- InChI
- InChI=1S/C3H7F/c1-3(2)4/h3H,1-2H3
- InChI Key
- PRNZBCYBKGCOFI-UHFFFAOYSA-N
- Formula
- C3H7F
- SMILES
- CC(C)F
- Molecular Weight1
- 62.09
- CAS
- 420-26-8
- Other Names
-
- 2-Fluoropropane
- ISOPROPYL FLUORIDE
- iso-C3H7F
- ω : Acentric Factor.
- Cp,gas : Ideal gas 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).
- 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).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2040 | KDB | |
| ΔfG° | -222.87 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -306.64 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 3.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 21.07 | kJ/mol | Joback Calculated Property |
| IE | 11.08 ± 0.02 | eV | NIST |
| log10WS | -1.04 | Crippen Calculated Property | |
| logPoct/wat | 1.364 | Crippen Calculated Property | |
| McVol | 54.900 | ml/mol | McGowan Calculated Property |
| Pc | 4200.00 | kPa | KDB |
| Inp | [370.00; 370.00] |
|
|
| Inp | 370.00 | NIST | |
| Inp | 370.00 | NIST | |
| Tboil | [263.00; 263.80] | K |
|
| Tboil | 263.80 | K | KDB |
| Tboil | 263.00 | K | NIST |
| Tboil | 263.20 ± 1.00 | K | NIST |
| Tboil | 263.05 ± 1.00 | K | NIST |
| Tc | 415.70 | K | KDB |
| Tfus | 140.00 | K | KDB |
| Vc | 0.215 | m3/kmol | KDB |
| Zc | 0.2618660 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [75.62; 107.56] | J/mol×K | [266.87; 420.50] |
|
| Cp,gas | 75.62 | J/mol×K | 266.87 | Joback Calculated Property |
| Cp,gas | 81.36 | J/mol×K | 292.48 | Joback Calculated Property |
| Cp,gas | 86.94 | J/mol×K | 318.08 | Joback Calculated Property |
| Cp,gas | 92.34 | J/mol×K | 343.69 | Joback Calculated Property |
| Cp,gas | 97.58 | J/mol×K | 369.29 | Joback Calculated Property |
| Cp,gas | 102.65 | J/mol×K | 394.90 | Joback Calculated Property |
| Cp,gas | 107.56 | J/mol×K | 420.50 | Joback Calculated Property |
| ΔvapH | 23.70 | kJ/mol | 227.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 210.86] | kPa | [193.30; 281.86] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.38020e+01 | |||
| Coefficient B | -1.99738e+03 | |||
| Coefficient C | -4.55080e+01 | |||
| Temperature range, min. | 193.30 | |||
| Temperature range, max. | 281.86 | |||
| Pvap | 1.33 | kPa | 193.30 | Calculated Property |
| Pvap | 3.10 | kPa | 203.14 | Calculated Property |
| Pvap | 6.52 | kPa | 212.98 | Calculated Property |
| Pvap | 12.65 | kPa | 222.82 | Calculated Property |
| Pvap | 22.86 | kPa | 232.66 | Calculated Property |
| Pvap | 38.96 | kPa | 242.50 | Calculated Property |
| Pvap | 63.12 | kPa | 252.34 | Calculated Property |
| Pvap | 97.87 | kPa | 262.18 | Calculated Property |
| Pvap | 146.07 | kPa | 272.02 | Calculated Property |
| Pvap | 210.86 | kPa | 281.86 | Calculated Property |
| Pvap | [1.33; 4135.31] | kPa | [190.15; 415.68] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.34958e+01 | |||
| Coefficient B | -3.84470e+03 | |||
| Coefficient C | -4.40734e+00 | |||
| Coefficient D | 3.80005e-06 | |||
| Temperature range, min. | 190.15 | |||
| Temperature range, max. | 415.68 | |||
| Pvap | 1.33 | kPa | 190.15 | Calculated Property |
| Pvap | 8.43 | kPa | 215.21 | Calculated Property |
| Pvap | 34.93 | kPa | 240.27 | Calculated Property |
| Pvap | 107.30 | kPa | 265.33 | Calculated Property |
| Pvap | 265.41 | kPa | 290.39 | Calculated Property |
| Pvap | 558.89 | kPa | 315.44 | Calculated Property |
| Pvap | 1041.56 | kPa | 340.50 | Calculated Property |
| Pvap | 1766.47 | kPa | 365.56 | Calculated Property |
| Pvap | 2782.84 | kPa | 390.62 | Calculated Property |
| Pvap | 4135.31 | kPa | 415.68 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 2-fluoro-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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