mirror of
https://github.com/CoolProp/CoolProp.git
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435 lines
10 KiB
JSON
435 lines
10 KiB
JSON
{
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"ALIASES": [
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"Fluoroethane",
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"FLUOROETHANE"
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],
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"ANCILLARIES": {
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"hL": {
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"A": [
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-44208.485231704544,
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83.12847468222475,
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2.203283634257494,
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-0.020346133549620914,
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8.977316339623045e-05,
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-2.1979946562987105e-07,
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2.841772557171562e-10,
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-1.5296695210330576e-13
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],
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"B": [
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1,
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-0.0026339932357263016
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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": 213.2762906030057,
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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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22057.637020880637,
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297.7605230019124,
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-6.544528234654651,
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0.0516362422871857,
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-0.00022310331279248142,
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5.499792034488991e-07,
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-7.290499422433691e-10,
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4.0705397401503114e-13
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],
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"B": [
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1,
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-0.002630000327725292
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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": 522.5366885574049,
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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": 375.25,
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"Tmax": 375.2499999999994,
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"Tmin": 130.0,
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"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.028081837897198092,
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"n": [
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0.004114007295473757,
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-6.483344699665786,
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4.717832719212871,
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-6.0036159561286375,
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-8.92774506978172,
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6.727500969566306
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],
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"reducing_value": 5010000.0,
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"t": [
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0.358,
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0.979,
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2.041,
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2.312,
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7.268,
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8.389
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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": 375.25,
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"Tmax": 375.2499999999994,
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"Tmin": 130.0,
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"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.030832559045790298,
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"n": [
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-0.007844518150924242,
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25.45019959482669,
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-31.3504385516059,
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1.1481149665076051,
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-2.6194902114004543,
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-3.261988824418926
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],
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"reducing_value": 5010000.0,
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"t": [
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0.361,
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0.847,
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0.865,
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2.188,
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2.386,
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5.603
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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": 375.25,
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"Tmax": 375.2499999999994,
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"Tmin": 130.0,
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"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.09082481888231797,
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"n": [
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7.345119166859648,
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-11.515617231318577,
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6.89480557431733,
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-1.9186452820369757,
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183.43884409350315,
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-184.35734585122438
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],
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"reducing_value": 6280.0,
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"t": [
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0.331,
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0.379,
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0.459,
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3.341,
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6.576,
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6.669
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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": 375.25,
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"Tmax": 375.2499999999994,
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"Tmin": 130.0,
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"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
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"max_abserror_percentage": 0.20059504347491597,
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"n": [
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-0.3089763166551767,
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-2.9925531954627664,
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-1.8199815337621044,
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-1.0253004294209247,
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-2.9173025831139583,
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-1.6688506440273063
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],
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"reducing_value": 6280.0,
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"t": [
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0.148,
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0.482,
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0.891,
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2.774,
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4.26,
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6.784
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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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-362.0685394155181,
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4.371521876875828,
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-0.027207523411000405,
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0.00010274816730228413,
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-2.2610739457652157e-07,
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2.589104403673439e-10,
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-1.0495225984811308e-13,
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-2.542899278325737e-17
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],
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"B": [
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1,
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-0.002632930776305461
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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": 0.5811676767686169,
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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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1112.9403396482628,
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-19.466048970498672,
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0.16654672834100476,
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-0.0008501656517607422,
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2.7010132051221676e-06,
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-5.261300644158279e-09,
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5.773356641430936e-12,
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-2.7357285662263413e-15
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],
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"B": [
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1,
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-0.002618018394056218
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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": 1.6329140883492297,
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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": 375.3,
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"a": [
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0.05385
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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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1.111
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]
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}
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},
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"CAS": "353-36-6",
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"ENVIRONMENTAL": {
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"ASHRAE34": "UNKNOWN",
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"FH": -1,
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"GWP100": 10.0,
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"GWP20": -1.0,
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"GWP500": -1.0,
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"HH": -1,
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"Name": "R161",
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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": "Wu-IJT-2012",
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"STATES": {
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"hs_anchor": {
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"T": 412.77500000000003,
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"T_units": "K",
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"hmolar": 29437.28228235374,
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"hmolar_units": "J/mol",
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"p": 8287479.703515435,
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"p_units": "Pa",
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"rhomolar": 5652.0,
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"rhomolar_units": "mol/m^3",
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"smolar": 103.03475477754932,
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"smolar_units": "J/mol/K"
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},
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"reducing": {
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"T": 375.25,
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"T_units": "K",
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"p": 5010000,
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"p_units": "Pa",
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"rhomolar": 6280,
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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": 130.0,
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"T_units": "K",
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"p": 0.00551226945206069,
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"p_units": "Pa",
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"rhomolar": 19913.25305828297,
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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": 130.0,
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"T_units": "K",
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"p": 0.00551226945206069,
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"p_units": "Pa",
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"rhomolar": 0.005099837512332045,
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"rhomolar_units": "mol/m^3"
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}
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},
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"T_max": 450,
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"T_max_units": "K",
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"Ttriple": 130,
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"Ttriple_units": "K",
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"accentric": 0.2162428410661867,
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"accentric_units": "-",
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"alpha0": [
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{
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"a1": -6.9187,
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"a2": 5.4788,
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"type": "IdealGasHelmholtzLead"
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},
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{
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"a": 3,
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"type": "IdealGasHelmholtzLogTau"
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},
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{
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"n": [
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2.059,
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9.253,
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6.088
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],
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"t": [
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1.11925383077948,
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4.125249833444371,
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10.34510326449034
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],
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"type": "IdealGasHelmholtzPlanckEinstein"
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},
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{
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"a1": 4.21805657510139e-05,
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"a2": -4.5424171382829e-06,
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"reference": "IIR",
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"type": "IdealGasHelmholtzEnthalpyEntropyOffset"
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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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1,
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1,
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2,
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3,
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4,
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2,
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7,
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1,
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2,
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3
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],
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"l": [
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0,
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0,
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0,
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0,
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0,
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1,
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1,
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2,
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2,
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2
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],
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"n": [
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1.511,
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-2.3,
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0.1683,
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0.04133,
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0.62187,
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-0.0265,
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-1.03,
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],
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"t": [
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0.37,
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0.97,
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1.14,
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0.744,
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1,
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1.26,
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1,
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1.8,
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3,
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2.25
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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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2.7,
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5.2,
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3.9,
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4.7,
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413
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],
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"d": [
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1,
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1,
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3,
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3,
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3
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],
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"epsilon": [
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0.683,
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0.892,
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0.785,
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1.33,
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0.86
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],
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"eta": [
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0.96,
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1.35,
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1.26,
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1.23,
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16.8
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],
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"gamma": [
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0.9,
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0.69,
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0.67,
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0.67,
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1.15
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],
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"n": [
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0.82,
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],
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"t": [
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1,
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1.2,
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5.3,
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1,
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4
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],
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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": 0.0480595,
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"molar_mass_units": "kg/mol",
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"p_max": 5000000,
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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": "R161",
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"REFPROP_NAME": "R161",
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"STATES": {
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"critical": {
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"T": 375.25,
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"T_units": "K",
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"p": 5010000.0,
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"p_units": "Pa",
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"rhomolar": 6280.0,
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"rhomolar_units": "mol/m^3"
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},
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"triple_liquid": {
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"T": 130.0,
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"T_units": "K",
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"p": 0.00551226945206069,
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"p_units": "Pa",
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"rhomolar": 19913.25305828297,
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"rhomolar_units": "mol/m^3"
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},
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"triple_vapor": {
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"T": 130.0,
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"T_units": "K",
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"p": 0.00551226945206069,
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"p_units": "Pa",
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"rhomolar": 0.005099837512332045,
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"rhomolar_units": "mol/m^3"
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}
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}
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} |