- InChI
- InChI=1S/C14H28O2/c1-3-4-5-6-7-8-9-10-11-12-13-16-14(2)15/h3-13H2,1-2H3
- InChI Key
- VZWGRQBCURJOMT-UHFFFAOYSA-N
- Formula
- C14H28O2
- SMILES
- CCCCCCCCCCCCOC(C)=O
- Molecular Weight1
- 228.37
- CAS
- 112-66-3
- Other Names
-
- 1-Dodecanol acetate
- Acetic acid, dodecyl ester
- Dodecan-1-ol, acetate
- Dodecan-1-yl acetate
- Dodecanol acetate
- Dodecanyl acetate
- Dodecyl acetate
- Dodecyl alcohol, acetate
- NSC 67366
- dodecyl ethanoate
- n-Dodecyl acetate
- n-Dodecyl ethanoate
- 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).
- 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔfG° | -166.92 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -577.09 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 34.80 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [79.60; 81.80] | kJ/mol |
|
| ΔvapH° | 79.60 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 81.80 | kJ/mol | NIST |
| log10WS | -4.55 | Crippen Calculated Property | |
| logPoct/wat | 4.470 | Crippen Calculated Property | |
| McVol | 215.560 | ml/mol | McGowan Calculated Property |
| Pc | 1579.71 | kPa | Joback Calculated Property |
| Inp | [1562.00; 1620.00] |
|
|
| Inp | 1606.00 | NIST | |
| Inp | 1596.00 | NIST | |
| Inp | 1594.00 | NIST | |
| Inp | 1594.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1589.60 | NIST | |
| Inp | Outlier 1562.00 | NIST | |
| Inp | 1587.00 | NIST | |
| Inp | 1620.00 | NIST | |
| Inp | 1611.00 | NIST | |
| Inp | 1609.00 | NIST | |
| Inp | 1610.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1608.50 | NIST | |
| Inp | 1605.90 | NIST | |
| Inp | 1610.00 | NIST | |
| Inp | 1606.00 | NIST | |
| Inp | 1585.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1605.90 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1606.00 | NIST | |
| Inp | 1580.00 | NIST | |
| Inp | 1613.00 | NIST | |
| Inp | 1606.00 | NIST | |
| Inp | 1606.00 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1588.00 | NIST | |
| Inp | 1606.00 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1576.00 | NIST | |
| I | [1868.00; 1900.00] |
|
|
| I | 1876.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1898.00 | NIST | |
| I | 1900.00 | NIST | |
| I | Outlier 1868.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1895.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1880.00 | NIST | |
| Tboil | 538.20 | K | NIST |
| Tc | 764.02 | K | Joback Calculated Property |
| Tfus | 319.70 | K | Joback Calculated Property |
| Vc | 0.844 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [567.02; 658.29] | J/mol×K | [596.01; 764.02] |
|
| Cp,gas | 567.02 | J/mol×K | 596.01 | Joback Calculated Property |
| Cp,gas | 583.90 | J/mol×K | 624.01 | Joback Calculated Property |
| Cp,gas | 600.10 | J/mol×K | 652.01 | Joback Calculated Property |
| Cp,gas | 615.63 | J/mol×K | 680.02 | Joback Calculated Property |
| Cp,gas | 630.49 | J/mol×K | 708.02 | Joback Calculated Property |
| Cp,gas | 644.71 | J/mol×K | 736.02 | Joback Calculated Property |
| Cp,gas | 658.29 | J/mol×K | 764.02 | Joback Calculated Property |
| η | [0.0001532; 0.0027735] | Pa×s | [319.70; 596.01] |
|
| η | 0.0027735 | Pa×s | 319.70 | Joback Calculated Property |
| η | 0.0012632 | Pa×s | 365.75 | Joback Calculated Property |
| η | 0.0006860 | Pa×s | 411.80 | Joback Calculated Property |
| η | 0.0004212 | Pa×s | 457.86 | Joback Calculated Property |
| η | 0.0002827 | Pa×s | 503.91 | Joback Calculated Property |
| η | 0.0002029 | Pa×s | 549.96 | Joback Calculated Property |
| η | 0.0001532 | Pa×s | 596.01 | Joback Calculated Property |
| ΔvapH | 70.50 | kJ/mol | 469.00 | NIST |
| Pvap | [8.00e-05; 5.97e-03] | kPa | [288.90; 333.40] |
|
| Pvap | 8.00e-05 | kPa | 288.90 | Vapour ... |
| Pvap | 1.10e-04 | kPa | 291.90 | Vapour ... |
| Pvap | 1.70e-04 | kPa | 296.00 | Vapour ... |
| Pvap | 2.40e-04 | kPa | 299.00 | Vapour ... |
| Pvap | 3.70e-04 | kPa | 303.10 | Vapour ... |
| Pvap | 4.90e-04 | kPa | 306.10 | Vapour ... |
| Pvap | 6.70e-04 | kPa | 309.20 | Vapour ... |
| Pvap | 9.00e-04 | kPa | 312.10 | Vapour ... |
| Pvap | 1.19e-03 | kPa | 315.20 | Vapour ... |
| Pvap | 1.63e-03 | kPa | 318.20 | Vapour ... |
| Pvap | 2.08e-03 | kPa | 321.30 | Vapour ... |
| Pvap | 2.80e-03 | kPa | 324.40 | Vapour ... |
| Pvap | 3.56e-03 | kPa | 327.40 | Vapour ... |
| Pvap | 4.56e-03 | kPa | 330.40 | Vapour ... |
| Pvap | 5.97e-03 | kPa | 333.40 | Vapour ... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 423.20 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [436.02; 567.22] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.81806e+01 | |||
| Coefficient B | -6.01367e+03 | |||
| Coefficient C | -9.99300e+01 | |||
| Temperature range, min. | 436.02 | |||
| Temperature range, max. | 567.22 | |||
| Pvap | 1.33 | kPa | 436.02 | Calculated Property |
| Pvap | 2.81 | kPa | 450.60 | Calculated Property |
| Pvap | 5.56 | kPa | 465.18 | Calculated Property |
| Pvap | 10.46 | kPa | 479.75 | Calculated Property |
| Pvap | 18.78 | kPa | 494.33 | Calculated Property |
| Pvap | 32.35 | kPa | 508.91 | Calculated Property |
| Pvap | 53.66 | kPa | 523.49 | Calculated Property |
| Pvap | 86.06 | kPa | 538.06 | Calculated Property |
| Pvap | 133.88 | kPa | 552.64 | Calculated Property |
| Pvap | 202.63 | kPa | 567.22 | Calculated Property |
Similar Compounds
Find more compounds similar to Lauryl acetate.
Sources
- Crippen Method
- Crippen Method
- Vapour pressures and enthalpies of vaporization of a series of the linear n-alkyl acetates
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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