Files
CoolProp/dev/fluids/RC318.json

540 lines
13 KiB
JSON

{
"ANCILLARIES": {
"hL": {
"A": [
97108.00777536437,
-4167.031039503142,
47.44081772402304,
-0.2789970803615067,
0.0009751338143115229,
-2.0391767778269797e-06,
2.3584227819664906e-09,
-1.1640351439756232e-12
],
"B": [
1,
-0.0025587270690500164
],
"Tmax": 388.28,
"Tmin": 233.35,
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 209.80633134013078,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"hLV": {
"A": [
-591505.8327839759,
15168.13419763823,
-158.85428133647085,
0.9127745782236029,
-0.003130733790315338,
6.41541353970224e-06,
-7.274991487312669e-09,
3.5245148421487234e-12
],
"B": [
1,
-0.002557104062343887
],
"Tmax": 388.28,
"Tmin": 233.35,
"_note": "coefficients are in increasing order; input in K, output in J/mol; value is enthalpy minus hs_anchor enthalpy",
"max_abs_error": 449.9345433735564,
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"pS": {
"T_r": 388.38,
"Tmax": 388.37999999999914,
"Tmin": 233.35,
"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.019138662643680693,
"n": [
-15.102617412971505,
8.53184439256971,
-1.3014556054852215,
-3.286800573693744,
-8.150652838303959,
0.020748299859318566
],
"reducing_value": 2777500.0,
"t": [
1.017,
1.071,
2.454,
3.687,
9.48,
0.506
],
"type": "pL",
"using_tau_r": true
},
"rhoL": {
"T_r": 388.38,
"Tmax": 388.37999999999914,
"Tmin": 233.35,
"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.5464670263682914,
"n": [
6.172092166054074,
-13.109692547967464,
382.2970506693918,
-475.82711917828664,
190.84639492080177,
-142.60801162239488
],
"reducing_value": 3099.38,
"t": [
0.52,
0.979,
2.105,
2.269,
3.362,
4.954
],
"type": "rhoLnoexp",
"using_tau_r": false
},
"rhoV": {
"T_r": 388.38,
"Tmax": 388.37999999999914,
"Tmin": 233.35,
"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.2883096383379913,
"n": [
0.06881363274511793,
-4.9709012896577605,
3.1335807931630963,
-4.8498027190461865,
-3405.1114368231356,
4685.608624866425
],
"reducing_value": 3099.38,
"t": [
0.117,
0.455,
0.746,
1.132,
8.848,
9.296
],
"type": "rhoV",
"using_tau_r": true
},
"sL": {
"A": [
-224.89393682750583,
-2.62584115379871,
0.055091607442938076,
-0.00038307686953836307,
1.4628864227106823e-06,
-3.2569547059529292e-09,
3.958840339199141e-12,
-2.036192981950933e-15
],
"B": [
1,
-0.0025587526016840204
],
"Tmax": 388.28,
"Tmin": 233.35,
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 0.5402880405253079,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
},
"sLV": {
"A": [
-399.0753403774678,
19.605275995057834,
-0.25120550112786844,
0.0015938651700138993,
-5.805980223002076e-06,
1.2401116774437711e-08,
-1.4502826328173382e-11,
7.19691776460456e-15
],
"B": [
1,
-0.0025572789472560593
],
"Tmax": 388.28,
"Tmin": 233.35,
"_note": "coefficients are in increasing order; input in K, output in J/mol/K; value is entropy minus hs_anchor entropy",
"max_abs_error": 1.1510941178453304,
"max_abs_error_units": "J/mol/K",
"type": "rational_polynomial"
},
"surface_tension": {
"BibTeX": "Mulero-JPCRD-2012",
"Tc": 388.38,
"a": [
0.0507
],
"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
"n": [
1.25
]
}
},
"EOS": [
{
"BibTeX_CP0": "Platzer-BOOK-1990",
"BibTeX_EOS": "Platzer-BOOK-1990",
"STATES": {
"hs_anchor": {
"T": 427.218,
"T_units": "K",
"hmolar": 80910.32651491373,
"hmolar_units": "J/mol",
"p": 4688214.666190826,
"p_units": "Pa",
"rhomolar": 2789.442,
"rhomolar_units": "mol/m^3",
"smolar": 314.20614745923746,
"smolar_units": "J/mol/K"
},
"reducing": {
"T": 388.38,
"T_units": "K",
"hmolar": 71730.94762603201,
"hmolar_units": "J/mol",
"p": 2777500,
"p_units": "Pa",
"rhomolar": 3099.38,
"rhomolar_units": "mol/m^3",
"smolar": 293.2686676934833,
"smolar_units": "J/mol/K"
},
"sat_min_liquid": {
"T": 233.35,
"T_units": "K",
"hmolar": 31957.19563750956,
"hmolar_units": "J/mol",
"p": 19461.056081372997,
"p_units": "Pa",
"rhomolar": 8645.18328651729,
"rhomolar_units": "mol/m^3",
"smolar": 168.26971481332566,
"smolar_units": "J/mol/K"
},
"sat_min_vapor": {
"T": 233.35,
"T_units": "K",
"hmolar": 57605.81616033167,
"hmolar_units": "J/mol",
"p": 19461.056081372997,
"p_units": "Pa",
"rhomolar": 10.156986147247,
"rhomolar_units": "mol/m^3",
"smolar": 278.18445707047107,
"smolar_units": "J/mol/K"
}
},
"T_max": 623,
"T_max_units": "K",
"Ttriple": 233.35,
"Ttriple_units": "K",
"acentric": 0.355345,
"acentric_units": "-",
"alpha0": [
{
"a1": 0,
"a2": 0,
"type": "IdealGasHelmholtzLead"
},
{
"a": -1,
"type": "IdealGasHelmholtzLogTau"
},
{
"T0": 298.15,
"Tc": 388.38,
"c": [
2.911028455074322,
0.06984062483537816,
-6.093191543939451e-05,
1.857067747732578e-08
],
"t": [
0,
1,
2,
3
],
"type": "IdealGasHelmholtzCP0PolyT"
},
{
"a1": -32.5172232538152,
"a2": 20.7826742209953,
"reference": "IIR",
"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
}
],
"alphar": [
{
"d": [
1,
1,
1,
1,
1,
2,
2,
2,
3,
3,
4,
4,
5,
0,
0,
0
],
"l": [
0,
0,
0,
0,
0,
0,
0,
0,
0,
0,
0,
0,
0,
0,
0,
0
],
"n": [
1.09415573664603,
-2.68265247887176,
1.73403070801418,
-1.63611253452478,
0.304834511239559,
0.102771559991302,
-0.023236791408773,
0.166151971110653,
-0.0250103944487447,
0.0935681090149423,
0.043192919662493,
-0.133439867188959,
0.025541668325497,
-1.04729119771286,
1.38034128674154,
-0.333625770182218
],
"t": [
0,
1,
2,
3,
4,
0,
1,
2,
0,
1,
0,
1,
1,
3,
4,
5
],
"type": "ResidualHelmholtzPower"
},
{
"d": [
2,
2,
2,
0,
0,
0
],
"g": [
0.99944,
0.99944,
0.99944,
0.99944,
0.99944,
0.99944
],
"l": [
2,
2,
2,
2,
2,
2
],
"n": [
-0.510485822124397,
1.81840742529488,
-1.38530904967474,
1.04729119771286,
-1.38034128674154,
0.333625770182218
],
"t": [
3,
4,
5,
3,
4,
5
],
"type": "ResidualHelmholtzExponential"
}
],
"critical_region_splines": {
"T_max": 388.38,
"T_min": 388.29054792405356,
"_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": [
1.1298449787658047e-09,
-1.2403349555998569e-05,
0.04432498442528143,
336.509525023081
],
"cV": [
-1.04204053156705e-09,
7.774300413950925e-06,
-0.018161009518633232,
401.01153126933485
],
"rhomolar_max": 3333.3908947283726,
"rhomolar_min": 2868.2068492030176
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",
"molar_mass": 0.2000312,
"molar_mass_units": "kg/mol",
"p_max": 60000000,
"p_max_units": "Pa",
"pseudo_pure": false
}
],
"INFO": {
"2DPNG_URL": "http://www.chemspider.com/ImagesHandler.ashx?id=13846040",
"ALIASES": [],
"CAS": "115-25-3",
"CHEMSPIDER_ID": 13846040,
"ENVIRONMENTAL": {
"ASHRAE34": "A1",
"FH": 0,
"GWP100": 10300.0,
"GWP20": 7310.0,
"GWP500": 14700.0,
"HH": 1,
"Name": "RC318",
"ODP": -1.0,
"PH": 2
},
"FORMULA": "C_{4}F_{8}",
"INCHI_KEY": "BCCOBQSFUDVTJQ-UHFFFAOYSA-N",
"INCHI_STRING": "InChI=1S/C4F8/c5-1(6)2(7,8)4(11,12)3(1,9)10",
"NAME": "RC318",
"REFPROP_NAME": "RC318",
"SMILES": "C1(C(C(C1(F)F)(F)F)(F)F)(F)F"
},
"STATES": {
"critical": {
"T": 388.38,
"T_units": "K",
"hmolar": 71723.09920314865,
"hmolar_units": "J/mol",
"p": 2777500.0,
"p_units": "Pa",
"rhomolar": 3099.38,
"rhomolar_units": "mol/m^3",
"smolar": 293.25026117992604,
"smolar_units": "J/mol/K"
},
"triple_liquid": {
"T": 233.35,
"T_units": "K",
"hmolar": 31957.19563750956,
"hmolar_units": "J/mol",
"p": 19461.056081372997,
"p_units": "Pa",
"rhomolar": 8645.18328651729,
"rhomolar_units": "mol/m^3",
"smolar": 168.26971481332566,
"smolar_units": "J/mol/K"
},
"triple_vapor": {
"T": 233.35,
"T_units": "K",
"hmolar": 57605.81616033167,
"hmolar_units": "J/mol",
"p": 19461.056081372997,
"p_units": "Pa",
"rhomolar": 10.156986147247,
"rhomolar_units": "mol/m^3",
"smolar": 278.18445707047107,
"smolar_units": "J/mol/K"
}
},
"TRANSPORT": {
"conductivity": {
"BibTeX": "Huber-IECR-2003",
"f_int": {
"T_reducing": 1.0,
"T_reducing_units": "K",
"a": [
0.00135697,
-1.11635e-07
],
"t": [
0,
1
]
},
"psi": {
"a": [
1.5249,
-0.147564
],
"rhomolar_reducing": 3099.0,
"rhomolar_reducing_units": "mol/m^3",
"t": [
0,
1
]
},
"q_D": 2808318238.622801,
"q_D_units": "m",
"reference_fluid": "Propane",
"type": "ECS"
},
"viscosity": {
"BibTeX": "Huber-IECR-2003",
"epsilon_over_k": 299.76,
"epsilon_over_k_units": "K",
"psi": {
"a": [
1.21141,
-0.0337573,
0.0
],
"rhomolar_reducing": 3099.0,
"rhomolar_reducing_units": "mol/m^3",
"t": [
0,
1,
2
]
},
"reference_fluid": "Propane",
"sigma_eta": 5.947e-10,
"sigma_eta_units": "m",
"type": "ECS"
}
}
}