mirror of
https://github.com/CoolProp/CoolProp.git
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496 lines
11 KiB
JSON
496 lines
11 KiB
JSON
{
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"ALIASES": [
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"propylene",
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"PROPYLENE"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-43449.042829786624,
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213.1249377020519,
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-0.16210220937993092,
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-0.001981758614296934,
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1.3633615837952145e-05,
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-4.449528012555178e-08,
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7.330345584768746e-11,
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-5.039244089712732e-14
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],
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"B": [
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1,
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-0.0027070315280724477
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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": 242.47068984066482,
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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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28437.42777746006,
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-82.11459985692579,
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-0.9260922905952403,
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0.010867038672228144,
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-5.745730116755436e-05,
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1.667087921155331e-07,
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-2.575660466646416e-10,
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1.6839335464444013e-13
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],
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"B": [
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1,
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-0.0027056869223002467
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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": 559.6975776629452,
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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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"parts": [
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{
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"T_0": 86.0,
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"T_max": 129,
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"T_min": 86.0,
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"a": 319600000.0,
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"c": 2.821,
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"p_0": 0
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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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"T_min": 129,
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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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"pL": {
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"T_r": 364.211,
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"Tmax": 364.2109999999991,
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"Tmin": 87.95300000000002,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.039256968605339004,
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"n": [
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0.001133775984851922,
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-5.98182751110803,
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3.6974583382927824,
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-0.9162432153073952
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],
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"reducing_value": 4555000.0,
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"t": [
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0.189,
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0.977,
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2.913,
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3.289,
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6.805,
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18.129
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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": 364.211,
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"Tmax": 364.2109999999991,
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"Tmin": 87.95300000000002,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.02358382509746182,
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"n": [
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],
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"t": [
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0.985,
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3.354,
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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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"Tmax": 364.2109999999991,
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"Tmin": 87.95300000000002,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.15187793211883793,
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"n": [
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1.1500616940414559,
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0.7037673936905474,
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0.6950815609799416,
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1.8850870474961088,
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2.21238242151199
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],
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"reducing_value": 5457.0,
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"t": [
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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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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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"Tmax": 364.2109999999991,
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"Tmin": 87.95300000000002,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.931595165746768,
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"n": [
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-5.13562614673855,
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4.2053374767917395,
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4.971018368148577,
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],
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"reducing_value": 5457.0,
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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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"using_tau_r": true
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},
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"sL": {
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"A": [
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4.474058496135499,
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0.00020407873804568927,
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-7.416229480453332e-07,
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1.6681986700703618e-09,
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-2.1125481072677604e-12,
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1.1487741169867998e-15
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],
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"B": [
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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/K; value is entropy minus hs_anchor entropy",
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"max_abs_error": 0.8620994483373341,
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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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1209.348785468865,
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0.270832448627616,
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6.764994306267737e-06,
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2.148854143535545e-11,
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],
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"B": [
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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/K; value is entropy minus hs_anchor entropy",
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"max_abs_error": 2.847437396322664,
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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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"CAS": "115-07-1",
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"ENVIRONMENTAL": {
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"ASHRAE34": "A3",
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"FH": 4,
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"GWP100": 3.1,
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"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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"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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"hs_anchor": {
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"T": 400.63210000000004,
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"hmolar": 26645.377075672735,
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"hmolar_units": "J/mol",
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"p": 7310423.540616656,
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},
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"p": 4555000,
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},
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"T": 87.953,
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"p": -1,
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"p_units": "Pa",
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"rhomolar": -1,
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"rhomolar_units": "mol/m^3"
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},
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"T": 87.953,
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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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"accentric": 0.146,
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"alpha0": [
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{
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{
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},
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{
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"n": [
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"t": [
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"type": "IdealGasHelmholtzPlanckEinstein"
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},
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{
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"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
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}
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"type": "ResidualHelmholtzPower"
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"beta": [
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"epsilon": [
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"eta": [
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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": 0.04207974,
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"molar_mass_units": "kg/mol",
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"p_max": 1000000000,
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"pseudo_pure": false
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}
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],
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"NAME": "Propylene",
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"REFPROP_NAME": "PROPYLEN",
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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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"p": 4555000.0,
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"p_units": "Pa",
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"rhomolar": 5457.0,
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},
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"triple_liquid": {
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"T": 87.953,
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"p": -1,
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"rhomolar": -1,
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"rhomolar_units": "mol/m^3"
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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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"p": -1,
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"p_units": "Pa",
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"rhomolar": -1,
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"rhomolar_units": "mol/m^3"
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}
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}
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} |