- InChI
- InChI=1S/C24H50O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19-20-21-22-23-24-25/h25H,2-24H2,1H3
- InChI Key
- TYWMIZZBOVGFOV-UHFFFAOYSA-N
- Formula
- C24H50O
- SMILES
- CCCCCCCCCCCCCCCCCCCCCCCCO
- Molecular Weight1
- 354.66
- CAS
- 506-51-4
- Other Names
-
- Lignoceric alcohol
- Lignocerol
- Lignoceryl alcohol
- N-tetracosanol-1
- Tetracosan-1-ol
- Tetracosanol
- Tetracosyl alcohol
- 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).
- 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 | 1.2730 | Relay (1.0) Calculated Property | |
| ΔfG° | 14.38 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -704.37 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 62.00 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 152.83 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.28 | eV | Relay (1.0) Calculated Property |
| log10WS | -8.65 | Relay (1.0) Calculated Property | |
| logPoct/wat | 8.581 | Crippen Calculated Property | |
| McVol | 354.890 | ml/mol | McGowan Calculated Property |
| Pc | 849.99 | kPa | Joback Calculated Property |
| Tboil | 637.35 | K | Relay (1.0) Calculated Property |
| Tc | 821.12 | K | Relay (1.0) Calculated Property |
| Tfus | 350.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 1.410 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [527.11; 1276.18] | 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 | -1.36370e+01 | |||
| Coefficient B | 2.31782e+00 | |||
| Coefficient C | -1.31220e-03 | |||
| Coefficient D | 2.84200e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 527.11 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 654.71 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 769.11 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 871.23 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 961.95 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 1042.19 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 1112.83 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 1174.78 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 1228.93 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 1276.18 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0118870; 0.0000216] | Pa×s | [350.15; 722.09] |
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 | -1.66838e+01 | |||
| Coefficient B | 4.28987e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 350.15 | |||
| Temperature range, max. | 722.09 | |||
| η | 0.0118870 | Pa×s | 350.15 | Calculated Property |
| η | 0.0032612 | Pa×s | 391.48 | Calculated Property |
| η | 0.0011454 | Pa×s | 432.80 | Calculated Property |
| η | 0.0004828 | Pa×s | 474.13 | Calculated Property |
| η | 0.0002337 | Pa×s | 515.46 | Calculated Property |
| η | 0.0001260 | Pa×s | 556.78 | Calculated Property |
| η | 0.0000740 | Pa×s | 598.11 | Calculated Property |
| η | 0.0000465 | Pa×s | 639.44 | Calculated Property |
| η | 0.0000310 | Pa×s | 680.76 | Calculated Property |
| η | 0.0000216 | Pa×s | 722.09 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [527.00; 730.65] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.51348e+01 | |||
| Coefficient B | -5.91214e+03 | |||
| Coefficient C | -1.28800e+02 | |||
| Temperature range, min. | 527.00 | |||
| Temperature range, max. | 730.65 | |||
| Pvap | 1.33 | kPa | 527.00 | Calculated Property |
| Pvap | 2.96 | kPa | 549.63 | Calculated Property |
| Pvap | 6.07 | kPa | 572.26 | Calculated Property |
| Pvap | 11.59 | kPa | 594.88 | Calculated Property |
| Pvap | 20.85 | kPa | 617.51 | Calculated Property |
| Pvap | 35.61 | kPa | 640.14 | Calculated Property |
| Pvap | 58.13 | kPa | 662.77 | Calculated Property |
| Pvap | 91.17 | kPa | 685.39 | Calculated Property |
| Pvap | 138.06 | kPa | 708.02 | Calculated Property |
| Pvap | 202.65 | kPa | 730.65 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Tetracosanol.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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