- InChI
- InChI=1S/C2H5F/c1-2-3/h2H2,1H3
- InChI Key
- UHCBBWUQDAVSMS-UHFFFAOYSA-N
- Formula
- C2H5F
- SMILES
- CCF
- Molecular Weight1
- 48.06
- CAS
- 353-36-6
- Other Names
-
- C2H5F
- Monofluoroethane
- R 161
- REFRIGERANT-161
- UN 2453
- ethyl fluoride
- fluoroethane
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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).
- ρg : Gas Density (kg/m3).
- ρl : Liquid Density (kg/m3).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 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 |
|---|---|---|---|
| ω | 0.2150 | KDB | |
| PAff | 683.40 | kJ/mol | NIST |
| BasG | 655.80 | kJ/mol | NIST |
| μ | 2.00 | debye | KDB |
| ΔfG° | -209.70 | kJ/mol | KDB |
| ΔfH°gas | -261.70 | kJ/mol | KDB |
| ΔfusH° | 4.02 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 15.24 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [11.78; 12.43] | eV |
|
| IE | 11.78 | eV | NIST |
| IE | 12.40 | eV | NIST |
| IE | 12.43 | eV | NIST |
| IE | 12.43 | eV | NIST |
| IE | 12.43 | eV | NIST |
| log10WS | -0.21 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.976 | Crippen Calculated Property | |
| McVol | 40.810 | ml/mol | McGowan Calculated Property |
| Pc | [5027.75; 5028.00] | kPa |
|
| Pc | 5028.00 | kPa | KDB |
| Pc | 5027.75 ± 5.06 | kPa | NIST |
| Pc | 5027.75 ± 5.06 | kPa | NIST |
| Tboil | [235.45; 303.90] | K |
|
| Tboil | 235.50 | K | KDB |
| Tboil | 236.00 | K | NIST |
| Tboil | 235.50 | K | NIST |
| Tboil | 303.90 ± 1.50 | K | NIST |
| Tboil | 235.45 ± 1.00 | K | NIST |
| Tc | [375.31; 375.31] | K |
|
| Tc | 375.31 | K | KDB |
| Tc | 375.31 ± 0.02 | K | NIST |
| Tc | 375.31 ± 0.02 | K | NIST |
| Tfus | 129.90 | K | KDB |
| Vc | 0.169 | m3/kmol | KDB |
| Zc | 0.2723050 | KDB |
Temperature Dependent Properties
Datasets
- Molar heat capacity at constant pressure, J/K/mol (2)
- Viscosity, Pa*s (1)
- Mass density, kg/m3 (2)
- Mass density, kg/m3 (1)
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 303.42 | 1340.00 | 107.27 |
| 303.47 | 1930.00 | 106.74 |
| 303.50 | 2520.00 | 106.24 |
| 303.53 | 3000.00 | 106.02 |
| 303.55 | 3510.00 | 105.63 |
| 303.57 | 4010.00 | 105.42 |
| 303.55 | 4550.00 | 104.88 |
| 303.52 | 5200.00 | 103.84 |
| 303.53 | 5540.00 | 103.57 |
| 303.53 | 5980.00 | 103.24 |
| 303.48 | 6470.00 | 102.68 |
| 303.51 | 7100.00 | 102.32 |
| 303.53 | 7520.00 | 102.26 |
| 303.50 | 8030.00 | 101.83 |
| 303.52 | 8440.00 | 101.93 |
| 303.53 | 9130.00 | 101.37 |
| 303.49 | 9530.00 | 100.86 |
| 303.50 | 10100.00 | 100.80 |
| 303.52 | 10520.00 | 100.64 |
| 303.51 | 11050.00 | 100.20 |
| 303.52 | 11560.00 | 100.42 |
| 303.54 | 12050.00 | 100.01 |
| 313.41 | 1510.00 | 112.39 |
| 313.31 | 2010.00 | 110.61 |
| 313.35 | 2560.00 | 110.04 |
| 313.33 | 3080.00 | 109.26 |
| 313.35 | 3500.00 | 108.56 |
| 313.36 | 4000.00 | 108.09 |
| 313.37 | 4510.00 | 107.49 |
| 313.39 | 5070.00 | 107.08 |
| 313.42 | 5490.00 | 106.99 |
| 313.41 | 6080.00 | 106.37 |
| 313.43 | 6510.00 | 106.03 |
| 313.37 | 7030.00 | 104.99 |
| 313.39 | 7490.00 | 104.67 |
| 313.42 | 7980.00 | 104.69 |
| 313.38 | 8490.00 | 103.71 |
| 313.40 | 9090.00 | 103.61 |
| 313.38 | 9510.00 | 102.92 |
| 313.40 | 10010.00 | 102.80 |
| 313.42 | 10490.00 | 102.75 |
| 313.43 | 10980.00 | 102.52 |
| 313.47 | 11470.00 | 102.55 |
| 324.11 | 2050.00 | 115.84 |
| 324.13 | 2570.00 | 114.70 |
| 324.15 | 3000.00 | 113.84 |
| 324.18 | 3500.00 | 113.06 |
| 324.16 | 4060.00 | 111.82 |
| 324.18 | 4510.00 | 111.09 |
| 324.21 | 5030.00 | 110.51 |
| 324.17 | 5510.00 | 109.38 |
| 324.14 | 5980.00 | 108.60 |
| 324.16 | 6470.00 | 107.92 |
| 324.19 | 7020.00 | 107.27 |
| 324.16 | 7520.00 | 106.39 |
| 324.13 | 8110.00 | 105.47 |
| 324.15 | 8550.00 | 105.20 |
| 324.19 | 9040.00 | 104.90 |
| 324.21 | 9450.00 | 104.56 |
| 324.17 | 10040.00 | 103.35 |
| 324.19 | 10510.00 | 103.17 |
| 324.19 | 11010.00 | 102.91 |
| 324.21 | 11610.00 | 102.46 |
| 324.22 | 12030.00 | 102.24 |
| 333.86 | 2520.00 | 124.88 |
| 333.92 | 3010.00 | 123.20 |
| 333.99 | 3510.00 | 121.92 |
| 334.00 | 4070.00 | 120.01 |
| 333.99 | 4620.00 | 118.27 |
| 333.97 | 5000.00 | 117.16 |
| 333.97 | 5500.00 | 115.91 |
| 333.98 | 5990.00 | 114.80 |
| 334.00 | 6530.00 | 113.92 |
| 334.02 | 7050.00 | 112.82 |
| 334.05 | 7490.00 | 112.09 |
| 334.05 | 8350.00 | 110.82 |
| 334.03 | 8960.00 | 109.42 |
| 333.99 | 9500.00 | 108.39 |
| 334.01 | 10060.00 | 108.00 |
| 334.03 | 10520.00 | 107.40 |
| 334.03 | 11040.00 | 107.08 |
| 334.05 | 11630.00 | 106.69 |
| 334.07 | 12280.00 | 106.31 |
| 343.40 | 2840.00 | 135.92 |
| 343.44 | 3020.00 | 134.94 |
| 343.77 | 3540.00 | 133.68 |
| 343.84 | 4040.00 | 131.08 |
| 343.88 | 4520.00 | 129.17 |
| 343.93 | 5100.00 | 126.98 |
| 343.91 | 5560.00 | 124.90 |
| 343.89 | 5970.00 | 123.05 |
| 343.90 | 6530.00 | 121.47 |
| 343.90 | 7040.00 | 120.17 |
| 343.90 | 7540.00 | 118.86 |
| 343.91 | 8070.00 | 117.76 |
| 343.91 | 8530.00 | 116.74 |
| 343.92 | 9010.00 | 115.78 |
| 343.92 | 9480.00 | 114.80 |
| 343.92 | 10010.00 | 113.86 |
| 343.92 | 10500.00 | 112.99 |
| 343.93 | 11010.00 | 112.27 |
| 343.96 | 11570.00 | 111.80 |
| 343.99 | 12130.00 | 111.22 |
| 353.68 | 3480.00 | 157.19 |
| 353.82 | 4030.00 | 149.07 |
| 353.86 | 4500.00 | 143.57 |
| 353.85 | 5030.00 | 138.32 |
| 353.82 | 5500.00 | 134.57 |
| 353.81 | 6000.00 | 131.53 |
| 353.79 | 6470.00 | 128.91 |
| 353.81 | 7130.00 | 126.37 |
| 353.80 | 7530.00 | 124.70 |
| 353.78 | 7950.00 | 123.23 |
| 353.77 | 8480.00 | 121.76 |
| 353.79 | 9090.00 | 120.56 |
| 353.80 | 9570.00 | 119.62 |
| 353.79 | 10010.00 | 118.76 |
| 353.80 | 10480.00 | 117.97 |
| 353.81 | 11040.00 | 117.35 |
| 353.84 | 11540.00 | 116.89 |
| 353.87 | 11950.00 | 116.16 |
| 363.33 | 4330.00 | 193.61 |
| 363.70 | 4990.00 | 171.83 |
| 363.66 | 5490.00 | 159.60 |
| 363.62 | 6030.00 | 150.44 |
| 363.62 | 6520.00 | 144.76 |
| 363.59 | 7000.00 | 139.97 |
| 363.59 | 7500.00 | 136.22 |
| 363.60 | 8030.00 | 132.67 |
| 363.59 | 8480.00 | 130.33 |
| 363.63 | 8990.00 | 128.17 |
| 363.61 | 9520.00 | 125.95 |
| 363.61 | 10000.00 | 123.85 |
| 363.66 | 10580.00 | 122.57 |
| 363.68 | 11000.00 | 121.51 |
| 363.71 | 11510.00 | 120.57 |
| 363.75 | 12010.00 | 119.55 |
| 373.37 | 5540.00 | 218.60 |
| 373.55 | 6030.00 | 187.59 |
| 373.58 | 6510.00 | 170.77 |
| 373.56 | 6990.00 | 159.83 |
| 373.57 | 7500.00 | 151.89 |
| 373.54 | 8000.00 | 146.44 |
| 373.53 | 8500.00 | 142.08 |
| 373.48 | 9010.00 | 138.16 |
| 373.47 | 9520.00 | 134.79 |
| 373.53 | 9990.00 | 132.61 |
| 373.58 | 10550.00 | 130.44 |
| 373.56 | 10990.00 | 128.66 |
| 373.53 | 11480.00 | 126.08 |
| 383.10 | 6560.00 | 239.16 |
| 383.57 | 7020.00 | 204.10 |
| 383.78 | 7490.00 | 182.33 |
| 383.86 | 7980.00 | 172.97 |
| 383.87 | 8520.00 | 160.93 |
| 383.81 | 9090.00 | 151.38 |
| 383.74 | 9490.00 | 145.93 |
| 383.71 | 10040.00 | 140.17 |
| 383.71 | 10550.00 | 136.16 |
| 383.74 | 11270.00 | 132.02 |
| 383.88 | 12030.00 | 129.42 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 305.15 | 2160.00 | 105.01 |
| 305.15 | 2580.00 | 104.34 |
| 305.15 | 3100.00 | 103.90 |
| 305.15 | 3480.00 | 104.19 |
| 305.15 | 4030.00 | 104.67 |
| 305.15 | 4460.00 | 104.39 |
| 305.15 | 4990.00 | 103.81 |
| 305.15 | 5490.00 | 102.94 |
| 310.15 | 2160.00 | 107.51 |
| 310.15 | 2580.00 | 106.21 |
| 310.15 | 3100.00 | 106.31 |
| 310.15 | 3480.00 | 106.26 |
| 310.15 | 4030.00 | 105.59 |
| 310.15 | 4460.00 | 105.06 |
| 310.15 | 4990.00 | 105.25 |
| 310.15 | 5490.00 | 104.39 |
| 315.15 | 2160.00 | 109.82 |
| 315.15 | 2580.00 | 108.66 |
| 315.15 | 3100.00 | 109.00 |
| 315.15 | 3480.00 | 108.23 |
| 315.15 | 4030.00 | 107.36 |
| 315.15 | 4460.00 | 106.26 |
| 315.15 | 4990.00 | 106.55 |
| 315.15 | 5490.00 | 105.83 |
| 320.15 | 2160.00 | 112.17 |
| 320.15 | 2580.00 | 111.69 |
| 320.15 | 3100.00 | 111.64 |
| 320.15 | 3480.00 | 110.44 |
| 320.15 | 4030.00 | 109.53 |
| 320.15 | 4460.00 | 108.18 |
| 320.15 | 4990.00 | 107.94 |
| 320.15 | 5490.00 | 107.46 |
| 325.15 | 2580.00 | 114.86 |
| 325.15 | 3100.00 | 114.09 |
| 325.15 | 3480.00 | 112.89 |
| 325.15 | 4030.00 | 111.88 |
| 325.15 | 4460.00 | 110.87 |
| 325.15 | 4990.00 | 109.67 |
| 325.15 | 5490.00 | 109.34 |
| 330.15 | 2580.00 | 117.79 |
| 330.15 | 3100.00 | 116.59 |
| 330.15 | 3480.00 | 115.92 |
| 330.15 | 4030.00 | 114.57 |
| 330.15 | 4460.00 | 114.00 |
| 330.15 | 4990.00 | 112.07 |
| 330.15 | 5490.00 | 111.50 |
| 335.15 | 3100.00 | 120.68 |
| 335.15 | 3480.00 | 119.81 |
| 335.15 | 4030.00 | 117.99 |
| 335.15 | 4460.00 | 117.51 |
| 335.15 | 4990.00 | 115.25 |
| 335.15 | 5490.00 | 114.14 |
| 340.15 | 3100.00 | 129.47 |
| 340.15 | 3480.00 | 125.24 |
| 340.15 | 4030.00 | 122.65 |
| 340.15 | 4460.00 | 121.40 |
| 340.15 | 4990.00 | 119.28 |
| 340.15 | 5490.00 | 117.41 |
| 345.15 | 3480.00 | 132.60 |
| 345.15 | 4030.00 | 128.70 |
| 345.15 | 4460.00 | 126.06 |
| 345.15 | 4990.00 | 124.23 |
| 345.15 | 5490.00 | 121.69 |
| 350.15 | 4030.00 | 136.59 |
| 350.15 | 4460.00 | 132.45 |
| 350.15 | 4990.00 | 130.05 |
| 350.15 | 5490.00 | 127.26 |
| 355.15 | 4030.00 | 148.79 |
| 355.15 | 4460.00 | 142.50 |
| 355.15 | 4990.00 | 136.68 |
| 355.15 | 5490.00 | 134.37 |
| 360.15 | 4460.00 | 159.27 |
| 360.15 | 4990.00 | 147.49 |
| 360.15 | 5490.00 | 142.78 |
| Reference | ||
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Viscosity, Pa*s - Gas |
| 293.32 | 106.00 | 9.5830e-06 |
| 293.33 | 191.00 | 9.5180e-06 |
| 293.36 | 288.00 | 9.5280e-06 |
| 293.40 | 406.00 | 9.5110e-06 |
| 293.41 | 497.00 | 9.6070e-06 |
| 293.39 | 592.00 | 9.8270e-06 |
| 293.35 | 693.00 | 9.9380e-06 |
| 293.33 | 748.00 | 0.0000 |
| 313.27 | 119.00 | 0.0000 |
| 313.25 | 165.00 | 0.0000 |
| 313.20 | 300.00 | 0.0000 |
| 313.18 | 397.00 | 0.0000 |
| 313.16 | 499.00 | 0.0000 |
| 313.15 | 599.00 | 0.0000 |
| 313.15 | 694.00 | 0.0000 |
| 313.14 | 885.00 | 0.0000 |
| 313.16 | 1007.00 | 0.0000 |
| 313.20 | 1093.00 | 0.0000 |
| 313.23 | 1188.00 | 0.0000 |
| 313.21 | 1269.00 | 0.0000 |
| 333.69 | 115.00 | 0.0000 |
| 333.68 | 140.00 | 0.0000 |
| 333.68 | 219.00 | 0.0000 |
| 333.67 | 417.00 | 0.0000 |
| 333.63 | 494.00 | 0.0000 |
| 333.61 | 575.00 | 0.0000 |
| 333.59 | 719.00 | 0.0000 |
| 333.61 | 794.00 | 0.0000 |
| 333.55 | 1004.00 | 0.0000 |
| 333.57 | 1102.00 | 0.0000 |
| 333.57 | 1205.00 | 0.0000 |
| 333.49 | 1305.00 | 0.0000 |
| 333.49 | 1402.00 | 0.0000 |
| 333.45 | 1503.00 | 0.0000 |
| 333.46 | 1627.00 | 0.0000 |
| 333.05 | 1802.00 | 0.0000 |
| 351.55 | 100.00 | 0.0000 |
| 351.57 | 193.00 | 0.0000 |
| 351.55 | 297.00 | 0.0000 |
| 351.56 | 404.00 | 0.0000 |
| 351.57 | 505.00 | 0.0000 |
| 351.57 | 606.00 | 0.0000 |
| 351.60 | 706.00 | 0.0000 |
| 351.62 | 800.00 | 0.0000 |
| 351.66 | 902.00 | 0.0000 |
| 351.61 | 995.00 | 0.0000 |
| 351.63 | 1098.00 | 0.0000 |
| 351.72 | 1199.00 | 0.0000 |
| 351.73 | 1294.00 | 0.0000 |
| 351.75 | 1392.00 | 0.0000 |
| 351.76 | 1491.00 | 0.0000 |
| 351.71 | 1578.00 | 0.0000 |
| 351.65 | 1692.00 | 0.0000 |
| 351.63 | 1990.00 | 0.0000 |
| 351.61 | 2090.00 | 0.0000 |
| 351.50 | 2208.00 | 0.0000 |
| 351.48 | 2396.00 | 0.0000 |
| 351.52 | 2512.00 | 0.0000 |
| 351.47 | 2592.00 | 0.0000 |
| 351.45 | 2662.00 | 0.0000 |
| 369.28 | 101.00 | 0.0000 |
| 369.28 | 201.00 | 0.0000 |
| 369.26 | 304.00 | 0.0000 |
| 369.28 | 400.00 | 0.0000 |
| 369.30 | 500.00 | 0.0000 |
| 369.32 | 601.00 | 0.0000 |
| 369.34 | 690.00 | 0.0000 |
| 369.23 | 788.00 | 0.0000 |
| 369.32 | 897.00 | 0.0000 |
| 369.32 | 991.00 | 0.0000 |
| 369.33 | 1096.00 | 0.0000 |
| 369.35 | 1191.00 | 0.0000 |
| 369.35 | 1289.00 | 0.0000 |
| 369.35 | 1391.00 | 0.0000 |
| 369.34 | 1492.00 | 0.0000 |
| 369.24 | 1599.00 | 0.0000 |
| 369.30 | 1692.00 | 0.0000 |
| 369.25 | 1743.00 | 0.0000 |
| 369.30 | 1808.00 | 0.0000 |
| 369.25 | 1879.00 | 0.0000 |
| 369.27 | 1999.00 | 0.0000 |
| 369.34 | 2176.00 | 0.0000 |
| 369.32 | 2308.00 | 0.0000 |
| 369.47 | 2400.00 | 0.0000 |
| 369.31 | 2466.00 | 0.0000 |
| 369.48 | 2603.00 | 0.0000 |
| 369.47 | 2704.00 | 0.0000 |
| 369.48 | 2904.00 | 0.0000 |
| 369.48 | 2996.00 | 0.0000 |
| 369.50 | 3094.00 | 0.0000 |
| 369.50 | 3204.00 | 0.0000 |
| 369.51 | 3306.00 | 0.0000 |
| 369.51 | 3405.00 | 0.0000 |
| 369.49 | 3512.00 | 0.0000 |
| 369.49 | 3623.00 | 0.0000 |
| 369.48 | 3701.00 | 0.0000 |
| 369.46 | 3806.00 | 0.0000 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Mass density, kg/m3 - Gas |
| 300.16 | 642.20 | 13.92 |
| 305.16 | 656.60 | 13.917 |
| 310.14 | 670.40 | 13.913 |
| 312.16 | 1205.60 | 27.61 |
| 314.16 | 1218.30 | 27.607 |
| 315.15 | 684.80 | 13.91 |
| 316.15 | 1231.80 | 27.605 |
| 318.15 | 1244.10 | 27.602 |
| 320.14 | 698.50 | 13.906 |
| 322.16 | 1268.70 | 27.596 |
| 324.15 | 1614.60 | 37.54 |
| 325.14 | 712.30 | 13.903 |
| 326.14 | 1634.40 | 37.536 |
| 326.16 | 1293.40 | 27.591 |
| 328.15 | 1652.50 | 37.533 |
| 330.15 | 1670.20 | 37.529 |
| 330.16 | 726.10 | 13.899 |
| 330.16 | 1317.60 | 27.585 |
| 332.15 | 2022.60 | 48.84 |
| 334.16 | 1341.90 | 27.58 |
| 334.16 | 1704.90 | 37.521 |
| 334.16 | 2047.70 | 48.835 |
| 335.15 | 739.50 | 13.896 |
| 336.16 | 2072.50 | 48.83 |
| 338.12 | 2287.80 | 56.23 |
| 338.16 | 1739.00 | 37.514 |
| 338.17 | 1365.60 | 27.574 |
| 338.20 | 2096.60 | 48.825 |
| 339.16 | 2108.20 | 48.823 |
| 340.12 | 2318.80 | 56.224 |
| 340.15 | 752.50 | 13.892 |
| 340.15 | 2419.00 | 60.32 |
| 340.16 | 2120.60 | 48.821 |
| 342.12 | 2347.80 | 56.219 |
| 342.16 | 1388.90 | 27.569 |
| 342.16 | 2144.20 | 48.816 |
| 342.16 | 2450.70 | 60.314 |
| 342.17 | 1773.50 | 37.506 |
| 344.12 | 2376.70 | 56.213 |
| 344.16 | 2167.50 | 48.811 |
| 344.16 | 2482.20 | 60.308 |
| 346.12 | 2404.50 | 56.208 |
| 346.14 | 2707.50 | 68.66 |
| 346.15 | 768.90 | 13.888 |
| 346.15 | 1412.40 | 27.563 |
| 346.15 | 2513.10 | 60.302 |
| 346.16 | 1806.70 | 37.499 |
| 346.16 | 2190.70 | 48.806 |
| 347.15 | 2725.90 | 68.657 |
| 348.13 | 2432.70 | 56.202 |
| 348.15 | 2743.80 | 68.653 |
| 348.16 | 2214.00 | 48.801 |
| 348.16 | 2543.00 | 60.296 |
| 350.15 | 1435.80 | 27.558 |
| 350.15 | 2460.50 | 56.196 |
| 350.15 | 2779.80 | 68.646 |
| 350.16 | 1840.50 | 37.491 |
| 350.16 | 2237.20 | 48.796 |
| 350.16 | 2573.40 | 60.29 |
| 350.16 | 2978.20 | 78.21 |
| 351.16 | 2999.90 | 78.206 |
| 352.15 | 2488.20 | 56.191 |
| 352.15 | 2815.00 | 68.639 |
| 352.16 | 2260.10 | 48.791 |
| 352.16 | 2603.30 | 60.284 |
| 352.17 | 3021.20 | 78.202 |
| 353.14 | 3180.20 | 85.66 |
| 353.16 | 3042.30 | 78.198 |
| 354.15 | 3204.50 | 85.656 |
| 354.16 | 790.70 | 13.883 |
| 354.16 | 1458.80 | 27.552 |
| 354.16 | 1873.70 | 37.484 |
| 354.16 | 2283.00 | 48.787 |
| 354.16 | 2515.30 | 56.185 |
| 354.16 | 2633.40 | 60.278 |
| 354.16 | 2850.70 | 68.633 |
| 354.17 | 3062.90 | 78.194 |
| 355.15 | 3227.80 | 85.651 |
| 356.14 | 2542.30 | 56.18 |
| 356.15 | 2663.10 | 60.272 |
| 356.15 | 2885.70 | 68.626 |
| 356.16 | 2305.70 | 48.782 |
| 356.16 | 3104.40 | 78.187 |
| 356.26 | 3251.20 | 85.647 |
| 357.26 | 3274.80 | 85.642 |
| 358.15 | 1481.80 | 27.547 |
| 358.15 | 1906.70 | 37.477 |
| 358.15 | 2569.20 | 56.174 |
| 358.15 | 2920.00 | 68.619 |
| 358.15 | 3297.70 | 85.639 |
| 358.16 | 2328.40 | 48.777 |
| 358.16 | 2692.50 | 60.266 |
| 358.16 | 3145.70 | 78.179 |
| 358.16 | 3506.40 | 97.915 |
| 359.16 | 3534.20 | 97.91 |
| 360.15 | 2595.90 | 56.168 |
| 360.15 | 2954.30 | 68.612 |
| 360.16 | 2721.30 | 60.26 |
| 360.16 | 3186.00 | 78.171 |
| 360.16 | 3343.90 | 85.63 |
| 360.16 | 3562.20 | 97.905 |
| 360.17 | 2350.80 | 48.772 |
| 360.17 | 3660.70 | 104.59 |
| 361.15 | 3589.90 | 97.9 |
| 361.16 | 3691.00 | 104.585 |
| 362.14 | 2622.70 | 56.163 |
| 362.15 | 811.80 | 13.877 |
| 362.15 | 2988.30 | 68.605 |
| 362.15 | 3226.20 | 78.163 |
| 362.15 | 3389.20 | 85.622 |
| 362.15 | 3617.00 | 97.896 |
| 362.16 | 1505.00 | 27.541 |
| 362.16 | 1939.60 | 37.469 |
| 362.16 | 3721.40 | 104.58 |
| 362.17 | 2373.00 | 48.767 |
| 362.17 | 2750.90 | 60.254 |
| 363.15 | 3644.50 | 97.891 |
| 363.16 | 3751.40 | 104.574 |
| 364.15 | 2649.20 | 56.157 |
| 364.15 | 3023.00 | 68.598 |
| 364.15 | 3434.40 | 85.613 |
| 364.15 | 3780.80 | 104.569 |
| 364.16 | 2394.90 | 48.762 |
| 364.16 | 3266.50 | 78.156 |
| 364.16 | 3671.60 | 97.886 |
| 364.17 | 2779.60 | 60.248 |
| 365.16 | 3698.90 | 97.881 |
| 365.16 | 3810.40 | 104.564 |
| 366.14 | 1527.70 | 27.536 |
| 366.14 | 2675.70 | 56.152 |
| 366.15 | 1971.50 | 37.462 |
| 366.15 | 3056.70 | 68.592 |
| 366.15 | 3306.20 | 78.148 |
| 366.15 | 3478.50 | 85.605 |
| 366.15 | 3725.20 | 97.876 |
| 366.15 | 3839.80 | 104.559 |
| 366.16 | 2417.40 | 48.757 |
| 366.16 | 2808.40 | 60.242 |
| 367.15 | 3751.80 | 97.871 |
| 367.15 | 3869.00 | 104.554 |
| 368.14 | 2702.00 | 56.146 |
| 368.14 | 3090.70 | 68.585 |
| 368.15 | 3346.00 | 78.14 |
| 368.15 | 3523.30 | 85.596 |
| 368.15 | 3898.10 | 104.548 |
| 368.16 | 2439.40 | 48.753 |
| 368.16 | 2837.30 | 60.236 |
| 368.16 | 3778.80 | 97.866 |
| 369.14 | 3805.10 | 97.861 |
| 369.15 | 3927.30 | 104.543 |
| 370.12 | 1550.10 | 27.531 |
| 370.13 | 3123.80 | 68.578 |
| 370.14 | 2728.00 | 56.14 |
| 370.14 | 3568.00 | 85.588 |
| 370.14 | 3831.80 | 97.857 |
| 370.15 | 833.20 | 13.872 |
| 370.15 | 2461.80 | 48.748 |
| 370.15 | 3385.90 | 78.132 |
| 370.15 | 3956.20 | 104.538 |
| 370.16 | 2004.00 | 37.454 |
| 370.16 | 2865.80 | 60.23 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Gas | Pressure, kPa - Gas | Mass density, kg/m3 - Gas |
| 378.02 | 4235.22 | 106.825 |
| 378.01 | 3335.39 | 71.042 |
| 378.01 | 2481.64 | 47.245 |
| 378.01 | 1776.12 | 31.42 |
| 378.01 | 1240.02 | 20.895 |
| 378.01 | 851.98 | 13.896 |
| 378.02 | 579.55 | 9.241 |
| 378.01 | 391.92 | 6.145 |
| 378.01 | 264.55 | 4.087 |
| 373.14 | 4091.85 | 106.604 |
| 373.14 | 3250.93 | 70.894 |
| 373.14 | 2430.12 | 47.146 |
| 373.14 | 1744.06 | 31.354 |
| 373.14 | 1219.77 | 20.851 |
| 373.13 | 838.52 | 13.867 |
| 373.15 | 570.74 | 9.221 |
| 373.14 | 386.27 | 6.133 |
| 373.14 | 260.73 | 4.078 |
| 368.27 | 3165.93 | 71.038 |
| 368.26 | 2378.24 | 47.243 |
| 368.26 | 1712.22 | 31.418 |
| 368.26 | 1199.41 | 20.894 |
| 368.26 | 825.10 | 13.895 |
| 368.26 | 561.93 | 9.24 |
| 368.26 | 380.26 | 6.145 |
| 368.26 | 256.54 | 4.087 |
| 363.36 | 3082.31 | 70.859 |
| 363.36 | 2325.74 | 47.122 |
| 363.37 | 1680.00 | 31.337 |
| 363.37 | 1178.86 | 20.84 |
| 363.37 | 811.80 | 13.859 |
| 363.36 | 553.08 | 9.217 |
| 363.37 | 374.25 | 6.129 |
| 363.36 | 252.39 | 4.076 |
| 358.61 | 2274.59 | 47.133 |
| 358.61 | 1648.32 | 31.345 |
| 358.61 | 1158.96 | 20.845 |
| 358.62 | 799.33 | 13.862 |
| 358.61 | 544.42 | 9.219 |
| 358.62 | 368.40 | 6.131 |
| 358.61 | 248.43 | 4.077 |
| 352.74 | 3018.69 | 77.15 |
| 352.74 | 2347.08 | 51.308 |
| 352.74 | 1723.98 | 34.121 |
| 352.75 | 1222.33 | 22.691 |
| 352.75 | 847.82 | 15.09 |
| 352.74 | 579.94 | 10.036 |
| 352.74 | 393.24 | 6.674 |
| 352.74 | 265.25 | 4.438 |
| 352.75 | 178.77 | 2.951 |
| 347.85 | 2287.35 | 51.336 |
| 347.85 | 1687.63 | 34.14 |
| 347.86 | 1199.98 | 22.704 |
| 347.85 | 833.34 | 15.099 |
| 347.85 | 570.22 | 10.041 |
| 347.86 | 386.83 | 6.677 |
| 347.86 | 260.96 | 4.441 |
| 347.85 | 175.51 | 2.953 |
| 343.02 | 2227.47 | 51.191 |
| 343.02 | 1651.35 | 34.043 |
| 343.02 | 1177.41 | 22.64 |
| 343.01 | 818.91 | 15.056 |
| 343.02 | 560.82 | 10.013 |
| 343.01 | 380.56 | 6.659 |
| 343.01 | 256.69 | 4.428 |
| 343.03 | 172.53 | 2.945 |
| 338.15 | 1614.54 | 34.027 |
| 338.16 | 1154.55 | 22.629 |
| 338.16 | 804.44 | 15.048 |
| 338.15 | 551.38 | 10.008 |
| 338.15 | 374.30 | 6.655 |
| 338.15 | 252.41 | 4.426 |
| 338.16 | 169.60 | 2.943 |
| 333.30 | 1131.52 | 22.599 |
| 333.30 | 789.86 | 15.029 |
| 333.29 | 541.96 | 9.995 |
| 333.30 | 368.16 | 6.647 |
| 333.30 | 248.18 | 4.42 |
| 333.31 | 166.70 | 2.94 |
| 328.42 | 1539.53 | 33.847 |
| 328.42 | 1108.32 | 22.509 |
| 328.42 | 775.13 | 14.969 |
| 328.42 | 532.98 | 9.955 |
| 328.43 | 361.91 | 6.62 |
| 328.42 | 243.93 | 4.403 |
| 328.43 | 163.80 | 2.928 |
| 323.51 | 1084.58 | 22.444 |
| 323.51 | 760.32 | 14.926 |
| 323.52 | 523.39 | 9.926 |
| 323.51 | 355.59 | 6.601 |
| 323.52 | 239.62 | 4.39 |
| 323.52 | 160.85 | 2.919 |
| 318.67 | 1060.94 | 22.39 |
| 318.67 | 745.44 | 14.89 |
| 318.66 | 513.87 | 9.903 |
| 318.67 | 349.39 | 6.585 |
| 318.67 | 235.35 | 4.379 |
| 318.67 | 158.08 | 2.912 |
| 313.80 | 1036.81 | 22.346 |
| 313.81 | 730.50 | 14.86 |
| 313.81 | 504.31 | 9.882 |
| 313.80 | 343.12 | 6.572 |
| 313.81 | 231.58 | 4.371 |
| 313.80 | 155.20 | 2.907 |
| 308.97 | 715.60 | 14.793 |
| 308.97 | 494.66 | 9.837 |
| 308.96 | 336.88 | 6.542 |
| 308.96 | 227.65 | 4.351 |
| 308.98 | 152.32 | 2.893 |
| 303.31 | 697.80 | 14.795 |
| 303.32 | 483.63 | 9.838 |
| 303.31 | 329.55 | 6.543 |
| 303.31 | 222.77 | 4.351 |
| 303.31 | 149.42 | 2.894 |
| 298.65 | 682.94 | 14.731 |
| 298.66 | 474.30 | 9.797 |
| 298.65 | 323.48 | 6.515 |
| 298.66 | 218.72 | 4.333 |
| 298.66 | 146.61 | 2.881 |
| 293.10 | 462.98 | 9.751 |
| 293.09 | 316.32 | 6.485 |
| 293.09 | 213.69 | 4.313 |
| 293.10 | 143.41 | 2.868 |
| 288.21 | 452.92 | 9.758 |
| 288.21 | 309.96 | 6.489 |
| 288.20 | 209.64 | 4.316 |
| 283.26 | 442.81 | 9.718 |
| 283.26 | 303.56 | 6.463 |
| 283.27 | 205.41 | 4.298 |
| 278.38 | 432.22 | 9.679 |
| 278.39 | 297.17 | 6.437 |
| 278.38 | 201.28 | 4.281 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.52 | 1000.00 | 727.11 |
| 293.20 | 1010.00 | 706.97 |
| 283.52 | 3000.00 | 731.96 |
| 332.98 | 3000.00 | 616.38 |
| 342.85 | 3000.00 | 582.54 |
| 313.14 | 3000.00 | 669.48 |
| 323.00 | 3000.00 | 644.53 |
| 293.20 | 3010.00 | 712.87 |
| 303.23 | 3010.00 | 692.69 |
| 283.52 | 4990.00 | 736.6 |
| 362.79 | 4990.00 | 521.7 |
| 332.98 | 5000.00 | 628.96 |
| 342.85 | 5000.00 | 600.31 |
| 313.14 | 5000.00 | 677.22 |
| 323.00 | 5000.00 | 654.18 |
| 352.86 | 5000.00 | 566.12 |
| 293.21 | 5010.00 | 718.27 |
| 303.23 | 5010.00 | 699.12 |
| 303.23 | 10000.00 | 713.26 |
| 283.51 | 10000.00 | 747.35 |
| 342.85 | 10000.00 | 630.51 |
| 313.14 | 10000.00 | 694.0 |
| 323.00 | 10000.00 | 673.87 |
| 352.86 | 10000.00 | 606.19 |
| 362.79 | 10000.00 | 579.49 |
| 293.21 | 10010.00 | 730.51 |
| 332.98 | 10010.00 | 653.01 |
| 303.23 | 15000.00 | 725.31 |
| 332.99 | 15000.00 | 671.15 |
| 283.51 | 15000.00 | 756.91 |
| 342.85 | 15000.00 | 651.87 |
| 313.14 | 15000.00 | 707.5 |
| 323.00 | 15000.00 | 689.57 |
| 352.86 | 15000.00 | 631.59 |
| 362.80 | 15000.00 | 610.29 |
| 293.21 | 15010.00 | 741.15 |
| 352.86 | 19990.00 | 650.88 |
| 362.80 | 19990.00 | 632.41 |
| 293.21 | 20000.00 | 750.65 |
| 342.85 | 20000.00 | 668.76 |
| 283.51 | 20000.00 | 765.51 |
| 313.15 | 20000.00 | 719.54 |
| 323.00 | 20000.00 | 702.96 |
| 332.99 | 20010.00 | 686.12 |
| 303.23 | 20010.00 | 735.85 |
| 362.80 | 24990.00 | 650.04 |
| 332.99 | 25000.00 | 698.88 |
| 342.85 | 25000.00 | 682.96 |
| 313.15 | 25000.00 | 729.96 |
| 283.51 | 25000.00 | 773.62 |
| 352.86 | 25000.00 | 666.7 |
| 323.00 | 25000.00 | 714.54 |
| 303.24 | 25010.00 | 745.33 |
| 293.21 | 25010.00 | 759.29 |
| 332.99 | 29990.00 | 710.09 |
| 352.86 | 29990.00 | 680.18 |
| 323.01 | 30000.00 | 724.71 |
| 342.85 | 30000.00 | 695.28 |
| 303.23 | 30000.00 | 753.95 |
| 283.51 | 30000.00 | 780.86 |
| 362.80 | 30000.00 | 664.91 |
| 313.15 | 30010.00 | 739.29 |
| 293.21 | 30010.00 | 767.25 |
| 332.99 | 39990.00 | 729.27 |
| 352.86 | 39990.00 | 702.62 |
| 313.15 | 40000.00 | 755.43 |
| 323.01 | 40000.00 | 742.42 |
| 342.85 | 40000.00 | 716.03 |
| 283.51 | 40000.00 | 794.13 |
| 362.80 | 40000.00 | 689.17 |
| 303.24 | 40010.00 | 769.21 |
| 293.22 | 40010.00 | 781.39 |
| 283.50 | 49990.00 | 805.67 |
| 362.80 | 49990.00 | 708.84 |
| 313.15 | 50000.00 | 770.06 |
| 303.24 | 50000.00 | 782.6 |
| 352.86 | 50000.00 | 721.07 |
| 293.22 | 50000.00 | 793.87 |
| 332.98 | 50000.00 | 745.52 |
| 323.01 | 50000.00 | 757.67 |
| 342.86 | 50010.00 | 733.53 |
| 352.86 | 59990.00 | 736.86 |
| 362.81 | 59990.00 | 725.55 |
| 313.15 | 60000.00 | 782.28 |
| 293.22 | 60000.00 | 805.15 |
| 342.85 | 60000.00 | 748.38 |
| 323.01 | 60000.00 | 770.9 |
| 283.50 | 60000.00 | 816.48 |
| 332.98 | 60000.00 | 759.62 |
| 303.24 | 60000.00 | 794.39 |
| 323.01 | 69990.00 | 783.33 |
| 332.99 | 69990.00 | 772.51 |
| 283.50 | 69990.00 | 826.06 |
| 342.86 | 70000.00 | 762.03 |
| 303.24 | 70000.00 | 805.57 |
| 352.86 | 70000.00 | 751.19 |
| 293.21 | 70000.00 | 815.59 |
| 313.15 | 70000.00 | 794.18 |
| 362.81 | 70000.00 | 740.64 |
| 283.50 | 79970.00 | 834.87 |
| 352.86 | 79990.00 | 763.56 |
| 342.86 | 79990.00 | 773.74 |
| 293.21 | 80000.00 | 825.0 |
| 303.24 | 80000.00 | 815.36 |
| 323.01 | 80000.00 | 794.16 |
| 313.15 | 80000.00 | 804.63 |
| 362.81 | 80000.00 | 753.56 |
| 332.99 | 80010.00 | 783.85 |
| 313.16 | 90000.00 | 814.08 |
| 352.86 | 90000.00 | 774.75 |
| 293.22 | 90000.00 | 833.51 |
| 303.25 | 90000.00 | 824.43 |
| 332.99 | 90000.00 | 794.07 |
| 323.00 | 90000.00 | 804.1 |
| 362.81 | 90000.00 | 765.31 |
| 342.86 | 90010.00 | 784.53 |
| 283.50 | 90040.00 | 843.3 |
| 352.87 | 99990.00 | 785.11 |
| 293.22 | 99990.00 | 841.66 |
| 362.81 | 99990.00 | 775.91 |
| 323.01 | 100000.00 | 813.21 |
| 313.16 | 100000.00 | 822.46 |
| 332.99 | 100000.00 | 803.45 |
| 283.51 | 100000.00 | 851.08 |
| 303.25 | 100000.00 | 832.9 |
| 342.87 | 100000.00 | 794.42 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [56.11; 129.58] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 7.16100e+00 | |||
| Coefficient B | 2.05620e-01 | |||
| Coefficient C | -1.01400e-04 | |||
| Coefficient D | 1.82000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 56.11 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 68.02 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 78.86 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 88.69 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 97.56 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 105.53 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 112.66 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 119.01 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 124.63 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 129.58 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 4823.60] | kPa | [169.30; 375.30] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.45899e+01 | |||
| Coefficient B | -2.19653e+03 | |||
| Coefficient C | -1.57210e+01 | |||
| Temperature range, min. | 169.30 | |||
| Temperature range, max. | 375.30 | |||
| Pvap | 1.33 | kPa | 169.30 | Calculated Property |
| Pvap | 8.52 | kPa | 192.19 | Calculated Property |
| Pvap | 35.58 | kPa | 215.08 | Calculated Property |
| Pvap | 110.67 | kPa | 237.97 | Calculated Property |
| Pvap | 278.49 | kPa | 260.86 | Calculated Property |
| Pvap | 598.60 | kPa | 283.74 | Calculated Property |
| Pvap | 1140.71 | kPa | 306.63 | Calculated Property |
| Pvap | 1978.59 | kPa | 329.52 | Calculated Property |
| Pvap | 3184.34 | kPa | 352.41 | Calculated Property |
| Pvap | 4823.60 | kPa | 375.30 | Calculated Property |
| Pvap | [9.37e-03; 5000.64] | kPa | [129.95; 375.31] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 4.35322e+01 | |||
| Coefficient B | -3.38922e+03 | |||
| Coefficient C | -4.57263e+00 | |||
| Coefficient D | 7.95831e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 129.95 | |||
| Temperature range, max. | 375.31 | |||
| Pvap | 9.37e-03 | kPa | 129.95 | Calculated Property |
| Pvap | 0.38 | kPa | 157.21 | Calculated Property |
| Pvap | 4.82 | kPa | 184.47 | Calculated Property |
| Pvap | 29.79 | kPa | 211.74 | Calculated Property |
| Pvap | 117.22 | kPa | 239.00 | Calculated Property |
| Pvap | 340.95 | kPa | 266.26 | Calculated Property |
| Pvap | 804.08 | kPa | 293.52 | Calculated Property |
| Pvap | 1632.97 | kPa | 320.79 | Calculated Property |
| Pvap | 2974.61 | kPa | 348.05 | Calculated Property |
| Pvap | 5000.64 | kPa | 375.31 | Calculated Property |
| Pvap | [1.35; 4929.79] | kPa | [169.54; 375.30] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46021e+01 | |||
| Coefficient B | -2.18837e+03 | |||
| Coefficient C | -1.64920e+01 | |||
| Reference | Vidaurri, 1975 | |||
| Temperature range, min. | 169.54 | |||
| Temperature range, max. | 375.30 | |||
| Pvap | 1.35 | kPa | 169.54 | Calculated Property |
| Pvap | 8.69 | kPa | 192.40 | Calculated Property |
| Pvap | 36.33 | kPa | 215.26 | Calculated Property |
| Pvap | 113.10 | kPa | 238.13 | Calculated Property |
| Pvap | 284.73 | kPa | 260.99 | Calculated Property |
| Pvap | 612.11 | kPa | 283.85 | Calculated Property |
| Pvap | 1166.43 | kPa | 306.71 | Calculated Property |
| Pvap | 2022.96 | kPa | 329.58 | Calculated Property |
| Pvap | 3255.15 | kPa | 352.44 | Calculated Property |
| Pvap | 4929.79 | kPa | 375.30 | Calculated Property |
| Pvap | [0.13; 100.21] | kPa | [156.00; 241.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.31803e+01 | |||
| Coefficient B | -1.66922e+03 | |||
| Coefficient C | -4.62960e+01 | |||
| Reference | Stull, 1947 | |||
| Temperature range, min. | 156.00 | |||
| Temperature range, max. | 241.00 | |||
| Pvap | 0.13 | kPa | 156.00 | Calculated Property |
| Pvap | 0.44 | kPa | 165.44 | Calculated Property |
| Pvap | 1.22 | kPa | 174.89 | Calculated Property |
| Pvap | 2.97 | kPa | 184.33 | Calculated Property |
| Pvap | 6.44 | kPa | 193.78 | Calculated Property |
| Pvap | 12.72 | kPa | 203.22 | Calculated Property |
| Pvap | 23.27 | kPa | 212.67 | Calculated Property |
| Pvap | 39.89 | kPa | 222.11 | Calculated Property |
| Pvap | 64.73 | kPa | 231.56 | Calculated Property |
| Pvap | 100.21 | kPa | 241.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethane, fluoro-.
Mixtures
- Ethane, fluoro- + Norflurane
- Ethane, fluoro- + 2,5,8,11,14-Pentaoxapentadecane
- Ethane, fluoro- + 2,5,8,11-Tetraoxadodecane
- Ethane, fluoro- + Ethane, 1,1'-oxybis[2-methoxy-
- Ethane, fluoro- + Ethane, pentafluoro-
- Ethane, fluoro- + 1,1,1,2,3,3,3-heptafluoropropane
- Ethane, 1,1,1-trifluoro- + Ethane, fluoro-
- Methane, difluoro- + Ethane, fluoro-
- Methane, difluoro- + Ethane, fluoro- + Ethane, pentafluoro-
- Ethane, fluoro- + Ethane, 1,1,2,2-tetrafluoro-
- Ethane, fluoro- + N,N-Dimethylacetamide
- Ethane, fluoro- + 2-Pyrrolidinone, 1-methyl-
- Ethane, fluoro- + Benzene, hexadecyl-
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Saturated Liquid Viscosity of Ethyl Fluoride (HFC161) from 233 K to 373 K
- Viscosity Measurements of Ethyl Fluoride (R161) from 243 K to 363 K at Pressures up to 30 MPa
- Compressed Liquid Density and Helmholtz Equation of State of Fluoroethane (R161)
- Gaseous PVT properties of ethyl fluoride
- PVTx properties in the gas phase for binary HFC-161/125 system
- An experimental study of PVTx properties in the gas phase for binary mixtures of HFC-161 and HFC-32
- Experimental vapor pressure data and a vapor pressure equation for fluoroethane (HFC-161)
- Measurements of gas phase PVTx properties for the ternary HFC-161/125/32 system
- Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-143a
- PVTx measurements in the gas phase for binary mixtures of HFC-161 and HFC-227ea
- Isothermal vapor-liquid equilibrium data for the binary mixture ethyl fluoride (HFC-161) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) over a temperature range from 253.15 K to 313.15 K
- Isothermal vapor-liquid equilibrium data for the binary mixture difluoromethane (HFC-32)+ ethyl fluoride (HFC-161) over a temperature range from 253.15 to 303.15 K
- Gas phase PVTx properties for binary mixtures of HFC-161 and HFC-134a
- Surface tension of ethyl fluoride (HFC161) from (233 to 373) K
- Thermal conductivity of ethyl fluoride (HFC161)
- Viscosity of Gaseous Ethyl Fluoride (HFC-161)
- Solubilities of R-161 and R-143a in 1-Hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide
- Vapor - liquid equilibria of fluoroethane (HFC-161) + 2,3,3,3 - tetrafluoroprop - 1 - ene (HFO- 1234yf)
- Gaseous absorption of fluorinated ethanes by ionic liquids
- Surface tension and liquid viscosity measurement of ethyl fluoride(R161) under saturation condition
- Measurements for isobaric specific heat capacity of ethyl fluoride (HFC-161) in liquid and vapor phase
- Vapor liquid equilibrium measurements for difluoromethane (R32) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) and fluoroethane (R161) + 2,3,3,3-tetrafluoroprop-1-ene (R1234yf)
- Sync-measurement experimental study of (fluoroethane + dimethylether tetraethylene glycol), (fluoroethane + dimethylether triethylene glycol) and (fluoroethane + dimethylether diethylene glycol) systems
- Diffusion coefficients and Henry's constants of hydrofluorocarbons in [HMIM][Tf2N], [HMIM][TfO], and [HMIM][BF4]
- Vapor liquid equilibria for binary mixtures of difluoromethane (R32) + fluoroethane (R161) and fluoroethane (R161) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))
- Isobaric Heat Capacity of HFC-161 in Liquid Phase at Temperatures up to 360.15 K and Pressures up to 5.5 MPa
- Investigation on the Vapor-Liquid Equilibrium for the Ternary Mixture HFC-32 + HFC-125 + HFC-161 at Temperatures from 265.15 K to 303.15 K
- 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
- Isothermal Vapor Liquid Equilibrium of HFC-161 + DMETrEG within the Temperature Range of 293.15 353.15 K and Comparison for HFC-161 Combined with Different Absorbents
- Measurements of Gaseous Pressure-Volume-Temperature Properties for Ethyl Fluoride
- Vapor Pressure Measurements of Ethyl Fluoride
- Isothermal Vapor-Liquid Equilibrium of (Pentafluoroethane + Fluoroethane) at Temperatures between (265.15 and 303.15) K Obtained with a Recirculating Still
- Vapor-Liquid-Liquid Equilibria of Hydrofluorocarbons + 1-Butyl-3-methylimidazolium Hexafluorophosphate
- Vapor-Liquid Equilibria for 1,1,2,2-Tetrafluoroethane (R134) + Fluoroethane (R161) at Temperatures between (263.15 and 288.15) K
- Isothermal Vapor-Liquid Equilibrium Data for the Binary Mixture Trifluoroethane (HFC-143a) + Ethyl Fluoride (HFC-161) over the Temperature Range (253.15 to 303.15) K
- Density Data for the Refrigerant Ethyl Fluoride (HFC-161) over a Temperature Range from (230 to 344) K
- 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
- Solubility and Miscibility for the Mixture of (Ethyl Fluoride + Alkylbenzene Oil)
- Vapor-Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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