Files
CoolProp/dev/fluids/p-Xylene.json
2014-11-07 16:25:42 -05:00

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{
"ALIASES": [
"pXylene",
"p-xylene",
"P-XYLENE"
],
"ANCILLARIES": {
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4.537631846023305,
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5.2211701280505017e-11,
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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",
"max_abs_error": 387.8138198691813,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
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0.060824344551203266,
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2.1934465426750028e-07,
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5.964215036127467e-14
],
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1,
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],
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"type": "rational_polynomial"
},
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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11.727352138248827,
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56.69266520413931
],
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"t": [
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1.227,
1.257,
2.906,
7.04,
15.693
],
"type": "pL",
"using_tau_r": true
},
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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19.915248950746882,
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1.271,
2.955,
4.359,
5.234
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},
"rhoL": {
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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26.985091589824126,
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"t": [
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6.974,
11.02,
11.7
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"type": "rhoLnoexp",
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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0.546,
0.651,
2.515,
3.948
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},
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3.3018684225127134e-08,
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5.298068083873676e-14,
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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/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 0.6264315550761879,
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"type": "rational_polynomial"
},
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0.031514127286592204,
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7.505683851429195e-08,
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2.607451906458159e-17
],
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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_units": "J/mol/K",
"type": "rational_polynomial"
},
"surface_tension": {
"BibTeX": "Mulero-JPCRD-2014",
"Tc": 616.168,
"a": [
0.0619
],
"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
"n": [
1.21
]
}
},
"CAS": "106-42-3",
"EOS": [
{
"BibTeX_CP0": "",
"BibTeX_EOS": "Zhou-JPCRD-2012",
"STATES": {
"hs_anchor": {
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},
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},
"sat_min_vapor": {
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"p": 580.0850024821935,
"p_units": "Pa",
"rhomolar": 0.24384664073930953,
"rhomolar_units": "mol/m^3",
"smolar": 78.13383837043023,
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}
},
"T_max": 700,
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"Ttriple": 286.4,
"Ttriple_units": "K",
"accentric": 0.324,
"accentric_units": "-",
"alpha0": [
{
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"a2": -0.52477835,
"type": "IdealGasHelmholtzLead"
},
{
"a": 4.2430504,
"type": "IdealGasHelmholtzLogTau"
},
{
"n": [
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19.549862,
16.656178,
5.9390291
],
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0.6718946780748107,
2.038405110294595,
4.299152179275782,
10.84282208748263
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}
],
"alphar": [
{
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5,
1,
4,
1,
1,
2,
3,
1,
3,
2,
2,
7
],
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0,
0,
0,
0,
0,
0,
0,
2,
2,
1,
2,
1
],
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0.0010786811,
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0.0421544125,
1.47865376,
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0.190290995,
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1.25159879,
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1,
0.83,
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0.281,
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1.1,
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2.62,
2.5,
1.2,
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],
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},
{
"beta": [
2.445,
1.483,
4.971,
413
],
"d": [
1,
1,
3,
3
],
"epsilon": [
0.54944,
0.7234,
0.4926,
0.8459
],
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1.179,
1.065,
1.764,
13.675
],
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1.267,
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1.1465
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1.3710318,
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],
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1.13,
4.5,
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2
],
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}
],
"critical_region_splines": {
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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",
"cL": [
0.0,
0.0,
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616.1979902589276
],
"cV": [
0.0,
0.0,
8.534367674093475e-06,
616.1450090962354
],
"rhomolar_max": 2728.633033173596,
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},
"gas_constant": 8.314472,
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"molar_mass_units": "kg/mol",
"p_max": 200000000,
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"pseudo_pure": false
}
],
"NAME": "p-Xylene",
"REFPROP_NAME": "PXYLENE",
"STATES": {
"critical": {
"T": 616.168,
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"p": 3531500.0,
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},
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"smolar_units": "J/mol/K"
},
"triple_vapor": {
"T": 286.40000000000003,
"T_units": "K",
"hmolar": 17947.385463889368,
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"p": 580.0850024821935,
"p_units": "Pa",
"rhomolar": 0.24384664073930953,
"rhomolar_units": "mol/m^3",
"smolar": 78.13383837043023,
"smolar_units": "J/mol/K"
}
}
}