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CoolProp/dev/fluids/R161.json

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{
"ANCILLARIES": {
"hL": {
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-44208.06787744796,
83.11502451831647,
2.2034724058299564,
-0.02034756142870472,
8.977950824938847e-05,
-2.1981606798257965e-07,
2.842009515003384e-10,
-1.5298119987590643e-13
],
"B": [
1,
-0.002633998519416297
],
"Tmax": 375.15,
"Tmin": 130.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 213.2189938015199,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"hLV": {
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297.8019527583096,
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0.051640526323812004,
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5.500283412737703e-07,
-7.291196362327358e-10,
4.070956348787284e-13
],
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1,
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],
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"Tmin": 130.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 522.4684359010557,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"pS": {
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"Tmin": 130.0,
"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.028081837897198092,
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4.717832719212871,
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6.727500969566306
],
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0.358,
0.979,
2.041,
2.312,
7.268,
8.389
],
"type": "pL",
"using_tau_r": true
},
"rhoL": {
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"Tmin": 130.0,
"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.09082481888231797,
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6.89480557431733,
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183.43884409350315,
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0.331,
0.379,
0.459,
3.341,
6.576,
6.669
],
"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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"t": [
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0.482,
0.891,
2.774,
4.26,
6.784
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"type": "rhoV",
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},
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4.371484182030741,
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0.00010274415135566685,
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2.588633871448754e-10,
-1.0488487608914702e-13,
-2.546962154308005e-17
],
"B": [
1,
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],
"Tmax": 375.15,
"Tmin": 130.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 0.5810079887806072,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
},
"sLV": {
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1112.9341756366573,
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0.1665441887853578,
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2.7009325045261515e-06,
-5.261094313458255e-09,
5.773068263475169e-12,
-2.735558475347271e-15
],
"B": [
1,
-0.002618024817634138
],
"Tmax": 375.15,
"Tmin": 130.0,
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 1.6327486011842343,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
},
"surface_tension": {
"BibTeX": "Mulero-JPCRD-2012",
"Tc": 375.3,
"a": [
0.05385
],
"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
"n": [
1.111
]
}
},
"EOS": [
{
"BibTeX_CP0": "",
"BibTeX_EOS": "Wu-IJT-2012",
"STATES": {
"hs_anchor": {
"T": 412.77500000000003,
"T_units": "K",
"hmolar": 29437.268109986722,
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"p": 8287479.703515427,
"p_units": "Pa",
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"rhomolar_units": "mol/m^3",
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},
"reducing": {
"T": 375.25,
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"hmolar": 24708.620430200757,
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"p": 5010000,
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"rhomolar": 6280,
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"smolar": 92.40626321706736,
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},
"sat_min_liquid": {
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"p": 5.512269644056271,
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"smolar": -23.671883018905913,
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},
"sat_min_vapor": {
"T": 130.0,
"T_units": "K",
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"hmolar_units": "J/mol",
"p": 5.512269644056271,
"p_units": "Pa",
"rhomolar": 0.005099846396055564,
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"smolar": 175.5995934256763,
"smolar_units": "J/mol/K"
}
},
"T_max": 450,
"T_max_units": "K",
"Ttriple": 130,
"Ttriple_units": "K",
"acentric": 0.2162428410661867,
"acentric_units": "-",
"alpha0": [
{
"a1": -6.9187,
"a2": 5.4788,
"type": "IdealGasHelmholtzLead"
},
{
"a": 3,
"type": "IdealGasHelmholtzLogTau"
},
{
"n": [
2.059,
9.253,
6.088
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"t": [
1.11925383077948,
4.125249833444371,
10.34510326449034
],
"type": "IdealGasHelmholtzPlanckEinstein"
},
{
"a1": 4.21805657510139e-05,
"a2": -4.5424171382829e-06,
"reference": "IIR",
"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
}
],
"alphar": [
{
"d": [
1,
1,
2,
3,
4,
2,
7,
1,
2,
3
],
"l": [
0,
0,
0,
0,
0,
1,
1,
2,
2,
2
],
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0.1683,
0.04133,
0.62187,
-0.0265,
-1.03,
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],
"t": [
0.37,
0.97,
1.14,
0.744,
1,
1.26,
1,
1.8,
3,
2.25
],
"type": "ResidualHelmholtzPower"
},
{
"beta": [
2.7,
5.2,
3.9,
4.7,
413
],
"d": [
1,
1,
3,
3,
3
],
"epsilon": [
0.683,
0.892,
0.785,
1.33,
0.86
],
"eta": [
0.96,
1.35,
1.26,
1.23,
16.8
],
"gamma": [
0.9,
0.69,
0.67,
0.67,
1.15
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"n": [
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],
"t": [
1,
1.2,
5.3,
1,
4
],
"type": "ResidualHelmholtzGaussian"
}
],
"critical_region_splines": {
"T_max": 375.25,
"T_min": 375.2498876027567,
"_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,
-1.0274211653082636e-06,
375.25645220491816
],
"cV": [
0.0,
0.0,
6.800670480519312e-07,
375.24572917893823
],
"rhomolar_max": 6389.397438091061,
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},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",
"molar_mass": 0.0480595,
"molar_mass_units": "kg/mol",
"p_max": 5000000,
"p_max_units": "Pa",
"pseudo_pure": false
}
],
"INFO": {
"2DPNG_URL": "http://www.chemspider.com/ImagesHandler.ashx?id=9243",
"ALIASES": [
"Fluoroethane",
"FLUOROETHANE"
],
"CAS": "353-36-6",
"CHEMSPIDER_ID": 9243,
"ENVIRONMENTAL": {
"ASHRAE34": "UNKNOWN",
"FH": -1,
"GWP100": 10.0,
"GWP20": -1.0,
"GWP500": -1.0,
"HH": -1,
"Name": "R161",
"ODP": -1.0,
"PH": -1
},
"FORMULA": "C_{2}F_{1}H_{5}",
"INCHI_KEY": "UHCBBWUQDAVSMS-UHFFFAOYSA-N",
"INCHI_STRING": "InChI=1S/C2H5F/c1-2-3/h2H2,1H3",
"NAME": "R161",
"REFPROP_NAME": "R161",
"SMILES": "CCF"
},
"STATES": {
"critical": {
"T": 375.25,
"T_units": "K",
"hmolar": 24704.381939700208,
"hmolar_units": "J/mol",
"p": 5010000.0,
"p_units": "Pa",
"rhomolar": 6280.0,
"rhomolar_units": "mol/m^3",
"smolar": 92.39649962952795,
"smolar_units": "J/mol/K"
},
"triple_liquid": {
"T": 130.0,
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"p": 5.512269644056271,
"p_units": "Pa",
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"rhomolar_units": "mol/m^3",
"smolar": -23.671883018905913,
"smolar_units": "J/mol/K"
},
"triple_vapor": {
"T": 130.0,
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"p": 5.512269644056271,
"p_units": "Pa",
"rhomolar": 0.005099846396055564,
"rhomolar_units": "mol/m^3",
"smolar": 175.5995934256763,
"smolar_units": "J/mol/K"
}
}
}
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