- InChI
- InChI=1S/C7F8/c8-2-1(7(13,14)15)3(9)5(11)6(12)4(2)10
- InChI Key
- USPWUOFNOTUBAD-UHFFFAOYSA-N
- Formula
- C7F8
- SMILES
- Fc1c(F)c(F)c(C(F)(F)F)c(F)c1F
- Molecular Weight1
- 236.06
- CAS
- 434-64-0
- Other Names
-
- (Trifluoromethyl)pentafluorobenzene
- OCTAFLUOROTOLUENE
- Pentafluoro(trifluoro-methyl)benzene
- Perfluorotoluene
- Toluene, octafluoro-
- pentafluoro(trifluoromethyl)benzene
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase 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).
- 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).
- ρc : Critical density (kg/m3).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- 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).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4750 | KDB | |
| EA | [0.86; 1.70] | eV |
|
| EA | 0.86 ± 0.11 | eV | NIST |
| EA | 1.70 ± 0.30 | eV | NIST |
| ΔfG° | -1483.32 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1269.40 ± 7.80 | kJ/mol | NIST |
| ΔfH°liquid | -1311.10 ± 7.80 | kJ/mol | NIST |
| ΔfusH° | 23.21 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [40.40; 41.60] | kJ/mol |
|
| ΔvapH° | 40.50 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 40.40 | kJ/mol | NIST |
| ΔvapH° | 41.60 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 41.60 ± 0.20 | kJ/mol | NIST |
| IE | [9.90; 10.54] | eV |
|
| IE | 10.20 | eV | NIST |
| IE | 10.40 ± 0.10 | eV | NIST |
| IE | 10.54 | eV | NIST |
| IE | 9.90 | eV | NIST |
| log10WS | -4.23 | Crippen Calculated Property | |
| logPoct/wat | 3.401 | Crippen Calculated Property | |
| McVol | 99.890 | ml/mol | McGowan Calculated Property |
| Pc | [2680.00; 2705.00] | kPa |
|
| Pc | 2705.00 | kPa | KDB |
| Pc | 2680.00 | kPa | NIST |
| Pc | 2705.00 ± 4.00 | kPa | NIST |
| ρc | 551.91 ± 0.54 | kg/m3 | NIST |
| S°liquid | [355.50; 360.10] | J/mol×K |
|
| S°liquid | 360.10 | J/mol×K | NIST |
| S°liquid | 355.50 | J/mol×K | NIST |
| Tboil | [377.00; 377.73] | K |
|
| Tboil | 377.73 | K | KDB |
| Tboil | 377.00 ± 1.00 | K | NIST |
| Tboil | 377.20 | K | NIST |
| Tc | [534.40; 534.47] | K |
|
| Tc | 534.47 | K | KDB |
| Tc | 534.40 | K | NIST |
| Tc | 534.47 ± 0.20 | K | NIST |
| Tc | 534.47 ± 0.05 | K | NIST |
| Tfus | 207.50 | K | KDB |
| Ttriple | [207.62; 207.69] | K |
|
| Ttriple | 207.62 ± 0.02 | K | NIST |
| Ttriple | 207.69 ± 0.02 | K | NIST |
| Vc | 0.428 | m3/kmol | KDB |
| Zc | 0.2605260 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [212.76; 248.31] | J/mol×K | [402.07; 553.75] |
|
| Cp,gas | 212.76 | J/mol×K | 402.07 | Joback Calculated Property |
| Cp,gas | 219.42 | J/mol×K | 427.35 | Joback Calculated Property |
| Cp,gas | 225.78 | J/mol×K | 452.63 | Joback Calculated Property |
| Cp,gas | 231.84 | J/mol×K | 477.91 | Joback Calculated Property |
| Cp,gas | 237.61 | J/mol×K | 503.19 | Joback Calculated Property |
| Cp,gas | 243.09 | J/mol×K | 528.47 | Joback Calculated Property |
| Cp,gas | 248.31 | J/mol×K | 553.75 | Joback Calculated Property |
| Cp,liquid | [262.30; 266.40] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 266.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 262.30 | J/mol×K | 298.15 | NIST |
| ΔfusH | [11.49; 11.58] | kJ/mol | [207.00; 207.69] |
|
| ΔfusH | 11.49 | kJ/mol | 207.00 | NIST |
| ΔfusH | 11.49 | kJ/mol | 207.00 | NIST |
| ΔfusH | 11.58 | kJ/mol | 207.62 | NIST |
| ΔfusH | 11.49 | kJ/mol | 207.69 | NIST |
| ΔvapH | [40.00; 40.90] | kJ/mol | [330.50; 334.50] |
|
| ΔvapH | 40.90 | kJ/mol | 330.50 | NIST |
| ΔvapH | 40.00 | kJ/mol | 334.50 | NIST |
| ν | [0.0000005; 0.0000006] | m2/s | [298.15; 318.15] |
|
| ν | 0.0000006 | m2/s | 298.15 | Viscosi... |
| ν | 0.0000006 | m2/s | 303.15 | Viscosi... |
| ν | 0.0000005 | m2/s | 308.15 | Viscosi... |
| ν | 0.0000005 | m2/s | 313.15 | Viscosi... |
| ν | 0.0000005 | m2/s | 318.15 | Viscosi... |
| Pvap | [2.18; 21.31] | kPa | [288.23; 333.93] |
|
| Pvap | 2.18 | kPa | 288.23 | Densiti... |
| Pvap | 2.95 | kPa | 293.20 | Densiti... |
| Pvap | 3.87 | kPa | 298.28 | Densiti... |
| Pvap | 5.09 | kPa | 303.18 | Densiti... |
| Pvap | 6.54 | kPa | 308.15 | Densiti... |
| Pvap | 8.43 | kPa | 313.15 | Densiti... |
| Pvap | 10.69 | kPa | 318.15 | Densiti... |
| Pvap | 13.38 | kPa | 323.15 | Densiti... |
| Pvap | 16.86 | kPa | 328.45 | Densiti... |
| Pvap | 21.31 | kPa | 333.93 | Densiti... |
| ΔfusS | 55.32 | J/mol×K | 207.69 | NIST |
| γ | [0.02; 0.02] | N/m | [287.15; 318.85] |
|
| γ | 0.02 | N/m | 287.15 | Surface... |
| γ | 0.02 | N/m | 293.15 | Surface... |
| γ | 0.02 | N/m | 298.25 | Surface... |
| γ | 0.02 | N/m | 303.35 | Surface... |
| γ | 0.02 | N/m | 308.55 | Surface... |
| γ | 0.02 | N/m | 313.75 | Surface... |
| γ | 0.02 | N/m | 318.85 | Surface... |
Similar Compounds
Find more compounds similar to Benzene, pentafluoro(trifluoromethyl)-.
Sources
- Crippen Method
- Crippen Method
- Densities and Vapor Pressures of Highly Fluorinated Compounds
- Surface Tension of Liquid Fluorocompounds
- Viscosities of Liquid Fluorocompounds
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.