mirror of
https://github.com/CoolProp/CoolProp.git
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528 lines
12 KiB
JSON
528 lines
12 KiB
JSON
{
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"ALIASES": [],
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"ANCILLARIES": {
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"hL": {
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"A": [
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3.707999994516502e-09,
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],
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"B": [
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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",
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"max_abs_error": 244.39478977885483,
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"max_abs_error_units": "J/mol",
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"type": "rational_polynomial"
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},
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],
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"B": [
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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",
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"max_abs_error": 508.83986085067534,
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"max_abs_error_units": "J/mol",
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"type": "rational_polynomial"
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},
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"pL": {
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"T_r": 227.51,
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"Tmax": 227.50999999999948,
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"Tmin": 120.00000000000001,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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},
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"pV": {
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"T_r": 227.51,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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],
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},
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"rhoL": {
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 4.396907124601834,
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"n": [
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18.15
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],
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"type": "rhoLnoexp",
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},
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"rhoV": {
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"Tmin": 120.00000000000001,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"type": "rhoV",
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"sL": {
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],
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"B": [
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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": 1.0993469538395004,
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"type": "rational_polynomial"
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"sLV": {
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0.1668557670186865,
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1.8287928320112446e-06,
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3.485540418463794e-09,
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3.311490828238214e-14
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"B": [
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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": 2.257760271761315,
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"max_abs_error_units": "J/mol/K",
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"type": "rational_polynomial"
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},
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"surface_tension": {
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"BibTeX": "Mulero-JPCRD-2012",
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"Tc": 227.51,
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"a": [
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0.0423
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],
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"description": "sigma = sum(a_i*(1-T/Tc)^n_i)",
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"n": [
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1.24
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]
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}
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},
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"CAS": "75-73-0",
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"ENVIRONMENTAL": {
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"ASHRAE34": "UNKNOWN",
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"FH": -1,
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"HH": -1,
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"Name": "R14",
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},
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"EOS": [
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{
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"BibTeX_CP0": "Platzer-BOOK-1990",
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"STATES": {
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"T": 250.26100000000002,
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}
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{
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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",
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"cL": [
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"gas_constant_units": "J/mol/K",
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"molar_mass": 0.0880046,
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"molar_mass_units": "kg/mol",
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"p_max": 51000000,
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"p_max_units": "Pa",
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"pseudo_pure": false
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}
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],
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"NAME": "R14",
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"REFPROP_NAME": "R14",
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"STATES": {
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"critical": {
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"T": 227.51,
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"p": 3750000.0,
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"p_units": "Pa",
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"rhomolar": 7109.4194,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 120.0,
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"p": 11294.329044434928,
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},
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"T": 120.0,
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"p": 11294.329044449365,
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}
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},
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"TRANSPORT": {
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"conductivity": {
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"BibTeX": "Huber-IECR-2003",
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"f_int": {
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"T_reducing": 1.0,
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"a": [
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1.90048e-07
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],
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},
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"psi": {
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],
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"t": [
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},
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"q_D": 4413724919.008148,
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"q_D_units": "m",
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"reference_fluid": "Nitrogen",
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|
"type": "ECS"
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|
},
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|
"viscosity": {
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"BibTeX": "Huber-IECR-2003",
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"epsilon_over_k": 164.44,
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|
"epsilon_over_k_units": "K",
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"psi": {
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"a": [
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|
1.10941,
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],
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"t": [
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]
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},
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"reference_fluid": "Nitrogen",
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|
"sigma_eta": 4.543e-10,
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|
"sigma_eta_units": "m",
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"type": "ECS"
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|
}
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}
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} |