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https://github.com/CoolProp/CoolProp.git
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588 lines
13 KiB
JSON
588 lines
13 KiB
JSON
{
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"ANCILLARIES": {
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"hL": {
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"A": [
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213.1260789486956,
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-0.0019815760230164946,
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1.3632677369658302e-05,
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-4.4492478844355654e-08,
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7.329895102645116e-11,
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],
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1,
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],
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"Tmax": 364.111,
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"Tmin": 87.953,
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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": 242.41546040908725,
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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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28438.115081306332,
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0.010862874538450237,
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1.6664298300451552e-07,
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1.6831999323158112e-13
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],
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1,
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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": 553.9157403966058,
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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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"melting_line": {
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"BibTeX": "Reeves-JCP-1964",
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"T_m": 88.05999999999997,
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"_note": "Modified coefficients to make minimum state agree with triple point",
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"parts": [
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{
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"T_0": 87.953,
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"T_max": 129,
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"a": 319600000.0,
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"c": 2.821,
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"p_0": 0.0007471728686974104
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},
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{
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"T_0": 109.6,
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"T_max": 145.3,
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"a": 306400000.0,
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"c": 3.871,
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"p_0": 445000000.0
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}
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],
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"type": "Simon"
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},
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"pS": {
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"T_r": 364.211,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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0.985,
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8.871,
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9.472,
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12.201
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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": 364.211,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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1.1500616940414559,
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0.7037673936905474,
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2.21238242151199
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0.286,
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0.521,
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0.701,
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5.657,
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6.864,
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15.279
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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": 364.211,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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4.2053374767917395,
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"t": [
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0.42,
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0.56,
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1.051,
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1.479,
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3.598,
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16.862
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],
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"type": "rhoV",
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},
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"sL": {
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0.00020407925887916563,
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1.6682068981045696e-09,
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1.1487831725277089e-15
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],
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"B": [
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1,
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],
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"Tmax": 364.111,
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"Tmin": 87.953,
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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": 0.8619163751196712,
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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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1209.3598590436613,
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0.2708371575305057,
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6.7652125945527675e-06,
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-1.6161377016041794e-08,
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2.148962075653635e-11,
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],
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"B": [
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1,
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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": 2.8299697075697434,
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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-2012",
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"Tc": 364.211,
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"a": [
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0.05268
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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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1.186
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]
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}
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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": "Lemmon-PROPYLENE-2013",
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"STATES": {
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"T": 400.63210000000004,
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"hmolar": 26645.377075672735,
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"p": 7310423.5406166725,
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"p": 4555000,
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},
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"T": 87.953,
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},
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}
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},
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"T_max": 575,
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"Ttriple": 87.953,
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"alpha0": [
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{
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": 3,
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},
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{
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"n": [
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1.544,
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4.013,
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8.923,
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6.02
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],
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"t": [
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0.8895942187358427,
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"type": "IdealGasHelmholtzPlanckEinstein"
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},
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{
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"reference": "IIR",
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"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
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}
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],
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"alphar": [
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{
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4,
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1,
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1,
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2,
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2,
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3,
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1,
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1,
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3,
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2,
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2,
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8
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],
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"l": [
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0,
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2,
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1
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"n": [
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],
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"t": [
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0.83
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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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0.77,
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0.83,
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0.607,
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0.4,
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0.66,
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0.07,
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387,
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41
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"d": [
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1,
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1,
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2,
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3,
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3,
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2,
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1,
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2,
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3
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],
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"epsilon": [
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1.94,
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1.3,
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0.38,
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0.91,
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0.7
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],
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"eta": [
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1.2,
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1.12,
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1.47,
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1.93,
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3.3,
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15.4,
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6
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],
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"gamma": [
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1.21,
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0.83,
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0.56,
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1.22,
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1.81,
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1.54,
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1.12,
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1.4
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],
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"n": [
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0.1475162,
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0.006378889,
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0.0150294,
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],
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"t": [
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1.6,
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3,
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2.5,
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2.72,
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4,
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4,
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1,
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|
4
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],
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"type": "ResidualHelmholtzGaussian"
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}
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],
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"critical_region_splines": {
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"T_max": 364.211,
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"T_min": 364.21077733486237,
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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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0.0,
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0.0,
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-3.6652101077273866e-06,
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364.2310010515579
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|
],
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"cV": [
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0.0,
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|
0.0,
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3.951799999729862e-06,
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364.1894350274015
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|
],
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"rhomolar_max": 5517.750988646923,
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"rhomolar_min": 5400.654755394478
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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": 0.04207974,
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|
"molar_mass_units": "kg/mol",
|
|
"p_max": 1000000000,
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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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"INFO": {
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"2DPNG_URL": "http://www.chemspider.com/ImagesHandler.ashx?id=7954",
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|
"ALIASES": [
|
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"propylene",
|
|
"PROPYLENE",
|
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"PROPYLEN",
|
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"R1270"
|
|
],
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|
"CAS": "115-07-1",
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|
"CHEMSPIDER_ID": 7954,
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|
"ENVIRONMENTAL": {
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|
"ASHRAE34": "A3",
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|
"FH": 4,
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|
"GWP100": 3.1,
|
|
"GWP20": -1.0,
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|
"GWP500": -1.0,
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|
"HH": 1,
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|
"Name": "Propylene",
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|
"ODP": -1.0,
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|
"PH": 1
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|
},
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|
"FORMULA": "C_{3}H_{6}",
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|
"INCHI_KEY": "QQONPFPTGQHPMA-UHFFFAOYSA-N",
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|
"INCHI_STRING": "InChI=1S/C3H6/c1-3-2/h3H,1H2,2H3",
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"NAME": "Propylene",
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|
"REFPROP_NAME": "PROPYLEN",
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"SMILES": "CC=C"
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},
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"STATES": {
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"critical": {
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"T": 364.211,
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|
"T_units": "K",
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"hmolar": 22348.096116413064,
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"hmolar_units": "J/mol",
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|
"p": 4555000.0,
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"p_units": "Pa",
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"rhomolar": 5457.0,
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"smolar": 83.55933414502688,
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|
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|
},
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"triple_liquid": {
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|
"T": 87.953,
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|
"T_units": "K",
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|
"hmolar": -8389.974818153365,
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|
"hmolar_units": "J/mol",
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|
"p": 0.0007469480313533406,
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"p_units": "Pa",
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"rhomolar": 18254.562780551245,
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|
"rhomolar_units": "mol/m^3",
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"smolar": -59.75246708119243,
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"smolar_units": "J/mol/K"
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},
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"triple_vapor": {
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"T": 87.953,
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|
"T_units": "K",
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|
"hmolar": 16247.981438019186,
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|
"hmolar_units": "J/mol",
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|
"p": 0.0007469480313533406,
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"p_units": "Pa",
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|
"rhomolar": 1.0217291002947073e-06,
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|
"rhomolar_units": "mol/m^3",
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|
"smolar": 220.37392151467708,
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|
"smolar_units": "J/mol/K"
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}
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},
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"TRANSPORT": {
|
|
"conductivity": {
|
|
"BibTeX": "Huber-IECR-2003",
|
|
"f_int": {
|
|
"T_reducing": 1.0,
|
|
"T_reducing_units": "K",
|
|
"a": [
|
|
0.00109939,
|
|
3.72539e-07
|
|
],
|
|
"t": [
|
|
0,
|
|
1
|
|
]
|
|
},
|
|
"psi": {
|
|
"a": [
|
|
1.3521,
|
|
-0.123177
|
|
],
|
|
"rhomolar_reducing": 5309.0,
|
|
"rhomolar_reducing_units": "mol/m^3",
|
|
"t": [
|
|
0,
|
|
1
|
|
]
|
|
},
|
|
"q_D": 1999999999.9999998,
|
|
"q_D_units": "m",
|
|
"reference_fluid": "Propane",
|
|
"type": "ECS"
|
|
},
|
|
"viscosity": {
|
|
"BibTeX": "Huber-IECR-2003",
|
|
"epsilon_over_k": 298.9,
|
|
"epsilon_over_k_units": "K",
|
|
"psi": {
|
|
"a": [
|
|
1.33962,
|
|
-0.256307,
|
|
0.0468211
|
|
],
|
|
"rhomolar_reducing": 5309.0,
|
|
"rhomolar_reducing_units": "mol/m^3",
|
|
"t": [
|
|
0,
|
|
1,
|
|
2
|
|
]
|
|
},
|
|
"reference_fluid": "Propane",
|
|
"sigma_eta": 4.678e-10,
|
|
"sigma_eta_units": "m",
|
|
"type": "ECS"
|
|
}
|
|
}
|
|
} |