- InChI
- InChI=1S/C2H2F4/c3-1-2(4,5)6/h1H2
- InChI Key
- LVGUZGTVOIAKKC-UHFFFAOYSA-N
- Formula
- C2H2F4
- SMILES
- FCC(F)(F)F
- Molecular Weight1
- 102.03
- CAS
- 811-97-2
- Other Names
-
- 1,1,1,2-Tetrafluoroethane
- 1,2,2,2-Tetrafluoroethane
- CF3CH2F
- Ethane, 1,1,1,2-tetrafluoro-
- Freon 134a
- HFA-134a
- NORFLURAN
- R 134a
- R-134a
- REFRIGERANT-134A
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- ν : Kinematic viscosity (m2/s).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- ρm,g : Gas Amount Density (mol/m3).
- Inp : Non-polar retention indices.
- D*i : Self diffusion coefficient (m2/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -810.44 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -877.80 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 5.84 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 15.48 | kJ/mol | Joback Calculated Property |
| log10WS | -1.18 | Crippen Calculated Property | |
| logPoct/wat | 1.518 | Crippen Calculated Property | |
| McVol | 46.120 | ml/mol | McGowan Calculated Property |
| Pc | [4029.00; 4068.00] | kPa |
|
| Pc | 4065.00 | kPa | KDB |
| Pc | 4051.00 | kPa | Critica... |
| Pc | 4053.00 | kPa | Critica... |
| Pc | 4053.00 | kPa | Critica... |
| Pc | 4048.10 ± 5.00 | kPa | NIST |
| Pc | 4048.20 ± 3.00 | kPa | NIST |
| Pc | 4047.80 ± 5.00 | kPa | NIST |
| Pc | 4054.00 ± 8.00 | kPa | NIST |
| Pc | 4052.00 ± 9.00 | kPa | NIST |
| Pc | 4055.10 ± 2.00 | kPa | NIST |
| Pc | 4068.00 ± 10.00 | kPa | NIST |
| Pc | 4055.00 ± 6.00 | kPa | NIST |
| Pc | Outlier 4029.00 ± 6.00 | kPa | NIST |
| Pc | 4064.00 ± 10.00 | kPa | NIST |
| Pc | 4067.00 ± 2.70 | kPa | NIST |
| Pc | 4065.00 ± 8.00 | kPa | NIST |
| Pc | 4067.00 ± 10.00 | kPa | NIST |
| ρc | [507.09; 515.15] | kg/m3 |
|
| ρc | 507.09 ± 5.10 | kg/m3 | NIST |
| ρc | 509.13 ± 3.06 | kg/m3 | NIST |
| ρc | 511.17 ± 5.10 | kg/m3 | NIST |
| ρc | 509.13 ± 2.04 | kg/m3 | NIST |
| ρc | 508.11 ± 5.10 | kg/m3 | NIST |
| ρc | 511.17 ± 3.06 | kg/m3 | NIST |
| ρc | Outlier 515.15 ± 2.55 | kg/m3 | NIST |
| ρc | 507.09 ± 5.10 | kg/m3 | NIST |
| ρc | 512.20 ± 5.10 | kg/m3 | NIST |
| ρc | 508.11 ± 3.06 | kg/m3 | NIST |
| ρc | 512.20 ± 2.04 | kg/m3 | NIST |
| Inp | [219.00; 219.00] |
|
|
| Inp | 219.00 | NIST | |
| Inp | 219.00 | NIST | |
| Inp | 219.00 | NIST | |
| Tboil | [246.60; 247.10] | K |
|
| Tboil | 246.60 | K | KDB |
| Tboil | 246.60 | K | NIST |
| Tboil | 247.10 ± 2.00 | K | NIST |
| Tc | [373.05; 374.30] | K |
|
| Tc | 374.30 | K | KDB |
| Tc | 374.07 ± 0.04 | K | NIST |
| Tc | 374.07 ± 0.02 | K | NIST |
| Tc | 374.07 ± 0.02 | K | NIST |
| Tc | 374.08 ± 0.02 | K | NIST |
| Tc | 373.80 ± 0.50 | K | NIST |
| Tc | 374.11 ± 0.05 | K | NIST |
| Tc | 374.11 ± 0.03 | K | NIST |
| Tc | 374.25 ± 0.05 | K | NIST |
| Tc | 374.18 ± 0.10 | K | NIST |
| Tc | 374.20 ± 0.10 | K | NIST |
| Tc | Outlier 373.05 ± 0.30 | K | NIST |
| Tc | 374.25 ± 0.15 | K | NIST |
| Tc | 374.30 ± 0.01 | K | NIST |
| Tc | 374.27 ± 0.10 | K | NIST |
| Tfus | 172.00 | K | KDB |
| Ttriple | [169.85; 169.85] | K |
|
| Ttriple | 169.85 ± 0.01 | K | NIST |
| Ttriple | 169.85 ± 0.01 | K | NIST |
| Ttriple | 169.85 ± 0.02 | K | NIST |
| Vc | 0.198 | m3/kmol | KDB |
| Zc | 0.2586240 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [71.67; 97.89] | J/mol×K | [239.01; 369.61] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 70 75 80 85 90 95 100 250 300 350 | ||||
| Cp,gas | 71.67 | J/mol×K | 239.01 | Joback Calculated Property |
| Cp,gas | 76.59 | J/mol×K | 260.78 | Joback Calculated Property |
| Cp,gas | 81.27 | J/mol×K | 282.54 | Joback Calculated Property |
| Cp,gas | 85.74 | J/mol×K | 304.31 | Joback Calculated Property |
| Cp,gas | 89.99 | J/mol×K | 326.08 | Joback Calculated Property |
| Cp,gas | 94.04 | J/mol×K | 347.85 | Joback Calculated Property |
| Cp,gas | 97.89 | J/mol×K | 369.61 | Joback Calculated Property |
| ΔfusH | 2.01 | kJ/mol | 169.40 | NIST |
| ΔvapH | [22.00; 26.40] | kJ/mol | [180.00; 321.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 22 23 24 25 26 200 250 300 | ||||
| ΔvapH | 26.40 | kJ/mol | 180.00 | NIST |
| ΔvapH | 25.00 | kJ/mol | 200.00 | NIST |
| ΔvapH | 23.80 | kJ/mol | 220.00 | NIST |
| ΔvapH | 23.70 | kJ/mol | 233.50 | NIST |
| ΔvapH | 22.70 | kJ/mol | 240.00 | NIST |
| ΔvapH | 22.00 | kJ/mol | 321.00 | NIST |
| ν | [7.9000000e-08; 0.0000002] | m2/s | [302.99; 368.26] |
|
|
T(K) Kinematic viscosity (m2/s) 8.00e-8 1.00e-7 1.20e-7 1.40e-7 1.60e-7 320 340 360 | ||||
| ν | 0.0000002 | m2/s | 302.99 | Liquid ... |
| ν | 0.0000001 | m2/s | 312.86 | Liquid ... |
| ν | 0.0000001 | m2/s | 322.92 | Liquid ... |
| ν | 0.0000001 | m2/s | 332.92 | Liquid ... |
| ν | 0.0000001 | m2/s | 342.90 | Liquid ... |
| ν | 9.7900000e-08 | m2/s | 352.89 | Liquid ... |
| ν | 8.5600000e-08 | m2/s | 363.27 | Liquid ... |
| ν | 7.9000000e-08 | m2/s | 368.26 | Liquid ... |
| Pvap | [84.10; 3245.53] | kPa | [243.10; 363.18] |
|
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 250 300 350 | ||||
| Pvap | 84.23 | kPa | 243.10 | Saturat... |
| Pvap | 84.10 | kPa | 243.14 | Experim... |
| Pvap | 84.50 | kPa | 243.15 | The inv... |
| Pvap | 92.40 | kPa | 245.14 | Experim... |
| Pvap | 101.40 | kPa | 247.14 | Experim... |
| Pvap | 106.12 | kPa | 248.08 | Saturat... |
| Pvap | 106.40 | kPa | 248.15 | The inv... |
| Pvap | 111.10 | kPa | 249.15 | Experim... |
| Pvap | 121.40 | kPa | 251.16 | Experim... |
| Pvap | 127.20 | kPa | 252.12 | PVTx pr... |
| Pvap | 133.58 | kPa | 253.13 | Measure... |
| Pvap | 133.60 | kPa | 253.13 | Measure... |
| Pvap | 133.50 | kPa | 253.15 | Isother... |
| Pvap | 132.70 | kPa | 253.15 | The inv... |
| Pvap | 131.00 | kPa | 253.15 | Vapor-L... |
| Pvap | 132.50 | kPa | 253.15 | Experim... |
| Pvap | 144.30 | kPa | 255.14 | Experim... |
| Pvap | 151.40 | kPa | 256.18 | PVTx pr... |
| Pvap | 157.10 | kPa | 257.16 | Experim... |
| Pvap | 163.90 | kPa | 258.15 | The inv... |
| Pvap | 163.90 | kPa | 258.15 | Vapor-l... |
| Pvap | 162.00 | kPa | 258.20 | Experim... |
| Pvap | 162.00 | kPa | 258.20 | Experim... |
| Pvap | 170.60 | kPa | 259.17 | Experim... |
| Pvap | 178.50 | kPa | 260.19 | PVTx pr... |
| Pvap | 185.00 | kPa | 261.16 | Experim... |
| Pvap | 193.00 | kPa | 262.20 | Experim... |
| Pvap | 193.00 | kPa | 262.20 | Experim... |
| Pvap | 200.47 | kPa | 262.99 | Measure... |
| Pvap | 200.48 | kPa | 263.00 | Measure... |
| Pvap | 199.39 | kPa | 263.01 | Saturat... |
| Pvap | 200.20 | kPa | 263.14 | Experim... |
| Pvap | 203.00 | kPa | 263.15 | Vapor-L... |
| Pvap | 202.60 | kPa | 263.15 | Experim... |
| Pvap | 200.60 | kPa | 263.15 | The inv... |
| Pvap | 200.60 | kPa | 263.15 | Vapor-l... |
| Pvap | 195.70 | kPa | 263.43 | Vapor l... |
| Pvap | 209.60 | kPa | 264.20 | PVTx pr... |
| Pvap | 216.40 | kPa | 265.13 | Experim... |
| Pvap | 233.70 | kPa | 267.13 | Experim... |
| Pvap | 243.30 | kPa | 268.15 | The inv... |
| Pvap | 245.50 | kPa | 268.15 | Experim... |
| Pvap | 243.30 | kPa | 268.15 | Vapor-l... |
| Pvap | 244.30 | kPa | 268.21 | PVTx pr... |
| Pvap | 252.10 | kPa | 269.14 | Experim... |
| Pvap | 271.60 | kPa | 271.14 | Experim... |
| Pvap | 283.00 | kPa | 272.14 | PVTx pr... |
| Pvap | 286.00 | kPa | 272.20 | Experim... |
| Pvap | 286.00 | kPa | 272.20 | Experim... |
| Pvap | 292.10 | kPa | 273.13 | Experim... |
| Pvap | 291.80 | kPa | 273.15 | Isother... |
| Pvap | 294.12 | kPa | 273.15 | Experim... |
| Pvap | 292.70 | kPa | 273.15 | The inv... |
| Pvap | 292.80 | kPa | 273.15 | Vapor-L... |
| Pvap | 294.20 | kPa | 273.15 | Measure... |
| Pvap | 294.30 | kPa | 273.17 | Experim... |
| Pvap | 295.50 | kPa | 273.31 | Measure... |
| Pvap | 295.50 | kPa | 273.31 | Measure... |
| Pvap | 287.10 | kPa | 273.32 | Vapor l... |
| Pvap | 313.90 | kPa | 275.13 | Experim... |
| Pvap | 314.60 | kPa | 275.15 | Vapor-l... |
| Pvap | 326.10 | kPa | 276.09 | PVTx pr... |
| Pvap | 337.20 | kPa | 277.16 | Experim... |
| Pvap | 339.50 | kPa | 277.22 | Vapour ... |
| Pvap | 349.60 | kPa | 278.15 | The inv... |
| Pvap | 353.00 | kPa | 278.15 | Vapor-L... |
| Pvap | 351.20 | kPa | 278.17 | Experim... |
| Pvap | 361.50 | kPa | 279.16 | Experim... |
| Pvap | 364.00 | kPa | 279.24 | Vapour ... |
| Pvap | 374.90 | kPa | 280.13 | PVTx pr... |
| Pvap | 387.30 | kPa | 281.16 | Experim... |
| Pvap | 389.70 | kPa | 281.25 | Vapour ... |
| Pvap | 404.00 | kPa | 282.55 | Bubble ... |
| Pvap | 411.00 | kPa | 282.60 | Experim... |
| Pvap | 411.00 | kPa | 282.60 | Experim... |
| Pvap | 412.95 | kPa | 283.03 | Saturat... |
| Pvap | 414.40 | kPa | 283.13 | Saturat... |
| Pvap | 415.50 | kPa | 283.15 | Vapor-l... |
| Pvap | 416.90 | kPa | 283.15 | Measure... |
| Pvap | 414.60 | kPa | 283.15 | Vapor-l... |
| Pvap | 414.00 | kPa | 283.15 | Vapor-l... |
| Pvap | 414.30 | kPa | 283.15 | The inv... |
| Pvap | 414.60 | kPa | 283.15 | Vapor-L... |
| Pvap | 416.60 | kPa | 283.15 | Experim... |
| Pvap | 416.00 | kPa | 283.15 | Vapour ... |
| Pvap | 413.80 | kPa | 283.15 | Isother... |
| Pvap | 415.40 | kPa | 283.16 | Experim... |
| Pvap | 415.71 | kPa | 283.16 | Measure... |
| Pvap | 415.71 | kPa | 283.17 | Measure... |
| Pvap | 414.30 | kPa | 283.17 | Experim... |
| Pvap | 407.20 | kPa | 283.22 | Vapor l... |
| Pvap | 416.70 | kPa | 283.24 | Vapour ... |
| Pvap | 428.70 | kPa | 284.10 | PVTx pr... |
| Pvap | 442.10 | kPa | 285.14 | Experim... |
| Pvap | 445.40 | kPa | 285.26 | Vapour ... |
| Pvap | 472.30 | kPa | 287.15 | Experim... |
| Pvap | 475.40 | kPa | 287.27 | Vapour ... |
| Pvap | 487.00 | kPa | 288.09 | PVTx pr... |
| Pvap | 488.20 | kPa | 288.15 | The inv... |
| Pvap | 488.20 | kPa | 288.16 | Experim... |
| Pvap | 488.40 | kPa | 288.17 | Isother... |
| Pvap | 483.60 | kPa | 288.30 | Vapor l... |
| Pvap | 503.40 | kPa | 289.14 | Experim... |
| Pvap | 506.90 | kPa | 289.27 | Vapour ... |
| Pvap | 536.30 | kPa | 291.14 | Experim... |
| Pvap | 539.90 | kPa | 291.29 | Vapour ... |
| Pvap | 554.10 | kPa | 292.13 | PVTx pr... |
| Pvap | 569.00 | kPa | 292.90 | Experim... |
| Pvap | 569.00 | kPa | 292.90 | Experim... |
| Pvap | 571.00 | kPa | 292.92 | Vapor-L... |
| Pvap | 571.10 | kPa | 293.14 | Saturat... |
| Pvap | 570.90 | kPa | 293.14 | Experim... |
| Pvap | 570.60 | kPa | 293.15 | Experim... |
| Pvap | 572.00 | kPa | 293.15 | Vapor-L... |
| Pvap | 571.10 | kPa | 293.15 | Experim... |
| Pvap | 570.70 | kPa | 293.15 | The inv... |
| Pvap | 571.70 | kPa | 293.15 | Vapor-l... |
| Pvap | 571.90 | kPa | 293.15 | Measure... |
| Pvap | 572.10 | kPa | 293.15 | Isother... |
| Pvap | 572.40 | kPa | 293.15 | Vapor-l... |
| Pvap | 571.50 | kPa | 293.15 | Vapor-l... |
| Pvap | 572.40 | kPa | 293.15 | Vapour ... |
| Pvap | 571.20 | kPa | 293.15 | Isother... |
| Pvap | 571.94 | kPa | 293.22 | Measure... |
| Pvap | 571.98 | kPa | 293.22 | Measure... |
| Pvap | 566.30 | kPa | 293.29 | Vapor l... |
| Pvap | 575.10 | kPa | 293.31 | Vapour ... |
| Pvap | 572.60 | kPa | 293.32 | Bubble ... |
| Pvap | 610.80 | kPa | 295.30 | Vapour ... |
| Pvap | 612.00 | kPa | 295.40 | Solubil... |
| Pvap | 630.30 | kPa | 296.32 | PVTx pr... |
| Pvap | 649.30 | kPa | 297.32 | Vapour ... |
| Pvap | 664.80 | kPa | 298.15 | Experim... |
| Pvap | 665.10 | kPa | 298.16 | Isother... |
| Pvap | 669.60 | kPa | 298.44 | Isother... |
| Pvap | 685.50 | kPa | 299.21 | Vapour ... |
| Pvap | 688.70 | kPa | 299.31 | Vapour ... |
| Pvap | 689.40 | kPa | 299.34 | Vapour ... |
| Pvap | 704.40 | kPa | 300.00 | Solubil... |
| Pvap | 707.10 | kPa | 300.17 | PVTx pr... |
| Pvap | 726.70 | kPa | 301.19 | Vapour ... |
| Pvap | 730.00 | kPa | 301.30 | Vapour ... |
| Pvap | 763.00 | kPa | 302.70 | Experim... |
| Pvap | 763.00 | kPa | 302.70 | Experim... |
| Pvap | 767.00 | kPa | 303.06 | Vapour ... |
| Pvap | 769.50 | kPa | 303.12 | Saturat... |
| Pvap | 769.20 | kPa | 303.12 | Saturat... |
| Pvap | 771.50 | kPa | 303.15 | Vapour ... |
| Pvap | 770.20 | kPa | 303.15 | Vapor-L... |
| Pvap | 768.90 | kPa | 303.15 | Vapor-l... |
| Pvap | 770.20 | kPa | 303.15 | Vapor-l... |
| Pvap | 770.40 | kPa | 303.15 | Measure... |
| Pvap | 767.00 | kPa | 303.15 | Vapor-l... |
| Pvap | 769.20 | kPa | 303.15 | Experim... |
| Pvap | 771.40 | kPa | 303.15 | Experim... |
| Pvap | 769.80 | kPa | 303.16 | Isother... |
| Pvap | 769.80 | kPa | 303.19 | Vapour ... |
| Pvap | 773.30 | kPa | 303.24 | Bubble ... |
| Pvap | 771.67 | kPa | 303.25 | Measure... |
| Pvap | 771.76 | kPa | 303.26 | Measure... |
| Pvap | 772.90 | kPa | 303.30 | P-T-x M... |
| Pvap | 773.50 | kPa | 303.31 | Vapour ... |
| Pvap | 775.70 | kPa | 303.45 | p-T-x M... |
| Pvap | 775.70 | kPa | 303.45 | Isother... |
| Pvap | 788.50 | kPa | 304.00 | Solubil... |
| Pvap | 792.40 | kPa | 304.12 | PVTx pr... |
| Pvap | 819.10 | kPa | 305.33 | Vapour ... |
| Pvap | 866.60 | kPa | 307.34 | Vapour ... |
| Pvap | 887.00 | kPa | 308.12 | PVTx pr... |
| Pvap | 886.00 | kPa | 308.15 | Experim... |
| Pvap | 885.90 | kPa | 308.15 | Isother... |
| Pvap | 892.20 | kPa | 308.44 | Isother... |
| Pvap | 892.20 | kPa | 308.44 | p-T-x M... |
| Pvap | 916.00 | kPa | 309.35 | Vapour ... |
| Pvap | 967.30 | kPa | 311.35 | Vapour ... |
| Pvap | 991.80 | kPa | 312.19 | PVTx pr... |
| Pvap | 1002.20 | kPa | 312.66 | Bubble ... |
| Pvap | 1014.90 | kPa | 313.11 | Saturat... |
| Pvap | 1015.30 | kPa | 313.15 | Isother... |
| Pvap | 1013.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 1012.80 | kPa | 313.15 | Measure... |
| Pvap | 1008.00 | kPa | 313.15 | Vapor-L... |
| Pvap | 1013.00 | kPa | 313.15 | Vapor-l... |
| Pvap | 1017.00 | kPa | 313.15 | Vapor-l... |
| Pvap | 1018.10 | kPa | 313.15 | Experim... |
| Pvap | 1017.70 | kPa | 313.15 | Experim... |
| Pvap | 1017.50 | kPa | 313.15 | Vapour ... |
| Pvap | 1018.80 | kPa | 313.15 | P-T-x M... |
| Pvap | 1013.60 | kPa | 313.15 | Vapor-L... |
| Pvap | 1015.50 | kPa | 313.15 | Vapor-l... |
| Pvap | 1018.09 | kPa | 313.18 | Measure... |
| Pvap | 1018.15 | kPa | 313.18 | Measure... |
| Pvap | 1018.80 | kPa | 313.30 | Isother... |
| Pvap | 1018.80 | kPa | 313.30 | p-T-x M... |
| Pvap | 1014.70 | kPa | 313.31 | Vapor l... |
| Pvap | 1019.30 | kPa | 313.31 | Vapour ... |
| Pvap | 1076.90 | kPa | 315.36 | Vapour ... |
| Pvap | 1103.50 | kPa | 316.20 | PVTx pr... |
| Pvap | 1133.00 | kPa | 317.32 | Vapour ... |
| Pvap | 1158.40 | kPa | 318.14 | Isother... |
| Pvap | 1158.10 | kPa | 318.15 | Experim... |
| Pvap | 1165.40 | kPa | 318.39 | p-T-x M... |
| Pvap | 1165.40 | kPa | 318.39 | Isother... |
| Pvap | 1195.50 | kPa | 319.38 | Vapour ... |
| Pvap | 1220.60 | kPa | 320.09 | PVTx pr... |
| Pvap | 1256.10 | kPa | 321.34 | Vapour ... |
| Pvap | 1304.90 | kPa | 322.82 | Bubble ... |
| Pvap | 1316.90 | kPa | 323.14 | Experim... |
| Pvap | 1316.10 | kPa | 323.15 | Isother... |
| Pvap | 1318.80 | kPa | 323.15 | Vapour ... |
| Pvap | 1317.20 | kPa | 323.15 | Vapor-l... |
| Pvap | 1314.70 | kPa | 323.15 | Vapor-l... |
| Pvap | 1318.00 | kPa | 323.15 | Vapor-l... |
| Pvap | 1308.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 1313.80 | kPa | 323.15 | Measure... |
| Pvap | 1317.40 | kPa | 323.15 | Experim... |
| Pvap | 1308.00 | kPa | 323.15 | Vapor-L... |
| Pvap | 1312.80 | kPa | 323.15 | Vapor-L... |
| Pvap | 1319.00 | kPa | 323.15 | P-T-x M... |
| Pvap | 1318.50 | kPa | 323.17 | Saturat... |
| Pvap | 1319.76 | kPa | 323.19 | Measure... |
| Pvap | 1319.87 | kPa | 323.20 | Measure... |
| Pvap | 1319.00 | kPa | 323.30 | Isother... |
| Pvap | 1319.00 | kPa | 323.30 | p-T-x M... |
| Pvap | 1487.96 | kPa | 328.05 | Saturat... |
| Pvap | 1489.60 | kPa | 328.15 | Experim... |
| Pvap | 1492.40 | kPa | 328.26 | p-T-x M... |
| Pvap | 1492.40 | kPa | 328.26 | Isother... |
| Pvap | 1532.30 | kPa | 329.37 | Vapour ... |
| Pvap | 1682.00 | kPa | 333.15 | Vapor-l... |
| Pvap | 1679.70 | kPa | 333.15 | Experim... |
| Pvap | 1671.00 | kPa | 333.15 | Vapor-L... |
| Pvap | 1673.00 | kPa | 333.15 | Vapor-L... |
| Pvap | 1681.60 | kPa | 333.15 | Vapour ... |
| Pvap | 1681.10 | kPa | 333.16 | Saturat... |
| Pvap | 1682.95 | kPa | 333.16 | Measure... |
| Pvap | 1683.15 | kPa | 333.17 | Measure... |
| Pvap | 1683.70 | kPa | 333.30 | Isother... |
| Pvap | 1683.70 | kPa | 333.30 | p-T-x M... |
| Pvap | 1680.40 | kPa | 333.32 | Vapor l... |
| Pvap | 1767.40 | kPa | 335.39 | Vapour ... |
| Pvap | 1851.90 | kPa | 337.41 | Vapour ... |
| Pvap | 1889.10 | kPa | 338.14 | Experim... |
| Pvap | 1889.60 | kPa | 338.24 | p-T-x M... |
| Pvap | 1889.60 | kPa | 338.24 | Isother... |
| Pvap | 1889.60 | kPa | 338.30 | P-T-x M... |
| Pvap | 1939.20 | kPa | 339.41 | Vapour ... |
| Pvap | 2029.50 | kPa | 341.43 | Vapour ... |
| Pvap | 2110.59 | kPa | 343.03 | Measure... |
| Pvap | 2110.88 | kPa | 343.04 | Measure... |
| Pvap | 2118.10 | kPa | 343.14 | Experim... |
| Pvap | 2117.00 | kPa | 343.15 | Vapor-l... |
| Pvap | 2106.00 | kPa | 343.15 | Vapor-L... |
| Pvap | 2114.50 | kPa | 343.15 | Vapour ... |
| Pvap | 2117.30 | kPa | 343.16 | Saturat... |
| Pvap | 2115.30 | kPa | 343.23 | Isother... |
| Pvap | 2115.30 | kPa | 343.23 | p-T-x M... |
| Pvap | 2123.00 | kPa | 343.43 | Vapour ... |
| Pvap | 2319.80 | kPa | 347.44 | Vapour ... |
| Pvap | 2361.20 | kPa | 348.13 | Experim... |
| Pvap | 2352.50 | kPa | 348.22 | Isother... |
| Pvap | 2419.40 | kPa | 349.46 | Vapour ... |
| Pvap | 2530.30 | kPa | 351.46 | Vapour ... |
| Pvap | 2620.85 | kPa | 352.93 | Saturat... |
| Pvap | 2605.90 | kPa | 353.10 | Isother... |
| Pvap | 2634.60 | kPa | 353.13 | Experim... |
| Pvap | 2629.00 | kPa | 353.15 | Vapour ... |
| Pvap | 2633.57 | kPa | 353.16 | Measure... |
| Pvap | 2633.73 | kPa | 353.16 | Measure... |
| Pvap | 2636.00 | kPa | 353.20 | Vapor l... |
| Pvap | 2605.90 | kPa | 353.45 | P-T-x M... |
| Pvap | 2641.10 | kPa | 353.48 | Vapour ... |
| Pvap | 2755.40 | kPa | 355.48 | Vapour ... |
| Pvap | 3054.30 | kPa | 360.48 | Vapour ... |
| Pvap | 3245.32 | kPa | 363.17 | Measure... |
| Pvap | 3245.53 | kPa | 363.18 | Measure... |
Datasets
- Viscosity, Pa*s (4)
- Mass density, kg/m3 (7)
- Amount density, mol/m3 (1)
- Self diffusion coefficient, m2/s (1)
- Thermal conductivity, W/m/K (1)
- Molar volume, m3/mol (1)
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Fluid (supercritical or subcritical phases) | Pressure, kPa - Fluid (supercritical or subcritical phases) | Viscosity, Pa*s - Fluid (supercritical or subcritical phases) |
| 293.15 | 10000.00 | 0.0003 |
| 293.15 | 25000.00 | 0.0003 |
| 293.15 | 50000.00 | 0.0004 |
| 293.15 | 100000.00 | 0.0005 |
| 293.15 | 150000.00 | 0.0007 |
| 293.15 | 200000.00 | 0.0008 |
| 298.15 | 10000.00 | 0.0002 |
| 298.15 | 25000.00 | 0.0003 |
| 298.15 | 50000.00 | 0.0003 |
| 298.15 | 100000.00 | 0.0005 |
| 298.15 | 150000.00 | 0.0006 |
| 298.15 | 200000.00 | 0.0008 |
| 298.15 | 250000.00 | 0.0010 |
| 313.15 | 10000.00 | 0.0002 |
| 313.15 | 25000.00 | 0.0002 |
| 313.15 | 50000.00 | 0.0003 |
| 313.15 | 100000.00 | 0.0004 |
| 313.15 | 150000.00 | 0.0006 |
| 313.15 | 200000.00 | 0.0007 |
| 313.15 | 250000.00 | 0.0009 |
| 313.15 | 300000.00 | 0.0011 |
| 313.15 | 350000.00 | 0.0013 |
| 313.15 | 400000.00 | 0.0014 |
| 323.15 | 10000.00 | 0.0002 |
| 323.15 | 25000.00 | 0.0002 |
| 323.15 | 50000.00 | 0.0003 |
| 323.15 | 100000.00 | 0.0004 |
| 323.15 | 150000.00 | 0.0005 |
| 323.15 | 200000.00 | 0.0006 |
| 323.15 | 250000.00 | 0.0008 |
| 323.15 | 300000.00 | 0.0009 |
| 348.15 | 10000.00 | 0.0001 |
| 348.15 | 25000.00 | 0.0002 |
| 348.15 | 50000.00 | 0.0002 |
| 348.15 | 100000.00 | 0.0003 |
| 348.15 | 150000.00 | 0.0004 |
| 348.15 | 200000.00 | 0.0005 |
| 348.15 | 250000.00 | 0.0006 |
| 348.15 | 300000.00 | 0.0008 |
| 348.15 | 350000.00 | 0.0009 |
| 348.15 | 400000.00 | 0.0010 |
| 373.15 | 25000.00 | 0.0002 |
| 373.15 | 50000.00 | 0.0002 |
| 373.15 | 100000.00 | 0.0003 |
| 373.15 | 150000.00 | 0.0004 |
| 373.15 | 200000.00 | 0.0005 |
| 373.15 | 250000.00 | 0.0006 |
| 373.15 | 300000.00 | 0.0006 |
| 373.15 | 350000.00 | 0.0008 |
| 373.15 | 400000.00 | 0.0009 |
| 398.15 | 50000.00 | 0.0002 |
| 398.15 | 100000.00 | 0.0003 |
| 398.15 | 150000.00 | 0.0003 |
| 438.15 | 50000.00 | 0.0001 |
| 438.15 | 100000.00 | 0.0002 |
| 438.15 | 150000.00 | 0.0003 |
| 438.15 | 200000.00 | 0.0003 |
| 438.15 | 250000.00 | 0.0004 |
| 438.15 | 300000.00 | 0.0005 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 253.14 | 1000.00 | 0.0004 |
| 253.14 | 5000.00 | 0.0004 |
| 253.14 | 10000.00 | 0.0004 |
| 253.14 | 15000.00 | 0.0004 |
| 253.14 | 20000.00 | 0.0004 |
| 253.14 | 25000.00 | 0.0005 |
| 253.14 | 30000.00 | 0.0005 |
| 273.15 | 1000.00 | 0.0003 |
| 273.15 | 5000.00 | 0.0003 |
| 273.15 | 10000.00 | 0.0003 |
| 273.15 | 15000.00 | 0.0003 |
| 273.15 | 20000.00 | 0.0003 |
| 273.15 | 25000.00 | 0.0004 |
| 273.15 | 30000.00 | 0.0004 |
| 293.15 | 1000.00 | 0.0002 |
| 293.15 | 5000.00 | 0.0002 |
| 293.15 | 10000.00 | 0.0002 |
| 293.15 | 15000.00 | 0.0003 |
| 293.15 | 20000.00 | 0.0003 |
| 293.15 | 25000.00 | 0.0003 |
| 293.15 | 30000.00 | 0.0003 |
| 313.14 | 2000.00 | 0.0002 |
| 313.14 | 5000.00 | 0.0002 |
| 313.14 | 10000.00 | 0.0002 |
| 313.14 | 15000.00 | 0.0002 |
| 313.14 | 20000.00 | 0.0002 |
| 313.14 | 25000.00 | 0.0002 |
| 313.14 | 30000.00 | 0.0003 |
| 333.16 | 2000.00 | 0.0001 |
| 333.16 | 5000.00 | 0.0001 |
| 333.16 | 10000.00 | 0.0002 |
| 333.16 | 15000.00 | 0.0002 |
| 333.16 | 20000.00 | 0.0002 |
| 333.16 | 25000.00 | 0.0002 |
| 333.16 | 30000.00 | 0.0002 |
| 353.16 | 3000.00 | 0.0001 |
| 353.16 | 5000.00 | 0.0001 |
| 353.16 | 10000.00 | 0.0001 |
| 353.16 | 15000.00 | 0.0001 |
| 353.16 | 20000.00 | 0.0002 |
| 353.16 | 25000.00 | 0.0002 |
| 353.16 | 30000.00 | 0.0002 |
| 253.16 | 3000.00 | 0.0004 |
| 253.16 | 10000.00 | 0.0004 |
| 273.15 | 3000.00 | 0.0003 |
| 273.15 | 10000.00 | 0.0003 |
| 293.15 | 3000.00 | 0.0002 |
| 293.15 | 10000.00 | 0.0002 |
| 313.14 | 3000.00 | 0.0002 |
| 313.14 | 10000.00 | 0.0002 |
| 333.16 | 3000.00 | 0.0001 |
| 333.16 | 10000.00 | 0.0002 |
| 353.15 | 5000.00 | 0.0001 |
| 353.15 | 10000.00 | 0.0001 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 313.50 | 1796.00 | 0.0002 |
| 313.01 | 1763.00 | 0.0002 |
| 312.96 | 1701.00 | 0.0002 |
| 312.83 | 1706.00 | 0.0002 |
| 312.82 | 4048.00 | 0.0002 |
| 312.76 | 4069.00 | 0.0002 |
| 312.75 | 4064.00 | 0.0002 |
| 312.77 | 3061.00 | 0.0002 |
| 312.78 | 3061.00 | 0.0002 |
| 312.78 | 3042.00 | 0.0002 |
| 332.81 | 4011.00 | 0.0001 |
| 332.81 | 4008.00 | 0.0001 |
| 332.80 | 4005.00 | 0.0001 |
| 332.80 | 3079.00 | 0.0001 |
| 332.79 | 3083.00 | 0.0001 |
| 332.79 | 3072.00 | 0.0001 |
| 354.96 | 4007.00 | 0.0001 |
| 355.51 | 4078.00 | 0.0001 |
| 355.94 | 4155.00 | 0.0001 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 258.15 | 1000.00 | 0.0003 |
| 258.15 | 5000.00 | 0.0003 |
| 258.15 | 10000.00 | 0.0004 |
| 258.15 | 15000.00 | 0.0004 |
| 258.15 | 20000.00 | 0.0004 |
| 258.15 | 25000.00 | 0.0004 |
| 258.15 | 30000.00 | 0.0005 |
| 258.15 | 35000.00 | 0.0005 |
| 258.15 | 40000.00 | 0.0005 |
| 278.14 | 1000.00 | 0.0003 |
| 278.14 | 5000.00 | 0.0003 |
| 278.14 | 10000.00 | 0.0003 |
| 278.14 | 15000.00 | 0.0003 |
| 278.14 | 20000.00 | 0.0003 |
| 278.14 | 25000.00 | 0.0003 |
| 278.14 | 30000.00 | 0.0004 |
| 278.14 | 35000.00 | 0.0004 |
| 278.14 | 40000.00 | 0.0004 |
| 298.14 | 1000.00 | 0.0002 |
| 298.14 | 5000.00 | 0.0002 |
| 298.14 | 10000.00 | 0.0002 |
| 298.14 | 15000.00 | 0.0002 |
| 298.14 | 20000.00 | 0.0003 |
| 298.14 | 25000.00 | 0.0003 |
| 298.14 | 30000.00 | 0.0003 |
| 298.14 | 35000.00 | 0.0003 |
| 298.14 | 40000.00 | 0.0003 |
| 318.13 | 2000.00 | 0.0002 |
| 318.13 | 5000.00 | 0.0002 |
| 318.13 | 10000.00 | 0.0002 |
| 318.13 | 15000.00 | 0.0002 |
| 318.13 | 20000.00 | 0.0002 |
| 318.13 | 25000.00 | 0.0002 |
| 318.13 | 30000.00 | 0.0002 |
| 318.13 | 35000.00 | 0.0003 |
| 318.13 | 40000.00 | 0.0003 |
| 338.13 | 2000.00 | 0.0001 |
| 338.13 | 5000.00 | 0.0001 |
| 338.13 | 10000.00 | 0.0001 |
| 338.13 | 15000.00 | 0.0002 |
| 338.13 | 20000.00 | 0.0002 |
| 338.13 | 25000.00 | 0.0002 |
| 338.13 | 30000.00 | 0.0002 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 303.26 | 1000.00 | 1188.74 |
| 283.52 | 1010.00 | 1262.83 |
| 323.07 | 1280.00 | 1102.44 |
| 343.05 | 2090.00 | 997.14 |
| 343.03 | 4990.00 | 1045.24 |
| 303.27 | 5000.00 | 1212.6 |
| 323.08 | 5000.00 | 1136.68 |
| 362.95 | 5000.00 | 921.91 |
| 283.53 | 5000.00 | 1279.7 |
| 283.54 | 10000.00 | 1298.2 |
| 323.08 | 10000.00 | 1170.98 |
| 343.02 | 10000.00 | 1097.0 |
| 362.95 | 10000.00 | 1012.79 |
| 303.28 | 10000.00 | 1237.15 |
| 303.29 | 19980.00 | 1275.91 |
| 283.54 | 20000.00 | 1329.16 |
| 343.02 | 20000.00 | 1162.16 |
| 362.96 | 20000.00 | 1101.23 |
| 323.09 | 20000.00 | 1220.67 |
| 343.02 | 39990.00 | 1241.93 |
| 283.54 | 39990.00 | 1376.78 |
| 362.97 | 40000.00 | 1196.59 |
| 323.12 | 40000.00 | 1287.6 |
| 303.29 | 40010.00 | 1332.33 |
| 323.11 | 60000.00 | 1335.02 |
| 362.98 | 60000.00 | 1257.2 |
| 303.30 | 60000.00 | 1374.15 |
| 343.02 | 60010.00 | 1295.73 |
| 283.54 | 60010.00 | 1413.66 |
| 303.30 | 79980.00 | 1408.2 |
| 323.11 | 80000.00 | 1372.84 |
| 362.99 | 80000.00 | 1302.95 |
| 343.03 | 80010.00 | 1337.58 |
| 283.54 | 80020.00 | 1444.29 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.26 | 1000.00 | 1265.88 |
| 283.26 | 5000.00 | 1282.35 |
| 283.26 | 10000.00 | 1300.86 |
| 283.26 | 20000.00 | 1331.64 |
| 283.26 | 40000.00 | 1379.61 |
| 283.25 | 60000.00 | 1416.44 |
| 283.26 | 80000.00 | 1446.35 |
| 302.85 | 1000.00 | 1190.34 |
| 302.85 | 5000.00 | 1214.03 |
| 302.85 | 10000.00 | 1238.45 |
| 302.84 | 20000.00 | 1276.99 |
| 302.84 | 40000.00 | 1333.11 |
| 302.85 | 60000.00 | 1374.79 |
| 302.84 | 80000.00 | 1408.64 |
| 322.62 | 5000.00 | 1140.59 |
| 322.63 | 10000.00 | 1174.6 |
| 322.63 | 20000.00 | 1224.02 |
| 322.64 | 40000.00 | 1290.68 |
| 322.64 | 60000.00 | 1338.04 |
| 322.64 | 80000.00 | 1375.39 |
| 342.56 | 5000.00 | 1047.23 |
| 342.56 | 10000.00 | 1098.48 |
| 342.56 | 20000.00 | 1163.35 |
| 342.56 | 40000.00 | 1242.84 |
| 342.57 | 60000.00 | 1296.48 |
| 342.57 | 80000.00 | 1337.6 |
| 362.57 | 5000.00 | 924.58 |
| 362.58 | 10000.00 | 1014.86 |
| 362.58 | 20000.00 | 1102.88 |
| 362.58 | 40000.00 | 1197.86 |
| 362.58 | 60000.00 | 1258.31 |
| 362.58 | 80000.00 | 1303.78 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 303.27 | 1010.00 | 1188.92 |
| 303.27 | 5010.00 | 1212.9 |
| 303.26 | 10020.00 | 1237.53 |
| 303.26 | 20020.00 | 1276.18 |
| 303.27 | 40000.00 | 1332.27 |
| 303.27 | 59990.00 | 1374.03 |
| 303.29 | 79930.00 | 1408.19 |
| 322.47 | 5000.00 | 1139.41 |
| 322.48 | 10000.00 | 1173.46 |
| 322.48 | 19990.00 | 1222.36 |
| 322.48 | 40000.00 | 1289.13 |
| 322.48 | 60010.00 | 1336.26 |
| 322.48 | 80000.00 | 1373.47 |
| 342.86 | 5010.00 | 1045.93 |
| 342.87 | 10010.00 | 1097.7 |
| 342.88 | 20010.00 | 1162.75 |
| 342.89 | 40000.00 | 1242.46 |
| 342.89 | 60010.00 | 1296.15 |
| 342.89 | 80000.00 | 1337.87 |
| 362.81 | 5000.00 | 921.95 |
| 362.82 | 10010.00 | 1013.37 |
| 362.83 | 20010.00 | 1101.82 |
| 362.83 | 40010.00 | 1197.04 |
| 362.84 | 60000.00 | 1257.56 |
| 362.84 | 79990.00 | 1303.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.61 | 1000.00 | 1262.74 |
| 283.61 | 5000.00 | 1279.71 |
| 283.61 | 10000.00 | 1298.25 |
| 283.61 | 20000.00 | 1329.21 |
| 283.59 | 40000.00 | 1376.92 |
| 283.59 | 60000.00 | 1413.86 |
| 283.60 | 80000.00 | 1444.35 |
| 303.46 | 1000.00 | 1188.35 |
| 303.46 | 5000.00 | 1212.37 |
| 303.46 | 10000.00 | 1237.01 |
| 303.46 | 20000.00 | 1275.97 |
| 303.46 | 40000.00 | 1332.37 |
| 303.47 | 60000.00 | 1374.37 |
| 303.47 | 80000.00 | 1408.33 |
| 323.24 | 3000.00 | 1119.53 |
| 323.24 | 5000.00 | 1136.67 |
| 323.24 | 10000.00 | 1171.08 |
| 323.24 | 20000.00 | 1220.9 |
| 323.24 | 40000.00 | 1287.9 |
| 323.24 | 60000.00 | 1335.45 |
| 323.25 | 80000.00 | 1373.28 |
| 343.03 | 3000.00 | 1015.76 |
| 343.01 | 5000.00 | 1046.15 |
| 343.02 | 10000.00 | 1098.02 |
| 343.02 | 20000.00 | 1163.58 |
| 343.03 | 40000.00 | 1243.36 |
| 343.03 | 60000.00 | 1297.19 |
| 343.03 | 80000.00 | 1338.42 |
| 362.73 | 5000.00 | 923.63 |
| 362.75 | 10000.00 | 1014.58 |
| 362.75 | 20000.00 | 1102.91 |
| 362.75 | 40000.00 | 1198.13 |
| 362.74 | 60000.00 | 1258.69 |
| 362.74 | 80000.00 | 1304.07 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.46 | 1000.00 | 1262.57 |
| 283.46 | 5000.00 | 1279.58 |
| 283.47 | 10000.00 | 1298.12 |
| 283.47 | 20000.00 | 1329.18 |
| 283.47 | 40000.00 | 1377.11 |
| 283.47 | 60000.00 | 1414.44 |
| 283.47 | 80000.00 | 1445.46 |
| 303.38 | 1000.00 | 1188.07 |
| 303.38 | 5000.00 | 1212.13 |
| 303.37 | 10000.00 | 1236.85 |
| 303.37 | 20000.00 | 1275.77 |
| 303.38 | 40000.00 | 1332.36 |
| 303.38 | 60000.00 | 1374.64 |
| 303.38 | 80000.00 | 1408.98 |
| 323.15 | 3000.00 | 1119.19 |
| 323.16 | 5000.00 | 1136.38 |
| 323.16 | 10000.00 | 1170.84 |
| 323.16 | 20000.00 | 1220.65 |
| 323.16 | 40000.00 | 1287.71 |
| 323.16 | 60000.00 | 1335.49 |
| 323.16 | 80000.00 | 1373.39 |
| 342.97 | 3000.00 | 1014.76 |
| 342.97 | 5000.00 | 1045.25 |
| 342.98 | 10000.00 | 1097.42 |
| 342.98 | 20000.00 | 1162.91 |
| 342.98 | 40000.00 | 1242.75 |
| 342.99 | 60000.00 | 1296.65 |
| 342.98 | 80000.00 | 1338.34 |
| 362.68 | 5000.00 | 922.4 |
| 362.68 | 10000.00 | 1013.83 |
| 362.68 | 20000.00 | 1102.6 |
| 362.68 | 40000.00 | 1197.86 |
| 362.68 | 60000.00 | 1258.47 |
| 362.68 | 80000.00 | 1304.15 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.57 | 5000.00 | 1279.4 |
| 283.57 | 10000.00 | 1297.9 |
| 283.56 | 20000.00 | 1328.7 |
| 283.55 | 40000.00 | 1376.3 |
| 283.55 | 60000.00 | 1413.1 |
| 283.55 | 80000.00 | 1443.2 |
| 303.39 | 1000.00 | 1188.5 |
| 303.39 | 5000.00 | 1212.5 |
| 303.39 | 10000.00 | 1237.0 |
| 303.39 | 20000.00 | 1275.9 |
| 303.39 | 40000.00 | 1332.1 |
| 303.40 | 60000.00 | 1373.9 |
| 303.39 | 80000.00 | 1407.4 |
| 322.89 | 3000.00 | 1120.9 |
| 322.91 | 5000.00 | 1137.8 |
| 322.91 | 10000.00 | 1172.0 |
| 322.93 | 20000.00 | 1221.5 |
| 322.93 | 40000.00 | 1288.4 |
| 322.93 | 60000.00 | 1335.8 |
| 322.94 | 80000.00 | 1372.8 |
| 342.75 | 3000.00 | 1017.4 |
| 342.75 | 5000.00 | 1047.5 |
| 342.76 | 10000.00 | 1098.8 |
| 342.77 | 20000.00 | 1164.1 |
| 342.77 | 40000.00 | 1243.6 |
| 342.78 | 60000.00 | 1297.3 |
| 342.78 | 80000.00 | 1338.2 |
| 362.57 | 5000.00 | 924.9 |
| 362.57 | 10000.00 | 1015.4 |
| 362.58 | 20000.00 | 1103.4 |
| 362.59 | 40000.00 | 1198.4 |
| 362.59 | 60000.00 | 1258.8 |
| 362.59 | 80000.00 | 1303.8 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 5000.00 | 308.00 | 1150.0 |
| 10100.00 | 308.00 | 1180.0 |
| 15400.00 | 308.00 | 1210.0 |
| 19600.00 | 288.00 | 1290.0 |
| 19600.00 | 298.00 | 1270.0 |
| 19600.00 | 308.00 | 1240.0 |
| 19600.00 | 318.00 | 1210.0 |
| 19600.00 | 328.00 | 1180.0 |
| 19600.00 | 308.00 | 1240.0 |
| 23700.00 | 308.00 | 1260.0 |
| Reference | ||
Amount density, mol/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Amount density, mol/m3 - Gas |
| 353.17 | 1761.50 | 776.7 |
| 353.17 | 1359.70 | 555.7 |
| 353.17 | 1026.00 | 397.6 |
| 353.17 | 762.10 | 284.5 |
| 353.17 | 559.90 | 203.6 |
| 353.17 | 408.20 | 145.7 |
| 353.17 | 296.00 | 104.2 |
| 353.17 | 213.80 | 74.57 |
| 413.17 | 2606.80 | 918.8 |
| 413.17 | 1968.80 | 657.4 |
| 413.17 | 1464.60 | 470.4 |
| 413.17 | 1077.60 | 336.6 |
| 413.17 | 786.70 | 240.8 |
| 413.17 | 571.00 | 172.3 |
| 413.17 | 412.80 | 123.3 |
| 413.17 | 297.50 | 88.22 |
| 413.17 | 214.00 | 63.12 |
| Reference | ||
Self diffusion coefficient, m2/s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Self diffusion coefficient, m2/s - Liquid |
| 670.00 | 298.15 | 0.0000 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Fluid (supercritical or subcritical phases) | Pressure, kPa - Fluid (supercritical or subcritical phases) | Thermal conductivity, W/m/K - Fluid (supercritical or subcritical phases) |
| 299.29 | 170.00 | 0.0129 |
| 299.63 | 170.00 | 0.0128 |
| 318.97 | 740.00 | 0.0149 |
| 318.97 | 740.00 | 0.0149 |
| 319.14 | 160.00 | 0.0146 |
| 345.58 | 180.00 | 0.0171 |
| 346.36 | 180.00 | 0.0174 |
| 348.54 | 180.00 | 0.0173 |
| 351.84 | 640.00 | 0.0176 |
| 363.88 | 180.00 | 0.0189 |
| 365.00 | 180.00 | 0.0189 |
| 365.41 | 180.00 | 0.0189 |
| 365.69 | 180.00 | 0.0189 |
| 366.52 | 180.00 | 0.0189 |
| 366.80 | 180.00 | 0.0189 |
| 372.42 | 680.00 | 0.0198 |
| 372.43 | 170.00 | 0.0197 |
| 372.43 | 680.00 | 0.0197 |
| 378.07 | 180.00 | 0.0200 |
| 378.63 | 440.00 | 0.0202 |
| 378.74 | 180.00 | 0.0201 |
| 378.90 | 330.00 | 0.0203 |
| 379.17 | 300.00 | 0.0202 |
| 379.43 | 150.00 | 0.0204 |
| 379.72 | 160.00 | 0.0200 |
| 392.65 | 180.00 | 0.0214 |
| 426.86 | 160.00 | 0.0247 |
| 436.44 | 180.00 | 0.0254 |
| 446.25 | 200.00 | 0.0267 |
| 446.25 | 760.00 | 0.0266 |
| 451.17 | 180.00 | 0.0268 |
| 455.69 | 100.00 | 0.0268 |
| 455.92 | 680.00 | 0.0272 |
| 466.31 | 650.00 | 0.0285 |
| 476.24 | 100.00 | 0.0292 |
| 496.18 | 100.00 | 0.0311 |
| 515.97 | 100.00 | 0.0330 |
| Reference | ||
Molar volume, m3/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Molar volume, m3/mol - Gas |
| 253.09 | 107.60 | 0.0187 |
| 272.92 | 158.90 | 0.0136 |
| 282.69 | 329.10 | 0.0065 |
| 282.80 | 121.40 | 0.0188 |
| 292.87 | 171.90 | 0.0136 |
| 292.89 | 126.20 | 0.0188 |
| 302.58 | 357.70 | 0.0065 |
| 313.10 | 135.40 | 0.0188 |
| 313.10 | 184.90 | 0.0136 |
| 323.07 | 386.50 | 0.0065 |
| 333.03 | 144.30 | 0.0188 |
| 333.03 | 1610.80 | 0.0012 |
| 333.05 | 197.50 | 0.0136 |
| 342.96 | 413.70 | 0.0065 |
| 343.00 | 1706.90 | 0.0012 |
| 352.93 | 153.20 | 0.0188 |
| 352.94 | 1798.60 | 0.0012 |
| 353.04 | 210.00 | 0.0136 |
| 362.89 | 440.70 | 0.0065 |
| 362.90 | 1888.60 | 0.0012 |
| 372.82 | 454.00 | 0.0065 |
| 372.84 | 162.10 | 0.0188 |
| 372.87 | 1976.60 | 0.0013 |
| 372.99 | 222.40 | 0.0136 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.69; 3482.14] | kPa | [172.00; 374.21] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.41969e+01 | |||
| Coefficient B | -2.08778e+03 | |||
| Coefficient C | -2.86360e+01 | |||
| Temperature range, min. | 172.00 | |||
| Temperature range, max. | 374.21 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 250 300 350 | ||||
| Pvap | 0.69 | kPa | 172.00 | Calculated Property |
| Pvap | 4.99 | kPa | 194.47 | Calculated Property |
| Pvap | 22.41 | kPa | 216.94 | Calculated Property |
| Pvap | 73.06 | kPa | 239.40 | Calculated Property |
| Pvap | 189.71 | kPa | 261.87 | Calculated Property |
| Pvap | 416.55 | kPa | 284.34 | Calculated Property |
| Pvap | 805.52 | kPa | 306.81 | Calculated Property |
| Pvap | 1411.49 | kPa | 329.27 | Calculated Property |
| Pvap | 2287.69 | kPa | 351.74 | Calculated Property |
| Pvap | 3482.14 | kPa | 374.21 | Calculated Property |
| Pvap | [0.72; 4272.46] | kPa | [172.15; 380.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.84910e+01 | |||
| Coefficient B | -3.73115e+03 | |||
| Coefficient C | -5.32695e+00 | |||
| Coefficient D | 9.21593e-06 | |||
| Temperature range, min. | 172.15 | |||
| Temperature range, max. | 380.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 250 300 350 | ||||
| Pvap | 0.72 | kPa | 172.15 | Calculated Property |
| Pvap | 5.14 | kPa | 195.24 | Calculated Property |
| Pvap | 23.34 | kPa | 218.34 | Calculated Property |
| Pvap | 77.26 | kPa | 241.43 | Calculated Property |
| Pvap | 203.87 | kPa | 264.53 | Calculated Property |
| Pvap | 455.62 | kPa | 287.62 | Calculated Property |
| Pvap | 899.45 | kPa | 310.72 | Calculated Property |
| Pvap | 1616.20 | kPa | 333.81 | Calculated Property |
| Pvap | 2702.02 | kPa | 356.91 | Calculated Property |
| Pvap | 4272.46 | kPa | 380.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Norflurane.
Mixtures
- Norflurane + Dimethyl ether
- Propane + Norflurane
- 2,5,8,11-Tetraoxadodecane + Norflurane
- Difluoromethane + Norflurane
- Cyclopropane + Norflurane
- Ethane, hexafluoro- + Norflurane
- Ethane, 1,2-dimethoxy- + Norflurane
- 3,3,3-Trifluoropropene + Norflurane
- Ammonia + Norflurane
- Norflurane + Propane, 1,1,1,3,3-pentafluoro
- N,N-Dimethylacetamide + Norflurane
- 2-Pyrrolidinone, 1-methyl- + Norflurane
- Butane + Norflurane
- CF3OCH3 + Norflurane
- Squalane + Norflurane
- Norflurane + Perfluoropropane + Isobutane
- Ethane, pentafluoro- + Butane + Norflurane
- Ethane, fluoro- + Norflurane
- Proline + Norflurane
- Formamide, N,N-dimethyl- + Norflurane
Find more mixtures with Norflurane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- High-Pressure Viscosity Measurements of 1,1,1,2-Tetrafluoroethane
- Thermophysical Properties of the Refrigerant Mixtures R417A and R417B from Dynamic Light Scattering (DLS)
- Vapour liquid equilibrium data for the 1,1,1,2 tetrafluoroethane (R134a) + dimethyl ether (DME) system at temperatures from 293.18 to 358.15K and pressures up to about 3 MPa up to about 3MPa
- Viscosity measurements and correlations of binary mixtures: 1,1,1,2-tetrafluoroethane (HFC-134a) + tetraethylene glycol dimethylether (TEGDME)
- Solubility and diffusivity of 1,1,1,2-tetrafluoroethane in room-temperature ionic liquids
- Measurement of vapor liquid equilibria for the binary systems of propane + 1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane + propane at various temperatures
- Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
- High-pressure viscosity behavior of x 1,1,1,2-tetrafluoroethane (HFC-134a) + (1-x) triethylene glycol dimethylether (TriEGDME) mixtures: Measurements and modeling
- Vapor liquid equilibria and critical loci of binary and ternary systems composed of CH2F2, C2HF5 and C2H2F4
- Vapor-liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K
- Isothermal vapour + liquid equilibrium measurements and correlation for the pentafluoroethane + cyclopropane and the cyclopropane + 1,1,1,2-tetrafluoroethane binary systems
- Vapor liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa
- Vapour liquid equilibria of the system 1,1,1,2-tetrafluoroethane + monoethylene-glycol dimethylether from 283.15 to 353.15 K: New modified UNIFAC parameters
- Phase equilibria of imidazolium ionic liquids and the refrigerant gas, 1,1,1,2-tetrafluoroethane (R-134a)
- Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-134a
- Vapor-liquid equilibria for the 1,1,1,2 -tetrafluoroethane (HFC-134a) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) and 1,1,1-trifluoroethane (HFC-143a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) systems
- An experimental study of PVTx properties in the gas phase for binary mixtures of HFO-1234yf and HFC-134a
- Gaseous absorption of fluorinated ethanes by ionic liquids
- Surface tension and liquid viscosity measurement for binary mixtures of R134a with R1234yf and R1234ze(E)
- Vapor-liquid equilibria measurements of 1,1,1,2-tetrafluoroethane (HFC-134a) + 2,3,3,3-tetrafluoroprop-1-ene (HFO-1234yf) + isobutane (HC-600a) ternary system
- Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
- Viscosity and self-diffusivity of ionic liquids with compressed hydrofluorocarbons: 1-hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)amide and 1,1,1,2- tetrafluoroethane.
- Solubility of cinnamic acid in supercritical carbon dioxide and subcritical 1,1,1,2-tetrafluoroethane: Experimental data and modelling
- Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system
- Bubble pressure measurements for the (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system
- Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
- Density measurements for 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
- Viscosity measurements for 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
- Liquid density of HFE-7200 and HFE-7500 from T = (283 to 363) K at pressures up to 100 MPa
- PVTx properties in the gas phase for binary R290/R134a system
- Liquid density of HFE-7000 and HFE-7100 from T = (283 to 363) K at pressures up to 100 MPa
- Gaseous pVTx measurements for (HFC134a + HC290) by a compact single-sinker densimeter
- (Vapour + liquid + liquid) equilibrium measurements and correlation for the {1,1,1,2-tetrafluoroethane (R134a) + n-butane (R600)} system
- Volumetric properties of binary mixtures of {difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))} at temperatures from 283.15 K to 363.15 K and pressures up to 100 MPa
- The investigation on the vapour liquid phase equilibrium of (ammonia + 1,1,1,2-tetrafluoroethane) system over the temperatures ranging from (243.150 to 283.150) K
- Measurements of isothermal vapor-liquid equilibrium for 2,3,3,3-tetrafluoroprop-1-ene + 1,1,1,2-tetrafluoroethane + propane system at temperatures from 283.15 to 323.15 K
- Thermal conductivity data for refrigerant mixtures containing R1234yf and R1234ze(E)
- P.rho.Tx properties of binary R134a/R245fa system
- Experimental measurements and correlation of isothermal vapor-liquid equilibria for HFC-32 + HFO-1234ze (E) and HFC-134a + HFO-1234ze (E) binary systems
- Solubilities of hydroxybenzaldehyde isomers and their mixture in subcritical 1,1,1,2-tetrafluoroethane
- Liquid Density of 2 Methoxyethyl Acetate, 2 Ethylhexyl Acetate and Diethyl Succinate at Temperatures from 283.15 K to 363.15 K and Pressures up to 100 MPa
- Experimental Clathrate Hydrate Dissociation Data for Systems Comprising Refrigerant + CaCl2 Aqueous Solutions
- P-T-x Measurements for 1,1,1,2-Tetrafluoroethane (R134a) + N,N dimethylacetamide (DMA), and N-methyl-2-pyrrolidone (NMP)
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + Dimethyl Ether Triethylene Glycol, 1,1-Difluoroethane + Dimethyl Ether Triethylene Glycol, and 1,1-Difluoroethane + N-Methyl-2-pyrrolidone Systems
- Experimental Study of PVTx Properties in the Gas Phase for Binary Mixtures of DME and HFC-134a
- Gaseous PVT Property Measurements of cis-1,3,3,3-Tetrafluoropropene
- Measurement and Correlation of Vapor-Liquid Equilibrium for R124 (1-Chloro-1,2,2,2-Tetrafluoroethane)-NMP (N-Methyl-2-Pyrrolidone) and R124-DMF (N,N-Dimethylformamide) Mixtures
- Measurement of Viscosity of cis-1,1,1,4,4,4-Hexafluoro-2-butene (R-1336mzz(Z)) by Tandem Capillary Tubes Method
- Liquid Density of n-Pentene, n-Hexene, and n-Heptene at Temperatures from 283.15 to 363.15 K and Pressures up to 100 MPa
- Measurement and Correlation of the Solubilities of Azoxystrobin, Flutriafol, and Tebuconazole in Subcritical 1,1,1,2-Tetrafluoroethane
- Critical Parameters and Vapor Pressures Measurements of Hydrofluoroethers at High Temperatures
- Surface Tension Measurements of Difluoromethane(R-32) and the Binary Mixture Difluoromethane(R-32) + 1,1,1,2-tetrafluoroethane(R-134a) from (253 to 333) K
- Surface Tension for the 1,1,1-Trifluoroethane (R-143a) + 1,1,1,2-Tetrafluoroethane (R-134a) System
- Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus
- Vapor-Liquid Equilibria of the Binary n-Butane (HC-600) + Difluoromethane (HFC-32), + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a) Mixture Systems
- Critical Parameters Measurements of Four HFE + HFC Binary Systems: Pentafluoromethoxyethane (HFE-245Mc) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
- Critical Properties of Four HFE + HFC Binary Systems: Trifluoromethoxymethane (HFE-143m) + Pentafluoroethane (HFC-125), + 1,1,1,2-Tetrafluoroethane (HFC-134a), + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea), and + 1,1,1,2,3,3-Hexafluoropropane (HFC-236ea)
- P-rho-T-x Measurements for (1,1,1,2-Tetrafluoroethane + Triethylene Glycol Dimethyl Ether) at High Haloalkane Content
- Vapor-Liquid Equilibria of the Difluoromethane + Dimethyl Ether and 1,1,1,2-Tetrafluoroethane + Dimethyl Ether Systems
- Acoustic Determination of Thermophysical Properties and Critical Parameters for R404A and Critical Line of xCO2 + (1 - x)R404A
- Solubility and Phase Behaviors of AOT Analogue Surfactants in 1,1,1,2-Tetrafluoroethane and Supercritical Carbon Dioxide
- Vapor-Liquid Equilibria for the Trifluoromethane + 1,1,1,2-Tetrafluoroethane System
- Vapor-Liquid-Liquid Equilibria of Hydrofluorocarbons + 1-Butyl-3-methylimidazolium Hexafluorophosphate
- Solubility Measurements of 1,1,1,2-Tetrafluoroethane (R134a) and of Propane in Squalane at Temperatures from (325 to 400) K and Pressures from (0.1 to 1) MPa
- P-V-T Behavior of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf) in the Vapor Phase from (243 to 373) K
- Solubility of Refrigerant 1,1,1,2-Tetrafluoroethane in the N,N-Dimethyl Formamide in the Temperature Range from (263.15 to 363.15) K
- Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf) for Reduced Temperatures Ranging from 0.67 to 0.93
- Compressed Liquid Viscosity of 1,1,1,3,3-Pentafluoropropane (R245fa) and 1,1,1,3,3,3-Hexafluoropropane (R236fa)
- Isochoric PVTx Measurements for the Carbon Dioxide + 1,1,1,2-Tetrafluoroethane Binary System
- Experimental Study of p-.rho.-T Relationship of Compressed Liquid Phase for Octafluoropropane and Two near Azeotropic Ternary HFC/HC Mixtures
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of Fluoroethane + N,N-Dimethylacetamide, Fluoroethane + N-Methyl-2-pyrrolidone, and 1,1,1,2-Tetrafluoroethane + N,N-Dimethylacetamide Systems
- Experimental Measurements and Thermodynamic Modeling of the Dissociation Conditions of Clathrate Hydrates for (Refrigerant + NaCl + Water) Systems
- Investigation on liquid density data at the bubble point and equations for the refrigerant HFC-404A over a wide temperature range
- Liquid Viscosity and Surface Tension of R1234yf and R1234ze Under Saturation Conditions by Surface Light Scattering
- Solubility of 4-Aminosalicylic Acid in Supercritical Carbon Dioxide and Subcritical 1,1,1,2-Tetrafluoroethane
- Isothermal Vapor-liquid Equilibrium of the ternary mixture of 1,1,1,2-tetrafluoroethane + 2,3,3,3-tetrafluoroprop-1- ene + dimethylether at temperatures from 253.15 to 323.15 K
- Vapor-Liquid Equilibria for the 1,1,1,2-Tetrafluoroethane (HFC-134a) + n-Butane (R-600) System
- Solubility Differences of Halocarbon Isomers in Ionic Liquid [emim][Tf2N]
- Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
- Solubilities of L-Proline in Subcritical HFC-134a and Supercritical CO2 Fluids
- Solubility of HFC134a (1,1,1,2-Tetrafluoroethane) in Two Dialkyl Carbonates
- Measurements of the Thermal Conductivity of HFC-134a in the Supercritical Region
- Saturated Pressure Measurements of 2,3,3,3-Tetrafluoroprop-1-ene (HFO-1234yf)
- Isothermal Vapor-Liquid Equilibrium Data of 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylformamide (DMF) Working Fluids for an Absorption Heat Transformer
- Kinematic Viscosity of R410A and R407C Refrigerant-Oil Mixtures in the Saturated Liquid Phase with Lubricant Mass Fraction in the Range of (0 to 0.0001)
- p-T-x Measurements for Some Working Fluids for an Absorption Heat Transformer: 1,1,1,2-Tetrafluoroethane (R134a) + Dimethylether Diethylene Glycol (DMEDEG) and Dimethylether Triethylene Glycol (DMETrEG)
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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