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Fix all instances of accentric->acentric in fluid files and codebase. Signed-off-by: Ian Bell <ian.h.bell@gmail.com>
434 lines
11 KiB
JSON
434 lines
11 KiB
JSON
{
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"ALIASES": [
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"R1234ZE(Z)",
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"R1234ZE"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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661341.6719107341,
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-15127.133650206008,
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138.91087893469512,
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-0.6980587134971441,
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0.002098499633604347,
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-3.7793519929234075e-06,
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3.774511596585241e-09,
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],
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"B": [
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1,
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],
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"Tmax": 423.16999999999996,
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"Tmin": 273.0,
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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": 179.97713685777762,
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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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4.150647373162431e-12
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],
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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": 437.77812959121843,
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"type": "rational_polynomial"
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},
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"pL": {
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"T_r": 423.27,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"n": [
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171.34274686639145
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"t": [
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0.631,
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0.974,
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3.244,
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3.59,
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7.592,
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6.934
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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": 423.27,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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0.993,
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3.259,
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4.649,
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8.29,
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18.573
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],
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"type": "pV",
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},
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"rhoL": {
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"T_r": 423.27,
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"Tmax": 423.2699999999993,
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"Tmin": 273.0,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.36780472644506457,
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68499.04449007797,
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],
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0.414,
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0.901,
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2.913,
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8.026,
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8.631,
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10.213
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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": 423.27,
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"Tmin": 273.0,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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2037392.973112241
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"t": [
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0.43,
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0.95,
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4.5,
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6.507,
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8.994,
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9.048
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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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1303.8187095473975,
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0.3004627114725399,
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4.598136568105457e-06,
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8.296774715164654e-12,
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-3.5487904739583724e-15
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],
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"B": [
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1,
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],
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"Tmax": 423.16999999999996,
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"Tmin": 273.0,
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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": 0.41975135410767805,
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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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78.44275112099125,
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0.003785229753629718,
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2.089341655885634e-08,
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-2.0967591691283893e-11,
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8.988690381042343e-15
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],
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"B": [
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1,
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],
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"Tmax": 423.16999999999996,
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"Tmin": 273.0,
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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": 1.0220801074081636,
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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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},
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"CAS": "29118-25-0",
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"EOS": [
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{
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"BibTeX_CP0": "",
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"BibTeX_EOS": "Akasaka-DELFT-2013",
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"STATES": {
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"hs_anchor": {
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"T": 465.59700000000004,
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"T_units": "K",
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"hmolar": 8356.216717020856,
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"hmolar_units": "J/mol",
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"p": 6082696.015266482,
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"p_units": "Pa",
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"rhomolar": 3714.0265196296004,
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"rhomolar_units": "mol/m^3",
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"smolar": 30.226552329410275,
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"smolar_units": "J/mol/K"
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},
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"reducing": {
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"T": 423.27,
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"T_units": "K",
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"hmolar": 1000.6072356724737,
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"hmolar_units": "J/mol",
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"p": 3533000,
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"p_units": "Pa",
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"rhomolar": 4126.696132921778,
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"rhomolar_units": "mol/m^3",
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"smolar": 15.115785966250435,
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"smolar_units": "J/mol/K"
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},
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"sat_min_liquid": {
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"T": 273.0,
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"T_units": "K",
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"hmolar": -27727.96883868131,
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"hmolar_units": "J/mol",
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"p": 67802.93935916605,
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"p_units": "Pa",
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"rhomolar": 11250.756301033874,
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"rhomolar_units": "mol/m^3",
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"smolar": -64.58713826359764,
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"smolar_units": "J/mol/K"
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},
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"sat_min_vapor": {
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"T": 273.0,
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"T_units": "K",
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"hmolar": -2603.769449881924,
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"hmolar_units": "J/mol",
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"p": 67802.93965438179,
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"p_units": "Pa",
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"rhomolar": 31.076296674814373,
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"rhomolar_units": "mol/m^3",
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"smolar": 27.44289609285729,
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"smolar_units": "J/mol/K"
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}
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},
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"T_max": 430,
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"T_max_units": "K",
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"Ttriple": 273,
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"Ttriple_units": "K",
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"acentric": 0.3274,
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"acentric_units": "-",
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"alpha0": [
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{
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"a1": 0,
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"a2": 0,
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": -1,
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"type": "IdealGasHelmholtzLogTau"
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},
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{
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"T0": 298,
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"Tc": 423.27,
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"c": [
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-1.6994,
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0.05794646443168663,
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-5.539762719017151e-05,
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1.998892498570471e-08
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],
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"t": [
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0,
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1,
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2,
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3
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],
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"type": "IdealGasHelmholtzCP0PolyT"
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}
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],
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"alphar": [
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{
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"d": [
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1,
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1,
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1,
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2,
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5,
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1,
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3,
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5,
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7,
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1,
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2,
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2,
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3,
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4,
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2,
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3,
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5
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],
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"l": [
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0,
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0,
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0,
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0,
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0,
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1,
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1,
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1,
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1,
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2,
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2,
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2,
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2,
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2,
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3,
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3,
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3
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],
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"n": [
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0.14534501,
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0.0092092105,
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0.09667436,
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0.024685924,
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0.36638206,
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0.086271444,
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0.015997412,
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0.004229399
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],
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"t": [
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0.685,
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0.8494,
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1.87,
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2,
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0.142,
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4.2,
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0.08,
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0,
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1.1,
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5.5,
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6.6,
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8.4,
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7.2,
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7.6,
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8.5,
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23,
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18
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],
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"type": "ResidualHelmholtzPower"
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}
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],
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"critical_region_splines": {
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"T_max": 423.27,
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"T_min": 423.26310506132734,
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"_note": "Coefficients for the critical cubic spline. T = c[0]*rho^3 + c[1]*rho^2 + c[2]*rho + c[3] with rho in mol/m^3 and T in K",
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"cL": [
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-1.0661006391670194e-09,
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1.2653370461499062e-05,
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488.933234607043
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],
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"cV": [
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-8.160851613585538e-10,
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9.267609720003654e-06,
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466.4282367596696
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],
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"rhomolar_max": 4225.213370352157,
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"rhomolar_min": 4025.0245673273625
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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": 0.1140415928,
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"molar_mass_units": "kg/mol",
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"p_max": 6000000,
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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": "R1234ze(Z)",
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"REFPROP_NAME": "N/A",
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"STATES": {
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"critical": {
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"T": 423.27,
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"T_units": "K",
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"p": 3533000.0,
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"p_units": "Pa",
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"rhomolar": 4121.303363626818,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 273.0,
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"T_units": "K",
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"hmolar": -27727.96883868131,
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"hmolar_units": "J/mol",
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"p": 67802.93935916605,
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"p_units": "Pa",
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"rhomolar": 11250.756301033874,
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"rhomolar_units": "mol/m^3",
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"smolar": -64.58713826359764,
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"smolar_units": "J/mol/K"
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},
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"triple_vapor": {
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"T": 273.0,
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"T_units": "K",
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"hmolar": -2603.769449881924,
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"hmolar_units": "J/mol",
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"p": 67802.93965438179,
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"p_units": "Pa",
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"rhomolar": 31.076296674814373,
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"rhomolar_units": "mol/m^3",
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"smolar": 27.44289609285729,
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"smolar_units": "J/mol/K"
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}
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}
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} |