- InChI
- InChI=1S/C3H4F4O/c4-2(5)3(6,7)1-8/h2,8H,1H2
- InChI Key
- NBUKAOOFKZFCGD-UHFFFAOYSA-N
- Formula
- C3H4F4O
- SMILES
- OCC(F)(F)C(F)F
- Molecular Weight1
- 132.06
- CAS
- 76-37-9
- Other Names
-
- 1,1,2,2-tetrafluoro-3-hydroxypropane
- 1,1,3-Trihydroperfluoro-1-propanol
- 1,1,3H-perfluoropropanol
- 1-Propanol, 2,2,3,3-tetrafluoro-
- 1-hydroxy-2,2,3,3-tetrafluoropropane
- 1H,1H,3H-Tetrafluoro-1-propanol
- 2,2,3,3-Tetrafluoro-propanol-1
- 2,2,3,3-Tetrafluoropropanol
- 2,2,3,3-Tetrafluoropropyl alcohol
- 2,2,3,3-tetrafluoropropan-1-ol
- 2,2,3,3-tetrafluoropropanol-1
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- ΔfH°liquid : Liquid phase 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).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- 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).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -1353.40 ± 0.67 | kJ/mol | NIST |
| ΔfG° | -941.28 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1055.95 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -1114.90 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 9.00 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [53.58; 53.60] | kJ/mol |
|
| ΔvapH° | 53.58 | kJ/mol | NIST |
| ΔvapH° | 53.60 | kJ/mol | NIST |
| IE | 11.58 | eV | NIST |
| log10WS | -0.97 | Crippen Calculated Property | |
| logPoct/wat | 0.879 | Crippen Calculated Property | |
| McVol | 66.080 | ml/mol | McGowan Calculated Property |
| Pc | 4072.51 | kPa | Joback Calculated Property |
| Inp | [636.00; 651.00] |
|
|
| Inp | 651.00 | NIST | |
| Inp | 640.00 | NIST | |
| Inp | 636.00 | NIST | |
| Tboil | [381.95; 382.70] | K |
|
| Tboil | 382.15 | K | Separat... |
| Tboil | 381.95 | K | Separat... |
| Tboil | 382.50 ± 0.50 | K | NIST |
| Tboil | 382.70 | K | NIST |
| Tc | 495.89 | K | Joback Calculated Property |
| Tfus | 174.17 | K | Joback Calculated Property |
| Vc | 0.278 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [135.42; 167.15] | J/mol×K | [353.63; 495.89] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 135 140 145 150 155 160 165 170 400 450 | ||||
| Cp,gas | 135.42 | J/mol×K | 353.63 | Joback Calculated Property |
| Cp,gas | 141.42 | J/mol×K | 377.34 | Joback Calculated Property |
| Cp,gas | 147.12 | J/mol×K | 401.05 | Joback Calculated Property |
| Cp,gas | 152.54 | J/mol×K | 424.76 | Joback Calculated Property |
| Cp,gas | 157.67 | J/mol×K | 448.47 | Joback Calculated Property |
| Cp,gas | 162.54 | J/mol×K | 472.18 | Joback Calculated Property |
| Cp,gas | 167.15 | J/mol×K | 495.89 | Joback Calculated Property |
| ΔvapH | [47.90; 50.30] | kJ/mol | [315.50; 341.50] |
|
| ΔvapH | 50.30 | kJ/mol | 315.50 | NIST |
| ΔvapH | 47.90 | kJ/mol | 341.50 | NIST |
| Pvap | [53.30; 101.30] | kPa | [365.01; 382.15] |
|
|
T(K) Vapor pressure (kPa) 50 60 70 80 90 100 365 370 375 380 | ||||
| Pvap | 53.30 | kPa | 365.01 | Isobari... |
| Pvap | 66.70 | kPa | 370.79 | Isobari... |
| Pvap | 80.00 | kPa | 375.66 | Isobari... |
| Pvap | 101.30 | kPa | 381.95 | Separat... |
| Pvap | 101.30 | kPa | 382.15 | Separat... |
| n0 | 1.31960 | 303.15 | Liquid-... | |
| ρl | [1401.00; 1493.20] | kg/m3 | [293.15; 342.25] |
|
|
T(K) Liquid Density (kg/m3) 1400 1420 1440 1460 1480 1500 300 320 340 | ||||
| ρl | 1493.20 | kg/m3 | 293.15 | Measure... |
| ρl | 1482.80 | kg/m3 | 301.55 | Measure... |
| ρl | 1474.20 | kg/m3 | 306.15 | Measure... |
| ρl | 1468.60 | kg/m3 | 309.05 | Measure... |
| ρl | 1460.20 | kg/m3 | 312.65 | Measure... |
| ρl | 1454.20 | kg/m3 | 316.15 | Measure... |
| ρl | 1447.60 | kg/m3 | 319.35 | Measure... |
| ρl | 1441.80 | kg/m3 | 323.25 | Measure... |
| ρl | 1434.00 | kg/m3 | 327.05 | Measure... |
| ρl | 1427.40 | kg/m3 | 330.65 | Measure... |
| ρl | 1416.80 | kg/m3 | 334.35 | Measure... |
| ρl | 1409.00 | kg/m3 | 338.25 | Measure... |
| ρl | 1401.00 | kg/m3 | 342.25 | Measure... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [295.10; 404.02] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48751e+01 | |||
| Coefficient B | -3.02459e+03 | |||
| Coefficient C | -8.77620e+01 | |||
| Temperature range, min. | 295.10 | |||
| Temperature range, max. | 404.02 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 295.10 | Calculated Property |
| Pvap | 2.98 | kPa | 307.20 | Calculated Property |
| Pvap | 6.12 | kPa | 319.30 | Calculated Property |
| Pvap | 11.72 | kPa | 331.41 | Calculated Property |
| Pvap | 21.09 | kPa | 343.51 | Calculated Property |
| Pvap | 35.98 | kPa | 355.61 | Calculated Property |
| Pvap | 58.62 | kPa | 367.71 | Calculated Property |
| Pvap | 91.72 | kPa | 379.82 | Calculated Property |
| Pvap | 138.50 | kPa | 391.92 | Calculated Property |
| Pvap | 202.63 | kPa | 404.02 | Calculated Property |
Similar Compounds
Find more compounds similar to 2,2,3,3-Tetrafluoro-1-propanol.
Mixtures
- 1-Pentanol, 2,2,3,3,4,4,5,5-octafluoro- + 2,2,3,3-Tetrafluoro-1-propanol
- Ethyl Acetate + 2,2,3,3-Tetrafluoro-1-propanol + Water
- Isopropyl acetate + 2,2,3,3-Tetrafluoro-1-propanol + Water
- 2,2,3,3-Tetrafluoro-1-propanol + Water
- Trichloromethane + 2,2,3,3-Tetrafluoro-1-propanol
- p-Xylene + 2,2,3,3-Tetrafluoro-1-propanol
- 2,2,3,3-Tetrafluoro-1-propanol + Formamide, N-methyl-
- Formamide, N,N-dimethyl- + 2,2,3,3-Tetrafluoro-1-propanol
- 2-Pyrrolidinone, 1-methyl- + 2,2,3,3-Tetrafluoro-1-propanol
- Diisopropyl ether + 2,2,3,3-Tetrafluoro-1-propanol + Water
- Propane, 2-methoxy-2-methyl- + 2,2,3,3-Tetrafluoro-1-propanol + Water
- Anisole + 2,2,3,3-Tetrafluoro-1-propanol + Water
- 1-Octanol + 2,2,3,3-Tetrafluoro-1-propanol + Water
Sources
- Crippen Method
- Crippen Method
- Measurements and correlations of density, viscosity, and vapour-liquid equilibrium for fluoro alcohols
- Liquid-liquid equilibrium for ternary systems of ethyl acetate/isopropyl acetate + 2,2,3,3-tetrafluoro-1-propanol + water at 298.15, 318.15 K
- Separation of azeotrope (2,2,3,3-tetrafluoro-1-propanol + water): Isobaric vapour-liquid phase equilibrium measurements and azeotropic distillation
- Liquid-liquid equilibrium for ternary systems of water + 2,2,3,3-tetrafluoro-1-propanol + isopropyl ether/tert-butyl methyl ether at 298.2, 308.2 K
- Separation of azeotropic mixture (2, 2, 3, 3-Tetrafluoro-1-propanol + water) by extractive distillation: Entrainers selection and vapour-liquid equilibrium measurements
- Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,3,3-Tetrafluoro-1-propanol + 2,2,3,3,4,4,5,5-Octafluoro-1-pentanol at 53.3, 66.7, 80.0 kPa
- Liquid-Liquid Equilibrium for Ternary Systems of Water + 2,2,3,3-Tetrafluoro-1-propanol + Anisole/1-Octanol at 298.2, 308.2, and 318.2 K
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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