- InChI
- InChI=1S/C3H4ClF3/c4-2-1-3(5,6)7/h1-2H2
- InChI Key
- ZPIFKCVYZBVZIV-UHFFFAOYSA-N
- Formula
- C3H4ClF3
- SMILES
- FC(F)(F)CCCl
- Molecular Weight1
- 132.51
- CAS
- 460-35-5
- Other Names
-
- 1,1,1-Trifluoro-3-chloropropane
- 1-Chloro-3,3,3-trifluoropropane
- 3,3,3-Trifluoro-1-chloropropane
- 3-Chloro-1,1,1-trifluoropropane
- CF3CH2CH2Cl
- Freon 253
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- 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).
- 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).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (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).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -1504.20 ± 0.92 | kJ/mol | NIST |
| ΔfG° | -619.14 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -718.07 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -799.31 ± 0.92 | kJ/mol | NIST |
| ΔfusH° | 9.55 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 22.91 | kJ/mol | Joback Calculated Property |
| log10WS | -1.89 | Crippen Calculated Property | |
| logPoct/wat | 2.178 | Crippen Calculated Property | |
| McVol | 70.680 | ml/mol | McGowan Calculated Property |
| Pc | 3633.35 | kPa | Joback Calculated Property |
| S°liquid | [271.67; 271.67] | J/mol×K |
|
| S°liquid | 271.67 | J/mol×K | NIST |
| S°liquid | 271.67 | J/mol×K | NIST |
| Tboil | 319.00 | K | NIST |
| Tc | 453.65 | K | Joback Calculated Property |
| Tfus | 157.68 | K | Joback Calculated Property |
| Ttriple | [179.32; 179.40] | K |
|
| Ttriple | 179.32 ± 0.02 | K | NIST |
| Ttriple | 179.40 ± 0.02 | K | NIST |
| Vc | 0.295 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [112.93; 147.12] | J/mol×K | [300.05; 453.65] |
|
| Cp,gas | 112.93 | J/mol×K | 300.05 | Joback Calculated Property |
| Cp,gas | 119.45 | J/mol×K | 325.65 | Joback Calculated Property |
| Cp,gas | 125.62 | J/mol×K | 351.25 | Joback Calculated Property |
| Cp,gas | 131.46 | J/mol×K | 376.85 | Joback Calculated Property |
| Cp,gas | 136.98 | J/mol×K | 402.45 | Joback Calculated Property |
| Cp,gas | 142.20 | J/mol×K | 428.05 | Joback Calculated Property |
| Cp,gas | 147.12 | J/mol×K | 453.65 | Joback Calculated Property |
| Cp,liquid | [171.08; 171.08] | J/mol×K | [298.15; 298.15] |
|
| Cp,liquid | 171.08 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 171.08 | J/mol×K | 298.15 | NIST |
| ΔfusH | [4.49; 5.31] | kJ/mol | [169.80; 179.40] |
|
| ΔfusH | 4.49 | kJ/mol | 169.80 | NIST |
| ΔfusH | 5.05 | kJ/mol | 179.30 | NIST |
| ΔfusH | 5.31 | kJ/mol | 179.40 | NIST |
| ΔvapH | [29.90; 33.70] | kJ/mol | [306.00; 321.00] |
|
| ΔvapH | 29.90 | kJ/mol | 306.00 | NIST |
| ΔvapH | 33.70 | kJ/mol | 321.00 | NIST |
| ΔfusS | [26.44; 28.20] | J/mol×K | [169.80; 179.30] |
|
| ΔfusS | 26.44 | J/mol×K | 169.80 | NIST |
| ΔfusS | 28.20 | J/mol×K | 179.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [233.90; 340.61] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.38810e+01 | |||
| Coefficient B | -2.47417e+03 | |||
| Coefficient C | -5.18870e+01 | |||
| Temperature range, min. | 233.90 | |||
| Temperature range, max. | 340.61 | |||
| Pvap | 1.33 | kPa | 233.90 | Calculated Property |
| Pvap | 3.06 | kPa | 245.76 | Calculated Property |
| Pvap | 6.39 | kPa | 257.61 | Calculated Property |
| Pvap | 12.30 | kPa | 269.47 | Calculated Property |
| Pvap | 22.14 | kPa | 281.33 | Calculated Property |
| Pvap | 37.61 | kPa | 293.18 | Calculated Property |
| Pvap | 60.80 | kPa | 305.04 | Calculated Property |
| Pvap | 94.14 | kPa | 316.90 | Calculated Property |
| Pvap | 140.42 | kPa | 328.75 | Calculated Property |
| Pvap | 202.67 | kPa | 340.61 | Calculated Property |
Similar Compounds
Find more compounds similar to Propane, 3-chloro-1,1,1-trifluoro-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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