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https://github.com/CoolProp/CoolProp.git
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428 lines
9.9 KiB
JSON
428 lines
9.9 KiB
JSON
{
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"ALIASES": [
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"R236fa"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-83742.15390121313,
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181.64639630706733,
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3.246925339773403,
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-0.029248096962148605,
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0.00012544041328450036,
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-3.0338809695826377e-07,
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3.9258892923414643e-10,
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-2.1313226114278644e-13
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],
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"B": [
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1,
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-0.0024892625525759636
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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": 290.23240463655566,
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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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10738.292339931428,
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965.3745171983893,
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-14.955621597750723,
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0.1037110531679675,
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-0.00040805028641448596,
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9.355249647914637e-07,
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-1.1696425415721625e-09,
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6.199020621810232e-13
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],
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"B": [
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1,
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-0.0024874907035567955
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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": 652.058897018715,
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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": 398.07,
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"Tmax": 398.0699999999993,
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"Tmin": 179.6,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.029205453110847657,
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"n": [
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-0.0049249850273236865,
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0.012816148225752128,
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-6.97674339296593,
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0.34709652116366274,
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-3.3890300356223824,
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-3.905418212194194
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],
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"reducing_value": 3200000.0,
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"t": [
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0.017,
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0.253,
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0.971,
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2.069,
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3.12,
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5.366
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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": 398.07,
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"Tmax": 398.0699999999993,
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"Tmin": 179.6,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.28623680659642936,
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"n": [
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-0.07455034494245859,
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6.37817405215639,
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],
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"reducing_value": 3200000.0,
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"t": [
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0.39,
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1.035,
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2.14,
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2.75,
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6.783,
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19.623
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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": 398.07,
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"Tmax": 398.0699999999993,
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"Tmin": 179.6,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.12903740875118697,
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"n": [
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-0.6129462210275856,
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2.32975618477472,
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0.44026610528146576,
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0.18569408128843393,
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0.41600763700797233,
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0.3257761223988926
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"reducing_value": 3626.0,
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"t": [
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0.177,
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0.276,
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0.561,
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0.741,
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1.15,
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3.764
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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": 398.07,
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"Tmax": 398.0699999999993,
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"Tmin": 179.6,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.5486542157663976,
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"n": [
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],
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"reducing_value": 3626.0,
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"t": [
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0.436,
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1.661,
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2.91,
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3.307,
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5.447,
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6.392
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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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-664.5735668307543,
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7.735411650208821,
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-0.047481125496898216,
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0.00018387753343467622,
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5.997600781237898e-10,
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-4.036414156136976e-13,
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7.940846375186454e-17
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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": 0.7421106932479589,
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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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1310.858367082982,
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0.14113283205914331,
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1.4831079706910145e-06,
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1.7057974023838458e-12,
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-4.964228463918875e-16
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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": 1.6824752605728324,
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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": 398.07,
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"a": [
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0.05389
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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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1.249
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]
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}
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},
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"CAS": "690-39-1",
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"ENVIRONMENTAL": {
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"ASHRAE34": "A1",
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"FH": 0,
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"GWP100": 9810.0,
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"GWP20": 8100.0,
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"GWP500": 7660.0,
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"HH": 1,
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"Name": "R236FA",
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"ODP": -1.0,
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"PH": 1
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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": "Pan-FPE-2012",
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"STATES": {
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"hs_anchor": {
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"T": 437.877,
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"T_units": "K",
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"hmolar": 68174.83773075993,
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"hmolar_units": "J/mol",
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"p": 5466375.384464217,
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"p_units": "Pa",
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"rhomolar": 3263.4,
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"rhomolar_units": "mol/m^3",
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"smolar": 255.52310767395352,
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"smolar_units": "J/mol/K"
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},
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"reducing": {
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"T": 398.07,
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"T_units": "K",
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"p": 3200000,
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"p_units": "Pa",
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"rhomolar": 3626,
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"rhomolar_units": "mol/m^3"
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},
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"sat_min_liquid": {
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"T": 179.60000000000002,
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"T_units": "K",
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"p": 160.32677874937644,
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"p_units": "Pa",
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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": 179.60000000000002,
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"T_units": "K",
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"p": 160.32677876319866,
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"p_units": "Pa",
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"rhomolar_units": "mol/m^3"
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}
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},
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"T_max": 400,
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"T_max_units": "K",
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"Ttriple": 179.6,
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"Ttriple_units": "K",
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"accentric": 0.3769117976336991,
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"accentric_units": "-",
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"alpha0": [
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{
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"a1": -17.5983849,
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"a2": 8.87150449,
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": 9.175,
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{
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"n": [
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"t": [
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"type": "IdealGasHelmholtzPlanckEinstein"
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}
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],
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"alphar": [
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{
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"d": [
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"l": [
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"n": [
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"t": [
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],
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"type": "ResidualHelmholtzPower"
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},
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{
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"beta": [
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"d": [
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"epsilon": [
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0.712,
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],
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"eta": [
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1.02,
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],
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"gamma": [
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1.13,
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"n": [
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"t": [
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"type": "ResidualHelmholtzGaussian"
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}
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],
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"gas_constant": 8.314472,
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"gas_constant_units": "J/mol/K",
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"molar_mass": 0.1520384,
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"molar_mass_units": "kg/mol",
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"p_max": 70000000,
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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": "R236FA",
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"REFPROP_NAME": "R236FA",
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"STATES": {
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"critical": {
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"T": 398.07,
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"T_units": "K",
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"p": 3200000.0,
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"p_units": "Pa",
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"rhomolar": 3626.0,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 179.60000000000002,
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"T_units": "K",
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"p": 160.32677874937644,
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"p_units": "Pa",
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"rhomolar": 11234.50556190224,
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"rhomolar_units": "mol/m^3"
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},
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"triple_vapor": {
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"T": 179.60000000000002,
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"T_units": "K",
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"p": 160.32677876319866,
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"p_units": "Pa",
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"rhomolar": 0.10739880724453124,
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"rhomolar_units": "mol/m^3"
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}
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}
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} |