mirror of
https://github.com/CoolProp/CoolProp.git
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447 lines
10 KiB
JSON
447 lines
10 KiB
JSON
{
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"ALIASES": [
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"DMC",
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"dimethylcarbonate",
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"DIMETHYLCARBONATE"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-20046.780787996202,
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-1463.9849712092594,
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14.444808805753437,
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-0.06521432209330619,
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0.00017132469704104282,
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-2.6650541082443664e-07,
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2.2732925252183504e-10,
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-8.222204740858438e-14
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],
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"B": [
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1,
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-0.0017770011579953502
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],
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"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
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"max_abs_error": 397.4163026412716,
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"max_abs_error_units": "J/mol",
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"type": "rational_polynomial"
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},
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"hLV": {
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"A": [
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-152099.06618199244,
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3769.494102411334,
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0.13764809169117898,
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-0.0003574494642693901,
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5.507419164946889e-07,
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-4.670775800004022e-10,
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1.6854482848731542e-13
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],
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"B": [
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1,
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-0.0017762360963626276
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],
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"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
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"max_abs_error": 912.6159527142613,
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"max_abs_error_units": "J/mol",
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"type": "rational_polynomial"
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},
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"pL": {
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"T_r": 557.0,
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"Tmax": 556.9999999999989,
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"Tmin": 277.06,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.11227216504992032,
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"n": [
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-6.837266302374972,
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114.75387978395011,
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418.1739993231517,
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-559.7253413542608,
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925.8612544918711
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],
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"reducing_value": 4908800.0,
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"t": [
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0.964,
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4.159,
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4.654,
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5.049,
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9.147,
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11.03
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],
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"type": "pL",
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"using_tau_r": true
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},
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"pV": {
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"T_r": 557.0,
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"Tmax": 556.9999999999989,
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"Tmin": 277.06,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.005628626505338463,
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"n": [
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-2.597007649585314,
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-3.425253357555481
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],
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"reducing_value": 4908800.0,
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"t": [
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0.945,
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1.114,
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1.224,
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2.157,
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2.469,
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4.522
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],
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"type": "pV",
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"using_tau_r": true
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},
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"rhoL": {
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"T_r": 557.0,
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"Tmax": 556.9999999999989,
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"Tmin": 277.06,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.27167700173059695,
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"n": [
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0.8639422657944309,
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3.3308155638028083,
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152.44139464976624,
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],
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"reducing_value": 4000.0,
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"t": [
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0.221,
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0.307,
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0.394,
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5.545,
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5.765,
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19.705
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],
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"type": "rhoLnoexp",
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"using_tau_r": false
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},
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"rhoV": {
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"T_r": 557.0,
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"Tmax": 556.9999999999989,
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"Tmin": 277.06,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.9630964865271263,
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"n": [
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11.090574157797857,
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],
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"reducing_value": 4000.0,
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"t": [
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0.318,
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0.882,
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0.995,
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3.273,
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5.755,
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13.354
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],
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"type": "rhoV",
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"using_tau_r": true
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},
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"sL": {
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"A": [
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-370.4545192411453,
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0.844528831212201,
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0.008532659716014959,
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-6.330323231913576e-05,
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2.0122914254578493e-07,
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-3.485368612681206e-10,
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3.189567481737155e-13,
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-1.21191645274887e-16
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],
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"B": [
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1,
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-0.0017776377145390587
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],
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"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
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"max_abs_error": 0.7007786248122301,
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"max_abs_error_units": "J/mol/K",
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"type": "rational_polynomial"
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},
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"sLV": {
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"A": [
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710.8267048015707,
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-4.61042921272275,
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0.005646702070950604,
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4.7337614099045484e-05,
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-2.374863058351081e-07,
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4.849176462749095e-10,
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-4.836030496175538e-13,
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1.940434068951136e-16
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],
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"B": [
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1,
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-0.001776547804535099
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],
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"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
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"max_abs_error": 1.6258104176559778,
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"max_abs_error_units": "J/mol/K",
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"type": "rational_polynomial"
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},
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"surface_tension": {
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"BibTeX": "Mulero-JPCRD-2014",
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"Tc": 557.0,
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"a": [
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0.0825
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],
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"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
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"n": [
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1.39
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]
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}
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},
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"CAS": "616-38-6",
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"ENVIRONMENTAL": {
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"ASHRAE34": "UNKNOWN",
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"FH": 3,
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"GWP100": -1.0,
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"GWP20": -1.0,
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"GWP500": -1.0,
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"HH": 2,
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"Name": "DimethylCarbonate",
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"ODP": -1.0,
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"PH": 0
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},
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"EOS": [
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{
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"BibTeX_CP0": "",
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"BibTeX_EOS": "Zhou-JPCRD-2011",
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"STATES": {
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"hs_anchor": {
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"T": 612.7,
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"T_units": "K",
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"hmolar": 58044.67342145647,
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"hmolar_units": "J/mol",
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"p": 8483749.081005774,
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"p_units": "Pa",
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"rhomolar": 3600.0,
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"rhomolar_units": "mol/m^3",
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"smolar": 115.98431089353645,
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"smolar_units": "J/mol/K"
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},
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"reducing": {
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"T": 557,
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"T_units": "K",
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"p": 4908800,
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"p_units": "Pa",
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"rhomolar": 4000,
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"rhomolar_units": "mol/m^3"
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},
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"sat_min_liquid": {
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"T": 277.06,
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"T_units": "K",
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"p": 2.226523726360071,
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"p_units": "Pa",
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"rhomolar": 12111.201661172097,
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"rhomolar_units": "mol/m^3"
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},
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"sat_min_vapor": {
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"T": 277.06,
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"T_units": "K",
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"p": 2.226523726360071,
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"p_units": "Pa",
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"rhomolar": 0.9680130259154924,
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"rhomolar_units": "mol/m^3"
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}
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},
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"T_max": 600,
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"T_max_units": "K",
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"Ttriple": 277.06,
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"Ttriple_units": "K",
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"accentric": 0.346,
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"accentric_units": "-",
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"alpha0": [
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{
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"a1": 4.9916462,
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"a2": -0.1709449,
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": 8.28421,
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"type": "IdealGasHelmholtzLogTau"
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},
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{
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"n": [
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"t": [
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],
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"type": "IdealGasHelmholtzPlanckEinstein"
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}
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],
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"alphar": [
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"l": [
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"n": [
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"t": [
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],
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"type": "ResidualHelmholtzPower"
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},
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{
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"beta": [
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"d": [
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],
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"epsilon": [
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],
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"eta": [
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],
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"gamma": [
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"n": [
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"type": "ResidualHelmholtzGaussian"
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}
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],
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"gas_constant": 8.314472,
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"gas_constant_units": "J/mol/K",
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"molar_mass": 0.0900779,
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"molar_mass_units": "kg/mol",
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"p_max": 60000000,
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"p_max_units": "Pa",
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"pseudo_pure": false
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}
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],
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"NAME": "DimethylCarbonate",
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"REFPROP_NAME": "DMC",
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"STATES": {
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"critical": {
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"T": 557.0,
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"T_units": "K",
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"p": 4908800.0,
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"p_units": "Pa",
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"rhomolar": 4000.0,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 277.06,
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"T_units": "K",
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"p": 2.226523726360071,
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"p_units": "Pa",
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"rhomolar": 12111.201661172097,
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"rhomolar_units": "mol/m^3"
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},
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"triple_vapor": {
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"T": 277.06,
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"T_units": "K",
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"p": 2.226523726360071,
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"p_units": "Pa",
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"rhomolar": 0.9680130259154924,
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"rhomolar_units": "mol/m^3"
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}
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}
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} |