mirror of
https://github.com/CoolProp/CoolProp.git
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400 lines
9.5 KiB
JSON
400 lines
9.5 KiB
JSON
{
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"ALIASES": [
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"HFE-143m",
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"HFE143M",
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"HFE-143M",
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"RE143A",
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"RE143a"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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378887.3968233684,
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-10235.405985982265,
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107.36956665002454,
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-0.6113000082928615,
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0.002077514974267441,
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-4.226949314169069e-06,
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4.768147406433093e-09,
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-2.3018117042900677e-12
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],
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"B": [
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1,
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-0.0026318881287905292
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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": 165.023019710703,
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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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"hLV": {
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"A": [
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6.158126400339369e-12
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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": 412.1653356048764,
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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": 377.921,
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"Tmax": 377.9209999999992,
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"Tmin": 240.0,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.030182989158467066,
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"n": [
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"t": [
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],
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"type": "pL",
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"using_tau_r": true
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},
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"pV": {
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"T_r": 377.921,
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"Tmin": 240.0,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"n": [
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535.477430612564
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"t": [
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],
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"type": "pV",
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"using_tau_r": true
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},
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"rhoL": {
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"T_r": 377.921,
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"Tmax": 377.9209999999992,
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"Tmin": 240.0,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.6804963381005225,
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"n": [
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"t": [
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14.608
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],
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"type": "rhoLnoexp",
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"using_tau_r": false
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},
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"rhoV": {
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"Tmin": 240.0,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"n": [
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],
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"type": "rhoV",
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"using_tau_r": true
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},
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"sL": {
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"A": [
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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/K; value is entropy minus hs_anchor entropy",
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"max_abs_error": 0.43115607181984217,
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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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"sLV": {
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"A": [
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2.672346148163148e-08,
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1.4717683768570267e-14
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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/K; value is entropy minus hs_anchor entropy",
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"max_abs_error": 1.0793800646766871,
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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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},
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"CAS": "421-14-7",
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"EOS": [
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{
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"BibTeX_CP0": "",
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"BibTeX_EOS": "Akasaka-IJR-2012",
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"STATES": {
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"hs_anchor": {
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"T": 415.7131,
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"T_units": "K",
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"hmolar": 45804.980982478475,
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"hmolar_units": "J/mol",
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"p": 6187531.691209243,
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"p_units": "Pa",
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"rhomolar": 4183.3266696,
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"rhomolar_units": "mol/m^3",
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"smolar": 172.32643268128248,
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"smolar_units": "J/mol/K"
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},
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"reducing": {
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"T": 377.921,
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"T_units": "K",
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"p": 3635000,
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"p_units": "Pa",
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},
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"sat_min_liquid": {
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"T": 240.0,
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"T_units": "K",
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"p": 65.35939300696849,
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"rhomolar_units": "mol/m^3"
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},
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"sat_min_vapor": {
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"T": 240.0,
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"T_units": "K",
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"p": 65.35939300696849,
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}
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},
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"T_max": 4220,
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"Ttriple": 240,
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{
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{
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"a": -1,
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"type": "IdealGasHelmholtzLogTau"
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{
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"T0": 273.15,
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"Tc": 377.921,
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"type": "IdealGasHelmholtzCP0Constant"
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{
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"c": [
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{
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"a1": 7.64964970449937e-05,
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"a2": -8.0498560479886e-05,
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"reference": "IIR",
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"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
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"type": "ResidualHelmholtzPower"
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"gas_constant": 8.314472,
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}
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],
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"NAME": "HFE143m",
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"REFPROP_NAME": "RE143A",
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"STATES": {
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"critical": {
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"T": 377.921,
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"p": 3635000.0,
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},
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}
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}
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} |