- InChI
- InChI=1S/CCl3F/c2-1(3,4)5
- InChI Key
- CYRMSUTZVYGINF-UHFFFAOYSA-N
- Formula
- CCl3F
- SMILES
- FC(Cl)(Cl)Cl
- Molecular Weight1
- 137.37
- CAS
- 75-69-4
- Other Names
-
- ARCTON 9
- Algofrene Type 1
- Arcton 11
- CCl3F
- CFCl3
- Chladone 11
- Chlorofluoromethane (CCl3F)
- Daiflon 11
- Daiflon S 1
- Distillex DS6
- Dymel 11
- Electro-CF 11
- F 11
- F 11 (halocarbon)
- F 11B
- FC 11
- FC 11, Halocarbon
- FKW 11
- Fluon 11
- Fluorocarbon 11
- Fluorochloroform
- Fluorotrichloromethane
- Freon 11
- Freon 11A
- Freon MF
- Frigen 11
- Frigen 11A
- Frigen S 11
- Genetron 11
- Genetron 11SBA
- Halon 11
- Isceon 131
- Isotron 11
- Kaltron 11
- Khladon 11
- Ledon 11
- Methane, fluorotrichloro-
- Methane, trichlorofluoro-
- Monofluorotrichloromethane
- Propellant 11
- R 11
- R 11, Halocarbon
- R-11
- REFRIGERANT-11
- Refrigerant 11
- Refrigerant R11
- Trichlorofluorocarbon
- Trichlorofluoromethane
- Trichloromethyl fluoride
- Triclorofluormethane
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- EA : Electron affinity (eV).
- 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).
- IE : Ionization energy (eV).
- 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- 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).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- 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.
- Zra : Rackett Parameter.
- 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 | 0.1890 | KDB | |
| μ | 0.50 | debye | KDB |
| EA | [1.02; 1.10] | eV |
|
| EA | 1.02 | eV | NIST |
| EA | 1.10 ± 0.30 | eV | NIST |
| ΔfG° | -245.50 | kJ/mol | KDB |
| ΔfH°gas | [-290.00; -268.30] | kJ/mol |
|
| ΔfH°gas | -284.70 | kJ/mol | KDB |
| ΔfH°gas | -278.00 ± 8.80 | kJ/mol | NIST |
| ΔfH°gas | -268.30 ± 8.40 | kJ/mol | NIST |
| ΔfH°gas | -290.00 ± 20.00 | kJ/mol | NIST |
| ΔfusH° | 6.60 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 28.86 | kJ/mol | Joback Calculated Property |
| IE | [11.46; 11.90] | eV |
|
| IE | 11.68 ± 0.13 | eV | NIST |
| IE | 11.73 ± 0.02 | eV | NIST |
| IE | Outlier 11.46 ± 0.02 | eV | NIST |
| IE | 11.77 ± 0.01 | eV | NIST |
| IE | 11.77 ± 0.02 | eV | NIST |
| IE | 11.76 ± 0.01 | eV | NIST |
| IE | 11.85 | eV | NIST |
| IE | 11.90 | eV | NIST |
| log10WS | -2.15 | Crippen Calculated Property | |
| logPoct/wat | 2.284 | Crippen Calculated Property | |
| McVol | 63.440 | ml/mol | McGowan Calculated Property |
| Pc | [4370.00; 4466.00] | kPa |
|
| Pc | 4410.00 | kPa | KDB |
| Pc | 4466.00 ± 12.00 | kPa | NIST |
| Pc | 4370.00 ± 50.00 | kPa | NIST |
| Pc | 4405.73 | kPa | NIST |
| ρc | [553.59; 570.21] | kg/m3 |
|
| ρc | 570.21 ± 0.55 | kg/m3 | NIST |
| ρc | 553.59 ± 5.54 | kg/m3 | NIST |
| ρc | 553.59 ± 1.37 | kg/m3 | NIST |
| Inp | [460.00; 486.00] |
|
|
| Inp | 470.00 | NIST | |
| Inp | 485.00 | NIST | |
| Inp | 486.00 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | Outlier 460.00 | NIST | |
| Inp | 478.00 | NIST | |
| Inp | 478.00 | NIST | |
| Inp | 484.00 | NIST | |
| Inp | 482.00 | NIST | |
| Inp | 484.00 | NIST | |
| Inp | Outlier 460.00 | NIST | |
| Inp | 484.00 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 486.00 | NIST | |
| I | [605.00; 605.00] |
|
|
| I | 605.00 | NIST | |
| I | 605.00 | NIST | |
| S°liquid | 225.60 | J/mol×K | NIST |
| Tboil | [296.80; 296.92] | K |
|
| Tboil | 296.90 | K | KDB |
| Tboil | 296.90 | K | NIST |
| Tboil | 296.80 ± 0.05 | K | NIST |
| Tboil | 296.92 | K | NIST |
| Tc | [471.10; 471.20] | K |
|
| Tc | 471.20 | K | KDB |
| Tc | 471.10 ± 0.50 | K | NIST |
| Tc | 471.15 ± 0.10 | K | NIST |
| Tc | 471.15 ± 0.04 | K | NIST |
| Tc | 471.15 | K | NIST |
| Tc | 471.15 ± 0.40 | K | NIST |
| Tfus | [162.00; 165.40] | K |
|
| Tfus | 162.04 | K | KDB |
| Tfus | 162.00 ± 2.00 | K | NIST |
| Tfus | 162.72 ± 0.01 | K | NIST |
| Tfus | 162.70 ± 0.10 | K | NIST |
| Tfus | Outlier 165.40 ± 0.20 | K | NIST |
| Tfus | 162.67 ± 0.05 | K | NIST |
| Ttriple | [162.10; 162.70] | K |
|
| Ttriple | 162.19 ± 0.05 | K | NIST |
| Ttriple | 162.69 ± 0.06 | K | NIST |
| Ttriple | 162.67 ± 0.06 | K | NIST |
| Ttriple | 162.68 ± 0.03 | K | NIST |
| Ttriple | 162.65 ± 0.02 | K | NIST |
| Ttriple | 162.69 ± 0.03 | K | NIST |
| Ttriple | 162.70 ± 0.01 | K | NIST |
| Ttriple | Outlier 162.10 ± 0.20 | K | NIST |
| Ttriple | 162.68 ± 0.07 | K | NIST |
| Vc | [0.247; 0.248] | m3/kmol |
|
| Vc | 0.248 | m3/kmol | KDB |
| Vc | 0.247 ± 0.006 | m3/kmol | NIST |
| Zc | 0.2791570 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [80.37; 95.16] | J/mol×K | [330.61; 525.49] |
|
| Cp,gas | 80.37 | J/mol×K | 330.61 | Joback Calculated Property |
| Cp,gas | 83.63 | J/mol×K | 363.09 | Joback Calculated Property |
| Cp,gas | 86.55 | J/mol×K | 395.57 | Joback Calculated Property |
| Cp,gas | 89.14 | J/mol×K | 428.05 | Joback Calculated Property |
| Cp,gas | 91.42 | J/mol×K | 460.53 | Joback Calculated Property |
| Cp,gas | 93.42 | J/mol×K | 493.01 | Joback Calculated Property |
| Cp,gas | 95.16 | J/mol×K | 525.49 | Joback Calculated Property |
| Cp,liquid | [121.55; 126.70] | J/mol×K | [298.15; 303.15] |
|
| Cp,liquid | 121.55 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 126.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 122.50 | J/mol×K | 303.15 | NIST |
| ΔfusH | [6.89; 7.90] | kJ/mol | [162.68; 165.40] |
|
| ΔfusH | 6.89 | kJ/mol | 162.68 | NIST |
| ΔfusH | 6.90 | kJ/mol | 162.70 | NIST |
| ΔfusH | 7.90 | kJ/mol | 165.40 | NIST |
| ΔvapH | [24.70; 28.50] | kJ/mol | [231.00; 446.00] |
|
| ΔvapH | 28.20 | kJ/mol | 231.00 | NIST |
| ΔvapH | 28.50 | kJ/mol | 257.00 | NIST |
| ΔvapH | 27.30 | kJ/mol | 265.00 | NIST |
| ΔvapH | 27.10 | kJ/mol | 265.00 | NIST |
| ΔvapH | 26.40 | kJ/mol | 289.00 | NIST |
| ΔvapH | 25.20 | kJ/mol | 290.00 | NIST |
| ΔvapH | 25.21 | kJ/mol | 290.40 | NIST |
| ΔvapH | 24.77 | kJ/mol | 297.10 | KDB |
| ΔvapH | 25.60 | kJ/mol | 329.00 | NIST |
| ΔvapH | 24.70 | kJ/mol | 393.00 | NIST |
| ΔvapH | 25.10 | kJ/mol | 446.00 | NIST |
| ρl | 1494.00 | kg/m3 | 290.00 | KDB |
| ΔfusS | [42.38; 47.80] | J/mol×K | [162.68; 165.40] |
|
| ΔfusS | 42.38 | J/mol×K | 162.68 | NIST |
| ΔfusS | 47.80 | J/mol×K | 165.40 | NIST |
| γ | 0.02 | N/m | 277.60 | KDB |
| ΔvapS | 86.81 | J/mol×K | 290.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 4420.29] | kPa | [214.36; 471.11] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40921e+01 | |||
| Coefficient B | -2.49136e+03 | |||
| Coefficient C | -3.38850e+01 | |||
| Temperature range, min. | 214.36 | |||
| Temperature range, max. | 471.11 | |||
| Pvap | 1.33 | kPa | 214.36 | Calculated Property |
| Pvap | 8.77 | kPa | 242.89 | Calculated Property |
| Pvap | 36.73 | kPa | 271.42 | Calculated Property |
| Pvap | 113.08 | kPa | 299.94 | Calculated Property |
| Pvap | 280.04 | kPa | 328.47 | Calculated Property |
| Pvap | 590.88 | kPa | 357.00 | Calculated Property |
| Pvap | 1104.49 | kPa | 385.53 | Calculated Property |
| Pvap | 1879.56 | kPa | 414.05 | Calculated Property |
| Pvap | 2969.72 | kPa | 442.58 | Calculated Property |
| Pvap | 4420.29 | kPa | 471.11 | Calculated Property |
| Pvap | [4.88e-03; 4467.78] | kPa | [162.04; 471.20] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.72409e+01 | |||
| Coefficient B | -5.39795e+03 | |||
| Coefficient C | -9.73971e+00 | |||
| Coefficient D | 1.15758e-05 | |||
| Temperature range, min. | 162.04 | |||
| Temperature range, max. | 471.20 | |||
| Pvap | 4.88e-03 | kPa | 162.04 | Calculated Property |
| Pvap | 0.29 | kPa | 196.39 | Calculated Property |
| Pvap | 4.33 | kPa | 230.74 | Calculated Property |
| Pvap | 28.32 | kPa | 265.09 | Calculated Property |
| Pvap | 111.85 | kPa | 299.44 | Calculated Property |
| Pvap | 319.38 | kPa | 333.80 | Calculated Property |
| Pvap | 735.39 | kPa | 368.15 | Calculated Property |
| Pvap | 1464.61 | kPa | 402.50 | Calculated Property |
| Pvap | 2643.90 | kPa | 436.85 | Calculated Property |
| Pvap | 4467.78 | kPa | 471.20 | Calculated Property |
Similar Compounds
Find more compounds similar to Trichloromonofluoromethane.
Mixtures
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Hydrogen substitution effect on the solubility of perhalogenated compounds in ionic liquid [bmim][PF6]
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.