- InChI
- InChI=1S/C3H2F6/c4-2(5,6)1-3(7,8)9/h1H2
- InChI Key
- NSGXIBWMJZWTPY-UHFFFAOYSA-N
- Formula
- C3H2F6
- SMILES
- FC(F)(F)CC(F)(F)F
- Molecular Weight1
- 152.04
- CAS
- 690-39-1
- Other Names
-
- 1,1,1,3,3,3-hexafluoropropane
- 2,2-dihydroperfluoropropane
- Bistrifluoromethylmethane
- HFC 236fa
- HFC-236fa
- R 236fa
- R-236fa
- bis(trifluoromethyl)methane
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 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 |
|---|---|---|---|
| ΔfH°gas | -1364.66 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 7.18 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 23.58 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 12.51 | eV | Relay (1.0) Calculated Property |
| logPoct/wat | 2.501 | Crippen Calculated Property | |
| McVol | 63.750 | ml/mol | McGowan Calculated Property |
| Pc | 3184.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value |
| Tboil | 272.10 ± 0.50 | K | NIST |
| Tc | 398.07 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value |
| Tfus | 177.05 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.277 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value |
Cheméo can also estimate Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
Datasets
- Molar heat capacity at constant pressure, J/K/mol (1)
- Viscosity, Pa*s (1)
- Mass density, kg/m3 (1)
- Thermal conductivity, W/m/K (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 |
| 315.15 | 1480.00 | 195.67 |
| 320.15 | 1480.00 | 198.71 |
| 325.15 | 1480.00 | 202.06 |
| 330.15 | 1480.00 | 205.71 |
| 335.15 | 1480.00 | 209.36 |
| 340.15 | 1480.00 | 213.46 |
| 345.15 | 1480.00 | 218.02 |
| 350.15 | 1480.00 | 223.34 |
| 315.15 | 2490.00 | 193.70 |
| 320.15 | 2490.00 | 196.59 |
| 325.15 | 2490.00 | 199.78 |
| 330.15 | 2490.00 | 203.28 |
| 335.15 | 2490.00 | 207.08 |
| 340.15 | 2490.00 | 210.73 |
| 345.15 | 2490.00 | 214.83 |
| 350.15 | 2490.00 | 219.24 |
| 355.15 | 2490.00 | 224.56 |
| 360.15 | 2490.00 | 231.10 |
| 365.15 | 2490.00 | 239.92 |
| 315.15 | 3540.00 | 192.48 |
| 320.15 | 3540.00 | 194.91 |
| 325.15 | 3540.00 | 197.95 |
| 330.15 | 3540.00 | 201.45 |
| 335.15 | 3540.00 | 205.10 |
| 340.15 | 3540.00 | 208.60 |
| 345.15 | 3540.00 | 212.25 |
| 350.15 | 3540.00 | 216.35 |
| 355.15 | 3540.00 | 221.22 |
| 360.15 | 3540.00 | 226.84 |
| 365.15 | 3540.00 | 233.53 |
| 315.15 | 4560.00 | 191.42 |
| 320.15 | 4560.00 | 193.70 |
| 325.15 | 4560.00 | 196.43 |
| 330.15 | 4560.00 | 199.78 |
| 335.15 | 4560.00 | 203.28 |
| 340.15 | 4560.00 | 206.77 |
| 345.15 | 4560.00 | 210.27 |
| 350.15 | 4560.00 | 214.07 |
| 355.15 | 4560.00 | 218.33 |
| 360.15 | 4560.00 | 223.50 |
| 365.15 | 4560.00 | 230.49 |
| 315.15 | 5410.00 | 190.05 |
| 320.15 | 5410.00 | 192.78 |
| 325.15 | 5410.00 | 195.67 |
| 330.15 | 5410.00 | 199.02 |
| 335.15 | 5410.00 | 202.21 |
| 340.15 | 5410.00 | 205.56 |
| 345.15 | 5410.00 | 208.90 |
| 350.15 | 5410.00 | 212.40 |
| 355.15 | 5410.00 | 216.35 |
| 360.15 | 5410.00 | 221.06 |
| 365.15 | 5410.00 | 227.45 |
| Reference | ||
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 253.15 | 1000.00 | 0.0005 |
| 253.15 | 5000.00 | 0.0006 |
| 253.15 | 10000.00 | 0.0006 |
| 253.15 | 15000.00 | 0.0006 |
| 253.15 | 20000.00 | 0.0007 |
| 253.15 | 25000.00 | 0.0007 |
| 253.15 | 30000.00 | 0.0008 |
| 253.15 | 35000.00 | 0.0008 |
| 253.15 | 40000.00 | 0.0008 |
| 263.16 | 1000.00 | 0.0005 |
| 263.16 | 5000.00 | 0.0005 |
| 263.16 | 10000.00 | 0.0005 |
| 263.16 | 15000.00 | 0.0006 |
| 263.16 | 20000.00 | 0.0006 |
| 263.16 | 25000.00 | 0.0006 |
| 263.16 | 30000.00 | 0.0007 |
| 263.16 | 35000.00 | 0.0007 |
| 263.16 | 40000.00 | 0.0007 |
| 273.14 | 1000.00 | 0.0004 |
| 273.14 | 5000.00 | 0.0004 |
| 273.14 | 10000.00 | 0.0005 |
| 273.14 | 15000.00 | 0.0005 |
| 273.14 | 20000.00 | 0.0005 |
| 273.14 | 25000.00 | 0.0005 |
| 273.14 | 30000.00 | 0.0006 |
| 273.14 | 35000.00 | 0.0006 |
| 273.14 | 40000.00 | 0.0006 |
| 283.14 | 1000.00 | 0.0003 |
| 283.14 | 5000.00 | 0.0004 |
| 283.14 | 10000.00 | 0.0004 |
| 283.14 | 15000.00 | 0.0004 |
| 283.14 | 20000.00 | 0.0005 |
| 283.14 | 25000.00 | 0.0005 |
| 283.14 | 30000.00 | 0.0005 |
| 283.14 | 35000.00 | 0.0005 |
| 283.14 | 40000.00 | 0.0006 |
| 293.14 | 1000.00 | 0.0003 |
| 293.14 | 5000.00 | 0.0003 |
| 293.14 | 10000.00 | 0.0004 |
| 293.14 | 15000.00 | 0.0004 |
| 293.14 | 20000.00 | 0.0004 |
| 293.14 | 25000.00 | 0.0004 |
| 293.14 | 30000.00 | 0.0005 |
| 293.14 | 35000.00 | 0.0005 |
| 293.14 | 40000.00 | 0.0005 |
| 303.14 | 1000.00 | 0.0003 |
| 303.14 | 5000.00 | 0.0003 |
| 303.14 | 10000.00 | 0.0003 |
| 303.14 | 15000.00 | 0.0003 |
| 303.14 | 20000.00 | 0.0004 |
| 303.14 | 25000.00 | 0.0004 |
| 303.14 | 30000.00 | 0.0004 |
| 303.14 | 35000.00 | 0.0004 |
| 303.14 | 40000.00 | 0.0005 |
| 313.14 | 1000.00 | 0.0002 |
| 313.14 | 5000.00 | 0.0003 |
| 313.14 | 10000.00 | 0.0003 |
| 313.14 | 15000.00 | 0.0003 |
| 313.14 | 20000.00 | 0.0003 |
| 313.14 | 25000.00 | 0.0003 |
| 313.14 | 30000.00 | 0.0004 |
| 313.14 | 35000.00 | 0.0004 |
| 313.14 | 40000.00 | 0.0004 |
| 323.13 | 1000.00 | 0.0002 |
| 323.13 | 5000.00 | 0.0002 |
| 323.13 | 10000.00 | 0.0003 |
| 323.13 | 15000.00 | 0.0003 |
| 323.13 | 20000.00 | 0.0003 |
| 323.13 | 25000.00 | 0.0003 |
| 323.13 | 30000.00 | 0.0003 |
| 323.13 | 35000.00 | 0.0004 |
| 323.13 | 40000.00 | 0.0004 |
| 333.13 | 1000.00 | 0.0002 |
| 333.13 | 5000.00 | 0.0002 |
| 333.13 | 10000.00 | 0.0002 |
| 333.13 | 15000.00 | 0.0002 |
| 333.13 | 20000.00 | 0.0003 |
| 333.13 | 25000.00 | 0.0003 |
| 333.13 | 30000.00 | 0.0003 |
| 333.13 | 35000.00 | 0.0003 |
| 333.13 | 40000.00 | 0.0003 |
| 343.13 | 2000.00 | 0.0002 |
| 343.13 | 5000.00 | 0.0002 |
| 343.13 | 10000.00 | 0.0002 |
| 343.13 | 15000.00 | 0.0002 |
| 343.13 | 20000.00 | 0.0002 |
| 343.13 | 25000.00 | 0.0003 |
| 343.13 | 30000.00 | 0.0003 |
| 343.13 | 35000.00 | 0.0003 |
| 343.13 | 40000.00 | 0.0003 |
| 353.13 | 2000.00 | 0.0001 |
| 353.13 | 5000.00 | 0.0002 |
| 353.13 | 10000.00 | 0.0002 |
| 353.13 | 15000.00 | 0.0002 |
| 353.13 | 20000.00 | 0.0002 |
| 353.13 | 25000.00 | 0.0002 |
| 353.13 | 30000.00 | 0.0003 |
| 353.13 | 35000.00 | 0.0003 |
| 353.13 | 40000.00 | 0.0003 |
| 363.14 | 2000.00 | 0.0001 |
| 363.14 | 5000.00 | 0.0001 |
| 363.14 | 10000.00 | 0.0002 |
| 363.14 | 15000.00 | 0.0002 |
| 363.14 | 20000.00 | 0.0002 |
| 363.14 | 25000.00 | 0.0002 |
| 363.14 | 30000.00 | 0.0002 |
| 363.14 | 35000.00 | 0.0003 |
| 363.14 | 40000.00 | 0.0003 |
| 373.14 | 2000.00 | 0.0001 |
| 373.14 | 5000.00 | 0.0001 |
| 373.14 | 10000.00 | 0.0002 |
| 373.14 | 15000.00 | 0.0002 |
| 373.14 | 20000.00 | 0.0002 |
| 373.14 | 25000.00 | 0.0002 |
| 373.14 | 30000.00 | 0.0002 |
| 373.14 | 35000.00 | 0.0002 |
| 373.14 | 40000.00 | 0.0002 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.38 | 1000.00 | 1380.41 |
| 293.38 | 3000.00 | 1389.7 |
| 293.38 | 5000.00 | 1398.14 |
| 293.38 | 10000.00 | 1417.22 |
| 293.38 | 15000.00 | 1434.22 |
| 293.38 | 20000.00 | 1449.45 |
| 293.38 | 25000.00 | 1463.39 |
| 293.38 | 30000.00 | 1476.18 |
| 293.38 | 35000.00 | 1488.18 |
| 293.38 | 40000.00 | 1499.36 |
| 293.38 | 50000.00 | 1519.84 |
| 293.38 | 60000.00 | 1538.35 |
| 293.38 | 70000.00 | 1555.2 |
| 303.23 | 1000.00 | 1346.41 |
| 303.23 | 3000.00 | 1356.85 |
| 303.23 | 5000.00 | 1366.62 |
| 303.23 | 10000.00 | 1388.23 |
| 303.23 | 15000.00 | 1407.04 |
| 303.23 | 20000.00 | 1423.79 |
| 303.23 | 25000.00 | 1438.88 |
| 303.23 | 30000.00 | 1452.75 |
| 303.23 | 35000.00 | 1465.54 |
| 303.23 | 40000.00 | 1477.52 |
| 303.23 | 50000.00 | 1499.35 |
| 303.23 | 60000.00 | 1518.78 |
| 303.23 | 70000.00 | 1536.58 |
| 313.10 | 1000.00 | 1310.15 |
| 313.10 | 3000.00 | 1322.54 |
| 313.10 | 5000.00 | 1333.75 |
| 313.10 | 10000.00 | 1358.32 |
| 313.10 | 15000.00 | 1379.33 |
| 313.10 | 20000.00 | 1397.77 |
| 313.10 | 25000.00 | 1414.16 |
| 313.10 | 30000.00 | 1429.13 |
| 313.10 | 35000.00 | 1442.8 |
| 313.10 | 40000.00 | 1455.53 |
| 313.10 | 50000.00 | 1478.52 |
| 313.10 | 60000.00 | 1499.21 |
| 313.10 | 70000.00 | 1517.63 |
| 322.94 | 1000.00 | 1272.73 |
| 322.94 | 3000.00 | 1287.52 |
| 322.94 | 5000.00 | 1300.71 |
| 322.94 | 10000.00 | 1328.74 |
| 322.94 | 15000.00 | 1352.16 |
| 322.94 | 20000.00 | 1372.4 |
| 322.94 | 25000.00 | 1390.33 |
| 322.94 | 30000.00 | 1406.5 |
| 322.94 | 35000.00 | 1421.01 |
| 322.94 | 40000.00 | 1434.57 |
| 322.94 | 50000.00 | 1459.05 |
| 322.94 | 60000.00 | 1480.75 |
| 322.94 | 70000.00 | 1500.21 |
| 333.06 | 1000.00 | 1230.59 |
| 333.06 | 3000.00 | 1248.74 |
| 333.06 | 5000.00 | 1264.58 |
| 333.06 | 10000.00 | 1297.09 |
| 333.06 | 15000.00 | 1323.56 |
| 333.06 | 20000.00 | 1345.92 |
| 333.06 | 25000.00 | 1365.48 |
| 333.06 | 30000.00 | 1382.82 |
| 333.06 | 35000.00 | 1398.61 |
| 333.06 | 40000.00 | 1413.18 |
| 333.06 | 50000.00 | 1439.06 |
| 333.06 | 60000.00 | 1461.86 |
| 333.06 | 70000.00 | 1482.19 |
| 343.19 | 3000.00 | 1207.31 |
| 343.19 | 5000.00 | 1226.45 |
| 343.19 | 10000.00 | 1264.58 |
| 343.19 | 15000.00 | 1294.29 |
| 343.19 | 20000.00 | 1319.04 |
| 343.19 | 25000.00 | 1340.43 |
| 343.19 | 30000.00 | 1359.27 |
| 343.19 | 35000.00 | 1376.24 |
| 343.19 | 40000.00 | 1391.75 |
| 343.19 | 50000.00 | 1419.24 |
| 343.19 | 60000.00 | 1443.29 |
| 343.19 | 70000.00 | 1464.6 |
| 353.23 | 3000.00 | 1161.43 |
| 353.23 | 5000.00 | 1185.57 |
| 353.23 | 10000.00 | 1230.77 |
| 353.23 | 15000.00 | 1264.63 |
| 353.23 | 20000.00 | 1292.08 |
| 353.23 | 25000.00 | 1315.3 |
| 353.23 | 30000.00 | 1335.89 |
| 353.23 | 35000.00 | 1354.11 |
| 353.23 | 40000.00 | 1370.58 |
| 353.23 | 50000.00 | 1399.7 |
| 353.23 | 60000.00 | 1424.96 |
| 353.23 | 70000.00 | 1447.34 |
| 363.22 | 5000.00 | 1140.64 |
| 363.22 | 10000.00 | 1195.26 |
| 363.22 | 15000.00 | 1233.73 |
| 363.22 | 20000.00 | 1264.17 |
| 363.22 | 25000.00 | 1289.66 |
| 363.22 | 30000.00 | 1311.7 |
| 363.22 | 35000.00 | 1331.22 |
| 363.22 | 40000.00 | 1348.77 |
| 363.22 | 50000.00 | 1379.54 |
| 363.22 | 60000.00 | 1406.01 |
| 363.22 | 70000.00 | 1429.34 |
| 373.17 | 5000.00 | 1091.26 |
| 373.17 | 10000.00 | 1158.13 |
| 373.17 | 15000.00 | 1202.21 |
| 373.17 | 20000.00 | 1236.05 |
| 373.17 | 25000.00 | 1263.9 |
| 373.17 | 30000.00 | 1287.72 |
| 373.17 | 35000.00 | 1308.62 |
| 373.17 | 40000.00 | 1327.34 |
| 373.17 | 50000.00 | 1359.88 |
| 373.17 | 60000.00 | 1387.66 |
| 373.17 | 70000.00 | 1412.03 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Thermal conductivity, W/m/K - Liquid |
| 252.57 | 10000.00 | 0.0912 |
| 252.80 | 5000.00 | 0.0891 |
| 252.87 | 100.00 | 0.0873 |
| 252.92 | 10000.00 | 0.0914 |
| 253.16 | 5000.00 | 0.0887 |
| 253.24 | 20000.00 | 0.0955 |
| 253.38 | 100.00 | 0.0872 |
| 253.41 | 30000.00 | 0.0972 |
| 253.47 | 20000.00 | 0.0949 |
| 253.51 | 20000.00 | 0.0952 |
| 253.60 | 10000.00 | 0.0911 |
| 253.65 | 5000.00 | 0.0891 |
| 253.66 | 100.00 | 0.0872 |
| 253.86 | 30000.00 | 0.0971 |
| 255.05 | 30000.00 | 0.0973 |
| 272.91 | 30000.00 | 0.0926 |
| 273.36 | 10000.00 | 0.0847 |
| 273.45 | 20000.00 | 0.0896 |
| 273.49 | 1000.00 | 0.0814 |
| 273.66 | 10000.00 | 0.0851 |
| 273.82 | 5000.00 | 0.0833 |
| 273.85 | 1000.00 | 0.0810 |
| 273.86 | 1000.00 | 0.0812 |
| 273.95 | 30000.00 | 0.0929 |
| 274.06 | 20000.00 | 0.0895 |
| 274.16 | 5000.00 | 0.0832 |
| 274.27 | 10000.00 | 0.0855 |
| 274.33 | 30000.00 | 0.0927 |
| 274.57 | 20000.00 | 0.0892 |
| 274.63 | 5000.00 | 0.0835 |
| 293.15 | 10000.00 | 0.0802 |
| 293.22 | 1000.00 | 0.0762 |
| 293.42 | 30000.00 | 0.0894 |
| 293.49 | 1000.00 | 0.0767 |
| 293.61 | 5000.00 | 0.0782 |
| 293.65 | 10000.00 | 0.0805 |
| 293.76 | 5000.00 | 0.0781 |
| 293.76 | 30000.00 | 0.0891 |
| 293.85 | 10000.00 | 0.0802 |
| 293.95 | 5000.00 | 0.0783 |
| 294.47 | 1000.00 | 0.0764 |
| 294.54 | 30000.00 | 0.0893 |
| 312.50 | 5000.00 | 0.0705 |
| 312.59 | 1000.00 | 0.0682 |
| 312.89 | 5000.00 | 0.0709 |
| 313.01 | 1000.00 | 0.0683 |
| 313.28 | 5000.00 | 0.0706 |
| 313.39 | 1000.00 | 0.0680 |
| 313.53 | 20000.00 | 0.0809 |
| 313.55 | 10000.00 | 0.0757 |
| 313.85 | 10000.00 | 0.0761 |
| 313.86 | 30000.00 | 0.0853 |
| 314.04 | 10000.00 | 0.0758 |
| 314.06 | 30000.00 | 0.0850 |
| 314.20 | 20000.00 | 0.0809 |
| 315.13 | 20000.00 | 0.0815 |
| 315.13 | 30000.00 | 0.0852 |
| 332.48 | 10000.00 | 0.0699 |
| 332.49 | 5000.00 | 0.0654 |
| 332.51 | 1000.00 | 0.0623 |
| 332.72 | 30000.00 | 0.0805 |
| 332.79 | 20000.00 | 0.0756 |
| 332.84 | 30000.00 | 0.0813 |
| 332.85 | 10000.00 | 0.0695 |
| 332.87 | 1000.00 | 0.0624 |
| 332.89 | 5000.00 | 0.0651 |
| 333.20 | 10000.00 | 0.0695 |
| 333.24 | 1000.00 | 0.0623 |
| 333.26 | 5000.00 | 0.0648 |
| 333.48 | 30000.00 | 0.0802 |
| 333.59 | 20000.00 | 0.0755 |
| 334.42 | 20000.00 | 0.0761 |
| 353.02 | 30000.00 | 0.0749 |
| 353.17 | 10000.00 | 0.0636 |
| 353.29 | 20000.00 | 0.0705 |
| 353.35 | 2000.00 | 0.0565 |
| 353.35 | 5000.00 | 0.0593 |
| 353.57 | 30000.00 | 0.0744 |
| 353.68 | 2000.00 | 0.0564 |
| 353.74 | 5000.00 | 0.0592 |
| 353.74 | 20000.00 | 0.0701 |
| 353.82 | 10000.00 | 0.0635 |
| 353.95 | 30000.00 | 0.0741 |
| 354.09 | 20000.00 | 0.0699 |
| 354.12 | 2000.00 | 0.0560 |
| 354.24 | 10000.00 | 0.0633 |
| 354.40 | 5000.00 | 0.0594 |
| 373.08 | 10000.00 | 0.0597 |
| 373.15 | 30000.00 | 0.0726 |
| 373.22 | 5000.00 | 0.0554 |
| 373.40 | 20000.00 | 0.0672 |
| 373.46 | 3000.00 | 0.0525 |
| 373.56 | 10000.00 | 0.0596 |
| 373.72 | 5000.00 | 0.0559 |
| 373.80 | 30000.00 | 0.0727 |
| 373.84 | 3000.00 | 0.0524 |
| 373.87 | 20000.00 | 0.0677 |
| 374.10 | 10000.00 | 0.0601 |
| 374.21 | 30000.00 | 0.0724 |
| 374.24 | 5000.00 | 0.0557 |
| 374.26 | 3000.00 | 0.0526 |
| 374.57 | 20000.00 | 0.0672 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [115.40; 219.46] | 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 | -1.22390e+01 | |||
| Coefficient B | 6.11200e-01 | |||
| Coefficient C | -5.81400e-04 | |||
| Coefficient D | 2.01900e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 115.40 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 140.16 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 160.14 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 175.96 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 188.27 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 197.71 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 204.90 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 210.50 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 215.14 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 219.46 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 2971.58] | kPa | [203.00; 398.07] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.36658e+01 | |||
| Coefficient B | -1.91902e+03 | |||
| Coefficient C | -5.95530e+01 | |||
| Temperature range, min. | 203.00 | |||
| Temperature range, max. | 398.07 | |||
| Pvap | 1.33 | kPa | 203.00 | Calculated Property |
| Pvap | 7.72 | kPa | 224.67 | Calculated Property |
| Pvap | 29.74 | kPa | 246.35 | Calculated Property |
| Pvap | 86.53 | kPa | 268.02 | Calculated Property |
| Pvap | 205.91 | kPa | 289.70 | Calculated Property |
| Pvap | 422.05 | kPa | 311.37 | Calculated Property |
| Pvap | 772.06 | kPa | 333.05 | Calculated Property |
| Pvap | 1292.46 | kPa | 354.72 | Calculated Property |
| Pvap | 2016.37 | kPa | 376.40 | Calculated Property |
| Pvap | 2971.58 | kPa | 398.07 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 1,1,1,3,3,3-hexafluoro-.
Mixtures
- Formamide, N,N-dimethyl- + Propane, 1,1,1,3,3,3-hexafluoro-
- 2-Pyrrolidinone, 1-methyl- + Propane, 1,1,1,3,3,3-hexafluoro-
- Propane, 1,1,1,3,3,3-hexafluoro- + N,N-Dimethylacetamide
- Ethane, 1,1'-oxybis[2-methoxy- + Propane, 1,1,1,3,3,3-hexafluoro-
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Vapor pressures of 1,1,1,2,3,3,3-heptafluoropropane, 1,1,1,3,3,3-hexafluoropropane and 1,1,1,3,3-pentafluoropropane
- Thermal conductivity of liquid 1,1,1,3,3,3-hexafluoropropane (HFC-236fa) from 253 K to 373 K and pressure up to 30 MPa
- Compressed liquid densities of 1,1,1,3,3-pentafluoropropane (HFC-245fa) and 1,1,1,3,3,3-hexafluoropropane (HFC-236fa)
- Isothermal vapor-liquid equilibrium measurements and assessments of 1,1,1,3,3,3-hexafluoropropane+N,N-dimethylformamide/N-methyl-2-pyrrolidone working pairs for absorption power cycles
- Isobaric heat capacities of R245fa and R236fa in liquid phase at temperatures from (315 to 365) K and pressures up to 5.5 MPa
- Solubilities and diffusivities of R227ea, R236fa and R245fa in 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide
- Compressed Liquid Viscosity of 1,1,1,3,3-Pentafluoropropane (R245fa) and 1,1,1,3,3,3-Hexafluoropropane (R236fa)
- Measurement and Correlation of Isothermal Vapor Liquid Equilibrium of 1,1,1,3,3-Pentafluoropropane + N,N-Dimethylacetamide and 1,1,1,3,3,3-Hexafluoropropane + N,N-Dimethylacetamide/Diethylene Glycol Dimethyl Ether Systems
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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