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

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{
"ALIASES": [
"ethylbenzene",
"ETHYLBENZENE",
"EBENZENE"
],
"ANCILLARIES": {
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1.16182336098948e-06,
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6.9925131882217655e-12,
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],
"B": [
1,
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],
"Tmax": 617.02,
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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": 577.4714066773122,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"hLV": {
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0.006906213960454069,
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3.447314161438705e-08,
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1.1370007218750129e-14
],
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1,
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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": 1376.65207822929,
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"type": "rational_polynomial"
},
"pL": {
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"Tmin": 178.2,
"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.029287453591875234,
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],
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1.41,
1.581,
4.148,
6.154,
15.215
],
"type": "pL",
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},
"pV": {
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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0.96,
3.544,
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14.911
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},
"rhoL": {
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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1.422,
1.801,
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"type": "rhoLnoexp",
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},
"rhoV": {
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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0.426,
0.545,
1.641,
2.034,
2.35,
5.977
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4.124860459434708,
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6.030194711252977e-05,
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1.633732055008026e-10,
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3.5669504586285435e-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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"type": "rational_polynomial"
},
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0.09649651478787952,
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7.340683208951656e-07,
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7.235767518238929e-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/K; value is entropy minus hs_anchor entropy",
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"type": "rational_polynomial"
},
"surface_tension": {
"BibTeX": "Mulero-JPCRD-2014",
"Tc": 617.12,
"a": [
0.0638
],
"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
"n": [
1.22
]
}
},
"CAS": "100-41-4",
"EOS": [
{
"BibTeX_CP0": "",
"BibTeX_EOS": "Zhou-JPCRD-2012",
"STATES": {
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},
"sat_min_vapor": {
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"hmolar": 6972.983095485733,
"hmolar_units": "J/mol",
"p": 0.0040029613919103525,
"p_units": "Pa",
"rhomolar": 2.701711909771278e-06,
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}
},
"T_max": 700,
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"Ttriple": 178.2,
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"accentric": 0.304,
"accentric_units": "-",
"alpha0": [
{
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"type": "IdealGasHelmholtzLead"
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{
"a": 4.2557889,
"type": "IdealGasHelmholtzLogTau"
},
{
"n": [
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11.201832,
25.440749
],
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7.16230230749287,
2.710980036297641
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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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1.5059649,
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0.18814732,
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1.1222031,
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2.31,
3.21,
1.26,
2.29,
1
],
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},
{
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1.488,
4,
418.6
],
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1,
1,
3,
3
],
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0.5494,
0.7235,
0.493,
0.8566
],
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1.178,
1.07,
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15.45
],
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1.2667,
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0.8573,
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],
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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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617.1837152780217
],
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0.0,
0.0,
2.3091817015124984e-05,
617.0567049600925
],
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},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",
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"molar_mass_units": "kg/mol",
"p_max": 60000000,
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"pseudo_pure": false
}
],
"NAME": "EthylBenzene",
"REFPROP_NAME": "EBENZENE",
"STATES": {
"critical": {
"T": 617.12,
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"p": 3622400.0,
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},
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"p": 0.00400362117221462,
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"smolar": -151.14886877937155,
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},
"triple_vapor": {
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"T_units": "K",
"hmolar": 6972.983095485733,
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"p": 0.0040029613919103525,
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"rhomolar": 2.701711909771278e-06,
"rhomolar_units": "mol/m^3",
"smolar": 130.06354628558384,
"smolar_units": "J/mol/K"
}
}
}