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CoolProp/dev/fluids/CycloPropane.json
Ian Bell 24d37e0e6d Added h and s to hs_anchor state 
Signed-off-by: Ian Bell <ian.h.bell@gmail.com>
2014-08-01 10:09:12 +02:00

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{
"ALIASES": [
"cyclopropane",
"Cyclopropane",
"CYCLOPROPANE"
],
"ANCILLARIES": {
"hL": {
"A": [
-253345.27767632276,
1248.3038108124997,
17.832092464779162,
-0.2165516899884562,
0.0009972038942279832,
-2.3684035826701307e-06,
2.8958118754073264e-09,
-1.4508224051993072e-12
],
"B": [
1,
-0.0024911778022501333
],
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 38.62652617999629,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"hLV": {
"A": [
-1311659.514457395,
32664.987076239664,
-333.7938182724562,
1.8516639266767503,
-0.006067443026175092,
1.17872724200856e-05,
-1.2603361077580505e-08,
5.733894257601881e-12
],
"B": [
1,
-0.002490105821465514
],
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 84.07903235766071,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"pL": {
"T_r": 398.3,
"Tmax": 398.29999999999905,
"Tmin": 273.0,
"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.1955382615515866,
"n": [
-0.3126990224115789,
-6.287859890805818,
6.987582031173733,
-1037.2571651529406,
45989.92002915465,
-4973989.497831943
],
"reducing_value": 5579700.0,
"t": [
0.596,
1.059,
2.997,
6.895,
10.211,
15.224
],
"type": "pL",
"using_tau_r": true
},
"pV": {
"T_r": 398.3,
"Tmax": 398.29999999999905,
"Tmin": 273.0,
"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.10977489544659047,
"n": [
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0.18406121015183027,
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],
"reducing_value": 5579700.0,
"t": [
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0.181,
0.421,
0.983,
6.3,
16.644
],
"type": "pV",
"using_tau_r": true
},
"rhoL": {
"T_r": 398.3,
"Tmax": 398.29999999999905,
"Tmin": 273.0,
"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
"max_abserror_percentage": 1.0200689433471744,
"n": [
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17.39312205196081,
-65.70893634663562,
917.3256648476147,
-909.8353253919709,
1550.3280904976405
],
"reducing_value": 6142.9149,
"t": [
0.109,
0.951,
1.509,
2.43,
2.535,
7.779
],
"type": "rhoLnoexp",
"using_tau_r": false
},
"rhoV": {
"T_r": 398.3,
"Tmax": 398.29999999999905,
"Tmin": 273.0,
"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 1.9812724524870484,
"n": [
-0.33841331698570076,
-4.9703350919635545,
5.62081036731097,
-352.4354033337558,
14193580833.179937,
-19206776520.109684
],
"reducing_value": 6142.9149,
"t": [
0.098,
0.654,
2.255,
5.732,
18.195,
18.473
],
"type": "rhoV",
"using_tau_r": true
},
"sL": {
"A": [
-3825.0954600322607,
65.49374738890369,
-0.4814738510291171,
0.0019340202588417179,
-4.513126188970276e-06,
5.994374780357294e-09,
-4.031462685408403e-12,
9.4762898335311e-16
],
"B": [
1,
-0.002490985129345838
],
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 0.09856764258082151,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
},
"sLV": {
"A": [
1189.2422752928803,
-4.162949365668244,
-0.11607129275733974,
0.0012560417074918171,
-5.614352056744316e-06,
1.317720872096359e-08,
-1.6039129748441434e-11,
8.025951437457725e-15
],
"B": [
1,
-0.0024901242977006547
],
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 0.21110000978237853,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
},
"surface_tension": {
"BibTeX": "Mulero-JPCRD-2014",
"Tc": 398.3,
"a": [
0.06812
],
"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
"n": [
1.314
]
}
},
"CAS": "75-19-4",
"ENVIRONMENTAL": {
"ASHRAE34": "UNKNOWN",
"FH": 2,
"GWP100": -1.0,
"GWP20": -1.0,
"GWP500": -1.0,
"HH": 2,
"Name": "CycloPropane",
"ODP": -1.0,
"PH": 0
},
"EOS": [
{
"BibTeX_CP0": "Polt-CT-1992",
"BibTeX_EOS": "Polt-CT-1992",
"STATES": {
"hs_anchor": {
"T": 438.13000000000005,
"T_units": "K",
"hmolar": 1832.8044750753984,
"hmolar_units": "J/mol",
"p": 8885152.833988935,
"p_units": "Pa",
"rhomolar": 5528.62341,
"rhomolar_units": "mol/m^3",
"smolar": 10.932672305121347,
"smolar_units": "J/mol/K"
},
"reducing": {
"T": 398.3,
"T_units": "K",
"p": 5579700,
"p_units": "Pa",
"rhomolar": 6142.9149,
"rhomolar_units": "mol/m^3"
},
"sat_min_liquid": {
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"T_units": "K",
"p": 342.7022037357092,
"p_units": "Pa",
"rhomolar": 15594.27233601817,
"rhomolar_units": "mol/m^3"
},
"sat_min_vapor": {
"T": 273.0,
"T_units": "K",
"p": 342.7022037357092,
"p_units": "Pa",
"rhomolar": 164.03030361467836,
"rhomolar_units": "mol/m^3"
}
},
"T_max": 473,
"T_max_units": "K",
"Ttriple": 145.7,
"Ttriple_units": "K",
"accentric": 0.1305495663687517,
"accentric_units": "-",
"alpha0": [
{
"a1": 0,
"a2": 0,
"type": "IdealGasHelmholtzLead"
},
{
"a": -1,
"type": "IdealGasHelmholtzLogTau"
},
{
"T0": 298.15,
"Tc": 398.3,
"c": [
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-0.04582023302189515,
0.0002558503477107775,
-3.908517142596848e-07,
2.051746651955177e-10
],
"t": [
0,
1,
2,
3,
4
],
"type": "IdealGasHelmholtzCP0PolyT"
},
{
"a1": -10.9358280454636,
"a2": 8.75156673092286,
"reference": "IIR",
"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
}
],
"alphar": [
{
"d": [
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],
"l": [
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],
"n": [
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"t": [
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],
"type": "ResidualHelmholtzPower"
}
],
"gas_constant": 8.3143,
"gas_constant_units": "J/mol/K",
"molar_mass": 0.042081,
"molar_mass_units": "kg/mol",
"p_max": 28000000,
"p_max_units": "Pa",
"pseudo_pure": false
}
],
"NAME": "CycloPropane",
"REFPROP_NAME": "CYCLOPRO",
"STATES": {
"critical": {
"T": 398.3,
"T_units": "K",
"p": 5579700.0,
"p_units": "Pa",
"rhomolar": 6142.9149,
"rhomolar_units": "mol/m^3"
},
"triple_liquid": {},
"triple_vapor": {}
}
}
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