github/CoolProp
1
1
Fork 0
mirror of https://github.com/CoolProp/CoolProp.git synced 2026-04-23 03:00:17 -04:00
Code Issues Packages Projects Releases Wiki Activity

Update critical splines for a lot of fluids based on the use of Maxwell solver

Browse Source 
Signed-off-by: Ian Bell <ian.h.bell@gmail.com>
This commit is contained in:
Ian Bell
2014-11-23 19:56:33 -05:00
parent 862032dbf0
commit 951aa83efc
44 changed files with 453 additions and 415 deletions
Download Patch File Download Diff File Expand all files Collapse all files

22
dev/fluids/Acetone.json
View File

@@ -373,22 +373,22 @@
],
"critical_region_splines": {
"T_max": 508.1,
"T_min": 508.09697325761744,
"T_min": 508.09970264118135,
"_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",
"cL": [
-1.5123933548972854e-11,
-1.7185082712306687e-08,
0.0011638028537861549,
504.579957217175
0.0,
0.0,
-7.911681289094714e-06,
508.1371849020588
],
"cV": [
1.9536072269032177e-10,
-2.983480058312324e-06,
0.015098157455448244,
482.76079813563524
0.0,
0.0,
8.31994940245324e-06,
508.0608962378085
],
"rhomolar_max": 4814.181193727979,
"rhomolar_min": 4590.050467927069
"rhomolar_max": 4737.584782275033,
"rhomolar_min": 4664.2595400179
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Argon.json
View File

@@ -526,22 +526,22 @@
],
"critical_region_splines": {
"T_max": 150.687,
"T_min": 150.68697834063298,
"T_min": 150.68698169043714,
"_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",
"cL": [
0.0,
0.0,
-6.171554333557227e-07,
150.69527446806111
-5.509866301146546e-07,
150.69438731448608
],
"cV": [
0.0,
0.0,
6.072607995401675e-07,
150.67885819354578
5.667184337162037e-07,
150.67940176246375
],
"rhomolar_max": 13442.525139946354,
"rhomolar_min": 13371.76233564158
"rhomolar_max": 13440.660161575233,
"rhomolar_min": 13375.121616690334
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

20
dev/fluids/D4.json
View File

@@ -381,22 +381,22 @@
],
"critical_region_splines": {
"T_max": 586.5,
"T_min": 583.1872205036263,
"T_min": 585.8223731516954,
"_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",
"cL": [
0.0,
-1.667552305553379e-05,
0.034382527265190706,
568.7770449657756
-7.862666279638519e-06,
0.016211685644670307,
578.1434596708557
],
"cV": [
6.813459579816792e-08,
-0.00021263235123370055,
0.22117438047692597,
509.81953537332856
6.746394257626074e-08,
-0.00021062780266197875,
0.2191796259421155,
510.4803477882244
],
"rhomolar_max": 1476.6422633230486,
"rhomolar_min": 675.0371135400856
"rhomolar_max": 1324.4971267138706,
"rhomolar_min": 824.503552249034
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/D6.json
View File

@@ -372,22 +372,22 @@
],
"critical_region_splines": {
"T_max": 645.78,
"T_min": 645.4997615767367,
"T_min": 645.5612757191427,
"_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",
"cL": [
-1.554702914197144e-07,
0.00027871311312902783,
-0.16613864293822964,
678.7008854032358
-1.198196800754583e-07,
0.00020830049432842273,
-0.11988515995442227,
668.5936073909794
],
"cV": [
2.1732433324774884e-07,
-0.00042927603672073575,
0.28201442644063596,
584.1491278422845
1.7569888176414546e-07,
-0.00035430081210555803,
0.23708993877492088,
593.1021821692563
],
"rhomolar_max": 725.3981107757561,
"rhomolar_min": 542.276230072255
"rhomolar_max": 715.9728372726955,
"rhomolar_min": 550.5496590706158
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Deuterium.json
View File

@@ -460,22 +460,22 @@
],
"critical_region_splines": {
"T_max": 38.34,
"T_min": 38.3399506598222,
"T_min": 38.3393455081093,
"_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",
"cL": [
0.0,
0.0,
-8.339819490855398e-07,
38.35436950898275
-3.0138638445784953e-06,
38.391928874042094
],
"cV": [
0.0,
0.0,
8.380089288669903e-07,
38.325561106155625
3.024694971483841e-06,
38.28788450564134
],
"rhomolar_max": 17289.162165151512,
"rhomolar_min": 17171.122133543762
"rhomolar_max": 17447.160404205744,
"rhomolar_min": 17013.617225249614
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

14
dev/fluids/DimethylEther.json
View File

@@ -410,22 +410,22 @@
],
"critical_region_splines": {
"T_max": 400.378,
"T_min": 400.3774167354802,
"T_min": 400.37798307940494,
"_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",
"cL": [
0.0,
0.0,
-1.846177917829548e-05,
400.48766296831906
-2.7743113901126396e-06,
400.39447940965727
],
"cV": [
0.0,
0.0,
1.8536722158567707e-05,
400.2678918703781
3.1494540868192204e-06,
400.3592922427243
],
"rhomolar_max": 5971.593082884313,
"rhomolar_min": 5908.534646267459
"rhomolar_max": 5946.0990251903795,
"rhomolar_min": 5934.627451427649
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Ethanol.json
View File

@@ -479,22 +479,22 @@
],
"critical_region_splines": {
"T_max": 514.71,
"T_min": 513.7464813947397,
"T_min": 514.622869613147,
"_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",
"cL": [
1.0321929712568178e-10,
-2.8791135673288862e-06,
0.023257198124035903,
456.514456977566
-4.321404777621795e-11,
-1.7076779247457985e-07,
0.006584159024686301,
490.68230210427
],
"cV": [
-2.567634017795019e-10,
3.6513286874767864e-06,
-0.016217580191766636,
536.0239643040333
-2.864544233706444e-10,
4.144580667152323e-06,
-0.01893530325526736,
540.986310635042
],
"rhomolar_max": 6943.380770596912,
"rhomolar_min": 4649.622177033432
"rhomolar_max": 6232.430871796149,
"rhomolar_min": 5611.7525953516915
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/HFE143m.json
View File

@@ -382,22 +382,22 @@
],
"critical_region_splines": {
"T_max": 377.921,
"T_min": 377.88522000242136,
"T_min": 377.88975653726936,
"_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",
"cL": [
4.9355266611563965e-11,
-1.1363349519029853e-06,
0.00736469652648742,
363.2831553274167
1.2548213865690152e-10,
-2.2189763500125694e-06,
0.012495023999688158,
355.1823983329997
],
"cV": [
-1.6224665103344288e-10,
1.8467354481248633e-06,
-0.0066516525010036605,
385.2331741502011
-2.2818544758356846e-10,
2.7463251549141047e-06,
-0.010740626529167381,
391.42531644901993
],
"rhomolar_max": 4935.29110614525,
"rhomolar_min": 4335.002308503029
"rhomolar_max": 4915.958005243979,
"rhomolar_min": 4357.2413514049285
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

20
dev/fluids/Helium.json
View File

@@ -460,22 +460,22 @@
],
"critical_region_splines": {
"T_max": 5.1953000000000005,
"T_min": 5.19073171770731,
"T_min": 5.19520893622453,
"_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",
"cL": [
-3.0333435224167437e-13,
1.5607506016709e-08,
-0.00026681298442982895,
6.710133323667334
0.0,
0.0,
9.016064727014562e-07,
5.178953874649923
],
"cV": [
0.0,
-4.479989405503328e-10,
1.624444158435496e-05,
5.048044137037824
0.0,
6.815469697713246e-08,
5.194064355343805
],
"rhomolar_max": 19915.76431162559,
"rhomolar_min": 14936.712852945791
"rhomolar_max": 18028.998312203898,
"rhomolar_min": 16793.866475690647
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Hydrogen.json
View File

@@ -432,22 +432,22 @@
],
"critical_region_splines": {
"T_max": 33.145,
"T_min": 33.13810506132737,
"T_min": 33.140418136928176,
"_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",
"cL": [
3.1007578284721566e-12,
-1.5869880447859634e-07,
0.0026850233556669507,
18.107690278950276
6.430433928390398e-12,
-3.15824835274259e-07,
0.005156102359493002,
5.156196888181069
],
"cV": [
-2.3396699485553584e-12,
9.516798742074658e-08,
-0.0012636720187622463,
38.58044486815464
-5.225396958873852e-12,
2.274807134854265e-07,
-0.0032854482527420407,
48.87593060548779
],
"rhomolar_max": 16262.923237049079,
"rhomolar_min": 14746.877675758724
"rhomolar_max": 16106.075389591539,
"rhomolar_min": 14901.511073260717
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/IsoButane.json
View File

@@ -475,22 +475,22 @@
],
"critical_region_splines": {
"T_max": 407.817,
"T_min": 407.73549293470376,
"T_min": 407.75175593000233,
"_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",
"cL": [
-5.728389280296945e-10,
6.296755366265217e-06,
-0.022991762972926447,
435.69130219666266
-4.4074892731107477e-10,
4.7123672337356735e-06,
-0.01666254100244952,
427.2704151083339
],
"cV": [
5.562666408422913e-10,
-6.761233991678565e-06,
0.027344254864717768,
371.015481302833
4.1509787184030793e-10,
-5.1719952249655754e-06,
0.021387369158083452,
378.44898088210823
],
"rhomolar_max": 4253.160501655689,
"rhomolar_min": 3479.687062549918
"rhomolar_max": 4218.938217762173,
"rhomolar_min": 3515.5103304226764
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/IsoButene.json
View File

@@ -370,22 +370,22 @@
],
"critical_region_splines": {
"T_max": 418.09000000000003,
"T_min": 418.08543171770737,
"T_min": 418.08950991019015,
"_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",
"cL": [
1.0856405178489673e-09,
-1.4451084442137125e-05,
0.06388776104495195,
324.24484504699296
0.0,
0.0,
-2.3926474256584434e-05,
418.18977339765
],
"cV": [
-6.230035048466998e-10,
6.9227418610441575e-06,
-0.02523563018482191,
448.11876326463465
0.0,
0.0,
2.5211881942311312e-05,
417.9848664523006
],
"rhomolar_max": 4246.188019158735,
"rhomolar_min": 4095.5716752458243
"rhomolar_max": 4190.48316039618,
"rhomolar_min": 4150.5611571944355
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Krypton.json
View File

@@ -369,22 +369,22 @@
],
"critical_region_splines": {
"T_max": 209.48000000000002,
"T_min": 209.47310506132737,
"T_min": 209.4785594520556,
"_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",
"cL": [
6.390300964893231e-11,
-2.199509680360674e-06,
0.02516089390363733,
113.79346021244321
7.439981467718757e-10,
-2.4434077759864862e-05,
0.26746352188901107,
-766.3592353019499
],
"cV": [
-3.436623953002642e-11,
1.0066209446840255e-06,
-0.009706635600422744,
240.19068612286947
-7.492939677469447e-10,
2.417791448185612e-05,
-0.2600344669020087,
1141.6344647277606
],
"rhomolar_max": 11108.82129459245,
"rhomolar_min": 10591.412518037536
"rhomolar_max": 10950.720003147018,
"rhomolar_min": 10746.269399995741
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/MD3M.json
View File

@@ -364,22 +364,22 @@
],
"critical_region_splines": {
"T_max": 628.36,
"T_min": 628.3495934234678,
"T_min": 628.3569917799531,
"_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",
"cL": [
7.278401833841499e-08,
-0.00016564557063869183,
0.12450370964999923,
597.405816117967
3.306215390839023e-07,
-0.0007009970408251223,
0.49499207140405216,
511.9476683657978
],
"cV": [
4.6976897100679125e-08,
-0.00011341900983330957,
0.08928269840896542,
605.3211026107697
-3.977392516737338e-07,
0.0007943503177039177,
-0.528334852377581,
745.381333245749
],
"rhomolar_max": 713.1509447889869,
"rhomolar_min": 661.6875900836687
"rhomolar_max": 699.3896862967481,
"rhomolar_min": 673.1968167336198
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

19
dev/fluids/MM.json
View File

@@ -430,6 +430,25 @@
"type": "ResidualHelmholtzGaussian"
}
],
"critical_region_splines": {
"T_max": 518.75,
"T_min": 518.2425865117793,
"_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",
"cL": [
-7.204081377481409e-09,
3.2242768485801064e-05,
-0.04789483097662979,
542.3479328063715
],
"cV": [
-2.379131509735468e-08,
9.657118716867812e-05,
-0.12666182160274833,
571.6341272287368
],
"rhomolar_max": 1924.5652666485823,
"rhomolar_min": 1384.2860882387943
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",
"molar_mass": 0.16237752,

22
dev/fluids/MethylStearate.json
View File

@@ -416,22 +416,22 @@
],
"critical_region_splines": {
"T_max": 775.0,
"T_min": 774.9931050613274,
"T_min": 774.9998288233945,
"_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",
"cL": [
3.695594514041921e-08,
-0.00015314359180175198,
0.1733360078297273,
715.4195409309607
0.0,
0.0,
-0.00010980425210695775,
775.0872175174486
],
"cV": [
-8.410775169091402e-09,
-4.503043200679788e-05,
0.08745473360028402,
738.1598907285911
0.0,
0.0,
0.00010988357503613521,
774.9127194763488
],
"rhomolar_max": 804.623188217212,
"rhomolar_min": 783.9995580899517
"rhomolar_max": 795.8589251075718,
"rhomolar_min": 792.7422002522696
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Neon.json
View File

@@ -447,22 +447,22 @@
],
"critical_region_splines": {
"T_max": 44.491800000000005,
"T_min": 44.49141355465158,
"T_min": 44.491722228412755,
"_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",
"cL": [
0.0,
0.0,
-1.5811616648711508e-06,
44.52956130288046
-7.086502874109214e-07,
44.50872398616395
],
"cV": [
0.0,
0.0,
1.5834258838542428e-06,
44.4539846230418
7.097427124728881e-07,
44.47484992454073
],
"rhomolar_max": 24126.40596873362,
"rhomolar_min": 23637.943519451463
"rhomolar_max": 23991.746074516006,
"rhomolar_min": 23772.422844948775
},
"gas_constant": 8.31434,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Neopentane.json
View File

@@ -369,22 +369,22 @@
],
"critical_region_splines": {
"T_max": 433.74,
"T_min": 433.73543171770734,
"T_min": 433.7374308769143,
"_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",
"cL": [
1.8157110662036835e-09,
-1.8874192929720874e-05,
0.0651915711809464,
358.895660684941
3.5552432643477683e-09,
-3.6044510806120894e-05,
0.12168351856799782,
296.9433793880215
],
"cV": [
-2.2365486585331262e-09,
2.089693784319932e-05,
-0.06492040004203695,
500.7835165371252
-5.6898059160504035e-09,
5.456581605156137e-05,
-0.1743388599380053,
619.3097765122714
],
"rhomolar_max": 3339.892894257803,
"rhomolar_min": 3198.06041887194
"rhomolar_max": 3321.0423374845595,
"rhomolar_min": 3218.167274770953
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Nitrogen.json
View File

@@ -521,22 +521,22 @@
],
"critical_region_splines": {
"T_max": 126.19200000000001,
"T_min": 126.19199998688855,
"T_min": 126.19197283625158,
"_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",
"cL": [
0.0,
0.0,
-1.547800694886972e-07,
126.19373104504585
-3.8150408064612515e-07,
126.1962667040463
],
"cV": [
0.0,
0.0,
9.95463660457675e-10,
126.19198886683252
7.925054408276641e-07,
126.18313669723965
],
"rhomolar_max": 11183.986174852074,
"rhomolar_min": 11170.73026187868
"rhomolar_max": 11255.103189047548,
"rhomolar_min": 11149.625676641272
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

14
dev/fluids/OrthoDeuterium.json
View File

@@ -437,22 +437,22 @@
],
"critical_region_splines": {
"T_max": 38.34,
"T_min": 38.33996730937413,
"T_min": 38.3396608555373,
"_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",
"cL": [
0.0,
0.0,
-6.850188755192064e-07,
38.3518028752252
-2.174063770932284e-06,
38.37745911877317
],
"cV": [
0.0,
0.0,
6.843466890793785e-07,
38.328208706547166
2.1783706563740146e-06,
38.30246667359068
],
"rhomolar_max": 17277.722226405003,
"rhomolar_min": 17182.23089934681
"rhomolar_max": 17385.995636942647,
"rhomolar_min": 17074.312784095087
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

22
dev/fluids/OrthoHydrogen.json
View File

@@ -400,22 +400,22 @@
],
"critical_region_splines": {
"T_max": 33.22,
"T_min": 33.216973257617425,
"T_min": 33.21859684084077,
"_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",
"cL": [
4.066468806855226e-12,
-2.0485786362827496e-07,
0.003417899984425546,
14.316580566669387
1.4231762427055805e-11,
-6.794822502274015e-07,
0.01080431180609879,
-23.99858599834753
],
"cV": [
-3.379814959674437e-12,
1.404217131242082e-07,
-0.0019188970430762365,
41.812545688089735
-1.3076458482547849e-11,
5.86239854331421e-07,
-0.008750877129877292,
76.70950470337729
],
"rhomolar_max": 15899.98591137461,
"rhomolar_min": 14989.857909343546
"rhomolar_max": 15742.198240172262,
"rhomolar_min": 15145.91854837676
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/ParaDeuterium.json
View File

@@ -435,22 +435,22 @@
],
"critical_region_splines": {
"T_max": 38.34,
"T_min": 38.33996730937413,
"T_min": 38.33992222841275,
"_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",
"cL": [
0.0,
0.0,
-6.849502299785245e-07,
38.35180169246253
-1.0134264329467987e-06,
38.35746133743967
],
"cV": [
0.0,
0.0,
6.848389037037868e-07,
38.32820022568919
1.0488475637710707e-06,
38.32192835647623
],
"rhomolar_max": 17277.727009113827,
"rhomolar_min": 17182.26523245882
"rhomolar_max": 17306.741226317383,
"rhomolar_min": 17155.850438196074
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Propylene.json
View File

@@ -479,22 +479,22 @@
],
"critical_region_splines": {
"T_max": 364.211,
"T_min": 364.21041673548024,
"T_min": 364.21077733486237,
"_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",
"cL": [
0.0,
0.0,
-6.505035916897591e-06,
364.2464979809985
-3.6652101077273866e-06,
364.2310010515579
],
"cV": [
0.0,
0.0,
6.4811926293276935e-06,
364.17563213182177
3.951799999729862e-06,
364.1894350274015
],
"rhomolar_max": 5546.663535640788,
"rhomolar_min": 5367.006606323258
"rhomolar_max": 5517.750988646923,
"rhomolar_min": 5400.654755394478
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

19
dev/fluids/R11.json
View File

@@ -455,6 +455,25 @@
"type": "ResidualHelmholtzPower"
}
],
"critical_region_splines": {
"T_max": 471.06,
"T_min": 471.059233646828,
"_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",
"cL": [
0.0,
0.0,
-4.043954354486559e-06,
471.07663294370076
],
"cV": [
0.0,
0.0,
2.3593786652777144e-06,
471.05029578252663
],
"rhomolar_max": 4302.545317673531,
"rhomolar_min": 3788.227991064693
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",
"molar_mass": 0.137368,

14
dev/fluids/R113.json
View File

@@ -396,22 +396,22 @@
],
"critical_region_splines": {
"T_max": 487.21000000000004,
"T_min": 487.20941673548026,
"T_min": 487.2099540373214,
"_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",
"cL": [
0.0,
0.0,
-2.1155772356204888e-05,
487.27322739169836
-5.934357667529962e-06,
487.22773577208176
],
"cV": [
0.0,
0.0,
2.1763182218616364e-05,
487.1449572672853
6.04290259183351e-06,
487.19193982414185
],
"rhomolar_max": 3016.2291002048787,
"rhomolar_min": 2961.858589771953
"rhomolar_max": 2996.404287808557,
"rhomolar_min": 2981.053046244005
},
"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R116.json
View File

@@ -366,22 +366,22 @@
],
"critical_region_splines": {
"T_max": 293.03000000000003,
"T_min": 293.02697325761744,
"T_min": 293.02870328483243,
"_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",
"cL": [
5.973701413916427e-10,
-8.378309573561642e-06,
0.039073782995767505,
232.42219731732985
1.5572847523698138e-09,
-2.1246768945374408e-05,
0.09657619729065436,
146.77536264781335
],
"cV": [
-4.2587664193266785e-10,
5.257573775768188e-06,
-0.02149722855677295,
322.1082759616395
-2.245407664058467e-09,
2.9392570484872764e-05,
-0.12820658247075012,
479.3707443682296
],
"rhomolar_max": 4535.77641861197,
"rhomolar_min": 4355.023810307573
"rhomolar_max": 4501.228807035586,
"rhomolar_min": 4388.313768041884
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R123.json
View File

@@ -490,22 +490,22 @@
],
"critical_region_splines": {
"T_max": 456.831,
"T_min": 456.7079808473738,
"T_min": 456.8175322777658,
"_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",
"cL": [
-5.2516982254248e-10,
4.95822393582125e-06,
-0.015285703141563677,
472.1032632289936
7.413160414272145e-10,
-8.948235265463442e-06,
0.035598147140066136,
410.0599459455676
],
"cV": [
5.019316578137991e-10,
-6.104407328102757e-06,
0.024431712288804266,
424.57182248409964
-8.21928748519765e-10,
7.918497516718821e-06,
-0.0250634281364805,
482.7835089382342
],
"rhomolar_max": 3965.7364882421543,
"rhomolar_min": 3221.873367889577
"rhomolar_max": 3721.7717264448725,
"rhomolar_min": 3470.2289437901068
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R134a.json
View File

@@ -400,22 +400,22 @@
],
"critical_region_splines": {
"T_max": 374.21,
"T_min": 374.15599701305536,
"T_min": 372.2699100419668,
"_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",
"cL": [
-2.358891970526994e-10,
3.35250579170572e-06,
-0.015826824353177796,
399.0175702243528
-3.17708038943435e-10,
4.6452314558692645e-06,
-0.022619828473249084,
410.8918226766174
],
"cV": [
2.033032586375043e-10,
-3.2541387283179285e-06,
0.017300443262052236,
343.6482870886872
0.0,
-7.013970375511672e-07,
0.007037892222874368,
356.5552608547758
],
"rhomolar_max": 5442.556273932187,
"rhomolar_min": 4580.218882520725
"rhomolar_max": 6712.160594134622,
"rhomolar_min": 3353.912381912076
},
"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R14.json
View File

@@ -435,22 +435,22 @@
],
"critical_region_splines": {
"T_max": 227.51,
"T_min": 226.05575499770643,
"T_min": 226.4221608783466,
"_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",
"cL": [
-4.497162085380202e-11,
7.584188775966138e-07,
-0.003964719969167488,
233.5234361790954
-3.276091146712226e-11,
4.7283262023474423e-07,
-0.0017555435908659005,
227.86433767755432
],
"cV": [
5.850937467308107e-11,
-1.409814381412894e-06,
0.011174057273190223,
198.30177311425936
4.0498841128300184e-11,
-1.0634186146259112e-06,
0.008979676508857887,
202.86623067561814
],
"rhomolar_max": 9311.871085841536,
"rhomolar_min": 4879.2736322840055
"rhomolar_max": 9048.167089998266,
"rhomolar_min": 5136.725032287401
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

14
dev/fluids/R143a.json
View File

@@ -401,22 +401,22 @@
],
"critical_region_splines": {
"T_max": 345.857,
"T_min": 345.85688760275673,
"T_min": 345.85695155523047,
"_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",
"cL": [
0.0,
0.0,
-5.242214594297355e-06,
345.88388443543613
-3.3974084744314594e-06,
345.8744234394907
],
"cV": [
0.0,
0.0,
5.221395136669298e-06,
345.8302223361114
3.4270760473903566e-06,
345.8394244118448
],
"rhomolar_max": 5149.890794010884,
"rhomolar_min": 5106.923714331294
"rhomolar_max": 5142.709330288575,
"rhomolar_min": 5114.314110128164
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R22.json
View File

@@ -493,22 +493,22 @@
],
"critical_region_splines": {
"T_max": 369.295,
"T_min": 369.29299461397886,
"T_min": 369.2949627574784,
"_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",
"cL": [
-6.068711638786403e-11,
9.60793099642547e-07,
-0.004959370923967982,
377.5706211619357
0.0,
0.0,
-2.3424000852304404e-06,
369.3091907750444
],
"cV": [
2.0197560844726486e-11,
-5.076049994717274e-07,
0.003926491093801074,
359.64667998370135
0.0,
0.0,
2.2501789373208953e-06,
369.28136792095836
],
"rhomolar_max": 6174.151068396738,
"rhomolar_min": 5939.762656878844
"rhomolar_max": 6074.119299984461,
"rhomolar_min": 6041.669084436526
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R236EA.json
View File

@@ -414,22 +414,22 @@
],
"critical_region_splines": {
"T_max": 412.44,
"T_min": 412.01703429466085,
"T_min": 412.1479040101896,
"_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",
"cL": [
-9.065638596766866e-10,
9.956613016634915e-06,
-0.036442262498707786,
456.8904836061875
-8.006455677667769e-10,
8.704410207568409e-06,
-0.031523658993000074,
450.4692091322586
],
"cV": [
8.719771420305249e-10,
-9.978606681376363e-06,
0.03803850767350116,
364.13631933098907
7.013200127318413e-10,
-8.186877070552625e-06,
0.03179200998315829,
371.36385032890547
],
"rhomolar_max": 4440.255966785143,
"rhomolar_min": 3017.4925122772956
"rhomolar_max": 4349.318832091479,
"rhomolar_min": 3109.4495886851687
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/R245fa.json
View File

@@ -407,22 +407,22 @@
],
"critical_region_splines": {
"T_max": 427.01,
"T_min": 427.0096135546516,
"T_min": 427.0098684058467,
"_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",
"cL": [
0.0,
0.0,
-2.7068259197787627e-06,
427.02048895043913
-1.216781979909817e-06,
427.01471503017217
],
"cV": [
0.0,
0.0,
3.086102462886277e-06,
426.9980413529563
1.440583268474931e-06,
427.00441773983465
],
"rhomolar_max": 4017.7669749909037,
"rhomolar_min": 3749.7788341360238
"rhomolar_max": 3983.149327890093,
"rhomolar_min": 3783.652171549889
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R41.json
View File

@@ -377,22 +377,22 @@
],
"critical_region_splines": {
"T_max": 317.28000000000003,
"T_min": 317.2695934234679,
"T_min": 317.2733788557714,
"_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",
"cL": [
8.947784934150927e-11,
-2.661886245206215e-06,
0.0262942665921942,
230.99772757769114
1.982286805306258e-10,
-5.721729832650934e-06,
0.05498977915002592,
141.30084034516577
],
"cV": [
-8.480951160041928e-11,
2.20398173327229e-06,
-0.018988536263903795,
371.46813146596344
-1.8833256878930853e-10,
5.06762626683171e-06,
-0.04539119693930791,
452.60575575095083
],
"rhomolar_max": 9571.518280811737,
"rhomolar_min": 9026.378810480832
"rhomolar_max": 9510.503612422926,
"rhomolar_min": 9087.67121079717
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/RC318.json
View File

@@ -433,22 +433,22 @@
],
"critical_region_splines": {
"T_max": 388.38,
"T_min": 388.25698084737377,
"T_min": 388.29054792405356,
"_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",
"cL": [
5.161678249152199e-10,
-6.54174243254277e-06,
0.0256755247809552,
356.27486161409246
1.1298449787658047e-09,
-1.2403349555998569e-05,
0.04432498442528143,
336.509525023081
],
"cV": [
-4.001990439211164e-10,
1.9669817951712655e-06,
-0.0006597242702549873,
383.44477922926757
-1.04204053156705e-09,
7.774300413950925e-06,
-0.018161009518633232,
401.01153126933485
],
"rhomolar_max": 3376.736130176733,
"rhomolar_min": 2825.886785898815
"rhomolar_max": 3333.3908947283726,
"rhomolar_min": 2868.2068492030176
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Toluene.json
View File

@@ -371,22 +371,22 @@
],
"critical_region_splines": {
"T_max": 591.75,
"T_min": 591.7342932852254,
"T_min": 591.743021298681,
"_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",
"cL": [
3.3834089871987155e-09,
-3.464558495481263e-05,
0.11764944401792847,
459.1727413679192
1.2106006975063367e-08,
-0.0001181388502205585,
0.38403809215740176,
175.87772723873658
],
"cV": [
-2.3379515587297088e-09,
1.972502928601055e-05,
-0.05458017218397031,
641.0297738234855
-1.1414134593821325e-08,
0.00010543398970811022,
-0.32435919800801977,
924.07044128592
],
"rhomolar_max": 3253.6261257770193,
"rhomolar_min": 3086.5243371577894
"rhomolar_max": 3222.9990473699186,
"rhomolar_min": 3115.8882394651837
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Xenon.json
View File

@@ -372,22 +372,22 @@
],
"critical_region_splines": {
"T_max": 289.733,
"T_min": 289.72843171770734,
"T_min": 289.73036241968293,
"_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",
"cL": [
2.4311831644858725e-10,
-6.354625581839551e-06,
0.05529442454906748,
129.54501621008842
6.004785820072694e-10,
-1.540656966562575e-05,
0.13172106414321377,
-85.54244066647958
],
"cV": [
-2.2130895526715094e-10,
5.34493631486394e-06,
-0.04294825043876369,
404.53030033147684
-6.058430701055764e-10,
1.4986162139205343e-05,
-0.12352266285870138,
628.9853784946181
],
"rhomolar_max": 8554.90344650679,
"rhomolar_min": 8248.286253998665
"rhomolar_max": 8512.969220623036,
"rhomolar_min": 8288.926931935599
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/n-Butane.json
View File

@@ -471,22 +471,22 @@
],
"critical_region_splines": {
"T_max": 425.125,
"T_min": 425.1219732576174,
"T_min": 425.12491360192047,
"_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",
"cL": [
-1.6020493306008252e-10,
1.133822562422527e-06,
-0.0014996904947787396,
423.23116044183894
0.0,
0.0,
-5.692661766826853e-06,
425.1473310005959
],
"cV": [
5.058796197557434e-11,
-1.3472509771444817e-06,
0.008234549282093268,
410.50072741365295
0.0,
0.0,
8.526909313167263e-06,
425.0915508992536
],
"rhomolar_max": 3985.810039412961,
"rhomolar_min": 3859.458487995192
"rhomolar_max": 3937.946709931644,
"rhomolar_min": 3912.637210218117
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/n-Decane.json
View File

@@ -371,22 +371,22 @@
],
"critical_region_splines": {
"T_max": 617.7,
"T_min": 617.6842932852254,
"T_min": 617.6916108089977,
"_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",
"cL": [
3.811704985816065e-08,
-0.00019945721156220926,
0.3466608020285197,
417.5042285213912
1.0320134681362064e-07,
-0.0005217594566020225,
0.8786599904848911,
124.80648856211926
],
"cV": [
-3.8653700756418197e-08,
0.00017824366286806788,
-0.2727502335438755,
756.1055367913187
-1.1142857846667393e-07,
0.0005339799193483449,
-0.8523592215306723,
1070.881951847099
],
"rhomolar_max": 1678.7818428517664,
"rhomolar_min": 1601.198950562281
"rhomolar_max": 1667.390392847361,
"rhomolar_min": 1612.6301589021477
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

20
dev/fluids/n-Dodecane.json
View File

@@ -380,22 +380,22 @@
],
"critical_region_splines": {
"T_max": 658.1,
"T_min": 658.0986713196614,
"T_min": 658.0987032848325,
"_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",
"cL": [
0.0,
-2.1192739463715689e-07,
0.0005637268697348361,
657.7251216316264
-2.0939062487280465e-07,
0.0005569790621618195,
657.7296089236623
],
"cV": [
1.345410821444352e-08,
-5.389362597299564e-05,
0.07196012902658075,
626.0728305909759
1.3346771828287604e-08,
-5.346984610199855e-05,
0.07140247657014234,
626.3174076977489
],
"rhomolar_max": 1409.180220111776,
"rhomolar_min": 1288.4723365719328
"rhomolar_max": 1408.694372900752,
"rhomolar_min": 1288.843365778471
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/n-Hexane.json
View File

@@ -388,22 +388,22 @@
],
"critical_region_splines": {
"T_max": 507.82,
"T_min": 506.8564813947396,
"T_min": 507.56389285976036,
"_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",
"cL": [
8.758829336463305e-09,
-8.028744783668493e-05,
0.24210552253394685,
267.0302268919283
1.3977737160597438e-07,
-0.0011682233690808838,
3.251884108736999,
-2507.157926239475
],
"cV": [
3.991905207393978e-09,
-3.342318035828356e-05,
0.09319459234659805,
421.2768792846532
5.874354703279542e-09,
-4.7886457822250056e-05,
0.130117701932496,
389.9695505583025
],
"rhomolar_max": 3123.268752501498,
"rhomolar_min": 2157.714974917123
"rhomolar_max": 2833.509856115492,
"rhomolar_min": 2364.9453716716366
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/n-Nonane.json
View File

@@ -370,22 +370,22 @@
],
"critical_region_splines": {
"T_max": 594.5500000000001,
"T_min": 594.5262937515283,
"T_min": 594.5305381064545,
"_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",
"cL": [
2.6268572567217745e-08,
-0.00015162277736042532,
0.2906990422823534,
409.3502826161235
3.439621959142905e-08,
-0.00019618497909856946,
0.3721332593263793,
359.74973708777674
],
"cV": [
-2.3832710380126962e-08,
0.00012016817674452382,
-0.2007737723861744,
705.5893640684056
-3.3806685877357655e-08,
0.00017381238995556715,
-0.2969386008307187,
763.0469880912561
],
"rhomolar_max": 1866.189822592916,
"rhomolar_min": 1755.3631417347385
"rhomolar_max": 1860.332444076972,
"rhomolar_min": 1760.985320673019
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/n-Pentane.json
View File

@@ -406,22 +406,22 @@
],
"critical_region_splines": {
"T_max": 469.70000000000005,
"T_min": 469.06161506402384,
"T_min": 469.36685791273345,
"_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",
"cL": [
-1.5350222378894414e-09,
1.4495090265584156e-05,
-0.04560406484397615,
517.5028217560338
-1.1076982598336214e-09,
1.0116271697455407e-05,
-0.03069871503131287,
500.6421885129799
],
"cV": [
1.3419945158856869e-09,
-1.3857242599790237e-05,
0.047489652270097,
415.6565744315043
4.3055773822385574e-10,
-5.541145426556296e-06,
0.022280143554586573,
441.03601546584997
],
"rhomolar_max": 3899.8810879232615,
"rhomolar_min": 2607.6316735875685
"rhomolar_max": 3750.9260751689894,
"rhomolar_min": 2757.127555479338
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/n-Propane.json
View File

@@ -452,22 +452,22 @@
],
"critical_region_splines": {
"T_max": 369.89,
"T_min": 369.88310506132734,
"T_min": 369.8896425409525,
"_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",
"cL": [
-1.2699463565482216e-10,
1.6385267569449435e-06,
-0.0068606698953377855,
379.1045100099181
0.0,
0.0,
-9.567201907483823e-06,
369.9378360095374
],
"cV": [
1.3753113621718563e-10,
-2.32949579930026e-06,
0.012980122776713688,
346.03538907178984
0.0,
0.0,
9.857730275302854e-06,
369.8407113486235
],
"rhomolar_max": 5155.238965206609,
"rhomolar_min": 4845.222396586998
"rhomolar_max": 5037.36296682965,
"rhomolar_min": 4963.738199610669
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",