -1376882.3191106108 -795019.7041121587 1.0623904260280357 8.59415748006841 -808447.2602100212 0.05879108748614492 0.5448324180244323 -790036.1207336787 0.20352355232601096 21.120499613123066 -803280.4365906577 1.0223156310422086 0.5296310565325039 -801913.2141124238 0.7646397332938777 7.849320590516409 -794050.473416772 0.6989082446227728 6.877882156513195 -814192.7894051562 0.8852798138822874 9.334648695392262
6 4 4 0.00010559049315627479 0.07015128064420798 -1376882.3191117246 -794658.0175977976 1.1251830517616783 8.514892100389922 -807677.5423918352 0.05879108748614492 0.5448324180244323 -789888.8933961166 0.20352350532323682 21.120426174002823 -803102.8847466783 1.022316535866388 0.5296311209773129 -801913.2141124238 0.7646397332938777 7.849320590516409 -794049.2325867265 0.698908158523472 6.877882600430561 -814193.8242471424 0.8852802073165494 9.334653075341238
7 5 5 0.00010559143289274391 0.1697956144703469 -1376882.3191117246 -794987.0313159251 1.2137224368583803 7.748229523847203 -807547.2398569525 0.05879108748614492 0.5448324180244323 -789724.873364379 0.20352350532323682 21.120426174002823 -802873.2925607098 1.022316535866388 0.5296311209773129 -801913.2141124238 0.7646397332938777 7.849320590516409 -794049.2325867265 0.698908158523472 6.877882600430561 -814193.8242471424 0.8852802073165494 9.334653075341238
8 6 6 0.00010559143289274391 0.0002104590846558891 -1376882.3191117246 -794919.3525195834 1.2137222016802447 7.748226963005033 -807602.8883771595 0.05879108748614492 0.5448324180244323 -789740.8658638338 0.20352350532323682 21.120426174002823 -802901.9082448303 1.022316535866388 0.5296311209773129 -801913.2141124238 0.7646397332938777 7.849320590516409 -794049.2325867265 0.698908158523472 6.877882600430561 -814193.8242471424 0.8852802073165494 9.334653075341238

@ -0,0 +1,13 @@
,iter,best_obj,rel_diff,best_ext_h0,Nd_intercept,Nd_beta0,Nd_beta1,Pr_intercept,Pr_beta0,Pr_beta1,Ce_intercept,Ce_beta0,Ce_beta1,La_intercept,La_beta0,La_beta1,Dy_intercept,Dy_beta0,Dy_beta1,Sm_intercept,Sm_beta0,Sm_beta1,Y_intercept,Y_beta0,Y_beta1
0,0,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20
1,1,0.033647778113830525,21.000000000000057,-1376877.1491014853,-796630.7472372957,0.7459820315595859,7.683962525237933,-808126.331804689,0.05879108393945308,0.5448323469435739,-798601.759258479,0.6005010041816041,4.910031852331482,-802384.4792986697,0.5930046452497859,5.277120552778203,-805107.4528195162,0.6129648575972374,5.360202430370018,-795364.2081485003,0.5978078971541942,5.279174082617606,-814654.8936071004,0.9657036817294907,8.515030539951253
2,2,0.011371891310485667,1.7809885286134581,-1377917.5261387695,-796507.2063621008,1.282838759795358,6.902804792440243,-808735.3933837808,0.05879108229837919,0.5448322898792433,-798307.3201515124,0.6005010298214011,4.910022284826427,-801912.301008032,0.5930045609171245,5.277127676968026,-801913.8255634321,0.7646294828913005,7.848342595191327,-795363.041378655,0.5978084651250514,5.279183026035014,-813457.4899543246,0.8866269789489127,9.867663759220948
3,3,0.008641080472189547,0.7095542768622557,-1377917.5261387695,-796048.7760914894,1.0825298224626023,6.211283570154922,-807884.6838503737,0.05879107717406858,0.5448320238819658,-799326.8310861788,0.6005020116531858,4.91004437191519,-801737.4462156398,0.5930048961782302,5.277144735292778,-801426.9157177466,0.5532849580804902,9.206773080251143,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
4,4,0.0077116880626842774,0.001045483581763083,-1377917.5261387695,-796123.8048527003,1.082532056501894,6.21126666931227,-807682.864923159,0.05879107717406858,0.5448320238819658,-798906.4762851987,0.6005020116531858,4.91004437191519,-801602.4497529072,0.5930048961782302,5.277144735292778,-801426.3864333024,0.5532852226657412,9.206784416704208,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
5,5,0.007654988377412918,0.0004889223754199215,-1377917.5269444608,-795978.009332054,1.0825315776813356,6.211262701179254,-807775.0879128327,0.05879107717406858,0.5448320238819658,-798839.9836325685,0.6005020116531858,4.91004437191519,-801517.285745487,0.5930048961782302,5.277144735292778,-801426.9000381464,0.5532852863195881,9.206787175138803,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
6,6,0.007610209179550956,0.0003179015187814805,-1377917.5269997541,-795889.1188724772,1.0825315776813356,6.211262701179254,-807684.2192836072,0.05879107717406858,0.5448320238819658,-798798.9084175534,0.6005020116531858,4.91004437191519,-801483.3687901833,0.5930048961782302,5.277144735292778,-801426.9000381464,0.5532852863195881,9.206787175138803,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
7,7,0.007598843960371909,0.00011070832700715566,-1377917.5269100612,-795897.0467890751,1.0825315776813356,6.211262701179254,-807644.9779835651,0.05879107717406858,0.5448320238819658,-798798.9084175534,0.6005020116531858,4.91004437191519,-801441.5615806901,0.5930048961782302,5.277144735292778,-801426.9000381464,0.5532852863195881,9.206787175138803,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
8,8,0.007598581095870595,3.145446182414225e-05,-1377917.5269485628,-795872.4794372824,1.0825315776813356,6.211262701179254,-807644.5039264921,0.05879107717406858,0.5448320238819658,-798798.9084175534,0.6005020116531858,4.91004437191519,-801441.5615806901,0.5930048961782302,5.277144735292778,-801426.9000381464,0.5532852863195881,9.206787175138803,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
9,9,0.0075985812451889985,0.0,-1377917.5269485628,-795872.4794372824,1.0825315776813356,6.211262701179254,-807644.5039264921,0.05879107717406858,0.5448320238819658,-798798.9084175534,0.6005020116531858,4.91004437191519,-801441.5615806901,0.5930048961782302,5.277144735292778,-801426.9000381464,0.5532852863195881,9.206787175138803,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
10,10,0.0075985812451889985,0.0,-1377917.5269485628,-795872.4794372824,1.0825315776813356,6.211262701179254,-807644.5039264921,0.05879107717406858,0.5448320238819658,-798798.9084175534,0.6005020116531858,4.91004437191519,-801441.5615806901,0.5930048961782302,5.277144735292778,-801426.9000381464,0.5532852863195881,9.206787175138803,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
11,11,0.0075985812451889985,0.0,-1377917.5269485628,-795872.4794372824,1.0825315776813356,6.211262701179254,-807644.5039264921,0.05879107717406858,0.5448320238819658,-798798.9084175534,0.6005020116531858,4.91004437191519,-801441.5615806901,0.5930048961782302,5.277144735292778,-801426.9000381464,0.5532852863195881,9.206787175138803,-795364.1985261647,0.5978087860273482,5.279188095059933,-813457.4899543246,0.8866269789489127,9.867663759220948
1 iter best_obj rel_diff best_ext_h0 Nd_intercept Nd_beta0 Nd_beta1 Pr_intercept Pr_beta0 Pr_beta1 Ce_intercept Ce_beta0 Ce_beta1 La_intercept La_beta0 La_beta1 Dy_intercept Dy_beta0 Dy_beta1 Sm_intercept Sm_beta0 Sm_beta1 Y_intercept Y_beta0 Y_beta1
2 0 0 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20
3 1 1 0.033647778113830525 21.000000000000057 -1376877.1491014853 -796630.7472372957 0.7459820315595859 7.683962525237933 -808126.331804689 0.05879108393945308 0.5448323469435739 -798601.759258479 0.6005010041816041 4.910031852331482 -802384.4792986697 0.5930046452497859 5.277120552778203 -805107.4528195162 0.6129648575972374 5.360202430370018 -795364.2081485003 0.5978078971541942 5.279174082617606 -814654.8936071004 0.9657036817294907 8.515030539951253
4 2 2 0.011371891310485667 1.7809885286134581 -1377917.5261387695 -796507.2063621008 1.282838759795358 6.902804792440243 -808735.3933837808 0.05879108229837919 0.5448322898792433 -798307.3201515124 0.6005010298214011 4.910022284826427 -801912.301008032 0.5930045609171245 5.277127676968026 -801913.8255634321 0.7646294828913005 7.848342595191327 -795363.041378655 0.5978084651250514 5.279183026035014 -813457.4899543246 0.8866269789489127 9.867663759220948
5 3 3 0.008641080472189547 0.7095542768622557 -1377917.5261387695 -796048.7760914894 1.0825298224626023 6.211283570154922 -807884.6838503737 0.05879107717406858 0.5448320238819658 -799326.8310861788 0.6005020116531858 4.91004437191519 -801737.4462156398 0.5930048961782302 5.277144735292778 -801426.9157177466 0.5532849580804902 9.206773080251143 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
6 4 4 0.0077116880626842774 0.001045483581763083 -1377917.5261387695 -796123.8048527003 1.082532056501894 6.21126666931227 -807682.864923159 0.05879107717406858 0.5448320238819658 -798906.4762851987 0.6005020116531858 4.91004437191519 -801602.4497529072 0.5930048961782302 5.277144735292778 -801426.3864333024 0.5532852226657412 9.206784416704208 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
7 5 5 0.007654988377412918 0.0004889223754199215 -1377917.5269444608 -795978.009332054 1.0825315776813356 6.211262701179254 -807775.0879128327 0.05879107717406858 0.5448320238819658 -798839.9836325685 0.6005020116531858 4.91004437191519 -801517.285745487 0.5930048961782302 5.277144735292778 -801426.9000381464 0.5532852863195881 9.206787175138803 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
8 6 6 0.007610209179550956 0.0003179015187814805 -1377917.5269997541 -795889.1188724772 1.0825315776813356 6.211262701179254 -807684.2192836072 0.05879107717406858 0.5448320238819658 -798798.9084175534 0.6005020116531858 4.91004437191519 -801483.3687901833 0.5930048961782302 5.277144735292778 -801426.9000381464 0.5532852863195881 9.206787175138803 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
9 7 7 0.007598843960371909 0.00011070832700715566 -1377917.5269100612 -795897.0467890751 1.0825315776813356 6.211262701179254 -807644.9779835651 0.05879107717406858 0.5448320238819658 -798798.9084175534 0.6005020116531858 4.91004437191519 -801441.5615806901 0.5930048961782302 5.277144735292778 -801426.9000381464 0.5532852863195881 9.206787175138803 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
10 8 8 0.007598581095870595 3.145446182414225e-05 -1377917.5269485628 -795872.4794372824 1.0825315776813356 6.211262701179254 -807644.5039264921 0.05879107717406858 0.5448320238819658 -798798.9084175534 0.6005020116531858 4.91004437191519 -801441.5615806901 0.5930048961782302 5.277144735292778 -801426.9000381464 0.5532852863195881 9.206787175138803 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
11 9 9 0.0075985812451889985 0.0 -1377917.5269485628 -795872.4794372824 1.0825315776813356 6.211262701179254 -807644.5039264921 0.05879107717406858 0.5448320238819658 -798798.9084175534 0.6005020116531858 4.91004437191519 -801441.5615806901 0.5930048961782302 5.277144735292778 -801426.9000381464 0.5532852863195881 9.206787175138803 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
12 10 10 0.0075985812451889985 0.0 -1377917.5269485628 -795872.4794372824 1.0825315776813356 6.211262701179254 -807644.5039264921 0.05879107717406858 0.5448320238819658 -798798.9084175534 0.6005020116531858 4.91004437191519 -801441.5615806901 0.5930048961782302 5.277144735292778 -801426.9000381464 0.5532852863195881 9.206787175138803 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948
13 11 11 0.0075985812451889985 0.0 -1377917.5269485628 -795872.4794372824 1.0825315776813356 6.211262701179254 -807644.5039264921 0.05879107717406858 0.5448320238819658 -798798.9084175534 0.6005020116531858 4.91004437191519 -801441.5615806901 0.5930048961782302 5.277144735292778 -801426.9000381464 0.5532852863195881 9.206787175138803 -795364.1985261647 0.5978087860273482 5.279188095059933 -813457.4899543246 0.8866269789489127 9.867663759220948

@ -0,0 +1 @@
{"(HA)2(org)_h0": -1376882.3191117246, "Nd_slope": 3, "Nd_intercept": -794919.3525195834, "Pr_slope": 3, "Pr_intercept": -807602.8883771595, "Ce_slope": 3, "Ce_intercept": -789740.8658638337, "La_slope": 3, "La_intercept": -802901.9082448303, "Dy_slope": 3, "Dy_intercept": -801913.2141124237, "Sm_slope": 3, "Sm_intercept": -794049.2325867265, "Y_slope": 3, "Y_intercept": -814193.8242471423, "Ce_beta0": 0.2035235053232368, "Ce_beta1": 21.120426174002823, "Ce_Cphi": -0.02618999999473301, "Dy_beta0": 0.7646397332938777, "Dy_beta1": 7.849320590516409, "Dy_Cphi": -0.019699989216349984, "La_beta0": 1.022316535866388, "La_beta1": 0.5296311209773129, "La_Cphi": -0.024339999997603376, "Nd_beta0": 1.2137222016802447, "Nd_beta1": 7.748226963005033, "Nd_Cphi": -0.01963615126026457, "Pr_beta0": 0.05879108748614492, "Pr_beta1": 0.5448324180244323, "Pr_Cphi": -0.02066999867229882, "Sm_beta0": 0.6989081585234721, "Sm_beta1": 6.877882600430561, "Sm_Cphi": -0.019920000110321332, "Y_beta0": 0.8852802073165494, "Y_beta1": 9.334653075341238, "Y_Cphi": -0.015467323909969704}

@ -0,0 +1,10 @@
,iter,best_obj,rel_diff,best_ext_h0,Nd_intercept,Nd_beta0,Nd_beta1,Pr_intercept,Pr_beta0,Pr_beta1,Ce_intercept,Ce_beta0,Ce_beta1,La_intercept,La_beta0,La_beta1,Dy_intercept,Dy_beta0,Dy_beta1,Sm_intercept,Sm_beta0,Sm_beta1,Y_intercept,Y_beta0,Y_beta1
0,0,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20
1,1,7.243881311122883e-06,21.000000000000057,-1376882.0784583509,-793959.2365328791,1.213718406400912,7.748153622541222,-805092.317983506,0.05879109101834264,0.5448322349963308,-789740.8658638337,0.2035235053232368,21.120426174002823,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794033.3277785552,0.6989082242196476,6.877882016105836,-814036.0292108656,0.8852797060008407,9.334636294454038
2,2,5.235683016217101e-06,5.0826146693579895e-05,-1376882.0784583509,-793959.2365328791,1.213718406400912,7.748153622541222,-805061.9201482645,0.05879109126451901,0.5448322298014207,-789740.8658638337,0.2035235053232368,21.120426174002823,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794023.0863911208,0.6989083059080712,6.877881736471866,-814036.0292108656,0.8852797060008407,9.334636294454038
3,3,5.234379962639123e-06,0.0004431912247434154,-1376882.0784583509,-793651.8526619686,1.213717095858249,7.748129467548838,-805038.8843481757,0.058791091500561485,0.5448322248125199,-789722.8075867157,0.20352350320923904,21.120419048363047,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794023.0863911208,0.6989083059080712,6.877881736471866,-814036.0292108656,0.8852797060008407,9.334636294454038
4,4,1.0136650760054431e-05,3.4483260160044286e-05,-1376882.0786722435,-793679.2203652804,1.213717095858249,7.748129467548838,-805038.8843481757,0.058791091500561485,0.5448322248125199,-789722.8075867157,0.20352350320923904,21.120419048363047,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794023.0863911208,0.6989083059080712,6.877881736471866,-814036.0292108656,0.8852797060008407,9.334636294454038
5,5,1.0461762551892658e-05,1.3733029030223567e-05,-1376882.079002063,-793690.1199850544,1.213717095858249,7.748129467548838,-805038.8843481757,0.058791091500561485,0.5448322248125199,-789722.8075867157,0.20352350320923904,21.120419048363047,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794023.0863911208,0.6989083059080712,6.877881736471866,-814036.0292108656,0.8852797060008407,9.334636294454038
6,6,1.0461847595183674e-05,0.0,-1376882.079002063,-793690.1199850544,1.213717095858249,7.748129467548838,-805038.8843481757,0.058791091500561485,0.5448322248125199,-789722.8075867157,0.20352350320923904,21.120419048363047,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794023.0863911208,0.6989083059080712,6.877881736471866,-814036.0292108656,0.8852797060008407,9.334636294454038
7,7,1.0568726787700163e-05,0.0,-1376882.079002063,-793690.1199850544,1.213717095858249,7.748129467548838,-805038.8843481757,0.058791091500561485,0.5448322248125199,-789722.8075867157,0.20352350320923904,21.120419048363047,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794023.0863911208,0.6989083059080712,6.877881736471866,-814036.0292108656,0.8852797060008407,9.334636294454038
8,8,1.1654800306565983e-05,0.0,-1376882.079002063,-793690.1199850544,1.213717095858249,7.748129467548838,-805038.8843481757,0.058791091500561485,0.5448322248125199,-789722.8075867157,0.20352350320923904,21.120419048363047,-797993.3842652582,1.0223168335791357,0.5296306654103653,-801345.4872245657,0.7646372240575223,7.849276225207628,-794023.0863911208,0.6989083059080712,6.877881736471866,-814036.0292108656,0.8852797060008407,9.334636294454038
1 iter best_obj rel_diff best_ext_h0 Nd_intercept Nd_beta0 Nd_beta1 Pr_intercept Pr_beta0 Pr_beta1 Ce_intercept Ce_beta0 Ce_beta1 La_intercept La_beta0 La_beta1 Dy_intercept Dy_beta0 Dy_beta1 Sm_intercept Sm_beta0 Sm_beta1 Y_intercept Y_beta0 Y_beta1
2 0 0 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20
3 1 1 7.243881311122883e-06 21.000000000000057 -1376882.0784583509 -793959.2365328791 1.213718406400912 7.748153622541222 -805092.317983506 0.05879109101834264 0.5448322349963308 -789740.8658638337 0.2035235053232368 21.120426174002823 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794033.3277785552 0.6989082242196476 6.877882016105836 -814036.0292108656 0.8852797060008407 9.334636294454038
4 2 2 5.235683016217101e-06 5.0826146693579895e-05 -1376882.0784583509 -793959.2365328791 1.213718406400912 7.748153622541222 -805061.9201482645 0.05879109126451901 0.5448322298014207 -789740.8658638337 0.2035235053232368 21.120426174002823 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794023.0863911208 0.6989083059080712 6.877881736471866 -814036.0292108656 0.8852797060008407 9.334636294454038
5 3 3 5.234379962639123e-06 0.0004431912247434154 -1376882.0784583509 -793651.8526619686 1.213717095858249 7.748129467548838 -805038.8843481757 0.058791091500561485 0.5448322248125199 -789722.8075867157 0.20352350320923904 21.120419048363047 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794023.0863911208 0.6989083059080712 6.877881736471866 -814036.0292108656 0.8852797060008407 9.334636294454038
6 4 4 1.0136650760054431e-05 3.4483260160044286e-05 -1376882.0786722435 -793679.2203652804 1.213717095858249 7.748129467548838 -805038.8843481757 0.058791091500561485 0.5448322248125199 -789722.8075867157 0.20352350320923904 21.120419048363047 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794023.0863911208 0.6989083059080712 6.877881736471866 -814036.0292108656 0.8852797060008407 9.334636294454038
7 5 5 1.0461762551892658e-05 1.3733029030223567e-05 -1376882.079002063 -793690.1199850544 1.213717095858249 7.748129467548838 -805038.8843481757 0.058791091500561485 0.5448322248125199 -789722.8075867157 0.20352350320923904 21.120419048363047 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794023.0863911208 0.6989083059080712 6.877881736471866 -814036.0292108656 0.8852797060008407 9.334636294454038
8 6 6 1.0461847595183674e-05 0.0 -1376882.079002063 -793690.1199850544 1.213717095858249 7.748129467548838 -805038.8843481757 0.058791091500561485 0.5448322248125199 -789722.8075867157 0.20352350320923904 21.120419048363047 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794023.0863911208 0.6989083059080712 6.877881736471866 -814036.0292108656 0.8852797060008407 9.334636294454038
9 7 7 1.0568726787700163e-05 0.0 -1376882.079002063 -793690.1199850544 1.213717095858249 7.748129467548838 -805038.8843481757 0.058791091500561485 0.5448322248125199 -789722.8075867157 0.20352350320923904 21.120419048363047 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794023.0863911208 0.6989083059080712 6.877881736471866 -814036.0292108656 0.8852797060008407 9.334636294454038
10 8 8 1.1654800306565983e-05 0.0 -1376882.079002063 -793690.1199850544 1.213717095858249 7.748129467548838 -805038.8843481757 0.058791091500561485 0.5448322248125199 -789722.8075867157 0.20352350320923904 21.120419048363047 -797993.3842652582 1.0223168335791357 0.5296306654103653 -801345.4872245657 0.7646372240575223 7.849276225207628 -794023.0863911208 0.6989083059080712 6.877881736471866 -814036.0292108656 0.8852797060008407 9.334636294454038

@ -0,0 +1,27 @@
,iter,best_obj,rel_diff,best_ext_h0,Nd_intercept,Nd_beta0,Nd_beta1,Pr_intercept,Pr_beta0,Pr_beta1,Ce_intercept,Ce_beta0,Ce_beta1,La_intercept,La_beta0,La_beta1,Dy_intercept,Dy_beta0,Dy_beta1,Sm_intercept,Sm_beta0,Sm_beta1,Y_intercept,Y_beta0,Y_beta1
0,0,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20,1e+20
1,1,0.03589758768077916,21.000000000000057,-1376877.1578525545,-796630.7472372957,0.7459820315595859,7.683962525237933,-804949.676541606,0.5878722433097117,5.446965040891874,-799671.8535977869,0.5683138771769763,4.330159786749355,-798281.080974753,0.05929999713109059,14.235546390790574,-805107.4528322341,0.6129648560200409,5.360202416896411,-795364.2084167162,0.5978078969216549,5.279174081605432,-814654.8936058494,0.9657036817607582,8.515030540098573
2,2,0.020523566039320422,2.5585440673715034,-1377356.1260593878,-797059.9776562914,0.7459837782866834,7.683963804574712,-807474.5742908432,0.412119358146579,0.5446965040891875,-798541.1385153377,0.5683086183011624,4.3301017748512365,-793826.8317553926,0.059179052561110786,19.77323694076803,-801913.8726103224,0.7646416177518945,7.84824568473698,-795363.0419325187,0.59780846432948,5.279183016139414,-813457.2158804197,0.8866130626375315,9.867928019371377
3,3,0.019477920445525317,7.677982352652354,-1375588.6756908477,-793163.8973856996,0.3209195035432397,13.123168416291694,-808683.1537883538,0.412118699519776,0.5446960424554511,-790111.3963314675,0.05683086183011624,23.89686703927439,-791050.7992598361,0.05905360634622211,29.84340866533762,-801427.30300279,0.5534942813794564,9.205560588460095,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
4,4,0.010207128776218969,0.42455280980920035,-1375610.9624283572,-794262.8311628923,0.3216915257810643,13.804909552933434,-808435.0647171926,0.41211840588454257,0.5446957279361009,-790207.5472086382,0.056830829357604154,23.89689998523618,-795480.9739022574,0.05878743947127101,19.151367921508545,-801426.8680903579,0.5534944284911872,9.205566903683641,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
5,5,0.014641607256599173,1.6866445651799755,-1375538.6750637838,-798938.0765541978,0.3566318051278,2.900470205622694,-805875.0643270919,0.41211840588454257,0.5446957279361009,-793436.7925485797,0.056742997228693914,13.80172079259027,-796954.8557059788,0.05868227362010503,12.498956039602165,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
6,6,0.009364477922161399,0.5171670324839205,-1375506.0331521921,-798500.5981007863,0.35663166857868867,2.9004640415749985,-807020.2949058269,0.41211840588454257,0.5446957279361009,-793926.4769803158,0.056743019042837614,13.801790803325336,-794407.3237807738,0.059071074021005275,18.80781812800432,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
7,7,0.008587420254580813,1.059528868598552,-1375505.5181543154,-798685.9967218107,0.35663172954569944,2.900465970474833,-807454.2257048099,0.41211840588454257,0.5446957279361009,-789725.2952172983,0.05719014118011185,22.726516278088134,-791396.077682103,0.05903562942413778,26.228646183949166,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
8,8,0.010436904878903537,0.29420985511692826,-1375548.1106216116,-799519.3918074799,0.35663172954569944,2.900465970474833,-808023.7799223613,0.41211840588454257,0.5446957279361009,-786951.389362888,0.05708292450340597,28.34019679365209,-791002.4212304557,0.05887049745806909,27.19304858223857,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
9,9,0.008122441324296938,0.5056025050774561,-1375532.8964810933,-799252.2437781714,0.35663172954569944,2.900465970474833,-807837.3724848758,0.41211840588454257,0.5446957279361009,-790021.4446221002,0.05689505465396167,23.449630511144804,-795447.5533695783,0.058631276343575414,18.611038118056705,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
10,10,0.012928748169505148,0.8333232355853131,-1375557.2637008368,-798461.2222513977,0.35663172954569944,2.900465970474833,-806951.4949354676,0.41211840588454257,0.5446957279361009,-795969.4556880995,0.056793906518569214,11.277961619380736,-797714.8073241808,0.05842557708316379,13.092573662989777,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
11,11,0.007800190819962697,0.36349221067564863,-1375530.569913902,-798291.6222911178,0.35663172954569944,2.900465970474833,-806824.7532982712,0.41211840588454257,0.5446957279361009,-795638.7226937105,0.0567939201459683,11.27792734701911,-795125.0133593426,0.058611088348722154,17.75722543814867,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
12,12,0.00921314263132423,1.6582390417163946,-1375352.6611008795,-799018.4755125245,0.35663172954569944,2.900465970474833,-807547.1998794067,0.41211840588454257,0.5446957279361009,-789593.3324594139,0.057780238237745564,22.7526002647588,-790289.6353698338,0.05869157014173162,28.5282029237168,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
13,13,0.0164949043385192,0.5442127617504667,-1375330.196734157,-799860.8096262615,0.35663172954569944,2.900465970474833,-808560.5669803121,0.41211840588454257,0.5446957279361009,-784843.309147467,0.05766909907971607,32.27291103838875,-788888.7517598639,0.058542471191840494,31.701224910845188,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
14,14,0.010623495713475158,0.602757119120526,-1375351.9855972743,-799632.2232496517,0.35663172954569944,2.900465970474833,-808321.7283717714,0.41211840588454257,0.5446957279361009,-788451.2944893743,0.057453027762948625,26.992114973264634,-795921.9019280333,0.058276332684925714,18.490011381032488,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
15,15,0.020076787588486848,1.0484920101715856,-1375285.2763873788,-798333.4293311803,0.35663172954569944,2.900465970474833,-806908.9647236438,0.41211840588454257,0.5446957279361009,-799190.3142882502,0.05726405467005661,2.6992114973264636,-795227.311995532,0.05860570542646566,16.240039078247854,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
16,16,0.007946994350521493,0.0013058079059853106,-1375281.5761035422,-798434.7113981954,0.35663172954569944,2.900465970474833,-806825.5999826461,0.41211840588454257,0.5446957279361009,-799709.74809272,0.05726405662551625,2.6992166442291183,-795558.7828092766,0.05860569942350758,16.24014965075902,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
17,17,0.00786340427833731,0.06642675860532837,-1375281.5757328654,-798645.9616186575,0.35663172954569944,2.900465970474833,-807277.1206417971,0.41211840588454257,0.5446957279361009,-799564.0986061025,0.05726405599313575,2.6992201079308553,-795074.773177479,0.058327655804418455,17.215637464507253,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
18,18,0.007639301074559701,0.03358010063393503,-1375274.53927792,-798757.6626722564,0.35663172954569944,2.900465970474833,-807442.731414953,0.41211840588454257,0.5446957279361009,-799932.191263451,0.05726405599313575,2.6992201079308553,-795454.173437478,0.05797530586210222,16.76361227782182,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
19,19,0.007567810584575274,0.00032734971823157984,-1375274.5400305095,-798776.6132373732,0.35663172954569944,2.900465970474833,-807407.5175994666,0.41211840588454257,0.5446957279361009,-799839.5141766575,0.05726405599313575,2.6992201079308553,-795567.5444104999,0.05797527817732809,16.763631654115574,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
20,20,0.007559522636647893,0.0003284988853867459,-1375274.539920735,-798878.7031945293,0.35663172954569944,2.900465970474833,-807474.2323978223,0.41211840588454257,0.5446957279361009,-799918.231712956,0.05726405599313575,2.6992201079308553,-795552.3072518674,0.05797526981415537,16.763625801929546,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
21,21,0.007557017666936972,0.00011741201128258779,-1375274.5398505423,-798875.2254308723,0.35663172954569944,2.900465970474833,-807474.2323978223,0.41211840588454257,0.5446957279361009,-799969.9761753903,0.05726405599313575,2.6992201079308553,-795590.7893224553,0.05797526981415537,16.763625801929546,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
22,22,0.007557912174965889,4.953375811471988e-06,-1375274.5395942358,-798879.1825600903,0.35663172954569944,2.900465970474833,-807474.2323978223,0.41211840588454257,0.5446957279361009,-799969.9761753903,0.05726405599313575,2.6992201079308553,-795590.7893224553,0.05797526981415537,16.763625801929546,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
23,23,0.007557925434292841,0.0,-1375274.5395942358,-798879.1825600903,0.35663172954569944,2.900465970474833,-807474.2323978223,0.41211840588454257,0.5446957279361009,-799969.9761753903,0.05726405599313575,2.6992201079308553,-795590.7893224553,0.05797526981415537,16.763625801929546,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
24,24,0.007557925434292841,0.0,-1375274.5395942358,-798879.1825600903,0.35663172954569944,2.900465970474833,-807474.2323978223,0.41211840588454257,0.5446957279361009,-799969.9761753903,0.05726405599313575,2.6992201079308553,-795590.7893224553,0.05797526981415537,16.763625801929546,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
25,25,0.007557925434292841,0.0,-1375274.5395942358,-798879.1825600903,0.35663172954569944,2.900465970474833,-807474.2323978223,0.41211840588454257,0.5446957279361009,-799969.9761753903,0.05726405599313575,2.6992201079308553,-795590.7893224553,0.05797526981415537,16.763625801929546,-801427.2924061618,0.5534945060571388,9.205570263716002,-795364.198868676,0.5978087854283536,5.279188087719687,-813457.2158804197,0.8866130626375315,9.867928019371377
1 iter best_obj rel_diff best_ext_h0 Nd_intercept Nd_beta0 Nd_beta1 Pr_intercept Pr_beta0 Pr_beta1 Ce_intercept Ce_beta0 Ce_beta1 La_intercept La_beta0 La_beta1 Dy_intercept Dy_beta0 Dy_beta1 Sm_intercept Sm_beta0 Sm_beta1 Y_intercept Y_beta0 Y_beta1
2 0 0 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20 1e+20
3 1 1 0.03589758768077916 21.000000000000057 -1376877.1578525545 -796630.7472372957 0.7459820315595859 7.683962525237933 -804949.676541606 0.5878722433097117 5.446965040891874 -799671.8535977869 0.5683138771769763 4.330159786749355 -798281.080974753 0.05929999713109059 14.235546390790574 -805107.4528322341 0.6129648560200409 5.360202416896411 -795364.2084167162 0.5978078969216549 5.279174081605432 -814654.8936058494 0.9657036817607582 8.515030540098573
4 2 2 0.020523566039320422 2.5585440673715034 -1377356.1260593878 -797059.9776562914 0.7459837782866834 7.683963804574712 -807474.5742908432 0.412119358146579 0.5446965040891875 -798541.1385153377 0.5683086183011624 4.3301017748512365 -793826.8317553926 0.059179052561110786 19.77323694076803 -801913.8726103224 0.7646416177518945 7.84824568473698 -795363.0419325187 0.59780846432948 5.279183016139414 -813457.2158804197 0.8866130626375315 9.867928019371377
5 3 3 0.019477920445525317 7.677982352652354 -1375588.6756908477 -793163.8973856996 0.3209195035432397 13.123168416291694 -808683.1537883538 0.412118699519776 0.5446960424554511 -790111.3963314675 0.05683086183011624 23.89686703927439 -791050.7992598361 0.05905360634622211 29.84340866533762 -801427.30300279 0.5534942813794564 9.205560588460095 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
6 4 4 0.010207128776218969 0.42455280980920035 -1375610.9624283572 -794262.8311628923 0.3216915257810643 13.804909552933434 -808435.0647171926 0.41211840588454257 0.5446957279361009 -790207.5472086382 0.056830829357604154 23.89689998523618 -795480.9739022574 0.05878743947127101 19.151367921508545 -801426.8680903579 0.5534944284911872 9.205566903683641 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
7 5 5 0.014641607256599173 1.6866445651799755 -1375538.6750637838 -798938.0765541978 0.3566318051278 2.900470205622694 -805875.0643270919 0.41211840588454257 0.5446957279361009 -793436.7925485797 0.056742997228693914 13.80172079259027 -796954.8557059788 0.05868227362010503 12.498956039602165 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
8 6 6 0.009364477922161399 0.5171670324839205 -1375506.0331521921 -798500.5981007863 0.35663166857868867 2.9004640415749985 -807020.2949058269 0.41211840588454257 0.5446957279361009 -793926.4769803158 0.056743019042837614 13.801790803325336 -794407.3237807738 0.059071074021005275 18.80781812800432 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
9 7 7 0.008587420254580813 1.059528868598552 -1375505.5181543154 -798685.9967218107 0.35663172954569944 2.900465970474833 -807454.2257048099 0.41211840588454257 0.5446957279361009 -789725.2952172983 0.05719014118011185 22.726516278088134 -791396.077682103 0.05903562942413778 26.228646183949166 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
10 8 8 0.010436904878903537 0.29420985511692826 -1375548.1106216116 -799519.3918074799 0.35663172954569944 2.900465970474833 -808023.7799223613 0.41211840588454257 0.5446957279361009 -786951.389362888 0.05708292450340597 28.34019679365209 -791002.4212304557 0.05887049745806909 27.19304858223857 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
11 9 9 0.008122441324296938 0.5056025050774561 -1375532.8964810933 -799252.2437781714 0.35663172954569944 2.900465970474833 -807837.3724848758 0.41211840588454257 0.5446957279361009 -790021.4446221002 0.05689505465396167 23.449630511144804 -795447.5533695783 0.058631276343575414 18.611038118056705 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
12 10 10 0.012928748169505148 0.8333232355853131 -1375557.2637008368 -798461.2222513977 0.35663172954569944 2.900465970474833 -806951.4949354676 0.41211840588454257 0.5446957279361009 -795969.4556880995 0.056793906518569214 11.277961619380736 -797714.8073241808 0.05842557708316379 13.092573662989777 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
13 11 11 0.007800190819962697 0.36349221067564863 -1375530.569913902 -798291.6222911178 0.35663172954569944 2.900465970474833 -806824.7532982712 0.41211840588454257 0.5446957279361009 -795638.7226937105 0.0567939201459683 11.27792734701911 -795125.0133593426 0.058611088348722154 17.75722543814867 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
14 12 12 0.00921314263132423 1.6582390417163946 -1375352.6611008795 -799018.4755125245 0.35663172954569944 2.900465970474833 -807547.1998794067 0.41211840588454257 0.5446957279361009 -789593.3324594139 0.057780238237745564 22.7526002647588 -790289.6353698338 0.05869157014173162 28.5282029237168 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
15 13 13 0.0164949043385192 0.5442127617504667 -1375330.196734157 -799860.8096262615 0.35663172954569944 2.900465970474833 -808560.5669803121 0.41211840588454257 0.5446957279361009 -784843.309147467 0.05766909907971607 32.27291103838875 -788888.7517598639 0.058542471191840494 31.701224910845188 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
16 14 14 0.010623495713475158 0.602757119120526 -1375351.9855972743 -799632.2232496517 0.35663172954569944 2.900465970474833 -808321.7283717714 0.41211840588454257 0.5446957279361009 -788451.2944893743 0.057453027762948625 26.992114973264634 -795921.9019280333 0.058276332684925714 18.490011381032488 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
17 15 15 0.020076787588486848 1.0484920101715856 -1375285.2763873788 -798333.4293311803 0.35663172954569944 2.900465970474833 -806908.9647236438 0.41211840588454257 0.5446957279361009 -799190.3142882502 0.05726405467005661 2.6992114973264636 -795227.311995532 0.05860570542646566 16.240039078247854 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
18 16 16 0.007946994350521493 0.0013058079059853106 -1375281.5761035422 -798434.7113981954 0.35663172954569944 2.900465970474833 -806825.5999826461 0.41211840588454257 0.5446957279361009 -799709.74809272 0.05726405662551625 2.6992166442291183 -795558.7828092766 0.05860569942350758 16.24014965075902 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
19 17 17 0.00786340427833731 0.06642675860532837 -1375281.5757328654 -798645.9616186575 0.35663172954569944 2.900465970474833 -807277.1206417971 0.41211840588454257 0.5446957279361009 -799564.0986061025 0.05726405599313575 2.6992201079308553 -795074.773177479 0.058327655804418455 17.215637464507253 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
20 18 18 0.007639301074559701 0.03358010063393503 -1375274.53927792 -798757.6626722564 0.35663172954569944 2.900465970474833 -807442.731414953 0.41211840588454257 0.5446957279361009 -799932.191263451 0.05726405599313575 2.6992201079308553 -795454.173437478 0.05797530586210222 16.76361227782182 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
21 19 19 0.007567810584575274 0.00032734971823157984 -1375274.5400305095 -798776.6132373732 0.35663172954569944 2.900465970474833 -807407.5175994666 0.41211840588454257 0.5446957279361009 -799839.5141766575 0.05726405599313575 2.6992201079308553 -795567.5444104999 0.05797527817732809 16.763631654115574 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
22 20 20 0.007559522636647893 0.0003284988853867459 -1375274.539920735 -798878.7031945293 0.35663172954569944 2.900465970474833 -807474.2323978223 0.41211840588454257 0.5446957279361009 -799918.231712956 0.05726405599313575 2.6992201079308553 -795552.3072518674 0.05797526981415537 16.763625801929546 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
23 21 21 0.007557017666936972 0.00011741201128258779 -1375274.5398505423 -798875.2254308723 0.35663172954569944 2.900465970474833 -807474.2323978223 0.41211840588454257 0.5446957279361009 -799969.9761753903 0.05726405599313575 2.6992201079308553 -795590.7893224553 0.05797526981415537 16.763625801929546 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
24 22 22 0.007557912174965889 4.953375811471988e-06 -1375274.5395942358 -798879.1825600903 0.35663172954569944 2.900465970474833 -807474.2323978223 0.41211840588454257 0.5446957279361009 -799969.9761753903 0.05726405599313575 2.6992201079308553 -795590.7893224553 0.05797526981415537 16.763625801929546 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
25 23 23 0.007557925434292841 0.0 -1375274.5395942358 -798879.1825600903 0.35663172954569944 2.900465970474833 -807474.2323978223 0.41211840588454257 0.5446957279361009 -799969.9761753903 0.05726405599313575 2.6992201079308553 -795590.7893224553 0.05797526981415537 16.763625801929546 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
26 24 24 0.007557925434292841 0.0 -1375274.5395942358 -798879.1825600903 0.35663172954569944 2.900465970474833 -807474.2323978223 0.41211840588454257 0.5446957279361009 -799969.9761753903 0.05726405599313575 2.6992201079308553 -795590.7893224553 0.05797526981415537 16.763625801929546 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377
27 25 25 0.007557925434292841 0.0 -1375274.5395942358 -798879.1825600903 0.35663172954569944 2.900465970474833 -807474.2323978223 0.41211840588454257 0.5446957279361009 -799969.9761753903 0.05726405599313575 2.6992201079308553 -795590.7893224553 0.05797526981415537 16.763625801929546 -801427.2924061618 0.5534945060571388 9.205570263716002 -795364.198868676 0.5978087854283536 5.279188087719687 -813457.2158804197 0.8866130626375315 9.867928019371377

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After

Width:  |  Height:  |  Size: 11 KiB

@ -0,0 +1,716 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org) Pr(H(A)2)3(org) Ce(H(A)2)3(org) La(H(A)2)3(org) Dy(H(A)2)3(org) Sm(H(A)2)3(org) Y(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-1377917.5269485628</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.320974226079</molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-4929625.060282971</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.973500071223</molarVolume>
</standardState>
</species>
<species name="Pr(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Pr:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-4941397.084772181</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.979936421078</molarVolume>
</standardState>
</species>
<species name="Ce(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Ce:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-4932551.489263242</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">1.0060487218</molarVolume>
</standardState>
</species>
<species name="La(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 La:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-4935194.142426379</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.981485801577</molarVolume>
</standardState>
</species>
<species name="Dy(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Dy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-4935179.480883835</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.961666360676</molarVolume>
</standardState>
</species>
<species name="Y(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Y:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-4947210.070800013</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.958888814485</molarVolume>
</standardState>
</species>
<species name="Sm(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Sm:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 19:20 7-29-2020">-4929116.779371853</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.9642 </molarVolume>
</standardState>
</species>
<species name="Gd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Gd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="yep">-4829446.858</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume>0.9642</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++ Pr+++ Ce+++ La+++ Dy+++ Sm+++ Y+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Pr+++">
<beta0 updated="Updated at 19:20 7-29-2020"> 0.058791077174068576, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 19:20 7-29-2020"> 0.5448320238819658, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 19:20 7-29-2020"> -0.02066999867229882, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Nd+++">
<beta0 updated="Updated at 19:20 7-29-2020"> 1.0825315776813356, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 19:20 7-29-2020"> 6.211262701179254, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 19:20 7-29-2020"> -0.01963615126026457, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="La+++">
<beta0 updated="Updated at 19:20 7-29-2020"> 0.5930048961782302, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 19:20 7-29-2020"> 5.2771447352927785, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 19:20 7-29-2020"> -0.024339999997603376, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Dy+++">
<beta0 updated="Updated at 19:20 7-29-2020"> 0.5532852863195881, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 19:20 7-29-2020"> 9.206787175138805, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 19:20 7-29-2020"> -0.019699989216349984, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Ce+++">
<beta0 updated="Updated at 19:20 7-29-2020"> 0.6005020116531858, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 19:20 7-29-2020"> 4.91004437191519, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 19:20 7-29-2020"> -0.02618999999473301, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Y+++">
<beta0 updated="Updated at 19:20 7-29-2020"> 0.8866269789489127, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 19:20 7-29-2020"> 9.867663759220948, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 19:20 7-29-2020"> -0.015467323909969704, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Sm+++">
<beta0 updated="Updated at 19:20 7-29-2020"> 0.5978087860273482, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 19:20 7-29-2020"> 5.279188095059934, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 19:20 7-29-2020"> -0.019920000110321332, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,716 @@
<ctml>
<validate reactions="yes" species="yes" />
<phase dim="3" id="PC88A_liquid">
<elementArray datasrc="elementz.xml">
Cl O H C P Nd Pr Ce La Dy Y Sm dummy
</elementArray>
<speciesArray datasrc="#species_PC88A_liquid">
(HA)2(org) dodecane Nd(H(A)2)3(org) Pr(H(A)2)3(org) Ce(H(A)2)3(org) La(H(A)2)3(org) Dy(H(A)2)3(org) Sm(H(A)2)3(org) Y(H(A)2)3(org)
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
(HA)2(org): 0.25
</soluteMolalities>
</state>
<thermo model="IdealSolidSolution">
<standardConc model="molar_volume" />
</thermo>
<standardConc model="molar_volume" />
<transport model="None" />
<kinetics model="none" />
</phase>
<speciesData id="species_PC88A_liquid">
<species name="(HA)2(org)">
<atomArray> C:16 H:35 O:3 P:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-1376882.3191117246</h0>
<s0 units="J/mol/K"> 558.9824 </s0>
<cp0 units="J/mol/K"> 0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.320974226079</molarVolume>
</standardState>
</species>
<species name="Nd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Nd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-4925566.309854757</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.973500071223</molarVolume>
</standardState>
</species>
<species name="Pr(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Pr:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-4938249.845712334</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.979936421078</molarVolume>
</standardState>
</species>
<species name="Ce(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Ce:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-4920387.823199008</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">1.0060487218</molarVolume>
</standardState>
</species>
<species name="La(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 La:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-4933548.865580005</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.981485801577</molarVolume>
</standardState>
</species>
<species name="Dy(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Dy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-4932560.171447597</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.961666360676</molarVolume>
</standardState>
</species>
<species name="Y(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Y:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-4944840.781582316</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume updated="Updated at 21:02:32">0.958888814485</molarVolume>
</standardState>
</species>
<species name="Sm(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Sm:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="Updated at 11:58 7-17-2020">-4924696.189921901</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.9642 </molarVolume>
</standardState>
</species>
<species name="Gd(H(A)2)3(org)">
<atomArray> C:48 H:102 O:9 P:3 Gd:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol" updated="yep">-4829446.858</h0>
<s0 units="J/mol/K"> 1117.965 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume>0.9642</molarVolume>
</standardState>
</species>
<species name="dodecane">
<atomArray> dummy:1 </atomArray>
<thermo>
<const_cp Tmax="300.0" Tmin="298.0">
<t0 units="K">298.14999999999998</t0>
<h0 units="J/mol"> 0.0 </h0>
<s0 units="J/mol/K"> 0.0 </s0>
<cp0 units="J/mol/K">0.0</cp0>
</const_cp>
</thermo>
<standardState model="constant_incompressible">
<molarVolume> 0.227113 </molarVolume>
</standardState>
</species>
</speciesData>
<phase dim="3" id="HCl_electrolyte">
<speciesArray datasrc="#species_waterSolution">
H2O(L) H+ OH- Cl- Nd+++ Pr+++ Ce+++ La+++ Dy+++ Sm+++ Y+++
</speciesArray>
<state>
<temperature units="K"> 298.15 </temperature>
<pressure units="Pa"> 100000.0 </pressure>
<soluteMolalities>
Cl-: 1.0E-7
H+: 1.0E-7
</soluteMolalities>
</state>
<thermo model="HMW">
<standardConc model="solvent_volume" />
<activityCoefficients TempModel="complex1" model="Pitzer">
<A_Debye model="water" />
<ionicRadius default="3.042843" units="Angstroms">
</ionicRadius>
<binarySaltParameters anion="Cl-" cation="H+">
<beta0> 0.177000779, 0.000125778, 0.0, -33.4777082, -0.262214535 </beta0>
<beta1> 0.292922504, -0.027938838, 0.0, 3402.47027, 19.7936248 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi> 0.000362, -0.00003036, 0.0, -2.91038E-11, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 12 </Alpha2>
<source>
refit of Holmes, H.F., Busey, J.M., Simonson, J.M., Mesmer, R.E.,
Archer, D.G., and Wood, R.H., 1987, The enthalpy of dilution of HCl(aq)
to 648 K and 4p MPa. Thermodynamic properties, Journal of Chemical
Thermodynamics, v. 19, p. 863-890.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Pr+++">
<beta0 updated="Updated at 11:58 7-17-2020"> 0.05879108748614492, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:58 7-17-2020"> 0.5448324180244323, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 10:47 7-17-2020"> -0.02066999867229882, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Nd+++">
<beta0 updated="Updated at 11:58 7-17-2020"> 1.2137222016802447, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:58 7-17-2020"> 7.748226963005033, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 10:47 7-17-2020"> -0.01963615126026457, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="La+++">
<beta0 updated="Updated at 11:58 7-17-2020"> 1.022316535866388, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:58 7-17-2020"> 0.5296311209773129, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 10:47 7-17-2020"> -0.024339999997603376, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Dy+++">
<beta0 updated="Updated at 11:58 7-17-2020"> 0.7646397332938777, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:58 7-17-2020"> 7.849320590516409, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 10:47 7-17-2020"> -0.019699989216349984, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Ce+++">
<beta0 updated="Updated at 11:58 7-17-2020"> 0.2035235053232368, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:58 7-17-2020"> 21.120426174002823, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 10:47 7-17-2020"> -0.02618999999473301, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Y+++">
<beta0 updated="Updated at 11:58 7-17-2020"> 0.8852802073165494, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:58 7-17-2020"> 9.334653075341238, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 10:47 7-17-2020"> -0.015467323909969704, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
<binarySaltParameters anion="Cl-" cation="Sm+++">
<beta0 updated="Updated at 11:58 7-17-2020"> 0.6989081585234721, 0.0, 0.0, 0.0, 0.0 </beta0>
<beta1 updated="Updated at 11:58 7-17-2020"> 6.877882600430561, 0.0, 0.0, 0.0, 0.0 </beta1>
<beta2> 0.0, 0.0, 0.0, 0.0, 0.0 </beta2>
<Cphi updated="Updated at 10:47 7-17-2020"> -0.019920000110321332, 0.0, 0.0, 0.0, 0.0 </Cphi>
<Alpha1> 2 </Alpha1>
<Alpha2> 0 </Alpha2>
<source>
Table S1: Pitzer parameters for osmotic and activity coeff Supp Info.
May, P. M.; Rowland, D.; Hefter, G.; Konigsberger, E.
A generic and updatable Pitzer characterization of aqueous binary electrolyte
solutions at 1 bar and 25 C.
Journal of Chemical and Engineering Data 2011,56, 5066&#8211;5077.
</source>
</binarySaltParameters>
</activityCoefficients>
<solvent> H2O(L) </solvent>
</thermo>
<elementArray datasrc="elementz.xml"> O H Nd Pr Ce La Dy Y Sm C N Cl P E </elementArray>
<kinetics model="none">
</kinetics>
</phase>
<speciesData id="species_waterSolution">
<species name="H2O(L)">
<atomArray>H:2 O:1 </atomArray>
<thermo>
<NASA P0="100000.0" Tmax="600.0" Tmin="273.14999999999998">
<floatArray name="coeffs" size="7">
7.255750050E+01, -6.624454020E-01, 2.561987460E-03, -4.365919230E-06,
2.781789810E-09, -4.188654990E+04, -2.882801370E+02
</floatArray>
</NASA>
</thermo>
<standardState model="waterPDSS">
<molarVolume> 0.018068 </molarVolume>
</standardState>
</species>
<species name="OH-">
<speciesChemFormula> OH- </speciesChemFormula>
<atomArray> O:1 H:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -37595 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -54977 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -2.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.12527 </a1>
<a2 units="cal/gmol"> 7.38 </a2>
<a3 units="cal-K/gmol/bar"> 1.8423 </a3>
<a4 units="cal-K/gmol"> -27821 </a4>
<c1 units="cal/gmol/K"> 4.15 </c1>
<c2 units="cal-K/gmol"> -103460 </c2>
<omega_Pr_Tr units="cal/gmol"> 172460 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -4.18 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="NO3-">
<speciesChemFormula> NO3- </speciesChemFormula>
<atomArray> N:1 O:3 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -26507 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -49429 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> 35.12 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> 0.73161 </a1>
<a2 units="cal/gmol"> 678.24 </a2>
<a3 units="cal-K/gmol/bar"> -4.6838 </a3>
<a4 units="cal-K/gmol"> -30594 </a4>
<c1 units="cal/gmol/K"> 7.7 </c1>
<c2 units="cal-K/gmol"> -67250 </c2>
<omega_Pr_Tr units="cal/gmol"> 109770 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 29.0 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Cl-">
<speciesChemFormula> Cl- </speciesChemFormula>
<atomArray> Cl:1 </atomArray>
<charge> -1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> -31379 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> -39933 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 13.56 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0.4032 </a1>
<a2 units="cal/mol"> 480.1 </a2>
<a3 units="cal-K/mol/bar"> 5.563 </a3>
<a4 units="cal-K/mol"> -28470 </a4>
<c1 units="cal/mol/K"> -4.4 </c1>
<c2 units="cal-K/mol"> -57140 </c2>
<omega_Pr_Tr units="cal/mol"> 145600 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 17.79 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="H+">
<speciesChemFormula> H+ </speciesChemFormula>
<atomArray> H:1 </atomArray>
<charge> +1 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="273.15">
<DG0_f_Pr_Tr units="cal/gmol"> 0 </DG0_f_Pr_Tr>
<DH0_f_Pr_TR units="cal/gmol"> 0 </DH0_f_Pr_TR>
<S0_Pr_Tr units="cal/gmol/K"> 0 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/mol/bar"> 0 </a1>
<a2 units="cal/mol"> 0 </a2>
<a3 units="cal-K/mol/bar"> 0 </a3>
<a4 units="cal-K/mol"> 0 </a4>
<c1 units="cal/mol/K"> 0 </c1>
<c2 units="cal-K/mol"> 0 </c2>
<omega_Pr_Tr units="cal/mol"> 0 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> 0 </molarVolume>
</standardState>
<source> ref:G9 </source>
</species>
<species name="Nd+++">
<speciesChemFormula> Nd+++ </speciesChemFormula>
<atomArray> Nd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -160600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.5 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.33707 </a1>
<a2 units="cal/gmol"> -1454.52 </a2>
<a3 units="cal-K/gmol/bar"> 8.3211 </a3>
<a4 units="cal-K/gmol"> -21777 </a4>
<c1 units="cal/gmol/K"> 1.6236 </c1>
<c2 units="cal-K/gmol"> -118344 </c2>
<omega_Pr_Tr units="cal/gmol"> 225500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -43.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Pr+++">
<speciesChemFormula> Pr+++ </speciesChemFormula>
<atomArray> Pr:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -162600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -168800 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32406 </a1>
<a2 units="cal/gmol"> -1419.98 </a2>
<a3 units="cal-K/gmol/bar"> 8.1257 </a3>
<a4 units="cal-K/gmol"> -21920 </a4>
<c1 units="cal/gmol/K"> -1.1975 </c1>
<c2 units="cal-K/gmol"> -127511 </c2>
<omega_Pr_Tr units="cal/gmol"> 223500 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -42.1 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Ce+++">
<speciesChemFormula> Ce+++ </speciesChemFormula>
<atomArray> Ce:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -161600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -167400 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29292 </a1>
<a2 units="cal/gmol"> -1493.38 </a2>
<a3 units="cal-K/gmol/bar"> 11.6196 </a3>
<a4 units="cal-K/gmol"> -21616 </a4>
<c1 units="cal/gmol/K"> 4.0445 </c1>
<c2 units="cal-K/gmol"> -108974 </c2>
<omega_Pr_Tr units="cal/gmol"> 222510 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -39.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="La+++">
<speciesChemFormula> La+++ </speciesChemFormula>
<atomArray> La:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -164000 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -169600 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -52 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.2788 </a1>
<a2 units="cal/gmol"> -1438.24 </a2>
<a3 units="cal-K/gmol/bar"> 10.9602 </a3>
<a4 units="cal-K/gmol"> -21844 </a4>
<c1 units="cal/gmol/K"> 4.2394 </c1>
<c2 units="cal-K/gmol"> -106122 </c2>
<omega_Pr_Tr units="cal/gmol"> 215720 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -38.6 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Dy+++">
<speciesChemFormula> Dy+++ </speciesChemFormula>
<atomArray> Dy:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158700 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -166500 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -55.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30003 </a1>
<a2 units="cal/gmol"> -1510.74 </a2>
<a3 units="cal-K/gmol/bar"> 11.6879 </a3>
<a4 units="cal-K/gmol"> -21545 </a4>
<c1 units="cal/gmol/K"> 9.5076 </c1>
<c2 units="cal-K/gmol"> -94919 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.7 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Y+++">
<speciesChemFormula> Y+++ </speciesChemFormula>
<atomArray> Y:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -163800 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -170900 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -60 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.30140 </a1>
<a2 units="cal/gmol"> -1514.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.7010 </a3>
<a4 units="cal-K/gmol"> -21531 </a4>
<c1 units="cal/gmol/K"> 7.1634 </c1>
<c2 units="cal-K/gmol"> -103067 </c2>
<omega_Pr_Tr units="cal/gmol"> 237920 </omega_Pr_Tr>
<molarVolume units="cm3/mol"> -40.8 </molarVolume>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Sm+++">
<speciesChemFormula> Sm+++ </speciesChemFormula>
<atomArray> Sm:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -159100 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -165200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -50.7 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.32065 </a1>
<a2 units="cal/gmol"> -1561.08 </a2>
<a3 units="cal-K/gmol/bar"> 11.8857 </a3>
<a4 units="cal-K/gmol"> -21337 </a4>
<c1 units="cal/gmol/K"> 1.9385 </c1>
<c2 units="cal-K/gmol"> -118548 </c2>
<omega_Pr_Tr units="cal/gmol"> 229550 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
<species name="Gd+++">
<speciesChemFormula> Gd+++ </speciesChemFormula>
<atomArray> Gd:1 </atomArray>
<charge> +3 </charge>
<thermo model="HKFT">
<HKFT Pref="1 atm" Tmax="625.15" Tmin="298.15">
<DG0_f_Pr_Tr units="cal/gmol"> -158600 </DG0_f_Pr_Tr>
<DH0_f_Pr_Tr units="cal/gmol"> -164200 </DH0_f_Pr_Tr>
<S0_Pr_Tr units="cal/gmol/K"> -49.2 </S0_Pr_Tr>
</HKFT>
</thermo>
<standardState model="HKFT">
<a1 units="cal/gmol/bar"> -0.29771 </a1>
<a2 units="cal/gmol"> -1505.06 </a2>
<a3 units="cal-K/gmol/bar"> 11.6656 </a3>
<a4 units="cal-K/gmol"> -21568 </a4>
<c1 units="cal/gmol/K"> 6.5606 </c1>
<c2 units="cal-K/gmol"> -103474 </c2>
<omega_Pr_Tr units="cal/gmol"> 232650 </omega_Pr_Tr>
</standardState>
<source>
ref:G9
</source>
</species>
</speciesData>
</ctml>

@ -0,0 +1,330 @@
# This file tests adding 0.1 M NaCl to the feed.
import llepe
import pandas as pd
import numpy as np
import json
import matplotlib as plt
import matplotlib
import cantera as ct
class ModLLEPE(llepe.LLEPE):
def __init__(self,
exp_data,
phases_xml_filename,
phase_names,
aq_solvent_name,
extractant_name,
diluant_name,
complex_names,
extracted_species_ion_names,
extracted_species_list=None,
aq_solvent_rho=None,
extractant_rho=None,
diluant_rho=None,
opt_dict=None,
objective_function='Log-MSE',
optimizer='scipy_minimize',
temp_xml_file_path=None,
dependant_params_dict=None,
custom_objects_dict=None,
nacl_molarity=0):
self.nacl_molarity = nacl_molarity
super().__init__(exp_data,
phases_xml_filename,
phase_names,
aq_solvent_name,
extractant_name,
diluant_name,
complex_names,
extracted_species_ion_names,
extracted_species_list,
aq_solvent_rho,
extractant_rho,
diluant_rho,
opt_dict,
objective_function,
optimizer,
temp_xml_file_path,
dependant_params_dict,
custom_objects_dict)
def set_in_moles(self, feed_vol):
"""Function that initializes mole fractions to input feed_vol
This function is called at initialization
Sets in_moles to a pd.DataFrame containing initial mole fractions
Columns for species and rows for different experiments
This function also calls update_predicted_dict
:param feed_vol: (float) feed volume of mixture (L)
"""
phases_copy = self._phases.copy()
exp_df = self._exp_df.copy()
solvent_name = self._aq_solvent_name
extractant_name = self._extractant_name
diluant_name = self._diluant_name
solvent_rho = self._aq_solvent_rho
extractant_rho = self._extractant_rho
diluant_rho = self._diluant_rho
extracted_species_names = self._extracted_species_ion_names
extracted_species_list = self._extracted_species_list
mixed = ct.Mixture(phases_copy)
aq_ind = None
solvent_ind = None
for ind, phase in enumerate(phases_copy):
if solvent_name in phase.species_names:
aq_ind = ind
solvent_ind = phase.species_names.index(solvent_name)
if aq_ind is None:
raise Exception('Solvent "{0}" not found \
in xml file'.format(solvent_name))
if aq_ind == 0:
org_ind = 1
else:
org_ind = 0
self._aq_ind = aq_ind
self._org_ind = org_ind
extractant_ind = phases_copy[org_ind].species_names.index(
extractant_name)
diluant_ind = phases_copy[org_ind].species_names.index(
diluant_name)
extracted_species_ind_list = [
phases_copy[aq_ind].species_names.index(
extracted_species_name)
for extracted_species_name in extracted_species_names]
extracted_species_charges = np.array(
[phases_copy[aq_ind].species(
extracted_species_ind).charge
for extracted_species_ind in extracted_species_ind_list])
self._extracted_species_charges = extracted_species_charges
mix_aq = mixed.phase(aq_ind)
mix_org = mixed.phase(org_ind)
solvent_mw = mix_aq.molecular_weights[solvent_ind] # g/mol
extractant_mw = mix_org.molecular_weights[extractant_ind]
diluant_mw = mix_org.molecular_weights[diluant_ind]
if solvent_rho is None:
solvent_rho = mix_aq(aq_ind).partial_molar_volumes[
solvent_ind] / solvent_mw * 1e6 # g/L
self._aq_solvent_rho = solvent_rho
if extractant_rho is None:
extractant_rho = mix_org(org_ind).partial_molar_volumes[
extractant_ind] / extractant_mw * 1e6
self._extractant_rho = extractant_rho
if diluant_rho is None:
diluant_rho = mix_org(org_ind).partial_molar_volumes[
extractant_ind] / extractant_mw * 1e6
self._diluant_rho = diluant_rho
in_moles_data = []
aq_phase_solvent_moles = feed_vol * solvent_rho / solvent_mw
for index, row in exp_df.iterrows():
h_plus_moles = feed_vol * row['h_i']
hydroxide_ions = 0
extracted_species_moles = np.array(
[feed_vol * row['{0}_aq_i'.format(
extracted_species)]
for extracted_species in extracted_species_list])
extracted_species_charge_sum = np.sum(
extracted_species_charges * extracted_species_moles)
chlorine_moles = extracted_species_charge_sum + h_plus_moles
extractant_moles = feed_vol * row['z_i']
extractant_vol = extractant_moles * extractant_mw / extractant_rho
diluant_vol = feed_vol - extractant_vol
diluant_moles = diluant_vol * diluant_rho / diluant_mw
complex_moles = np.zeros(len(extracted_species_list))
species_moles_aq = [aq_phase_solvent_moles,
h_plus_moles,
hydroxide_ions,
chlorine_moles]
species_moles_aq.extend(list(extracted_species_moles))
species_moles_aq.append(self.nacl_molarity * feed_vol)
species_moles_aq[3] += self.nacl_molarity * feed_vol
species_moles_org = [extractant_moles, diluant_moles]
species_moles_org.extend(list(complex_moles))
if aq_ind == 0:
species_moles = species_moles_aq + species_moles_org
else:
species_moles = species_moles_org + species_moles_aq
in_moles_data.append(species_moles)
self._in_moles = pd.DataFrame(
in_moles_data, columns=mixed.species_names)
self.update_predicted_dict()
return None
font = {'family': 'sans serif',
'size': 24}
matplotlib.rc('font', **font)
plt.rc('xtick', labelsize=18)
plt.rc('ytick', labelsize=18)
plt.rcParams['lines.linewidth'] = 4
matplotlib.rcParams['lines.markersize'] = 10
def ext_to_complex(h0, custom_obj_dict, mini_species):
linear_params = custom_obj_dict['lin_param_df']
row = linear_params[linear_params['species'] == mini_species]
return row['slope'].values[0] * h0[0] + row['intercept'].values[0]
def mod_lin_param_df(lp_df, input_val, mini_species, mini_lin_param):
new_lp_df = lp_df.copy()
index = new_lp_df.index[new_lp_df['species'] == mini_species].tolist()[0]
new_lp_df.at[index, mini_lin_param] = input_val
return new_lp_df
info_df = pd.read_csv('outputs/multi_only_iterative_fitter_output.csv')
test_row = -1
pitzer_params_filename = "../../data/jsons/min_h0_pitzer_params.txt"
with open(pitzer_params_filename) as file:
pitzer_params_dict = json.load(file)
pitzer_params_df = pd.DataFrame(pitzer_params_dict)
species_list = 'Nd,Pr,Ce,La,Dy,Sm,Y'.split(',')
pitzer_param_list = ['beta0', 'beta1']
labeled_data = pd.read_csv("../../data/csvs/"
"no_formiga_or_5_oa_PC88A_HCL_NdPrCeLaDySmY.csv")
labeled_data = labeled_data.sort_values(['Feed Pr[M]', 'Feed Ce[M]'],
ascending=True)
exp_data = labeled_data.drop(labeled_data.columns[0], axis=1)
xml_file = "test_PC88A_HCL_NdPrCeLaDySmY_w_pitzer.xml"
lin_param_df = pd.read_csv("../../data/csvs"
"/zeroes_removed_min_h0_pitzer_lin_params.csv")
estimator_params = {'exp_data': exp_data,
'phases_xml_filename': xml_file,
'phase_names': ['HCl_electrolyte', 'PC88A_liquid'],
'aq_solvent_name': 'H2O(L)',
'extractant_name': '(HA)2(org)',
'diluant_name': 'dodecane',
'complex_names': ['{0}(H(A)2)3(org)'.format(species)
for species in species_list],
'extracted_species_ion_names': ['{0}+++'.format(species)
for species in
species_list],
'aq_solvent_rho': 1000.0,
'extractant_rho': 960.0,
'diluant_rho': 750.0,
'temp_xml_file_path': 'outputs/temp.xml',
'objective_function': llepe.lmse_perturbed_obj,
'nacl_molarity': 0
}
dependant_params_dict = {}
for species, complex_name in zip(species_list,
estimator_params['complex_names']):
inner_dict = {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': complex_name,
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'function': ext_to_complex,
'kwargs': {"mini_species": species},
'independent_params': '(HA)2(org)_h0'}
dependant_params_dict['{0}_h0'.format(complex_name)] = inner_dict
info_dict = {'(HA)2(org)_h0': {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': '(HA)2(org)',
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'input_value':
info_df.iloc[test_row, :]['best_ext_h0']}}
for species in species_list:
for pitzer_param in pitzer_param_list:
pitzer_str = "{0}_{1}".format(species, pitzer_param)
value = info_df.iloc[test_row, :][pitzer_str]
pitzer_params_dict[pitzer_str]['input_value'] = value
lin_str = "{0}_slope".format(species)
inner_dict = {'custom_object_name': 'lin_param_df',
'function': mod_lin_param_df,
'kwargs': {'mini_species': species,
'mini_lin_param': 'slope'},
'input_value': 3
}
info_dict[lin_str] = inner_dict
lin_str = "{0}_intercept".format(species)
value = info_df.iloc[test_row, :][lin_str]
inner_dict = {'custom_object_name': 'lin_param_df',
'function': mod_lin_param_df,
'kwargs': {'mini_species': species,
'mini_lin_param': 'intercept'},
'input_value': value
}
info_dict[lin_str] = inner_dict
info_dict.update(pitzer_params_dict)
estimator = ModLLEPE(**estimator_params)
estimator.set_custom_objects_dict({'lin_param_df': lin_param_df})
estimator.update_custom_objects_dict(info_dict)
estimator.update_xml(info_dict,
dependant_params_dict=dependant_params_dict)
exp_data = estimator.get_exp_df()
feed_cols = []
for col in exp_data.columns:
if 'aq_i' in col:
feed_cols.append(col)
exp_data['total_re'] = exp_data[feed_cols].sum(axis=1)
label_list = []
for index, row in exp_data[feed_cols].iterrows():
bool_list = list((row > 0).values)
label = ''
for species, el in zip(species_list, bool_list):
if el:
label = '{0}-{1}'.format(label, species)
label = label[1:]
label_list.append(label)
r2s = ""
for species in species_list:
# if species=='La':
# save_name = 'outputs' \
# '/parity_iterative_fitter_{0}_org_eq'.format(species)
save_name = None
# fig, ax = estimator.parity_plot('{0}_org_eq'.format(species),
# c_data='z_i',
# c_label='Feed total RE '
# 'molarity (mol/L)',
# print_r_squared=True,
# save_path=save_name)
r2s += str(estimator.r_squared('{0}_org_eq'.format(species))) + ','
fig, ax = estimator.parity_plot('{0}_org_eq'.format(species),
data_labels=list(labeled_data['label']),
print_r_squared=True,
save_path=save_name)
ax.legend(loc=4)
pred_df = pd.DataFrame(estimator.get_predicted_dict())
new_cols = []
for col in pred_df.columns:
new_cols.append("pred_{0}".format(col))
pred_df.columns = new_cols
new_cols = ['label',
'h_i',
'h_eq',
'z_i',
'z_eq'
]
for species in species_list:
new_cols.append("{0}_aq_i".format(species))
new_cols.append("{0}_aq_eq".format(species))
new_cols.append("{0}_d_eq".format(species))
labeled_data.columns = new_cols
total_df = labeled_data.join(pred_df)
# total_df.to_csv('if_mse_total_df.csv')
# short_info_dict = {}
# for key, value in info_dict.items():
# short_info_dict[key] = value['input_value']
# with open("outputs/iterative_fitter_short_info_dict.txt", 'w') as file:
# json.dump(short_info_dict, file)

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<!DOCTYPE html>
<!--[if IE 8]><html class="no-js lt-ie9" lang="python" > <![endif]-->
<!--[if gt IE 8]><!--> <html class="no-js" lang="python" > <!--<![endif]-->
<head>
<meta charset="utf-8">
<meta name="viewport" content="width=device-width, initial-scale=1.0">
<title>Overview: module code &mdash; LLEPE 1.0.0 documentation</title>
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<script type="text/javascript" id="documentation_options" data-url_root="../" src="../_static/documentation_options.js"></script>
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<p class="caption"><span class="caption-text">User Guide</span></p>
<ul>
<li class="toctree-l1"><a class="reference internal" href="../guide/install.html">Installation</a></li>
<li class="toctree-l1"><a class="reference internal" href="../guide/quickstart.html">Getting Started</a></li>
</ul>
<p class="caption"><span class="caption-text">Searchers</span></p>
<ul>
<li class="toctree-l1"><a class="reference internal" href="../modules/reeps.html">LLEPE</a></li>
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<h1>All modules for which code is available</h1>
<ul><li><a href="llepe/llepe.html">llepe.llepe</a></li>
<li><a href="reeps/reeps.html">reeps.reeps</a></li>
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.. _install:
************
Installation
************
Prerequisites
=============
LLEPE requires python3 (>=3.5) with the development headers.
Stable Release
==============
There is currently no stable release
Bleeding-edge version
=====================
To install the latest master version:
.. code-block:: bash
pip install git+https://xgitlab.cels.anl.gov/summer-2020/parameter-estimation.git
Development version
===================
To contribute to Stable-Baselines, with support for running tests and building the documentation.
.. code-block:: bash
git clone https://xgitlab.cels.anl.gov/summer-2020/parameter-estimation.git && cd parameter-estimation
pip install -e .[docs,tests]
Using Docker Images
===================
Not set up yet.

@ -0,0 +1,49 @@
.. _quickstart:
***************
Getting Started
***************
Here is a quick example of how to fit an xml thermodynamic model to experimental data.
This code fits Nd standard enthalpy in the "twophase.xml" cantera file to the
experimental data in "Nd_exp_data.csv".
This code requires that you copy and paste the "elementz.xml" file in the llepe's data folder into
the Cantera's data folder located in your environments site-packages folder.
The code then produces a parity plot of the measured and predicted concentrations of Nd 3+ in the
aqueous phase.
.. code-block:: python
from llepe import LLEPE
opt_dict = {'Nd(H(A)2)3(org)_h0': {'upper_element_name': 'species',
'upper_attrib_name': 'name',
'upper_attrib_value': 'Nd(H(A)2)3(org)',
'lower_element_name': 'h0',
'lower_attrib_name': None,
'lower_attrib_value': None,
'input_format': '{0}',
'input_value': -4.7e6}}
searcher_parameters = {'exp_data': 'Nd_exp_data.csv',
'phases_xml_filename': 'twophase.xml',
'opt_dict': opt_dict,
'phase_names': ['HCl_electrolyte', 'PC88A_liquid'],
'aq_solvent_name': 'H2O(L)',
'extractant_name': '(HA)2(org)',
'diluant_name': 'dodecane',
'complex_names': ['Nd(H(A)2)3(org)'],
'extracted_species_ion_names': ['Nd+++'],
'aq_solvent_rho': 1000.0,
'extractant_rho': 960.0,
'diluant_rho': 750.0}
searcher = LLEPE(**searcher_parameters)
est_enthalpy = searcher.fit()
searcher.update_xml(est_enthalpy)
searcher.parity_plot(print_r_squared=True)
The code should return something like this
.. figure:: ../_static/img/quick_start_output.png

@ -0,0 +1,38 @@
.. reeps documentation master file, created by Titus Quah
sphinx-quickstart on Tue Jun 9 10:13:23 2020.
You can adapt this file completely to your liking, but it should at least
contain the root `toctree` directive.
Welcome to llepe's docs! - the Liquid-Liquid Extraction Parameter Estimator
===========================================================================
LLEPE is a package for thermodynamic parameter estimation for liquid-liquid extraction modeling
LLEPE takes experimental data in a csv and system data in a xml.
The package then uses Cantera, another python package, to simulate equilibrium.
Error between predicted and experimental data is then minimized.
.. toctree::
:maxdepth: 2
:caption: User Guide
guide/install
guide/quickstart
.. toctree::
:maxdepth: 1
:caption: Searchers
modules/reeps
Indices and tables
==================
* :ref:`genindex`
* :ref:`modindex`
* :ref:`search`

@ -0,0 +1,15 @@
.. _reeps:
.. automodule:: llepe
LLEPE
=====
Parameters
----------
.. autoclass:: LLEPE
:members:
:inherited-members:

@ -0,0 +1,701 @@
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div.sphinxsidebar #searchbox input[type="text"] {
float: left;
width: 80%;
padding: 0.25em;
box-sizing: border-box;
}
div.sphinxsidebar #searchbox input[type="submit"] {
float: left;
width: 20%;
border-left: none;
padding: 0.25em;
box-sizing: border-box;
}
img {
border: 0;
max-width: 100%;
}
/* -- search page ----------------------------------------------------------- */
ul.search {
margin: 10px 0 0 20px;
padding: 0;
}
ul.search li {
padding: 5px 0 5px 20px;
background-image: url(file.png);
background-repeat: no-repeat;
background-position: 0 7px;
}
ul.search li a {
font-weight: bold;
}
ul.search li div.context {
color: #888;
margin: 2px 0 0 30px;
text-align: left;
}
ul.keywordmatches li.goodmatch a {
font-weight: bold;
}
/* -- index page ------------------------------------------------------------ */
table.contentstable {
width: 90%;
margin-left: auto;
margin-right: auto;
}
table.contentstable p.biglink {
line-height: 150%;
}
a.biglink {
font-size: 1.3em;
}
span.linkdescr {
font-style: italic;
padding-top: 5px;
font-size: 90%;
}
/* -- general index --------------------------------------------------------- */
table.indextable {
width: 100%;
}
table.indextable td {
text-align: left;
vertical-align: top;
}
table.indextable ul {
margin-top: 0;
margin-bottom: 0;
list-style-type: none;
}
table.indextable > tbody > tr > td > ul {
padding-left: 0em;
}
table.indextable tr.pcap {
height: 10px;
}
table.indextable tr.cap {
margin-top: 10px;
background-color: #f2f2f2;
}
img.toggler {
margin-right: 3px;
margin-top: 3px;
cursor: pointer;
}
div.modindex-jumpbox {
border-top: 1px solid #ddd;
border-bottom: 1px solid #ddd;
margin: 1em 0 1em 0;
padding: 0.4em;
}
div.genindex-jumpbox {
border-top: 1px solid #ddd;
border-bottom: 1px solid #ddd;
margin: 1em 0 1em 0;
padding: 0.4em;
}
/* -- domain module index --------------------------------------------------- */
table.modindextable td {
padding: 2px;
border-collapse: collapse;
}
/* -- general body styles --------------------------------------------------- */
div.body {
min-width: 450px;
max-width: 800px;
}
div.body p, div.body dd, div.body li, div.body blockquote {
-moz-hyphens: auto;
-ms-hyphens: auto;
-webkit-hyphens: auto;
hyphens: auto;
}
a.headerlink {
visibility: hidden;
}
a.brackets:before,
span.brackets > a:before{
content: "[";
}
a.brackets:after,
span.brackets > a:after {
content: "]";
}
h1:hover > a.headerlink,
h2:hover > a.headerlink,
h3:hover > a.headerlink,
h4:hover > a.headerlink,
h5:hover > a.headerlink,
h6:hover > a.headerlink,
dt:hover > a.headerlink,
caption:hover > a.headerlink,
p.caption:hover > a.headerlink,
div.code-block-caption:hover > a.headerlink {
visibility: visible;
}
div.body p.caption {
text-align: inherit;
}
div.body td {
text-align: left;
}
.first {
margin-top: 0 !important;
}
p.rubric {
margin-top: 30px;
font-weight: bold;
}
img.align-left, .figure.align-left, object.align-left {
clear: left;
float: left;
margin-right: 1em;
}
img.align-right, .figure.align-right, object.align-right {
clear: right;
float: right;
margin-left: 1em;
}
img.align-center, .figure.align-center, object.align-center {
display: block;
margin-left: auto;
margin-right: auto;
}
img.align-default, .figure.align-default {
display: block;
margin-left: auto;
margin-right: auto;
}
.align-left {
text-align: left;
}
.align-center {
text-align: center;
}
.align-default {
text-align: center;
}
.align-right {
text-align: right;
}
/* -- sidebars -------------------------------------------------------------- */
div.sidebar {
margin: 0 0 0.5em 1em;
border: 1px solid #ddb;
padding: 7px 7px 0 7px;
background-color: #ffe;
width: 40%;
float: right;
}
p.sidebar-title {
font-weight: bold;
}
/* -- topics ---------------------------------------------------------------- */
div.topic {
border: 1px solid #ccc;
padding: 7px 7px 0 7px;
margin: 10px 0 10px 0;
}
p.topic-title {
font-size: 1.1em;
font-weight: bold;
margin-top: 10px;
}
/* -- admonitions ----------------------------------------------------------- */
div.admonition {
margin-top: 10px;
margin-bottom: 10px;
padding: 7px;
}
div.admonition dt {
font-weight: bold;
}
div.admonition dl {
margin-bottom: 0;
}
p.admonition-title {
margin: 0px 10px 5px 0px;
font-weight: bold;
}
div.body p.centered {
text-align: center;
margin-top: 25px;
}
/* -- tables ---------------------------------------------------------------- */
table.docutils {
border: 0;
border-collapse: collapse;
}
table.align-center {
margin-left: auto;
margin-right: auto;
}
table.align-default {
margin-left: auto;
margin-right: auto;
}
table caption span.caption-number {
font-style: italic;
}
table caption span.caption-text {
}
table.docutils td, table.docutils th {
padding: 1px 8px 1px 5px;
border-top: 0;
border-left: 0;
border-right: 0;
border-bottom: 1px solid #aaa;
}
table.footnote td, table.footnote th {
border: 0 !important;
}
th {
text-align: left;
padding-right: 5px;
}
table.citation {
border-left: solid 1px gray;
margin-left: 1px;
}
table.citation td {
border-bottom: none;
}
th > p:first-child,
td > p:first-child {
margin-top: 0px;
}
th > p:last-child,
td > p:last-child {
margin-bottom: 0px;
}
/* -- figures --------------------------------------------------------------- */
div.figure {
margin: 0.5em;
padding: 0.5em;
}
div.figure p.caption {
padding: 0.3em;
}
div.figure p.caption span.caption-number {
font-style: italic;
}
div.figure p.caption span.caption-text {
}
/* -- field list styles ----------------------------------------------------- */
table.field-list td, table.field-list th {
border: 0 !important;
}
.field-list ul {
margin: 0;
padding-left: 1em;
}
.field-list p {
margin: 0;
}
.field-name {
-moz-hyphens: manual;
-ms-hyphens: manual;
-webkit-hyphens: manual;
hyphens: manual;
}
/* -- hlist styles ---------------------------------------------------------- */
table.hlist td {
vertical-align: top;
}
/* -- other body styles ----------------------------------------------------- */
ol.arabic {
list-style: decimal;
}
ol.loweralpha {
list-style: lower-alpha;
}
ol.upperalpha {
list-style: upper-alpha;
}
ol.lowerroman {
list-style: lower-roman;
}
ol.upperroman {
list-style: upper-roman;
}
li > p:first-child {
margin-top: 0px;
}
li > p:last-child {
margin-bottom: 0px;
}
dl.footnote > dt,
dl.citation > dt {
float: left;
}
dl.footnote > dd,
dl.citation > dd {
margin-bottom: 0em;
}
dl.footnote > dd:after,
dl.citation > dd:after {
content: "";
clear: both;
}
dl.field-list {
display: grid;
grid-template-columns: fit-content(30%) auto;
}
dl.field-list > dt {
font-weight: bold;
word-break: break-word;
padding-left: 0.5em;
padding-right: 5px;
}
dl.field-list > dt:after {
content: ":";
}
dl.field-list > dd {
padding-left: 0.5em;
margin-top: 0em;
margin-left: 0em;
margin-bottom: 0em;
}
dl {
margin-bottom: 15px;
}
dd > p:first-child {
margin-top: 0px;
}
dd ul, dd table {
margin-bottom: 10px;
}
dd {
margin-top: 3px;
margin-bottom: 10px;
margin-left: 30px;
}
dt:target, span.highlighted {
background-color: #fbe54e;
}
rect.highlighted {
fill: #fbe54e;
}
dl.glossary dt {
font-weight: bold;
font-size: 1.1em;
}
.optional {
font-size: 1.3em;
}
.sig-paren {
font-size: larger;
}
.versionmodified {
font-style: italic;
}
.system-message {
background-color: #fda;
padding: 5px;
border: 3px solid red;
}
.footnote:target {
background-color: #ffa;
}
.line-block {
display: block;
margin-top: 1em;
margin-bottom: 1em;
}
.line-block .line-block {
margin-top: 0;
margin-bottom: 0;
margin-left: 1.5em;
}
.guilabel, .menuselection {
font-family: sans-serif;
}
.accelerator {
text-decoration: underline;
}
.classifier {
font-style: oblique;
}
.classifier:before {
font-style: normal;
margin: 0.5em;
content: ":";
}
abbr, acronym {
border-bottom: dotted 1px;
cursor: help;
}
/* -- code displays --------------------------------------------------------- */
pre {
overflow: auto;
overflow-y: hidden; /* fixes display issues on Chrome browsers */
}
span.pre {
-moz-hyphens: none;
-ms-hyphens: none;
-webkit-hyphens: none;
hyphens: none;
}
td.linenos pre {
padding: 5px 0px;
border: 0;
background-color: transparent;
color: #aaa;
}
table.highlighttable {
margin-left: 0.5em;
}
table.highlighttable td {
padding: 0 0.5em 0 0.5em;
}
div.code-block-caption {
padding: 2px 5px;
font-size: small;
}
div.code-block-caption code {
background-color: transparent;
}
div.code-block-caption + div > div.highlight > pre {
margin-top: 0;
}
div.doctest > div.highlight span.gp { /* gp: Generic.Prompt */
user-select: none;
}
div.code-block-caption span.caption-number {
padding: 0.1em 0.3em;
font-style: italic;
}
div.code-block-caption span.caption-text {
}
div.literal-block-wrapper {
padding: 1em 1em 0;
}
div.literal-block-wrapper div.highlight {
margin: 0;
}
code.descname {
background-color: transparent;
font-weight: bold;
font-size: 1.2em;
}
code.descclassname {
background-color: transparent;
}
code.xref, a code {
background-color: transparent;
font-weight: bold;
}
h1 code, h2 code, h3 code, h4 code, h5 code, h6 code {
background-color: transparent;
}
.viewcode-link {
float: right;
}
.viewcode-back {
float: right;
font-family: sans-serif;
}
div.viewcode-block:target {
margin: -1px -10px;
padding: 0 10px;
}
/* -- math display ---------------------------------------------------------- */
img.math {
vertical-align: middle;
}
div.body div.math p {
text-align: center;
}
span.eqno {
float: right;
}
span.eqno a.headerlink {
position: relative;
left: 0px;
z-index: 1;
}
div.math:hover a.headerlink {
visibility: visible;
}
/* -- printout stylesheet --------------------------------------------------- */
@media print {
div.document,
div.documentwrapper,
div.bodywrapper {
margin: 0 !important;
width: 100%;
}
div.sphinxsidebar,
div.related,
div.footer,
#top-link {
display: none;
}
}

@ -0,0 +1,266 @@
/*
* classic.css_t
* ~~~~~~~~~~~~~
*
* Sphinx stylesheet -- classic theme.
*
* :copyright: Copyright 2007-2020 by the Sphinx team, see AUTHORS.
* :license: BSD, see LICENSE for details.
*
*/
@import url("basic.css");
/* -- page layout ----------------------------------------------------------- */
html {
/* CSS hack for macOS's scrollbar (see #1125) */
background-color: #FFFFFF;
}
body {
font-family: sans-serif;
font-size: 100%;
background-color: #11303d;
color: #000;
margin: 0;
padding: 0;
}
div.document {
background-color: #1c4e63;
}
div.documentwrapper {
float: left;
width: 100%;
}
div.bodywrapper {
margin: 0 0 0 230px;
}
div.body {
background-color: #ffffff;
color: #000000;
padding: 0 20px 30px 20px;
}
div.footer {
color: #ffffff;
width: 100%;
padding: 9px 0 9px 0;
text-align: center;
font-size: 75%;
}
div.footer a {
color: #ffffff;
text-decoration: underline;
}
div.related {
background-color: #133f52;
line-height: 30px;
color: #ffffff;
}
div.related a {
color: #ffffff;
}
div.sphinxsidebar {
}
div.sphinxsidebar h3 {
font-family: 'Trebuchet MS', sans-serif;
color: #ffffff;
font-size: 1.4em;
font-weight: normal;
margin: 0;
padding: 0;
}
div.sphinxsidebar h3 a {
color: #ffffff;
}
div.sphinxsidebar h4 {
font-family: 'Trebuchet MS', sans-serif;
color: #ffffff;
font-size: 1.3em;
font-weight: normal;
margin: 5px 0 0 0;
padding: 0;
}
div.sphinxsidebar p {
color: #ffffff;
}
div.sphinxsidebar p.topless {
margin: 5px 10px 10px 10px;
}
div.sphinxsidebar ul {
margin: 10px;
padding: 0;
color: #ffffff;
}
div.sphinxsidebar a {
color: #98dbcc;
}
div.sphinxsidebar input {
border: 1px solid #98dbcc;
font-family: sans-serif;
font-size: 1em;
}
/* -- hyperlink styles ------------------------------------------------------ */
a {
color: #355f7c;
text-decoration: none;
}
a:visited {
color: #355f7c;
text-decoration: none;
}
a:hover {
text-decoration: underline;
}
/* -- body styles ----------------------------------------------------------- */
div.body h1,
div.body h2,
div.body h3,
div.body h4,
div.body h5,
div.body h6 {
font-family: 'Trebuchet MS', sans-serif;
background-color: #f2f2f2;
font-weight: normal;
color: #20435c;
border-bottom: 1px solid #ccc;
margin: 20px -20px 10px -20px;
padding: 3px 0 3px 10px;
}
div.body h1 { margin-top: 0; font-size: 200%; }
div.body h2 { font-size: 160%; }
div.body h3 { font-size: 140%; }
div.body h4 { font-size: 120%; }
div.body h5 { font-size: 110%; }
div.body h6 { font-size: 100%; }
a.headerlink {
color: #c60f0f;
font-size: 0.8em;
padding: 0 4px 0 4px;
text-decoration: none;
}
a.headerlink:hover {
background-color: #c60f0f;
color: white;
}
div.body p, div.body dd, div.body li, div.body blockquote {
text-align: justify;
line-height: 130%;
}
div.admonition p.admonition-title + p {
display: inline;
}
div.admonition p {
margin-bottom: 5px;
}
div.admonition pre {
margin-bottom: 5px;
}
div.admonition ul, div.admonition ol {
margin-bottom: 5px;
}
div.note {
background-color: #eee;
border: 1px solid #ccc;
}
div.seealso {
background-color: #ffc;
border: 1px solid #ff6;
}
div.topic {
background-color: #eee;
}
div.warning {
background-color: #ffe4e4;
border: 1px solid #f66;
}
p.admonition-title {
display: inline;
}
p.admonition-title:after {
content: ":";
}
pre {
padding: 5px;
background-color: #eeffcc;
color: #333333;
line-height: 120%;
border: 1px solid #ac9;
border-left: none;
border-right: none;
}
code {
background-color: #ecf0f3;
padding: 0 1px 0 1px;
font-size: 0.95em;
}
th, dl.field-list > dt {
background-color: #ede;
}
.warning code {
background: #efc2c2;
}
.note code {
background: #d6d6d6;
}
.viewcode-back {
font-family: sans-serif;
}
div.viewcode-block:target {
background-color: #f4debf;
border-top: 1px solid #ac9;
border-bottom: 1px solid #ac9;
}
div.code-block-caption {
color: #efefef;
background-color: #1c4e63;
}

@ -0,0 +1 @@
.fa:before{-webkit-font-smoothing:antialiased}.clearfix{*zoom:1}.clearfix:before,.clearfix:after{display:table;content:""}.clearfix:after{clear:both}@font-face{font-family:FontAwesome;font-weight:normal;font-style:normal;src:url("../fonts/fontawesome-webfont.eot");src:url("../fonts/fontawesome-webfont.eot?#iefix") format("embedded-opentype"),url("../fonts/fontawesome-webfont.woff") format("woff"),url("../fonts/fontawesome-webfont.ttf") format("truetype"),url("../fonts/fontawesome-webfont.svg#FontAwesome") format("svg")}.fa:before{display:inline-block;font-family:FontAwesome;font-style:normal;font-weight:normal;line-height:1;text-decoration:inherit}a .fa{display:inline-block;text-decoration:inherit}li .fa{display:inline-block}li .fa-large:before,li .fa-large:before{width:1.875em}ul.fas{list-style-type:none;margin-left:2em;text-indent:-0.8em}ul.fas li .fa{width:.8em}ul.fas li .fa-large:before,ul.fas li .fa-large:before{vertical-align:baseline}.fa-book:before{content:""}.icon-book:before{content:""}.fa-caret-down:before{content:""}.icon-caret-down:before{content:""}.fa-caret-up:before{content:""}.icon-caret-up:before{content:""}.fa-caret-left:before{content:""}.icon-caret-left:before{content:""}.fa-caret-right:before{content:""}.icon-caret-right:before{content:""}.rst-versions{position:fixed;bottom:0;left:0;width:300px;color:#fcfcfc;background:#1f1d1d;font-family:"Lato","proxima-nova","Helvetica Neue",Arial,sans-serif;z-index:400}.rst-versions a{color:#2980B9;text-decoration:none}.rst-versions .rst-badge-small{display:none}.rst-versions .rst-current-version{padding:12px;background-color:#272525;display:block;text-align:right;font-size:90%;cursor:pointer;color:#27AE60;*zoom:1}.rst-versions .rst-current-version:before,.rst-versions .rst-current-version:after{display:table;content:""}.rst-versions .rst-current-version:after{clear:both}.rst-versions .rst-current-version .fa{color:#fcfcfc}.rst-versions .rst-current-version .fa-book{float:left}.rst-versions .rst-current-version .icon-book{float:left}.rst-versions .rst-current-version.rst-out-of-date{background-color:#E74C3C;color:#fff}.rst-versions .rst-current-version.rst-active-old-version{background-color:#F1C40F;color:#000}.rst-versions.shift-up{height:auto;max-height:100%;overflow-y:scroll}.rst-versions.shift-up .rst-other-versions{display:block}.rst-versions .rst-other-versions{font-size:90%;padding:12px;color:gray;display:none}.rst-versions .rst-other-versions hr{display:block;height:1px;border:0;margin:20px 0;padding:0;border-top:solid 1px #413d3d}.rst-versions .rst-other-versions dd{display:inline-block;margin:0}.rst-versions .rst-other-versions dd a{display:inline-block;padding:6px;color:#fcfcfc}.rst-versions.rst-badge{width:auto;bottom:20px;right:20px;left:auto;border:none;max-width:300px;max-height:90%}.rst-versions.rst-badge .icon-book{float:none}.rst-versions.rst-badge .fa-book{float:none}.rst-versions.rst-badge.shift-up .rst-current-version{text-align:right}.rst-versions.rst-badge.shift-up .rst-current-version .fa-book{float:left}.rst-versions.rst-badge.shift-up .rst-current-version .icon-book{float:left}.rst-versions.rst-badge .rst-current-version{width:auto;height:30px;line-height:30px;padding:0 6px;display:block;text-align:center}@media screen and (max-width: 768px){.rst-versions{width:85%;display:none}.rst-versions.shift{display:block}}

@ -0,0 +1,52 @@
/* Main colors from https://color.adobe.com/fr/Copy-of-NOUEBO-Original-color-theme-11116609 */
:root{
--main-bg-color: #324D5C;
--link-color: #14B278;
}
/* Header fonts y */
h1, h2, .rst-content .toctree-wrapper p.caption, h3, h4, h5, h6, legend, p.caption {
font-family: "Lato","proxima-nova","Helvetica Neue",Arial,sans-serif;
}
/* Docs background */
.wy-side-nav-search{
background-color: var(--main-bg-color);
}
/* Mobile version */
.wy-nav-top{
background-color: var(--main-bg-color);
}
/* Change link colors (except for the menu) */
a {
color: var(--link-color);
}
a:hover {
color: #4F778F;
}
.wy-menu a {
color: #b3b3b3;
}
.wy-menu a:hover {
color: #b3b3b3;
}
a.icon.icon-home {
color: #b3b3b3;
}
.version{
color: var(--link-color) !important;
}
/* Make code blocks have a background */
.codeblock,pre.literal-block,.rst-content .literal-block,.rst-content pre.literal-block,div[class^='highlight'] {
background: #f8f8f8;;
}

File diff suppressed because one or more lines are too long

@ -0,0 +1 @@
/* This file intentionally left blank. */

@ -0,0 +1 @@
@import url("classic.css");

@ -0,0 +1,315 @@
/*
* doctools.js
* ~~~~~~~~~~~
*
* Sphinx JavaScript utilities for all documentation.
*
* :copyright: Copyright 2007-2020 by the Sphinx team, see AUTHORS.
* :license: BSD, see LICENSE for details.
*
*/
/**
* select a different prefix for underscore
*/
$u = _.noConflict();
/**
* make the code below compatible with browsers without
* an installed firebug like debugger
if (!window.console || !console.firebug) {
var names = ["log", "debug", "info", "warn", "error", "assert", "dir",
"dirxml", "group", "groupEnd", "time", "timeEnd", "count", "trace",
"profile", "profileEnd"];
window.console = {};
for (var i = 0; i < names.length; ++i)
window.console[names[i]] = function() {};
}
*/
/**
* small helper function to urldecode strings
*/
jQuery.urldecode = function(x) {
return decodeURIComponent(x).replace(/\+/g, ' ');
};
/**
* small helper function to urlencode strings
*/
jQuery.urlencode = encodeURIComponent;
/**
* This function returns the parsed url parameters of the
* current request. Multiple values per key are supported,
* it will always return arrays of strings for the value parts.
*/
jQuery.getQueryParameters = function(s) {
if (typeof s === 'undefined')
s = document.location.search;
var parts = s.substr(s.indexOf('?') + 1).split('&');
var result = {};
for (var i = 0; i < parts.length; i++) {
var tmp = parts[i].split('=', 2);
var key = jQuery.urldecode(tmp[0]);
var value = jQuery.urldecode(tmp[1]);
if (key in result)
result[key].push(value);
else
result[key] = [value];
}
return result;
};
/**
* highlight a given string on a jquery object by wrapping it in
* span elements with the given class name.
*/
jQuery.fn.highlightText = function(text, className) {
function highlight(node, addItems) {
if (node.nodeType === 3) {
var val = node.nodeValue;
var pos = val.toLowerCase().indexOf(text);
if (pos >= 0 &&
!jQuery(node.parentNode).hasClass(className) &&
!jQuery(node.parentNode).hasClass("nohighlight")) {
var span;
var isInSVG = jQuery(node).closest("body, svg, foreignObject").is("svg");
if (isInSVG) {
span = document.createElementNS("http://www.w3.org/2000/svg", "tspan");
} else {
span = document.createElement("span");
span.className = className;
}
span.appendChild(document.createTextNode(val.substr(pos, text.length)));
node.parentNode.insertBefore(span, node.parentNode.insertBefore(
document.createTextNode(val.substr(pos + text.length)),
node.nextSibling));
node.nodeValue = val.substr(0, pos);
if (isInSVG) {
var rect = document.createElementNS("http://www.w3.org/2000/svg", "rect");
var bbox = node.parentElement.getBBox();
rect.x.baseVal.value = bbox.x;
rect.y.baseVal.value = bbox.y;
rect.width.baseVal.value = bbox.width;
rect.height.baseVal.value = bbox.height;
rect.setAttribute('class', className);
addItems.push({
"parent": node.parentNode,
"target": rect});
}
}
}
else if (!jQuery(node).is("button, select, textarea")) {
jQuery.each(node.childNodes, function() {
highlight(this, addItems);
});
}
}
var addItems = [];
var result = this.each(function() {
highlight(this, addItems);
});
for (var i = 0; i < addItems.length; ++i) {
jQuery(addItems[i].parent).before(addItems[i].target);
}
return result;
};
/*
* backward compatibility for jQuery.browser
* This will be supported until firefox bug is fixed.
*/
if (!jQuery.browser) {
jQuery.uaMatch = function(ua) {
ua = ua.toLowerCase();
var match = /(chrome)[ \/]([\w.]+)/.exec(ua) ||
/(webkit)[ \/]([\w.]+)/.exec(ua) ||
/(opera)(?:.*version|)[ \/]([\w.]+)/.exec(ua) ||
/(msie) ([\w.]+)/.exec(ua) ||
ua.indexOf("compatible") < 0 && /(mozilla)(?:.*? rv:([\w.]+)|)/.exec(ua) ||
[];
return {
browser: match[ 1 ] || "",
version: match[ 2 ] || "0"
};
};
jQuery.browser = {};
jQuery.browser[jQuery.uaMatch(navigator.userAgent).browser] = true;
}
/**
* Small JavaScript module for the documentation.
*/
var Documentation = {
init : function() {
this.fixFirefoxAnchorBug();
this.highlightSearchWords();
this.initIndexTable();
if (DOCUMENTATION_OPTIONS.NAVIGATION_WITH_KEYS) {
this.initOnKeyListeners();
}
},
/**
* i18n support
*/
TRANSLATIONS : {},
PLURAL_EXPR : function(n) { return n === 1 ? 0 : 1; },
LOCALE : 'unknown',
// gettext and ngettext don't access this so that the functions
// can safely bound to a different name (_ = Documentation.gettext)
gettext : function(string) {
var translated = Documentation.TRANSLATIONS[string];
if (typeof translated === 'undefined')
return string;
return (typeof translated === 'string') ? translated : translated[0];
},
ngettext : function(singular, plural, n) {
var translated = Documentation.TRANSLATIONS[singular];
if (typeof translated === 'undefined')
return (n == 1) ? singular : plural;
return translated[Documentation.PLURALEXPR(n)];
},
addTranslations : function(catalog) {
for (var key in catalog.messages)
this.TRANSLATIONS[key] = catalog.messages[key];
this.PLURAL_EXPR = new Function('n', 'return +(' + catalog.plural_expr + ')');
this.LOCALE = catalog.locale;
},
/**
* add context elements like header anchor links
*/
addContextElements : function() {
$('div[id] > :header:first').each(function() {
$('<a class="headerlink">\u00B6</a>').
attr('href', '#' + this.id).
attr('title', _('Permalink to this headline')).
appendTo(this);
});
$('dt[id]').each(function() {
$('<a class="headerlink">\u00B6</a>').
attr('href', '#' + this.id).
attr('title', _('Permalink to this definition')).
appendTo(this);
});
},
/**
* workaround a firefox stupidity
* see: https://bugzilla.mozilla.org/show_bug.cgi?id=645075
*/
fixFirefoxAnchorBug : function() {
if (document.location.hash && $.browser.mozilla)
window.setTimeout(function() {
document.location.href += '';
}, 10);
},
/**
* highlight the search words provided in the url in the text
*/
highlightSearchWords : function() {
var params = $.getQueryParameters();
var terms = (params.highlight) ? params.highlight[0].split(/\s+/) : [];
if (terms.length) {
var body = $('div.body');
if (!body.length) {
body = $('body');
}
window.setTimeout(function() {
$.each(terms, function() {
body.highlightText(this.toLowerCase(), 'highlighted');
});
}, 10);
$('<p class="highlight-link"><a href="javascript:Documentation.' +
'hideSearchWords()">' + _('Hide Search Matches') + '</a></p>')
.appendTo($('#searchbox'));
}
},
/**
* init the domain index toggle buttons
*/
initIndexTable : function() {
var togglers = $('img.toggler').click(function() {
var src = $(this).attr('src');
var idnum = $(this).attr('id').substr(7);
$('tr.cg-' + idnum).toggle();
if (src.substr(-9) === 'minus.png')
$(this).attr('src', src.substr(0, src.length-9) + 'plus.png');
else
$(this).attr('src', src.substr(0, src.length-8) + 'minus.png');
}).css('display', '');
if (DOCUMENTATION_OPTIONS.COLLAPSE_INDEX) {
togglers.click();
}
},
/**
* helper function to hide the search marks again
*/
hideSearchWords : function() {
$('#searchbox .highlight-link').fadeOut(300);
$('span.highlighted').removeClass('highlighted');
},
/**
* make the url absolute
*/
makeURL : function(relativeURL) {
return DOCUMENTATION_OPTIONS.URL_ROOT + '/' + relativeURL;
},
/**
* get the current relative url
*/
getCurrentURL : function() {
var path = document.location.pathname;
var parts = path.split(/\//);
$.each(DOCUMENTATION_OPTIONS.URL_ROOT.split(/\//), function() {
if (this === '..')
parts.pop();
});
var url = parts.join('/');
return path.substring(url.lastIndexOf('/') + 1, path.length - 1);
},
initOnKeyListeners: function() {
$(document).keydown(function(event) {
var activeElementType = document.activeElement.tagName;
// don't navigate when in search box or textarea
if (activeElementType !== 'TEXTAREA' && activeElementType !== 'INPUT' && activeElementType !== 'SELECT'
&& !event.altKey && !event.ctrlKey && !event.metaKey && !event.shiftKey) {
switch (event.keyCode) {
case 37: // left
var prevHref = $('link[rel="prev"]').prop('href');
if (prevHref) {
window.location.href = prevHref;
return false;
}
case 39: // right
var nextHref = $('link[rel="next"]').prop('href');
if (nextHref) {
window.location.href = nextHref;
return false;
}
}
}
});
}
};
// quick alias for translations
_ = Documentation.gettext;
$(document).ready(function() {
Documentation.init();
});

@ -0,0 +1,12 @@
var DOCUMENTATION_OPTIONS = {
URL_ROOT: document.getElementById("documentation_options").getAttribute('data-url_root'),
VERSION: '1.0.0',
LANGUAGE: 'python',
COLLAPSE_INDEX: false,
BUILDER: 'html',
FILE_SUFFIX: '.html',
LINK_SUFFIX: '.html',
HAS_SOURCE: true,
SOURCELINK_SUFFIX: '.txt',
NAVIGATION_WITH_KEYS: false
};

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