- InChI
- InChI=1S/C14H30O/c1-3-5-6-7-8-9-10-11-13-14(15)12-4-2/h14-15H,3-13H2,1-2H3
- InChI Key
- HRDGAIGDKJXHIU-UHFFFAOYSA-N
- Formula
- C14H30O
- SMILES
- CCCCCCCCCCC(O)CCC
- Molecular Weight1
- 214.39
- CAS
- 1653-33-4
- Other Names
-
- tetradecan-4-ol
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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.
- I : 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 |
|---|---|---|---|
| ω | 0.8402 | Relay (1.0) Calculated Property | |
| ΔfG° | -72.26 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -503.68 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 32.58 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 96.70 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.74 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.02 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.678 | Crippen Calculated Property | |
| McVol | 213.990 | ml/mol | McGowan Calculated Property |
| Pc | 1649.77 | kPa | Joback Calculated Property |
| Inp | 1681.00 | NIST | |
| I | [1967.00; 1990.00] |
|
|
| I | 1967.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 1967.00 | NIST | |
| Tboil | 546.84 | K | Relay (1.0) Calculated Property |
| Tc | 724.29 | K | Relay (1.0) Calculated Property |
| Tfus | 300.21 | K | Relay (1.0) Calculated Property |
| Vc | 0.842 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [314.66; 760.81] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -6.22900e+00 | |||
| Coefficient B | 1.37374e+00 | |||
| Coefficient C | -7.71400e-04 | |||
| Coefficient D | 1.64700e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 314.66 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 390.51 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 458.58 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 519.39 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 573.44 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 621.28 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 663.41 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 700.37 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 732.66 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 760.81 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0226239; 0.0001158] | Pa×s | [293.36; 540.27] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.53312e+01 | |||
| Coefficient B | 3.38609e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 293.36 | |||
| Temperature range, max. | 540.27 | |||
| η | 0.0226239 | Pa×s | 293.36 | Calculated Property |
| η | 0.0084309 | Pa×s | 320.79 | Calculated Property |
| η | 0.0036705 | Pa×s | 348.23 | Calculated Property |
| η | 0.0018044 | Pa×s | 375.66 | Calculated Property |
| η | 0.0009770 | Pa×s | 403.10 | Calculated Property |
| η | 0.0005721 | Pa×s | 430.53 | Calculated Property |
| η | 0.0003571 | Pa×s | 457.96 | Calculated Property |
| η | 0.0002351 | Pa×s | 485.40 | Calculated Property |
| η | 0.0001619 | Pa×s | 512.83 | Calculated Property |
| η | 0.0001158 | Pa×s | 540.27 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [432.72; 586.85] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.62855e+01 | |||
| Coefficient B | -5.38620e+03 | |||
| Coefficient C | -9.60380e+01 | |||
| Temperature range, min. | 432.72 | |||
| Temperature range, max. | 586.85 | |||
| Pvap | 1.33 | kPa | 432.72 | Calculated Property |
| Pvap | 2.89 | kPa | 449.85 | Calculated Property |
| Pvap | 5.84 | kPa | 466.97 | Calculated Property |
| Pvap | 11.09 | kPa | 484.10 | Calculated Property |
| Pvap | 19.93 | kPa | 501.22 | Calculated Property |
| Pvap | 34.17 | kPa | 518.35 | Calculated Property |
| Pvap | 56.17 | kPa | 535.47 | Calculated Property |
| Pvap | 88.96 | kPa | 552.60 | Calculated Property |
| Pvap | 136.27 | kPa | 569.72 | Calculated Property |
| Pvap | 202.64 | kPa | 586.85 | Calculated Property |
Similar Compounds
Find more compounds similar to 4-Tetradecanol.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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