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https://github.com/CoolProp/CoolProp.git
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470 lines
11 KiB
JSON
470 lines
11 KiB
JSON
{
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"ALIASES": [
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"R142B"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-59595.71861626421,
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214.00809458001083,
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0.39536642106616643,
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-0.005484574949127999,
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2.5775282032387285e-05,
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-6.793471988011212e-08,
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9.450262804539914e-11,
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-5.486614736485975e-14
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],
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"B": [
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1,
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-0.0024157168647948365
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],
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"Tmax": 410.15999999999997,
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"Tmin": 142.72,
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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": 338.64606920889037,
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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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31098.909123757687,
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78.71386788282098,
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-3.1961176860131495,
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0.025272729377753465,
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-0.00010746715139229126,
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2.613866397206111e-07,
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-3.4308795319465256e-10,
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1.9010669868052338e-13
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],
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"B": [
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1,
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],
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"Tmax": 410.15999999999997,
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"Tmin": 142.72,
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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": 717.8032873139482,
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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": 410.26,
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"Tmax": 410.25999999999914,
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"Tmin": 142.72,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.016702977994387247,
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"n": [
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1.620065366585568,
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],
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"t": [
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0.993,
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2.56,
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3.61,
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3.733,
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14.147
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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": 410.26,
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"Tmax": 410.25999999999914,
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"Tmin": 142.72,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.019960603250079867,
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"n": [
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"t": [
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0.416,
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1.491,
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3.189,
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5.386,
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4.774
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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": 410.26,
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"Tmax": 410.25999999999914,
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"Tmin": 142.72,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.5611813999881976,
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"n": [
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11.7638029884687,
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8.696072645236315,
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],
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"t": [
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0.247,
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0.26,
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1.896,
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3.015,
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7.62,
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15.172
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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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"T_r": 410.26,
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"Tmin": 142.72,
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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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"t": [
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4.103
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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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4.864430918411126e-10,
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1.8172154008414147e-16
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],
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"B": [
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1,
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],
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"Tmax": 410.15999999999997,
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"Tmin": 142.72,
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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": 0.876424140634338,
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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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0.14573728647268305,
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2.1145751936881395e-06,
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3.993940064364762e-12,
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],
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"B": [
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1,
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],
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"Tmax": 410.15999999999997,
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"Tmin": 142.72,
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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": 2.097572706102178,
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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": 410.26,
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"a": [
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0.05685
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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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1.237
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]
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}
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},
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"CAS": "75-68-3",
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"ENVIRONMENTAL": {
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"ASHRAE34": "A2",
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"FH": 1,
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"GWP100": 2310.0,
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"GWP20": 5490.0,
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"GWP500": 705.0,
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"HH": 1,
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"Name": "R142b",
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"ODP": 0.07,
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"PH": 0
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},
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"EOS": [
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{
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"BibTeX_CP0": "",
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"BibTeX_EOS": "Lemmon-JCED-2006",
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"STATES": {
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"hs_anchor": {
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"T": 451.286,
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"hmolar": 50097.29941072175,
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"p": 6671860.880474911,
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},
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{
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{
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},
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{
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"n": [
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"n": [
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"t": [
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"type": "ResidualHelmholtzPower"
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"p_max": 60000000,
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"pseudo_pure": false
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}
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],
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"NAME": "R142b",
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"REFPROP_NAME": "R142B",
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"STATES": {
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"critical": {
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"T": 410.26,
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"p": 4055000.0,
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},
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"p": 3.6326525623367987,
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"smolar_units": "J/mol/K"
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},
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"triple_vapor": {
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"T": 142.72,
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"p": 3.632651716840062,
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"p_units": "Pa",
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"smolar": 228.21204191688244,
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"smolar_units": "J/mol/K"
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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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"T_reducing_units": "K",
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"a": [
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9.88196e-07
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],
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"t": [
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]
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},
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"psi": {
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"a": [
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],
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"rhomolar_reducing": 4438.0,
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"t": [
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]
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},
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"q_D": 1624288967.5044746,
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"q_D_units": "m",
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"reference_fluid": "Propane",
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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": 278.2,
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"epsilon_over_k_units": "K",
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"psi": {
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"a": [
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0.9716,
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0.019181,
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0.0
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"t": [
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},
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"reference_fluid": "Propane",
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"sigma_eta": 5.362000000000001e-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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} |