- InChI
- InChI=1S/C6F14/c7-1(8,3(11,12)5(15,16)17)2(9,10)4(13,14)6(18,19)20
- InChI Key
- ZJIJAJXFLBMLCK-UHFFFAOYSA-N
- Formula
- C6F14
- SMILES
-
FC(F)(F)C(F)(F)C(F)(F)C(F)(F)C
(F)(F)C(F)(F)F - Molecular Weight1
- 338.04
- CAS
- 355-42-0
- Other Names
-
- AF 0150
- Fluorinert FC72
- Flutec PP1
- Hexane, 1,1,1,2,2,3,3,4,4,5,5,6,6,6-tetradecafluoro-
- PERFLUORO-N-HEXANE
- PERFLUOROHEXANE
- PP 1 (Fluorocarbon)
- Perflexane
- Perfluoro-compound FC-72
- TETRADECAFLUOROHEXANE
- flutec PP 1
- n-Perfluorohexane
- n-Tetradecafluorohexane
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- 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).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5140 | KDB | |
| ΔfG° | -2710.66 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -2965.21 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 9.93 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [31.40; 32.50] | kJ/mol |
|
| ΔvapH° | 32.50 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 31.40 | kJ/mol | NIST |
| ΔvapH° | 32.40 | kJ/mol | NIST |
| log10WS | -4.91 | Crippen Calculated Property | |
| logPoct/wat | 4.652 | Crippen Calculated Property | |
| McVol | 120.180 | ml/mol | McGowan Calculated Property |
| Pc | [1868.00; 1905.00] | kPa |
|
| Pc | 1868.00 | kPa | KDB |
| Pc | 1868.13 ± 20.00 | kPa | NIST |
| Pc | 1905.00 | kPa | NIST |
| Pc | 1868.10 ± 3.44 | kPa | NIST |
| ρc | [557.77; 557.77] | kg/m3 |
|
| ρc | 557.77 ± 3.04 | kg/m3 | NIST |
| ρc | 557.77 ± 5.58 | kg/m3 | NIST |
| Tboil | [329.80; 332.50] | K |
|
| Tboil | 329.80 | K | KDB |
| Tboil | 332.20 | K | NIST |
| Tboil | 332.50 ± 0.50 | K | NIST |
| Tboil | 330.30 | K | NIST |
| Tc | [447.65; 451.70] | K |
|
| Tc | 448.77 | K | KDB |
| Tc | 448.77 ± 1.30 | K | NIST |
| Tc | 449.00 | K | NIST |
| Tc | 448.77 ± 0.20 | K | NIST |
| Tc | Outlier 451.70 ± 0.50 | K | NIST |
| Tc | 447.65 ± 0.50 | K | NIST |
| Tfus | [182.50; 187.10] | K |
|
| Tfus | 186.00 | K | KDB |
| Tfus | 182.50 ± 0.50 | K | NIST |
| Tfus | 185.00 ± 1.00 | K | NIST |
| Tfus | 186.89 ± 0.06 | K | NIST |
| Tfus | 187.10 ± 0.10 | K | NIST |
| Ttriple | [185.00; 187.45] | K |
|
| Ttriple | 185.00 ± 2.00 | K | NIST |
| Ttriple | 187.45 ± 0.30 | K | NIST |
| Vc | 0.606 | m3/kmol | KDB |
| Zc | 0.3033810 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [263.70; 328.86] | J/mol×K | [307.08; 418.08] |
|
| Cp,gas | 263.70 | J/mol×K | 307.08 | Joback Calculated Property |
| Cp,gas | 276.21 | J/mol×K | 325.58 | Joback Calculated Property |
| Cp,gas | 288.03 | J/mol×K | 344.08 | Joback Calculated Property |
| Cp,gas | 299.18 | J/mol×K | 362.58 | Joback Calculated Property |
| Cp,gas | 309.69 | J/mol×K | 381.08 | Joback Calculated Property |
| Cp,gas | 319.57 | J/mol×K | 399.58 | Joback Calculated Property |
| Cp,gas | 328.86 | J/mol×K | 418.08 | Joback Calculated Property |
| Cp,liquid | [240.20; 248.00] | J/mol×K | [273.00; 273.00] |
|
| Cp,liquid | 240.20 | J/mol×K | 273.00 | NIST |
| Cp,liquid | 248.00 | J/mol×K | 273.00 | NIST |
| ΔfusH | 6.84 | kJ/mol | 185.00 | NIST |
| ΔvapH | [31.50; 34.40] | kJ/mol | [297.50; 441.00] |
|
| ΔvapH | 34.40 | kJ/mol | 297.50 | NIST |
| ΔvapH | 31.50 | kJ/mol | 316.50 | NIST |
| ΔvapH | 33.40 | kJ/mol | 441.00 | NIST |
| ν | [0.0000003; 0.0000004] | m2/s | [298.15; 318.15] |
|
| ν | 0.0000004 | m2/s | 298.15 | Viscosi... |
| ν | 0.0000004 | m2/s | 303.15 | Viscosi... |
| ν | 0.0000004 | m2/s | 308.15 | Viscosi... |
| ν | 0.0000004 | m2/s | 313.15 | Viscosi... |
| ν | 0.0000003 | m2/s | 318.15 | Viscosi... |
| Pvap | [18.78; 111.39] | kPa | [288.31; 333.10] |
|
| Pvap | 18.78 | kPa | 288.31 | Densiti... |
| Pvap | 23.58 | kPa | 293.22 | Densiti... |
| Pvap | 29.28 | kPa | 298.09 | Densiti... |
| Pvap | 36.19 | kPa | 302.98 | Densiti... |
| Pvap | 44.38 | kPa | 307.97 | Densiti... |
| Pvap | 54.56 | kPa | 313.17 | Densiti... |
| Pvap | 65.86 | kPa | 318.15 | Densiti... |
| Pvap | 78.91 | kPa | 323.13 | Densiti... |
| Pvap | 94.08 | kPa | 328.11 | Densiti... |
| Pvap | 111.39 | kPa | 333.10 | Densiti... |
| ρl | [1590.50; 1742.50] | kg/m3 | [278.15; 328.15] |
|
| ρl | 1742.50 | kg/m3 | 278.15 | Liquid ... |
| ρl | 1728.30 | kg/m3 | 283.15 | Liquid ... |
| ρl | 1713.80 | kg/m3 | 288.15 | Liquid ... |
| ρl | 1699.20 | kg/m3 | 293.15 | Liquid ... |
| ρl | 1701.00 | kg/m3 | 298.15 | VLE mea... |
| ρl | 1667.00 | kg/m3 | 298.15 | Phase E... |
| ρl | 1684.40 | kg/m3 | 298.15 | Liquid ... |
| ρl | 1670.07 | kg/m3 | 298.15 | Liquid-... |
| ρl | 1669.40 | kg/m3 | 303.15 | Liquid ... |
| ρl | 1654.10 | kg/m3 | 308.15 | Liquid ... |
| ρl | 1638.60 | kg/m3 | 313.15 | Liquid ... |
| ρl | 1622.90 | kg/m3 | 318.15 | Liquid ... |
| ρl | 1606.40 | kg/m3 | 323.15 | Liquid ... |
| ρl | 1590.50 | kg/m3 | 328.15 | Liquid ... |
| csound,fluid | [510.70; 571.89] | m/s | [278.15; 298.15] |
|
| csound,fluid | 571.89 | m/s | 278.15 | Propert... |
| csound,fluid | 540.31 | m/s | 288.15 | Propert... |
| csound,fluid | 510.70 | m/s | 298.15 | Propert... |
| γ | [0.01; 0.01] | N/m | [283.15; 308.15] |
|
| γ | 0.01 | N/m | 283.15 | Surface... |
| γ | 0.01 | N/m | 288.15 | Surface... |
| γ | 0.01 | N/m | 293.15 | Surface... |
| γ | 0.01 | N/m | 298.15 | Surface... |
| γ | 0.01 | N/m | 303.15 | Surface... |
| γ | 0.01 | N/m | 308.15 | Surface... |
Datasets
Molar volume, m3/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar volume, m3/mol - Liquid |
| 288.05 | 101.33 | 0.0002 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [243.80; 353.65] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49601e+01 | |||
| Coefficient B | -3.09560e+03 | |||
| Coefficient C | -3.28200e+01 | |||
| Temperature range, min. | 243.80 | |||
| Temperature range, max. | 353.65 | |||
| Pvap | 1.33 | kPa | 243.80 | Calculated Property |
| Pvap | 2.97 | kPa | 256.01 | Calculated Property |
| Pvap | 6.11 | kPa | 268.21 | Calculated Property |
| Pvap | 11.68 | kPa | 280.42 | Calculated Property |
| Pvap | 21.01 | kPa | 292.62 | Calculated Property |
| Pvap | 35.86 | kPa | 304.83 | Calculated Property |
| Pvap | 58.46 | kPa | 317.03 | Calculated Property |
| Pvap | 91.54 | kPa | 329.24 | Calculated Property |
| Pvap | 138.35 | kPa | 341.44 | Calculated Property |
| Pvap | 202.63 | kPa | 353.65 | Calculated Property |
| Pvap | [7.27; 1736.48] | kPa | [270.00; 445.42] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.25737e+02 | |||
| Coefficient B | -7.95388e+03 | |||
| Coefficient C | -1.70953e+01 | |||
| Coefficient D | 1.93783e-05 | |||
| Temperature range, min. | 270.00 | |||
| Temperature range, max. | 445.42 | |||
| Pvap | 7.27 | kPa | 270.00 | Calculated Property |
| Pvap | 19.82 | kPa | 289.49 | Calculated Property |
| Pvap | 46.16 | kPa | 308.98 | Calculated Property |
| Pvap | 95.08 | kPa | 328.47 | Calculated Property |
| Pvap | 177.88 | kPa | 347.96 | Calculated Property |
| Pvap | 308.62 | kPa | 367.46 | Calculated Property |
| Pvap | 504.63 | kPa | 386.95 | Calculated Property |
| Pvap | 787.70 | kPa | 406.44 | Calculated Property |
| Pvap | 1185.92 | kPa | 425.93 | Calculated Property |
| Pvap | 1736.48 | kPa | 445.42 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexane, tetradecafluoro-.
Mixtures
- Hexane, tetradecafluoro- + 1H,1H,7H-Dodecafluoro-1-heptanol
- n-Hexane + Hexane, tetradecafluoro-
- Hexane, tetradecafluoro- + Octane
- Hexane, tetradecafluoro- + Tetrafluoromethane
- Hexane, tetradecafluoro- + Pentane
- Hexane, tetradecafluoro- + Heptane
- Heptane, 2-methyl- + Hexane, tetradecafluoro-
- Hexane, tetradecafluoro- + Cyclohexane
- Hexane, tetradecafluoro- + Ethane, hexafluoro-
- 2-Propanol, 1,1,1,3,3,3-hexafluoro- + Hexane, tetradecafluoro- + Water
- 2-Propanol, 1,1,1,3,3,3-hexafluoro- + Hexane, tetradecafluoro- + Methyl Alcohol
- Hexane, tetradecafluoro- + Methyl Alcohol
- Hexane, tetradecafluoro- + Acetone
- Toluene + Hexane, tetradecafluoro-
- Hexane, tetradecafluoro- + Carbon dioxide + Methyl Alcohol
- Hexane, tetradecafluoro- + Carbon dioxide + Acetone
- Toluene + Hexane, tetradecafluoro- + Carbon dioxide
- Hexane, tetradecafluoro- + Di-n-propyl ether
- Hexane, tetradecafluoro- + n-Butyl ether
- Hexane, tetradecafluoro- + Butane, 1-methoxy-
Find more mixtures with Hexane, tetradecafluoro-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Liquid-Liquid Coexistence Curve of n-Perfluorohexane - n-Hexane System
- Vapor liquid liquid equilibria of perfluorohexane +CO2 + methanol, +toluene, and +acetone at 313K
- Liquid liquid equilibrium of (1H,1H,7H-perfluoroheptan-1-ol + perfluoroalkane) binary mixtures
- Thermodynamic study of perfluorohexane + ether mixtures VLE, LLE, and HE
- Properties of saturated fluorocarbons: Experimental data and modeling using perturbed-chain-SAFT
- Liquid-liquid equilibrium data for binary perfluoroalkane (C6 and C8) + n-alkane systems
- Perfluoroalkanes and perfluoroalkylalkane surfactants in solution: Partial molar volumes in n-octane and hetero-SAFT-VR modelling
- Liquid-liquid equilibria containing fluorous solvents as environmentally benign solvent
- Viscosity of liquid systems involving hydrogenated and fluorinated substances: Liquid mixtures of (hexane + perfluorohexane)
- VLE measurements and modelling for the binary systems of (CF4 + C6F14) and (CF4 + C8F18)
- New experimental VLE data for the binary mixture of carbon dioxide + perfluorohexane (CO2 + C6F14) from 273 K to 333 K
- Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
- Isothermal Vapor-Liquid Equilibrium (VLE) and Vapor- Liquid-Liquid Equilibrium (VLLE) Data for Two Binary Systems Containing Perfluorohexane with Carbon Monoxide or Hydrogen Sulphide at (293, 313 and 333) K
- Phase Equilibria for Perfluoroethane + (n-Perfluorohexane or n-Perfluorooctane) Binary Systems: Measurement and Modeling
- Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
- High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
- Densities and Vapor Pressures of Highly Fluorinated Compounds
- Surface Tension of Liquid Fluorocompounds
- Liquid - Liquid Equilibria for the Ternary Systems of Per fl uorohexane + Methyl Nona fl uorobutyl Ether + Toluene, + 1,4-Dioxane, or + Dimethylformamide at 298.15 K
- Liquid Liquid Equilibria for the Ternary Systems of Perfluorohexane or Perfluamine + Hydrofluoroether + Tetrahydrofuran at 298.15 K or 273.15 K
- Liquid Liquid Equilibria for the Ternary Systems of FC3283 + HFE7300 + Hexane, FC3283 + HFE7500 + Octane, and FC72 + HFE7100 + (Acetonitrile or Ethyl Acetate) at 273.15 K, 298.15 K, and 313.15 K
- Liquid Liquid Equilibria in Ternary Systems of Hexafluoroisopropanol + Perfluorocarbon + Water or Methanol at 298.15 K
- Viscosities of Liquid Fluorocompounds
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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