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Updated saturation spline curves

Browse Source 
Signed-off-by: Ian Bell <ian.h.bell@gmail.com>
This commit is contained in:
Ian Bell
2014-09-03 17:31:04 +01:00
parent fca950907f
commit 9b211f2145
58 changed files with 658 additions and 658 deletions
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22
dev/fluids/Acetone.json
View File

@@ -353,22 +353,22 @@
],
"critical_region_splines": {
"T_max": 508.1,
"T_min": 508.09697325761744,
"T_min": 508.0999999999062,
"_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,
-4.656219323212737e-09,
508.10002188423084
],
"cV": [
1.9536072269032177e-10,
-2.983480058312324e-06,
0.015098157455448244,
482.76079813563524
0.0,
0.0,
4.64031360324759e-09,
508.0999781905261
],
"rhomolar_max": 4814.181193727979,
"rhomolar_min": 4590.050467927069
"rhomolar_max": 4700.020155407677,
"rhomolar_min": 4699.9797791519495
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Argon.json
View File

@@ -506,22 +506,22 @@
],
"critical_region_splines": {
"T_max": 150.687,
"T_min": 150.68697834063298,
"T_min": 150.68674395835467,
"_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
-2.124793992189458e-06,
150.7154880259892
],
"cV": [
0.0,
0.0,
6.072607995401675e-07,
150.67885819354578
2.1223479463722503e-06,
150.65854476919804
],
"rhomolar_max": 13442.525139946354,
"rhomolar_min": 13371.76233564158
"rhomolar_max": 13527.931526630135,
"rhomolar_min": 13286.788909807183
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

8
dev/fluids/Benzene.json
View File

@@ -527,11 +527,11 @@
],
"type": "polynomial"
}
},
},
"viscosity": {
"BibTeX": "Avgeri-JPCRD-2014-Benzene",
"dilute": {
"C": 2.1357e-08,
"C": 2.1357e-08,
"a": [
0.234018,
-0.476136,
@@ -541,7 +541,7 @@
"molar_mass_units": "kg/mol",
"t": [
0,
1,
1,
3
],
"type": "collision_integral"
@@ -576,7 +576,7 @@
],
"type": "Rainwater-Friend"
},
"sigma_eta": 5.40e-10,
"sigma_eta": 5.4e-10,
"sigma_eta_units": "m"
}
}

22
dev/fluids/CarbonMonoxide.json
View File

@@ -367,22 +367,22 @@
],
"critical_region_splines": {
"T_max": 132.86,
"T_min": 132.85867131966137,
"T_min": 132.85999999951312,
"_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": [
3.1174266374072594e-11,
-1.0578676813227408e-06,
0.011945990965038183,
87.96227472439597
0.0,
0.0,
-4.587508257048314e-09,
132.8600497744646
],
"cV": [
-2.7988602187391993e-11,
8.673443114829891e-07,
-0.008936706896165105,
163.4668663127422
0.0,
0.0,
4.611514127080118e-09,
132.85994996507173
],
"rhomolar_max": 11038.842068491349,
"rhomolar_min": 10664.189840198747
"rhomolar_max": 10850.106136720144,
"rhomolar_min": 10849.894418190801
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/CycloHexane.json
View File

@@ -449,22 +449,22 @@
],
"critical_region_splines": {
"T_max": 553.6,
"T_min": 553.5979946139788,
"T_min": 553.5999997660659,
"_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": [
1.56104739484658e-08,
-0.00015385588557227471,
0.5052887091787223,
0.6345188298942561
0.0,
0.0,
-8.175876311970891e-07,
553.602635902523
],
"cV": [
-1.5338245208003638e-08,
0.0001454870563719106,
-0.45981527881664047,
1037.8236160527126
0.0,
0.0,
8.181583620573008e-07,
553.5973622574407
],
"rhomolar_max": 3252.773506033089,
"rhomolar_min": 3195.2323910542696
"rhomolar_max": 3224.286127290438,
"rhomolar_min": 3223.7140723774714
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Cyclopentane.json
View File

@@ -387,22 +387,22 @@
],
"critical_region_splines": {
"T_max": 511.72,
"T_min": 511.7095934234679,
"T_min": 511.71999999967744,
"_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": [
-4.880588052926918e-09,
5.252717316693226e-05,
-0.18764912368477027,
734.1005944101676
0.0,
0.0,
-3.3125554580735164e-08,
511.72012653961855
],
"cV": [
5.250582737174832e-09,
-6.357124543112242e-05,
0.2558285044919253,
169.4290891702673
0.0,
0.0,
3.3109614501400934e-08,
511.71987352127263
],
"rhomolar_max": 3873.2904355172786,
"rhomolar_min": 3766.813756733369
"rhomolar_max": 3820.0097389577454,
"rhomolar_min": 3819.990256554135
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/D6.json
View File

@@ -352,22 +352,22 @@
],
"critical_region_splines": {
"T_max": 645.78,
"T_min": 645.4997615767367,
"T_min": 642.4672205036263,
"_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
0.0,
-6.230392935143472e-05,
0.07816508273019042,
621.263969382756
],
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2.1732433324774884e-07,
-0.00042927603672073575,
0.28201442644063596,
584.1491278422845
3.6584356889802007e-07,
-0.0006916100001806448,
0.43580969539355185,
554.2417982977918
],
"rhomolar_max": 725.3981107757561,
"rhomolar_min": 542.276230072255
"rhomolar_max": 857.8775266580042,
"rhomolar_min": 421.67935851484685
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Deuterium.json
View File

@@ -440,22 +440,22 @@
],
"critical_region_splines": {
"T_max": 38.34,
"T_min": 38.3399506598222,
"T_min": 38.339416735480214,
"_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
-2.853182978628294e-06,
38.389160342721766
],
"cV": [
0.0,
0.0,
8.380089288669903e-07,
38.325561106155625
2.8554684120896426e-06,
38.2908002792597
],
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"rhomolar_max": 17434.42590754112,
"rhomolar_min": 17025.73770897889
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

14
dev/fluids/DimethylCarbonate.json
View File

@@ -409,22 +409,22 @@
],
"critical_region_splines": {
"T_max": 557.0,
"T_min": 556.9999904919641,
"T_min": 556.9998876027566,
"_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,
-2.1173490191325178e-07,
557.0008469396076
-1.3572331448181178e-06,
557.0054289325793
],
"cV": [
0.0,
0.0,
2.0050706260121842e-07,
556.9991979717496
1.2967566129304942e-06,
556.9948129735483
],
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"rhomolar_min": 3952.580044972171
"rhomolar_max": 4082.813512058265,
"rhomolar_min": 3913.3243337382946
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/DimethylEther.json
View File

@@ -389,22 +389,22 @@
],
"critical_region_splines": {
"T_max": 400.378,
"T_min": 400.3774167354802,
"T_min": 400.37110506132734,
"_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
-1.2340856080204133e-11,
-3.6668010216655235e-07,
0.005662449102513134,
382.2672995716492
],
"cV": [
0.0,
0.0,
1.8536722158567707e-05,
400.2678918703781
3.2678596450956466e-11,
-1.1690463919857066e-06,
0.010429215559579295,
372.82769480948826
],
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"rhomolar_min": 5908.534646267459
"rhomolar_max": 6048.293446297928,
"rhomolar_min": 5831.9191440537215
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/EthylBenzene.json
View File

@@ -381,22 +381,22 @@
],
"critical_region_splines": {
"T_max": 617.12,
"T_min": 617.1197439583547,
"T_min": 617.1169732576175,
"_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,
-2.3245131740117315e-05,
617.1837152780217
-5.889287007942239e-10,
2.7489748115156017e-06,
-0.0017958058182523087,
613.5170511389289
],
"cV": [
0.0,
0.0,
2.3091817015124984e-05,
617.0567049600925
2.7233018397998547e-10,
-4.332169254554028e-06,
0.017610902629837312,
595.7882622446201
],
"rhomolar_max": 2752.0308502563307,
"rhomolar_min": 2729.928018264121
"rhomolar_max": 2778.835947943192,
"rhomolar_min": 2703.079602802352
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Ethylene.json
View File

@@ -510,22 +510,22 @@
],
"critical_region_splines": {
"T_max": 282.35,
"T_min": 282.3497439583547,
"T_min": 282.34697325761744,
"_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,
-3.634935446259431e-06,
282.37775915135825
-5.3490529714823425e-11,
1.1806509186406972e-06,
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303.55881549532984
],
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0.0,
0.0,
3.6437107681563877e-06,
282.3221738335621
5.6266047158959514e-11,
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0.010531516936650963,
254.66645559595844
],
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"rhomolar_min": 7566.496505023215
"rhomolar_max": 7866.912063903078,
"rhomolar_min": 7408.049532488636
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/HFE143m.json
View File

@@ -362,22 +362,22 @@
],
"critical_region_splines": {
"T_max": 377.921,
"T_min": 377.88522000242136,
"T_min": 377.92099999999897,
"_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
0.0,
0.0,
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377.9210032250623
],
"cV": [
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1.8467354481248633e-06,
-0.0066516525010036605,
385.2331741502011
0.0,
0.0,
5.712986843822467e-10,
377.9209973445233
],
"rhomolar_max": 4935.29110614525,
"rhomolar_min": 4335.002308503029
"rhomolar_max": 4648.142188502035,
"rhomolar_min": 4648.138929822613
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

20
dev/fluids/Helium.json
View File

@@ -440,22 +440,22 @@
],
"critical_region_splines": {
"T_max": 5.1953000000000005,
"T_min": 5.19073171770731,
"T_min": 5.141297013055385,
"_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
-4.82863868046167e-13,
2.5798878786242034e-08,
-0.0004593197751427837,
7.920274522054607
],
"cV": [
0.0,
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1.624444158435496e-05,
5.048044137037824
-1.5275455601862228e-09,
5.538880201235252e-05,
4.693200509758024
],
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"rhomolar_max": 22647.96434858185,
"rhomolar_min": 12184.179354171467
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Hydrogen.json
View File

@@ -412,22 +412,22 @@
],
"critical_region_splines": {
"T_max": 33.145,
"T_min": 33.13810506132737,
"T_min": 33.144999999992066,
"_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
0.0,
0.0,
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33.145005527098824
],
"cV": [
-2.3396699485553584e-12,
9.516798742074658e-08,
-0.0012636720187622463,
38.58044486815464
0.0,
0.0,
3.1573424275146666e-10,
33.14499510359337
],
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"rhomolar_min": 14746.877675758724
"rhomolar_max": 15508.022271289323,
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},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/IsoButane.json
View File

@@ -454,22 +454,22 @@
],
"critical_region_splines": {
"T_max": 407.817,
"T_min": 407.73549293470376,
"T_min": 406.8534813947396,
"_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
-9.941703745512649e-10,
1.1401780743865456e-05,
-0.04357798580431196,
463.3231742084145
],
"cV": [
5.562666408422913e-10,
-6.761233991678565e-06,
0.027344254864717768,
371.015481302833
0.0,
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0.00839238089576816,
391.53680162488934
],
"rhomolar_max": 4253.160501655689,
"rhomolar_min": 3479.687062549918
"rhomolar_max": 4815.639002152002,
"rhomolar_min": 2935.903033135107
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/IsoButene.json
View File

@@ -349,22 +349,22 @@
],
"critical_region_splines": {
"T_max": 418.09000000000003,
"T_min": 418.08543171770737,
"T_min": 418.08999999951317,
"_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,
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418.09008581994766
],
"cV": [
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6.9227418610441575e-06,
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448.11876326463465
0.0,
0.0,
2.0591910110230444e-08,
418.0899141317349
],
"rhomolar_max": 4246.188019158735,
"rhomolar_min": 4095.5716752458243
"rhomolar_max": 4170.023655555847,
"rhomolar_min": 4169.976356154625
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Isopentane.json
View File

@@ -365,22 +365,22 @@
],
"critical_region_splines": {
"T_max": 460.35,
"T_min": 460.34697325761744,
"T_min": 460.34999999967744,
"_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": [
8.005022701910341e-10,
-8.44526357152168e-06,
0.029554133854069683,
426.02215187987395
0.0,
0.0,
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460.350045140452
],
"cV": [
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4.689391032778603e-06,
-0.013394755215389163,
472.83487531264404
0.0,
0.0,
1.384341277338779e-08,
460.34995471819684
],
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"rhomolar_min": 3197.125647678554
"rhomolar_max": 3271.023375025736,
"rhomolar_min": 3270.9766981300554
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Krypton.json
View File

@@ -349,22 +349,22 @@
],
"critical_region_splines": {
"T_max": 209.48000000000002,
"T_min": 209.47310506132737,
"T_min": 209.47999999926515,
"_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
0.0,
0.0,
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209.48010167726926
],
"cV": [
-3.436623953002642e-11,
1.0066209446840255e-06,
-0.009706635600422744,
240.19068612286947
0.0,
0.0,
9.068846146505593e-09,
209.47990160301933
],
"rhomolar_max": 11108.82129459245,
"rhomolar_min": 10591.412518037536
"rhomolar_max": 10850.078419187403,
"rhomolar_min": 10849.918967439311
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Methane.json
View File

@@ -518,22 +518,22 @@
],
"critical_region_splines": {
"T_max": 190.564,
"T_min": 190.5639673093741,
"T_min": 190.56361355465157,
"_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,
-8.298041773773189e-07,
190.57241349076935
-2.9498492462244708e-06,
190.59390889908818
],
"cV": [
0.0,
0.0,
8.001489626516288e-07,
190.5558871872486
3.00418301102579e-06,
190.53354020391578
],
"rhomolar_max": 10178.523590876614,
"rhomolar_min": 10098.272325109083
"rhomolar_max": 10270.133117949952,
"rhomolar_min": 10010.492245451042
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

2
dev/fluids/Methanol.json
View File

@@ -455,7 +455,7 @@
"rhomolar": 0.00012793439653979163,
"rhomolar_units": "mol/m^3"
}
},
},
"TRANSPORT": {
"viscosity": {
"BibTeX": "Xiang-JPCRD-2006",

22
dev/fluids/MethylPalmitate.json
View File

@@ -395,22 +395,22 @@
],
"critical_region_splines": {
"T_max": 755.0,
"T_min": 754.9979946139788,
"T_min": 754.9999999319605,
"_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": [
-8.453804974988888e-07,
0.0022314430347624794,
-1.9626065342276378,
1330.1589912157262
0.0,
0.0,
-1.7213757676923328e-06,
755.0015440740636
],
"cV": [
8.346377269227008e-07,
-0.002289692013105165,
2.0930363910460232,
117.46650514532276
0.0,
0.0,
1.7239651981209695e-06,
754.9984536032173
],
"rhomolar_max": 903.4045446436754,
"rhomolar_min": 890.603960171529
"rhomolar_max": 897.0395262628024,
"rhomolar_min": 896.9605331088118
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Neon.json
View File

@@ -427,22 +427,22 @@
],
"critical_region_splines": {
"T_max": 44.491800000000005,
"T_min": 44.49141355465158,
"T_min": 44.48723171770732,
"_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
-1.1025814119387474e-13,
1.491524533973909e-09,
0.00011741598951019355,
42.338817257479654
],
"cV": [
0.0,
0.0,
1.5834258838542428e-06,
44.4539846230418
1.7438239837612905e-13,
-1.890874143571898e-08,
0.0006047801629533931,
38.4577598458307
],
"rhomolar_max": 24126.40596873362,
"rhomolar_min": 23637.943519451463
"rhomolar_max": 24720.30951969461,
"rhomolar_min": 23047.532486140095
},
"gas_constant": 8.31434,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Neopentane.json
View File

@@ -349,22 +349,22 @@
],
"critical_region_splines": {
"T_max": 433.74,
"T_min": 433.73543171770734,
"T_min": 433.73999999926514,
"_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
0.0,
0.0,
-2.793653710159193e-08,
433.7400913524763
],
"cV": [
-2.2365486585331262e-09,
2.089693784319932e-05,
-0.06492040004203695,
500.7835165371252
0.0,
0.0,
2.7689755256340264e-08,
433.7399094545003
],
"rhomolar_max": 3339.892894257803,
"rhomolar_min": 3198.06041887194
"rhomolar_max": 3270.026304880335,
"rhomolar_min": 3269.973461489175
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/Nitrogen.json
View File

@@ -501,22 +501,22 @@
],
"critical_region_splines": {
"T_max": 126.19200000000001,
"T_min": 126.19199998688855,
"T_min": 126.19199984500558,
"_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
-1.7874713257311775e-07,
126.19399909031777
],
"cV": [
0.0,
0.0,
9.95463660457675e-10,
126.19198886683252
1.1629442664483669e-08,
126.19186993745916
],
"rhomolar_max": 11183.986174852074,
"rhomolar_min": 11170.73026187868
"rhomolar_max": 11184.76858012661,
"rhomolar_min": 11170.573704081868
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

14
dev/fluids/OrthoDeuterium.json
View File

@@ -417,22 +417,22 @@
],
"critical_region_splines": {
"T_max": 38.34,
"T_min": 38.33996730937413,
"T_min": 38.33961355465158,
"_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
-2.3235096620580277e-06,
38.38003407147726
],
"cV": [
0.0,
0.0,
6.843466890793785e-07,
38.328208706547166
2.3247053545885936e-06,
38.29994532674044
],
"rhomolar_max": 17277.722226405003,
"rhomolar_min": 17182.23089934681
"rhomolar_max": 17396.319664916562,
"rhomolar_min": 17063.76588019465
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

22
dev/fluids/OrthoHydrogen.json
View File

@@ -379,22 +379,22 @@
],
"critical_region_splines": {
"T_max": 33.22,
"T_min": 33.216973257617425,
"T_min": 33.21999999998802,
"_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
0.0,
0.0,
-4.57432325893615e-10,
33.220007064832
],
"cV": [
-3.379814959674437e-12,
1.404217131242082e-07,
-0.0019188970430762365,
41.812545688089735
0.0,
0.0,
4.301031431449862e-10,
33.219993357254666
],
"rhomolar_max": 15899.98591137461,
"rhomolar_min": 14989.857909343546
"rhomolar_max": 15444.566501913807,
"rhomolar_min": 15444.512461229047
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/ParaDeuterium.json
View File

@@ -415,22 +415,22 @@
],
"critical_region_splines": {
"T_max": 38.34,
"T_min": 38.33996730937413,
"T_min": 38.33961355465158,
"_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
-2.3234750017306126e-06,
38.38003347427982
],
"cV": [
0.0,
0.0,
6.848389037037868e-07,
38.32820022568919
2.3248386159631863e-06,
38.29994303064696
],
"rhomolar_max": 17277.727009113827,
"rhomolar_min": 17182.26523245882
"rhomolar_max": 17396.32214598207,
"rhomolar_min": 17063.77540885253
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

22
dev/fluids/ParaHydrogen.json
View File

@@ -419,22 +419,22 @@
],
"critical_region_splines": {
"T_max": 32.938,
"T_min": 32.93599461397884,
"T_min": 32.93799999997271,
"_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": [
4.253205081213295e-12,
-2.116493776473347e-07,
0.0034966692458426726,
13.749966028178376
0.0,
0.0,
-6.176636722223463e-10,
32.938009597258144
],
"cV": [
-3.141534424322369e-12,
1.338646257848717e-07,
-0.0018846003827776433,
41.68699310689614
0.0,
0.0,
5.786265121310599e-10,
32.93799100930126
],
"rhomolar_max": 15953.359013823481,
"rhomolar_min": 15115.765516662266
"rhomolar_max": 15538.044190612114,
"rhomolar_min": 15537.952830972841
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Propylene.json
View File

@@ -458,22 +458,22 @@
],
"critical_region_splines": {
"T_max": 364.211,
"T_min": 364.21041673548024,
"T_min": 364.20410506132737,
"_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
-2.0397446597019764e-10,
3.2958687540071058e-06,
-0.017748737115287072,
396.06517964228243
],
"cV": [
0.0,
0.0,
6.4811926293276935e-06,
364.17563213182177
2.0280477994216778e-10,
-3.3625914669476956e-06,
0.018581444515139024,
329.9897393682322
],
"rhomolar_max": 5546.663535640788,
"rhomolar_min": 5367.006606323258
"rhomolar_max": 5722.778431306117,
"rhomolar_min": 5189.89767929224
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R113.json
View File

@@ -376,22 +376,22 @@
],
"critical_region_splines": {
"T_max": 487.21000000000004,
"T_min": 487.20941673548026,
"T_min": 487.2031050613274,
"_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
3.6894468782358206e-10,
-4.073513681283046e-06,
0.014462353513138904,
470.5229580953627
],
"cV": [
0.0,
0.0,
2.1763182218616364e-05,
487.1449572672853
1.1946318431162753e-09,
-1.1482911409880193e-05,
0.03662536226299625,
448.42495860364784
],
"rhomolar_max": 3016.2291002048787,
"rhomolar_min": 2961.858589771953
"rhomolar_max": 3085.865073202007,
"rhomolar_min": 2900.0292736747374
},
"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R116.json
View File

@@ -346,22 +346,22 @@
],
"critical_region_splines": {
"T_max": 293.03000000000003,
"T_min": 293.02697325761744,
"T_min": 293.02999999985843,
"_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
0.0,
0.0,
-7.658301925164341e-09,
293.0300340334938
],
"cV": [
-4.2587664193266785e-10,
5.257573775768188e-06,
-0.02149722855677295,
322.1082759616395
0.0,
0.0,
7.708669659796271e-09,
293.02996574267206
],
"rhomolar_max": 4535.77641861197,
"rhomolar_min": 4355.023810307573
"rhomolar_max": 4444.018490179812,
"rhomolar_min": 4443.981630049213
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R12.json
View File

@@ -394,22 +394,22 @@
],
"critical_region_splines": {
"T_max": 385.12,
"T_min": 385.11941673548023,
"T_min": 385.11310506132736,
"_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,
-1.583911139375003e-05,
385.1940127028315
1.384320477183494e-11,
-6.214242836621232e-07,
0.004900765150571461,
374.37610683053464
],
"cV": [
0.0,
0.0,
1.5981068543804365e-05,
385.04532396245855
1.8819672379934522e-10,
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0.01632960178423799,
356.56849340248095
],
"rhomolar_max": 4709.605576782584,
"rhomolar_min": 4636.284039366143
"rhomolar_max": 4800.06197048058,
"rhomolar_min": 4549.199865356502
},
"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R123.json
View File

@@ -470,22 +470,22 @@
],
"critical_region_splines": {
"T_max": 456.831,
"T_min": 456.7079808473738,
"T_min": 456.83099999999655,
"_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
0.0,
0.0,
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456.83100538489015
],
"cV": [
5.019316578137991e-10,
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0.024431712288804266,
424.57182248409964
0.0,
0.0,
1.577833587606056e-09,
456.8309943254525
],
"rhomolar_max": 3965.7364882421543,
"rhomolar_min": 3221.873367889577
"rhomolar_max": 3596.419300284971,
"rhomolar_min": 3596.414813901929
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R1234yf.json
View File

@@ -392,22 +392,22 @@
],
"critical_region_splines": {
"T_max": 367.85,
"T_min": 367.84983035809745,
"T_min": 367.84799461397887,
"_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,
-7.28092281910778e-06,
367.8803614481557
-6.280447767869642e-11,
4.941333351258848e-07,
-0.0008447696692286383,
367.3343146300655
],
"cV": [
0.0,
0.0,
7.273842039048367e-06,
367.8196680786972
8.488656120290226e-11,
-1.3525258087977996e-06,
0.006851813473070161,
356.6416038903997
],
"rhomolar_max": 4193.299505682264,
"rhomolar_min": 4146.67781322612
"rhomolar_max": 4252.211021596844,
"rhomolar_min": 4087.906435621643
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/R1234ze(E).json
View File

@@ -405,22 +405,22 @@
],
"critical_region_splines": {
"T_max": 382.52,
"T_min": 382.5199506598222,
"T_min": 382.5194167354802,
"_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,
-7.9305911732753e-07,
382.5234022236133
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382.53813455270046
],
"cV": [
0.0,
0.0,
6.090875342473237e-07,
382.51738701447806
3.54150649256091e-06,
382.5048069371469
],
"rhomolar_max": 4352.215006013345,
"rhomolar_min": 4208.993289113025
"rhomolar_max": 4427.979956342802,
"rhomolar_min": 4125.306098974923
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R1234ze(Z).json
View File

@@ -348,22 +348,22 @@
],
"critical_region_splines": {
"T_max": 423.27,
"T_min": 423.26310506132734,
"T_min": 423.26999999889085,
"_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": [
-1.0661006391670194e-09,
1.2653370461499062e-05,
-0.04997314613163001,
488.933234607043
0.0,
0.0,
-2.4196343285339583e-08,
423.27009972047097
],
"cV": [
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9.267609720003654e-06,
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466.4282367596696
0.0,
0.0,
3.019678505019119e-08,
423.2698755498882
],
"rhomolar_max": 4225.213370352157,
"rhomolar_min": 4025.0245673273625
"rhomolar_max": 4121.349202957066,
"rhomolar_min": 4121.266633051825
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R134a.json
View File

@@ -380,22 +380,22 @@
],
"critical_region_splines": {
"T_max": 374.21,
"T_min": 374.15599701305536,
"T_min": 373.5716150640238,
"_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
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4.632248820128229e-06,
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410.803318485873
],
"cV": [
2.033032586375043e-10,
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0.017300443262052236,
343.6482870886872
3.734362612529562e-10,
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0.02879764276811166,
325.5497395319938
],
"rhomolar_max": 5442.556273932187,
"rhomolar_min": 4580.218882520725
"rhomolar_max": 6152.557816507652,
"rhomolar_min": 3872.298405322532
},
"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R143a.json
View File

@@ -381,22 +381,22 @@
],
"critical_region_splines": {
"T_max": 345.857,
"T_min": 345.85688760275673,
"T_min": 345.8556713196614,
"_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
-2.8895140603394883e-11,
2.005756782258384e-07,
0.00022262855324051985,
343.3373934663645
],
"cV": [
0.0,
0.0,
5.221395136669298e-06,
345.8302223361114
5.7189072201719986e-11,
-1.123885386251343e-06,
0.0070151907568205005,
331.72539959954764
],
"rhomolar_max": 5149.890794010884,
"rhomolar_min": 5106.923714331294
"rhomolar_max": 5201.926128087604,
"rhomolar_min": 5055.283375792975
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R152A.json
View File

@@ -468,22 +468,22 @@
],
"critical_region_splines": {
"T_max": 386.411,
"T_min": 386.2879808473738,
"T_min": 386.41099999999204,
"_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": [
-1.1446811820239007e-10,
1.646295645058246e-06,
-0.007684872988074046,
397.9206701191548
0.0,
0.0,
-1.441541916647247e-09,
386.41100803148214
],
"cV": [
1.0521854870590392e-10,
-2.0174071540863595e-06,
0.012681483095329345,
360.1823139464937
0.0,
0.0,
1.4566499622392455e-09,
386.4109918843441
],
"rhomolar_max": 6176.35151183272,
"rhomolar_min": 4954.90121849081
"rhomolar_max": 5571.457898124929,
"rhomolar_min": 5571.4469054491965
},
"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",

18
dev/fluids/R161.json
View File

@@ -397,22 +397,22 @@
],
"critical_region_splines": {
"T_max": 375.25,
"T_min": 375.2498876027567,
"T_min": 375.24867131966136,
"_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,
-1.0274211653082636e-06,
375.25645220491816
-2.3597508647707754e-08,
0.00029638470861520266,
374.31935201494827
],
"cV": [
0.0,
0.0,
6.800670480519312e-07,
375.24572917893823
-1.4520865417565774e-08,
0.00018238206964464205,
374.6773203013158
],
"rhomolar_max": 6389.397438091061,
"rhomolar_min": 6114.726232371929
"rhomolar_max": 6517.288765706664,
"rhomolar_min": 5977.507922869694
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R218.json
View File

@@ -344,22 +344,22 @@
],
"critical_region_splines": {
"T_max": 345.02,
"T_min": 345.01867131966134,
"T_min": 345.01999999990613,
"_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": [
2.115849844779737e-09,
-2.2622652824384362e-05,
0.08030859728161308,
250.32261200217556
0.0,
0.0,
-1.156582542340429e-08,
345.0200386298569
],
"cV": [
-1.5113366978895236e-09,
1.3734866737761167e-05,
-0.04116930680731554,
385.6167633643665
0.0,
0.0,
1.1490855119850737e-08,
345.0199616205439
],
"rhomolar_max": 3371.3072650243957,
"rhomolar_min": 3308.7608519066903
"rhomolar_max": 3340.008115750424,
"rhomolar_min": 3339.9918305420742
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R22.json
View File

@@ -473,22 +473,22 @@
],
"critical_region_splines": {
"T_max": 369.295,
"T_min": 369.29299461397886,
"T_min": 369.29499999999473,
"_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,
-8.277256091856358e-10,
369.29500501454385
],
"cV": [
2.0197560844726486e-11,
-5.076049994717274e-07,
0.003926491093801074,
359.64667998370135
0.0,
0.0,
9.036108521741466e-10,
369.2949945257267
],
"rhomolar_max": 6174.151068396738,
"rhomolar_min": 5939.762656878844
"rhomolar_max": 6058.226375538457,
"rhomolar_min": 6058.214137613641
},
"gas_constant": 8.31451,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R227EA.json
View File

@@ -416,22 +416,22 @@
],
"critical_region_splines": {
"T_max": 374.90000000000003,
"T_min": 374.8931050613274,
"T_min": 374.89999999993785,
"_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": [
-5.875126621910152e-10,
5.780632973589872e-06,
-0.01887717891595377,
395.3469681114307
0.0,
0.0,
-4.848721869600648e-09,
374.90001694628296
],
"cV": [
1.1730303150524067e-10,
-1.607222079285808e-06,
0.006935903946970884,
365.2834297632339
0.0,
0.0,
4.855705508254663e-09,
374.8999830293093
],
"rhomolar_max": 3618.508261092158,
"rhomolar_min": 3362.517912603551
"rhomolar_max": 3495.0128237303156,
"rhomolar_min": 3494.9871917055066
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R236EA.json
View File

@@ -394,22 +394,22 @@
],
"critical_region_splines": {
"T_max": 412.44,
"T_min": 412.01703429466085,
"T_min": 407.44,
"_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
-7.988424303242158e-10,
8.554876458658245e-06,
-0.030487020885094897,
448.58939769263844
],
"cV": [
8.719771420305249e-10,
-9.978606681376363e-06,
0.03803850767350116,
364.13631933098907
0.0,
-1.915826026167026e-06,
0.01423841902647334,
385.9850174488125
],
"rhomolar_max": 4440.255966785143,
"rhomolar_min": 3017.4925122772956
"rhomolar_max": 5423.60551214582,
"rhomolar_min": 2100.4999798205076
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

182
dev/fluids/R245fa.json
View File

@@ -43,74 +43,12 @@
"max_abs_error_units": "J/mol",
"type": "rational_polynomial"
},
"pV": {
"Tmin": 171.05000000000001,
"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"Tmax": 427.0,
"using_tau_r": true,
"max_abserror_percentage": 0.021575129298945228,
"t": [
0.775,
0.971,
2.155,
3.232,
9.097,
11.456
],
"reducing_value": 3651000.0,
"T_r": 427.01,
"n": [
0.21292235127871662,
-7.22997740109537,
0.4023556144042939,
-4.366079807014841,
-9.155639983057442,
14.533193893397405
],
"type": "pV"
},
"rhoV": {
"Tmin": 171.05000000000001,
"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
"Tmax": 427.0,
"using_tau_r": true,
"max_abserror_percentage": 0.26467661268476661,
"t": [
0.075,
0.466,
1.018,
2.817,
6.14,
8.5
],
"reducing_value": 3875.0,
"T_r": 427.01,
"n": [
-0.12316786769188867,
-3.5467162730203325,
-2.100626576983384,
-3.02259697521286,
-10.604906302496444,
12.900898794193413
],
"type": "rhoV"
},
"pL": {
"Tmin": 171.05000000000001,
"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"Tmax": 427.0,
"using_tau_r": true,
"max_abserror_percentage": 0.013022195594358799,
"t": [
7.194,
1.03,
1.145,
2.84,
4.613,
18.798
],
"reducing_value": 3651000.0,
"T_r": 427.01,
"Tmax": 427.0,
"Tmin": 171.05,
"description": "p' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.013022195594358799,
"n": [
-0.9670903356725931,
-11.756404923945222,
@@ -119,24 +57,50 @@
-2.217939014066299,
28.8905424182831
],
"type": "pL"
"reducing_value": 3651000.0,
"t": [
7.194,
1.03,
1.145,
2.84,
4.613,
18.798
],
"type": "pL",
"using_tau_r": true
},
"pV": {
"T_r": 427.01,
"Tmax": 427.0,
"Tmin": 171.05,
"description": "p'' = pc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.021575129298945228,
"n": [
0.21292235127871662,
-7.22997740109537,
0.4023556144042939,
-4.366079807014841,
-9.155639983057442,
14.533193893397405
],
"reducing_value": 3651000.0,
"t": [
0.775,
0.971,
2.155,
3.232,
9.097,
11.456
],
"type": "pV",
"using_tau_r": true
},
"rhoL": {
"Tmin": 171.05000000000001,
"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
"Tmax": 427.0,
"using_tau_r": false,
"max_abserror_percentage": 0.040900248845132658,
"t": [
0.144,
0.165,
0.53,
1.993,
2.646,
3.593
],
"reducing_value": 3875.0,
"T_r": 427.01,
"Tmax": 427.0,
"Tmin": 171.05,
"description": "rho' = rhoc*(1+sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.04090024884513266,
"n": [
-0.645916749226158,
1.2435143264412414,
@@ -145,7 +109,43 @@
2.697825229930464,
-1.236775453941409
],
"type": "rhoLnoexp"
"reducing_value": 3875.0,
"t": [
0.144,
0.165,
0.53,
1.993,
2.646,
3.593
],
"type": "rhoLnoexp",
"using_tau_r": false
},
"rhoV": {
"T_r": 427.01,
"Tmax": 427.0,
"Tmin": 171.05,
"description": "rho'' = rhoc*exp(Tc/T*sum(n_i*theta^t_i))",
"max_abserror_percentage": 0.2646766126847666,
"n": [
-0.12316786769188867,
-3.5467162730203325,
-2.100626576983384,
-3.02259697521286,
-10.604906302496444,
12.900898794193413
],
"reducing_value": 3875.0,
"t": [
0.075,
0.466,
1.018,
2.817,
6.14,
8.5
],
"type": "rhoV",
"using_tau_r": true
},
"sL": {
"A": [
@@ -387,22 +387,22 @@
],
"critical_region_splines": {
"T_max": 427.01,
"T_min": 427.0098876027567,
"T_min": 427.00867131966135,
"_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,
-1.084584597428029e-06,
427.014202765315
-3.531037635318706e-08,
0.0002736554167372022,
426.47979263007164
],
"cV": [
0.0,
0.0,
1.2920303634458716e-06,
427.00499338234164
-4.30215593700091e-08,
0.00033341708511756433,
426.3640043975847
],
"rhomolar_max": 3978.6316056494643,
"rhomolar_min": 3788.0072740848295
"rhomolar_max": 4068.9809495988143,
"rhomolar_min": 3699.261392719093
},
"gas_constant": 8.3144621,
"gas_constant_units": "J/mol/K",

14
dev/fluids/R32.json
View File

@@ -374,22 +374,22 @@
],
"critical_region_splines": {
"T_max": 351.255,
"T_min": 351.25499816776613,
"T_min": 351.254978340633,
"_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,
-4.041924265889875e-07,
351.25829420247135
-9.240003401086692e-07,
351.2625306809423
],
"cV": [
0.0,
0.0,
1.4328717651880036e-07,
351.2538321973893
8.673043856669974e-07,
351.24793139588286
],
"rhomolar_max": 8154.617673148497,
"rhomolar_min": 8137.297455089546
"rhomolar_max": 8173.525464736033,
"rhomolar_min": 8125.111398713756
},
"gas_constant": 8.314471,
"gas_constant_units": "J/mol/K",

22
dev/fluids/R41.json
View File

@@ -357,22 +357,22 @@
],
"critical_region_splines": {
"T_max": 317.28000000000003,
"T_min": 317.2695934234679,
"T_min": 317.2799999997863,
"_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
0.0,
0.0,
-5.946649378688733e-09,
317.2800553038393
],
"cV": [
-8.480951160041928e-11,
2.20398173327229e-06,
-0.018988536263903795,
371.46813146596344
0.0,
0.0,
5.876648086292159e-09,
317.2799453471728
],
"rhomolar_max": 9571.518280811737,
"rhomolar_min": 9026.378810480832
"rhomolar_max": 9300.035945660456,
"rhomolar_min": 9299.963628495072
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Toluene.json
View File

@@ -351,22 +351,22 @@
],
"critical_region_splines": {
"T_max": 591.75,
"T_min": 591.7342932852254,
"T_min": 591.7499999988909,
"_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
0.0,
0.0,
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591.7501661936486
],
"cV": [
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1.972502928601055e-05,
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641.0297738234855
0.0,
0.0,
5.267522401490593e-08,
591.7498330722151
],
"rhomolar_max": 3253.6261257770193,
"rhomolar_min": 3086.5243371577894
"rhomolar_max": 3169.0211483621283,
"rhomolar_min": 3168.9789444501107
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Water.json
View File

@@ -643,22 +643,22 @@
],
"critical_region_splines": {
"T_max": 647.096,
"T_min": 647.0954167354802,
"T_min": 647.0891050613274,
"_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,
-2.6319631259532804e-06,
647.1430429930077
-4.042762309098527e-12,
2.0584764946656947e-07,
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666.6888430405046
],
"cV": [
0.0,
0.0,
2.6053577217441603e-06,
647.0494325447503
3.9619849743940495e-12,
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0.004177682638992649,
621.0723284163671
],
"rhomolar_max": 18095.336161027783,
"rhomolar_min": 17649.856810851063
"rhomolar_max": 18580.861739248718,
"rhomolar_min": 17158.467276424304
},
"gas_constant": 8.314371357587,
"gas_constant_units": "J/mol/K",

22
dev/fluids/Xenon.json
View File

@@ -352,22 +352,22 @@
],
"critical_region_splines": {
"T_max": 289.733,
"T_min": 289.72843171770734,
"T_min": 289.73299999832597,
"_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,
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0.05529442454906748,
129.54501621008842
0.0,
0.0,
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289.73316415186304
],
"cV": [
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5.34493631486394e-06,
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404.53030033147684
0.0,
0.0,
1.9705426830168584e-08,
289.73283447441463
],
"rhomolar_max": 8554.90344650679,
"rhomolar_min": 8248.286253998665
"rhomolar_max": 8400.08566414265,
"rhomolar_min": 8399.915046038452
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

14
dev/fluids/m-Xylene.json
View File

@@ -386,22 +386,22 @@
],
"critical_region_splines": {
"T_max": 616.89,
"T_min": 616.8899937003947,
"T_min": 616.8899255305433,
"_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,
-2.3188404050194553e-07,
616.8906179709679
-1.5295569802554634e-06,
616.8940762693524
],
"cV": [
0.0,
0.0,
2.1811620743863226e-07,
616.8894187203072
1.4085684731752365e-06,
616.886246165019
],
"rhomolar_max": 2692.1670497921914,
"rhomolar_min": 2636.1181240342576
"rhomolar_max": 2713.686945041748,
"rhomolar_min": 2612.131106477632
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

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

@@ -451,22 +451,22 @@
],
"critical_region_splines": {
"T_max": 425.125,
"T_min": 425.1219732576174,
"T_min": 425.12499999999653,
"_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,
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425.12500625397735
],
"cV": [
5.058796197557434e-11,
-1.3472509771444817e-06,
0.008234549282093268,
410.50072741365295
0.0,
0.0,
1.671186275109249e-09,
425.12499344432126
],
"rhomolar_max": 3985.810039412961,
"rhomolar_min": 3859.458487995192
"rhomolar_max": 3922.7717979270105,
"rhomolar_min": 3922.767549762673
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

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

@@ -351,22 +351,22 @@
],
"critical_region_splines": {
"T_max": 617.7,
"T_min": 617.6842932852254,
"T_min": 617.6999999974735,
"_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
0.0,
0.0,
-1.726981763252328e-07,
617.7002832250092
],
"cV": [
-3.8653700756418197e-08,
0.00017824366286806788,
-0.2727502335438755,
756.1055367913187
0.0,
0.0,
1.8026843741974914e-07,
617.6997043597627
],
"rhomolar_max": 1678.7818428517664,
"rhomolar_min": 1601.198950562281
"rhomolar_max": 1640.014630074043,
"rhomolar_min": 1639.9859844635084
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

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

@@ -359,22 +359,22 @@
],
"critical_region_splines": {
"T_max": 658.1,
"T_min": 658.0986713196614,
"T_min": 658.0842932852254,
"_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
-8.162186259380569e-07,
0.002171141544995267,
656.6561908725781
],
"cV": [
1.345410821444352e-08,
-5.389362597299564e-05,
0.07196012902658075,
626.0728305909759
0.0,
-1.7627161847925473e-06,
0.00468882505154816,
654.9819313407205
],
"rhomolar_max": 1409.180220111776,
"rhomolar_min": 1288.4723365719328
"rhomolar_max": 1468.7201111458296,
"rhomolar_min": 1235.6044584051854
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

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

@@ -350,22 +350,22 @@
],
"critical_region_splines": {
"T_max": 594.5500000000001,
"T_min": 594.5262937515283,
"T_min": 594.5499999988909,
"_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
0.0,
0.0,
-9.62836132236938e-08,
594.55017427334
],
"cV": [
-2.3832710380126962e-08,
0.00012016817674452382,
-0.2007737723861744,
705.5893640684056
0.0,
0.0,
1.0501270033534904e-07,
594.5498099270125
],
"rhomolar_max": 1866.189822592916,
"rhomolar_min": 1755.3631417347385
"rhomolar_max": 1810.011518970226,
"rhomolar_min": 1809.9894381092934
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

26
dev/fluids/n-Propane.json
View File

@@ -56,9 +56,9 @@
"T_0": 85.525,
"T_max": 175,
"T_min": 85.525,
"a": 718000000.0,
"a": 718000000.0,
"c": 1.283,
"p_0": 0.00017200108942021548
"p_0": 0.00017207065534365437
}
],
"type": "Simon"
@@ -432,22 +432,22 @@
],
"critical_region_splines": {
"T_max": 369.89,
"T_min": 369.88310506132734,
"T_min": 369.8899999999947,
"_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,
-1.1383796297589533e-09,
369.8900056918981
],
"cV": [
1.3753113621718563e-10,
-2.32949579930026e-06,
0.012980122776713688,
346.03538907178984
0.0,
0.0,
1.237688468336273e-09,
369.88999381155764
],
"rhomolar_max": 5155.238965206609,
"rhomolar_min": 4845.222396586998
"rhomolar_max": 5000.004634865591,
"rhomolar_min": 4999.995734219138
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",

20
dev/fluids/p-Xylene.json
View File

@@ -384,22 +384,22 @@
],
"critical_region_splines": {
"T_max": 616.168,
"T_min": 616.1676135546516,
"T_min": 616.1634317177073,
"_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,
-1.1132572209863086e-05,
616.1979902589276
-5.4532827442939e-09,
4.400267120267819e-05,
-0.11835258016741836,
722.277453847427
],
"cV": [
0.0,
0.0,
8.534367674093475e-06,
616.1450090962354
-3.3155928616944385e-07,
0.0017863883843951315,
613.7618063017552
],
"rhomolar_max": 2728.633033173596,
"rhomolar_min": 2648.6389243240715
"rhomolar_max": 2784.1283761391046,
"rhomolar_min": 2576.5395234223492
},
"gas_constant": 8.314472,
"gas_constant_units": "J/mol/K",