- InChI
- InChI=1S/C14H28O2/c1-3-5-6-7-8-9-10-11-12-13-14(15)16-4-2/h3-13H2,1-2H3
- InChI Key
- MMXKVMNBHPAILY-UHFFFAOYSA-N
- Formula
- C14H28O2
- SMILES
- CCCCCCCCCCCC(=O)OCC
- Molecular Weight1
- 228.38
- CAS
- 106-33-2
- Other Names
-
- Ethyl dodecylate
- Ethyl ester dodecanoic acid
- Ethyl ester of dodecanoic acid
- Ethyl laurinate
- Ethyl n-dodecanoate
- Ethyl n-dodecanote
- Lauric acid, ethyl ester
- ethyl dodecanoate
- ethyl laurate
- ω : Acentric Factor.
- 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).
- 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).
- 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).
- 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.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×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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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.7511 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -8778.00 ± 1.00 | kJ/mol | NIST |
| ΔfG° | -243.37 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -658.93 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 39.83 | kJ/mol | Solid liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate |
| ΔvapH° | 80.00 | kJ/mol | NIST |
| IE | 9.58 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.95 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.470 | Crippen Calculated Property | |
| McVol | 215.560 | ml/mol | McGowan Calculated Property |
| Pc | 1529.46 | kPa | Joback Calculated Property |
| Inp | [267.60; 1603.00] |
|
|
| Inp | 1593.00 | NIST | |
| Inp | 1596.00 | NIST | |
| Inp | 1581.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1588.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1558.00 | NIST | |
| Inp | 1582.00 | NIST | |
| Inp | 1581.00 | NIST | |
| Inp | 1593.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1596.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1596.00 | NIST | |
| Inp | 1581.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1581.00 | NIST | |
| Inp | 1590.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1590.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1581.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1593.00 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1596.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1588.00 | NIST | |
| Inp | 1563.00 | NIST | |
| Inp | 1593.00 | NIST | |
| Inp | 1593.00 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1596.00 | NIST | |
| Inp | 1594.00 | NIST | |
| Inp | 1598.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1590.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1581.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1578.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1570.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1592.00 | NIST | |
| Inp | 1603.00 | NIST | |
| Inp | 1603.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1590.00 | NIST | |
| Inp | 1591.00 | NIST | |
| Inp | 1582.00 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1594.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1596.00 | NIST | |
| Inp | 1598.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1583.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1579.00 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | Outlier 267.60 | NIST | |
| Inp | 1576.00 | NIST | |
| Inp | 1558.00 | NIST | |
| Inp | 1577.00 | NIST | |
| Inp | 1597.00 | NIST | |
| Inp | 1595.00 | NIST | |
| Inp | 1579.00 | NIST | |
| I | [1811.00; 1874.00] |
|
|
| I | 1842.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1840.00 | NIST | |
| I | Outlier 1874.00 | NIST | |
| I | 1846.00 | NIST | |
| I | Outlier 1873.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1825.00 | NIST | |
| I | Outlier 1811.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1824.00 | NIST | |
| I | 1824.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1828.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1843.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1820.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1822.00 | NIST | |
| I | 1820.00 | NIST | |
| I | 1822.00 | NIST | |
| I | 1820.00 | NIST | |
| I | 1822.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1818.00 | NIST | |
| I | 1827.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1818.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1824.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1842.00 | NIST | |
| I | Outlier 1873.00 | NIST | |
| Tboil | [448.00; 463.00] | K |
|
| Tboil | 448.00 ± 2.00 | K | NIST |
| Tboil | 463.00 ± 1.50 | K | NIST |
| Tc | 716.34 | K | Relay (1.0) Calculated Property |
| Tfus | [262.50; 273.20] | K |
|
| Tfus | 273.20 | K | Solid-liquid equilibrium in ternary mixtures of ethyl laurate, ethyl palmitate and ethyl stearate |
| Tfus | 272.20 | K | High pressure solid-liquid equilibrium of fatty acid ethyl esters binary systems |
| Tfus | 262.50 ± 0.20 | K | NIST |
| Ttriple | 273.00 | K | Influence of Additives (Isoamyl Laurate or Isoamyl Nonanoate) in the Solid-Liquid Equilibrium of Fatty Acid Ethyl Esters |
| Vc | 0.847 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
Datasets
- Molar heat capacity at constant pressure, J/K/mol (1)
- Mass density, kg/m3 (2)
- Speed of sound, m/s (1)
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 313.27 | 140.00 | 474.00 |
| 313.26 | 5030.00 | 472.00 |
| 313.26 | 9990.00 | 471.00 |
| 313.27 | 14970.00 | 470.00 |
| 313.29 | 20040.00 | 470.00 |
| 313.28 | 25150.00 | 469.00 |
| 323.22 | 160.00 | 480.00 |
| 323.23 | 4980.00 | 478.00 |
| 323.23 | 10110.00 | 477.00 |
| 323.23 | 14920.00 | 476.00 |
| 323.22 | 20140.00 | 475.00 |
| 323.22 | 25150.00 | 474.00 |
| 333.20 | 140.00 | 487.00 |
| 333.20 | 4920.00 | 485.00 |
| 333.20 | 10150.00 | 483.00 |
| 333.20 | 15060.00 | 482.00 |
| 333.20 | 19970.00 | 481.00 |
| 333.21 | 25020.00 | 480.00 |
| 343.15 | 140.00 | 493.00 |
| 343.16 | 5160.00 | 491.00 |
| 343.16 | 10270.00 | 489.00 |
| 343.19 | 15130.00 | 488.00 |
| 343.19 | 20220.00 | 487.00 |
| 343.21 | 25180.00 | 486.00 |
| 353.14 | 180.00 | 501.00 |
| 353.14 | 4970.00 | 498.00 |
| 353.17 | 9950.00 | 496.00 |
| 353.17 | 14920.00 | 494.00 |
| 353.17 | 20020.00 | 492.00 |
| 353.18 | 24950.00 | 491.00 |
| 363.17 | 110.00 | 508.00 |
| 363.18 | 5010.00 | 507.00 |
| 363.29 | 10190.00 | 505.00 |
| 363.29 | 15070.00 | 503.00 |
| 363.29 | 20150.00 | 501.00 |
| 363.29 | 25100.00 | 500.00 |
| 373.19 | 110.00 | 516.00 |
| 373.20 | 4900.00 | 514.00 |
| 373.21 | 10170.00 | 512.00 |
| 373.21 | 15020.00 | 511.00 |
| 373.22 | 19850.00 | 509.00 |
| 373.25 | 24930.00 | 508.00 |
| 383.23 | 100.00 | 523.00 |
| 383.23 | 5000.00 | 521.00 |
| 383.23 | 10040.00 | 520.00 |
| 383.24 | 15080.00 | 518.00 |
| 383.25 | 19940.00 | 517.00 |
| 383.28 | 25150.00 | 515.00 |
| 393.22 | 110.00 | 532.00 |
| 393.20 | 4910.00 | 530.00 |
| 393.22 | 10100.00 | 530.00 |
| 393.27 | 15020.00 | 529.00 |
| 393.23 | 19780.00 | 528.00 |
| 393.27 | 24830.00 | 527.00 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 869.69 |
| 1000.00 | 283.15 | 870.36 |
| 3000.00 | 283.15 | 871.92 |
| 5000.00 | 283.15 | 872.91 |
| 10000.00 | 283.15 | 876.08 |
| 15000.00 | 283.15 | 878.96 |
| 20000.00 | 283.15 | 881.89 |
| 25000.00 | 283.15 | 884.58 |
| 30000.00 | 283.15 | 887.29 |
| 35000.00 | 283.15 | 890.05 |
| 40000.00 | 283.15 | 892.47 |
| 50000.00 | 283.15 | 897.22 |
| 60000.00 | 283.15 | 901.93 |
| 100.00 | 293.15 | 862.5 |
| 1000.00 | 293.15 | 863.0 |
| 3000.00 | 293.15 | 864.24 |
| 5000.00 | 293.15 | 865.2 |
| 10000.00 | 293.15 | 868.58 |
| 15000.00 | 293.15 | 871.64 |
| 20000.00 | 293.15 | 874.58 |
| 25000.00 | 293.15 | 877.55 |
| 30000.00 | 293.15 | 880.26 |
| 35000.00 | 293.15 | 882.89 |
| 40000.00 | 293.15 | 885.52 |
| 50000.00 | 293.15 | 890.85 |
| 60000.00 | 293.15 | 895.29 |
| 100.00 | 303.15 | 854.28 |
| 1000.00 | 303.15 | 855.02 |
| 3000.00 | 303.15 | 856.39 |
| 5000.00 | 303.15 | 857.69 |
| 10000.00 | 303.15 | 860.98 |
| 15000.00 | 303.15 | 864.33 |
| 20000.00 | 303.15 | 867.23 |
| 25000.00 | 303.15 | 870.25 |
| 30000.00 | 303.15 | 873.21 |
| 35000.00 | 303.15 | 876.08 |
| 40000.00 | 303.15 | 878.71 |
| 50000.00 | 303.15 | 883.88 |
| 60000.00 | 303.15 | 888.85 |
| 100.00 | 313.15 | 846.91 |
| 1000.00 | 313.15 | 847.32 |
| 3000.00 | 313.15 | 848.68 |
| 5000.00 | 313.15 | 850.07 |
| 10000.00 | 313.15 | 853.51 |
| 15000.00 | 313.15 | 856.86 |
| 20000.00 | 313.15 | 860.1 |
| 25000.00 | 313.15 | 863.29 |
| 30000.00 | 313.15 | 866.24 |
| 35000.00 | 313.15 | 869.1 |
| 40000.00 | 313.15 | 871.83 |
| 50000.00 | 313.15 | 877.43 |
| 60000.00 | 313.15 | 882.35 |
| 100.00 | 323.15 | 838.9 |
| 1000.00 | 323.15 | 839.64 |
| 3000.00 | 323.15 | 841.1 |
| 5000.00 | 323.15 | 842.59 |
| 10000.00 | 323.15 | 846.29 |
| 15000.00 | 323.15 | 849.77 |
| 20000.00 | 323.15 | 853.3 |
| 25000.00 | 323.15 | 856.35 |
| 30000.00 | 323.15 | 859.5 |
| 35000.00 | 323.15 | 862.45 |
| 40000.00 | 323.15 | 865.48 |
| 50000.00 | 323.15 | 871.16 |
| 60000.00 | 323.15 | 876.11 |
| 100.00 | 333.15 | 831.05 |
| 1000.00 | 333.15 | 831.72 |
| 3000.00 | 333.15 | 833.53 |
| 5000.00 | 333.15 | 835.15 |
| 10000.00 | 333.15 | 838.84 |
| 15000.00 | 333.15 | 842.47 |
| 20000.00 | 333.15 | 846.07 |
| 25000.00 | 333.15 | 849.47 |
| 30000.00 | 333.15 | 852.73 |
| 35000.00 | 333.15 | 855.75 |
| 40000.00 | 333.15 | 859.06 |
| 50000.00 | 333.15 | 864.9 |
| 60000.00 | 333.15 | 870.44 |
| 100.00 | 343.15 | 823.11 |
| 1000.00 | 343.15 | 824.13 |
| 3000.00 | 343.15 | 825.84 |
| 5000.00 | 343.15 | 827.55 |
| 10000.00 | 343.15 | 831.53 |
| 15000.00 | 343.15 | 835.33 |
| 20000.00 | 343.15 | 839.18 |
| 25000.00 | 343.15 | 842.57 |
| 30000.00 | 343.15 | 846.08 |
| 35000.00 | 343.15 | 849.44 |
| 40000.00 | 343.15 | 852.46 |
| 50000.00 | 343.15 | 858.61 |
| 60000.00 | 343.15 | 864.08 |
| 100.00 | 353.15 | 815.47 |
| 1000.00 | 353.15 | 816.33 |
| 3000.00 | 353.15 | 818.26 |
| 5000.00 | 353.15 | 819.99 |
| 10000.00 | 353.15 | 824.24 |
| 15000.00 | 353.15 | 828.35 |
| 20000.00 | 353.15 | 832.01 |
| 25000.00 | 353.15 | 835.81 |
| 30000.00 | 353.15 | 839.36 |
| 35000.00 | 353.15 | 842.72 |
| 40000.00 | 353.15 | 846.01 |
| 50000.00 | 353.15 | 852.29 |
| 60000.00 | 353.15 | 858.27 |
| 100.00 | 363.15 | 807.52 |
| 1000.00 | 363.15 | 808.53 |
| 3000.00 | 363.15 | 810.45 |
| 5000.00 | 363.15 | 812.32 |
| 10000.00 | 363.15 | 816.46 |
| 15000.00 | 363.15 | 821.01 |
| 20000.00 | 363.15 | 824.82 |
| 25000.00 | 363.15 | 828.56 |
| 30000.00 | 363.15 | 832.36 |
| 35000.00 | 363.15 | 835.98 |
| 40000.00 | 363.15 | 839.55 |
| 50000.00 | 363.15 | 845.99 |
| 60000.00 | 363.15 | 852.14 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 303.06 | 100.00 | 853.9 |
| 303.07 | 3050.00 | 856.6 |
| 303.26 | 5990.00 | 858.4 |
| 303.22 | 9020.00 | 860.5 |
| 303.23 | 11990.00 | 862.5 |
| 303.24 | 15030.00 | 864.5 |
| 313.08 | 100.00 | 846.3 |
| 313.08 | 3010.00 | 848.3 |
| 313.10 | 5980.00 | 850.4 |
| 313.15 | 9030.00 | 852.6 |
| 313.17 | 12010.00 | 854.4 |
| 313.26 | 15030.00 | 857.5 |
| 323.14 | 100.00 | 838.3 |
| 323.09 | 3050.00 | 840.8 |
| 323.17 | 5980.00 | 842.9 |
| 323.17 | 8980.00 | 845.0 |
| 323.17 | 11990.00 | 847.0 |
| 323.18 | 15020.00 | 849.0 |
| 333.17 | 100.00 | 830.8 |
| 333.17 | 3010.00 | 833.0 |
| 333.07 | 6000.00 | 835.8 |
| 333.20 | 9040.00 | 838.1 |
| 333.17 | 12040.00 | 840.3 |
| 333.15 | 15040.00 | 842.5 |
| 342.95 | 100.00 | 823.2 |
| 343.00 | 3000.00 | 825.3 |
| 343.19 | 5980.00 | 828.3 |
| 343.28 | 9020.00 | 830.8 |
| 343.19 | 11980.00 | 832.8 |
| 343.19 | 15020.00 | 834.9 |
| 353.15 | 100.00 | 815.3 |
| 353.15 | 3050.00 | 818.4 |
| 353.20 | 6030.00 | 820.9 |
| 353.19 | 9020.00 | 823.2 |
| 353.18 | 12010.00 | 825.6 |
| 353.19 | 15020.00 | 827.9 |
| Reference | ||
Speed of sound, m/s
Operational condition: Frequency, MHz = 2 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 293.15 | 100.00 | 1339.9 |
| 293.15 | 10000.00 | 1390.8 |
| 293.15 | 20000.00 | 1436.7 |
| 293.15 | 30000.00 | 1479.3 |
| 293.15 | 40000.00 | 1519.0 |
| 293.15 | 50000.00 | 1555.9 |
| 293.15 | 60000.00 | 1591.9 |
| 293.15 | 70000.00 | 1626.2 |
| 293.15 | 80000.00 | 1659.7 |
| 293.15 | 90000.00 | 1690.9 |
| 293.15 | 100000.00 | 1720.9 |
| 293.15 | 120000.00 | 1778.5 |
| 313.15 | 100.00 | 1266.1 |
| 313.15 | 10000.00 | 1317.6 |
| 313.15 | 20000.00 | 1365.0 |
| 313.15 | 30000.00 | 1409.3 |
| 313.15 | 40000.00 | 1452.1 |
| 313.15 | 50000.00 | 1491.4 |
| 313.15 | 60000.00 | 1529.2 |
| 313.15 | 70000.00 | 1564.8 |
| 313.15 | 80000.00 | 1600.2 |
| 313.15 | 90000.00 | 1632.3 |
| 313.15 | 100000.00 | 1663.0 |
| 313.15 | 120000.00 | 1721.9 |
| 313.15 | 140000.00 | 1777.9 |
| 313.15 | 160000.00 | 1830.9 |
| 333.15 | 100.00 | 1194.0 |
| 333.15 | 10000.00 | 1250.3 |
| 333.15 | 20000.00 | 1300.9 |
| 333.15 | 30000.00 | 1348.0 |
| 333.15 | 40000.00 | 1393.4 |
| 333.15 | 50000.00 | 1434.3 |
| 333.15 | 60000.00 | 1473.3 |
| 333.15 | 70000.00 | 1509.8 |
| 333.15 | 80000.00 | 1545.4 |
| 333.15 | 90000.00 | 1578.6 |
| 333.15 | 100000.00 | 1610.9 |
| 333.15 | 120000.00 | 1674.1 |
| 333.15 | 140000.00 | 1730.4 |
| 333.15 | 160000.00 | 1782.7 |
| 333.15 | 180000.00 | 1835.3 |
| 333.15 | 200000.00 | 1883.8 |
| 353.15 | 100.00 | 1125.7 |
| 353.15 | 10000.00 | 1186.0 |
| 353.15 | 20000.00 | 1240.6 |
| 353.15 | 30000.00 | 1290.3 |
| 353.15 | 40000.00 | 1337.1 |
| 353.15 | 50000.00 | 1379.7 |
| 353.15 | 60000.00 | 1419.8 |
| 353.15 | 70000.00 | 1458.8 |
| 353.15 | 80000.00 | 1496.2 |
| 353.15 | 90000.00 | 1530.6 |
| 353.15 | 100000.00 | 1564.4 |
| 353.15 | 120000.00 | 1627.0 |
| 353.15 | 140000.00 | 1685.1 |
| 353.15 | 160000.00 | 1740.7 |
| 353.15 | 180000.00 | 1793.6 |
| 353.15 | 200000.00 | 1843.5 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [318.81; 749.71] | 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 | 1.55710e+01 | |||
| Coefficient B | 1.27904e+00 | |||
| Coefficient C | -6.43200e-04 | |||
| Coefficient D | 9.83000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 318.81 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 391.92 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 457.99 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 517.34 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 570.28 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 617.12 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 658.18 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 693.75 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 724.16 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 749.71 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [412.32; 573.39] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.52891e+01 | |||
| Coefficient B | -4.79892e+03 | |||
| Coefficient C | -9.24240e+01 | |||
| Temperature range, min. | 412.32 | |||
| Temperature range, max. | 573.39 | |||
| Pvap | 1.33 | kPa | 412.32 | Calculated Property |
| Pvap | 2.95 | kPa | 430.22 | Calculated Property |
| Pvap | 6.03 | kPa | 448.11 | Calculated Property |
| Pvap | 11.51 | kPa | 466.01 | Calculated Property |
| Pvap | 20.71 | kPa | 483.91 | Calculated Property |
| Pvap | 35.40 | kPa | 501.80 | Calculated Property |
| Pvap | 57.84 | kPa | 519.70 | Calculated Property |
| Pvap | 90.85 | kPa | 537.60 | Calculated Property |
| Pvap | 137.80 | kPa | 555.49 | Calculated Property |
| Pvap | 202.64 | kPa | 573.39 | Calculated Property |
Similar Compounds
Find more compounds similar to Dodecanoic acid, ethyl ester.
Mixtures
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Octadecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Octadecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Tetradecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Dodecane
- Hexadecane + Dodecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Ethanol
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Tetradecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Ethyl Oleate
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Ethyl Oleate
- Dodecanoic acid, ethyl ester + Nonanoic acid, 3-methylbutyl ester
- Isoamyl laurate + Dodecanoic acid, ethyl ester
- Carbon dioxide + Dodecanoic acid, ethyl ester
- Cyclohexane, ethyl- + Dodecanoic acid, ethyl ester
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Measurement and correlation of vapor liquid equilibria for ethanol + ethyl laurate and ethanol + ethyl myristate systems near critical temperature of ethanol
- Solid liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate
- Solid-liquid equilibrium in ternary mixtures of ethyl laurate, ethyl palmitate and ethyl stearate
- Solid-liquid equilibrium in ternary mixtures of ethyl laurate, ethyl palmitate and ethyl myristate
- High pressure solid-liquid equilibrium of fatty acid ethyl esters binary systems
- Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
- Experimental and correlational study of isobaric molar heat capacities of fatty acid esters: Ethyl nonanoate and ethyl dodecanoate
- Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
- Measurement and correlation of density and viscosity of n-hexadecane with three fatty acid ethyl esters
- High-pressure liquid densities and derived thermodynamic properties for methyl laurate and ethyl laurate
- Phase equilibrium measurements and thermodynamic modeling of binary mixtures containing a diesel compound n-dodecane + biodiesel compounds: Ethyl dodecanoate and ethyl octanoate
- Measurement of speed of sound, density compressibility and viscosity in liquid methyl laurate and ethyl laurate up to 200 MPa by using acoustic wave sensors
- Thermophysical properties of fatty acid methyl and ethyl esters
- Measurement and correlation of viscosities and densities of methyl dodecanoate and ethyl dodecanoate at elevated pressures
- High Pressure Phase Equilibria of the CO2/Saturated Ethyl Esters Homologous Series
- Influence of Additives (Isoamyl Laurate or Isoamyl Nonanoate) in the Solid-Liquid Equilibrium of Fatty Acid Ethyl Esters
- Density, Viscosity, and Refractive Index of Binary Mixtures of Fatty Acid Ethyl Esters with Ethylcyclohexane
- Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
- Experimental Vapor Pressures of Five Saturated Fatty Acid Ethyl Ester (FAEE) Components of Biodiesel
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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