- InChI
- InChI=1S/C18H36O2/c1-3-5-6-7-8-9-10-11-12-13-14-15-16-17-18(19)20-4-2/h3-17H2,1-2H3
- InChI Key
- XIRNKXNNONJFQO-UHFFFAOYSA-N
- Formula
- C18H36O2
- SMILES
- CCCCCCCCCCCCCCCC(=O)OCC
- Molecular Weight1
- 284.48
- CAS
- 628-97-7
- Other Names
-
- Ethyl hexadecanoate
- Ethyl hexadecanoate (Ethyl palmitate)
- Ethyl n-hexadecanoate
- Ethyl palmitate
- Palmitic acid, ethyl ester
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH : Enthalpy of sublimation 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.
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.8919 | Relay (... Calculated Property | |
| ΔcH°liquid | -11368.00 ± 1.00 | kJ/mol | NIST |
| ΔfG° | -133.24 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -740.04 | kJ/mol | Relay (... Calculated Property |
| ΔfusH° | 55.75 | kJ/mol | Solid l... |
| ΔvapH° | 94.13 | kJ/mol | Relay (... Calculated Property |
| IE | 9.69 | eV | Relay (... Calculated Property |
| log10WS | -6.35 | Relay (... Calculated Property | |
| logPoct/wat | 6.031 | Crippen Calculated Property | |
| McVol | 271.920 | ml/mol | McGowan Calculated Property |
| Pc | 1189.06 | kPa | Joback Calculated Property |
| Inp | [341.90; 2013.00] |
|
|
| Inp | 1976.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1982.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1992.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1990.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1990.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1996.00 | NIST | |
| Inp | 1995.70 | NIST | |
| Inp | 1995.70 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1966.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1983.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1991.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1993.50 | NIST | |
| Inp | 2013.00 | NIST | |
| Inp | 1999.00 | NIST | |
| Inp | 1991.00 | NIST | |
| Inp | 1992.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 1985.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1996.00 | NIST | |
| Inp | 1996.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 2005.00 | NIST | |
| Inp | 1996.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1992.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1987.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1990.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1996.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1990.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1995.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1986.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1974.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1995.00 | NIST | |
| Inp | 1992.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1991.00 | NIST | |
| Inp | 1991.00 | NIST | |
| Inp | 1992.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1996.00 | NIST | |
| Inp | 2000.00 | NIST | |
| Inp | 2000.00 | NIST | |
| Inp | 1995.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1992.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1990.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 2000.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 1996.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 2005.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | Outlier 341.90 | NIST | |
| Inp | Outlier 342.60 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1990.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | Outlier 341.90 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1986.00 | NIST | |
| Inp | 1991.00 | NIST | |
| Inp | 2000.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 1976.00 | NIST | |
| I | [2205.00; 2288.00] |
|
|
| I | 2240.00 | NIST | |
| I | 2248.00 | NIST | |
| I | 2245.00 | NIST | |
| I | 2259.00 | NIST | |
| I | 2257.00 | NIST | |
| I | 2273.00 | NIST | |
| I | 2243.00 | NIST | |
| I | 2227.00 | NIST | |
| I | 2235.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2250.00 | NIST | |
| I | 2253.00 | NIST | |
| I | Outlier 2288.00 | NIST | |
| I | 2241.00 | NIST | |
| I | 2226.00 | NIST | |
| I | Outlier 2215.00 | NIST | |
| I | 2252.00 | NIST | |
| I | 2220.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2280.00 | NIST | |
| I | 2238.00 | NIST | |
| I | 2224.00 | NIST | |
| I | 2224.00 | NIST | |
| I | 2224.00 | NIST | |
| I | 2256.00 | NIST | |
| I | 2255.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2258.00 | NIST | |
| I | 2254.00 | NIST | |
| I | Outlier 2205.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2238.00 | NIST | |
| I | 2251.00 | NIST | |
| I | 2259.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2259.00 | NIST | |
| I | 2241.00 | NIST | |
| I | 2259.00 | NIST | |
| I | 2261.00 | NIST | |
| I | Outlier 2207.00 | NIST | |
| I | 2261.00 | NIST | |
| I | 2263.00 | NIST | |
| I | 2281.00 | NIST | |
| I | 2243.00 | NIST | |
| I | 2258.00 | NIST | |
| I | 2276.00 | NIST | |
| I | 2256.00 | NIST | |
| I | 2245.00 | NIST | |
| I | 2257.00 | NIST | |
| I | 2255.00 | NIST | |
| I | 2229.00 | NIST | |
| I | 2260.00 | NIST | |
| I | 2256.00 | NIST | |
| I | 2259.00 | NIST | |
| I | 2249.00 | NIST | |
| I | 2271.00 | NIST | |
| I | 2243.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2271.00 | NIST | |
| I | 2271.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2274.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2248.00 | NIST | |
| I | 2274.00 | NIST | |
| I | 2255.00 | NIST | |
| I | 2274.00 | NIST | |
| I | 2225.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2248.00 | NIST | |
| I | 2229.00 | NIST | |
| I | 2262.00 | NIST | |
| I | 2230.00 | NIST | |
| I | 2262.00 | NIST | |
| I | 2251.00 | NIST | |
| I | 2235.00 | NIST | |
| I | 2245.00 | NIST | |
| I | 2235.00 | NIST | |
| I | 2251.00 | NIST | |
| I | 2259.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 2271.00 | NIST | |
| I | 2248.00 | NIST | |
| I | 2246.00 | NIST | |
| I | 2262.00 | NIST | |
| I | 2261.00 | NIST | |
| I | 2243.00 | NIST | |
| I | 2257.00 | NIST | |
| Tboil | 576.90 | K | Relay (... Calculated Property |
| Tc | 756.04 | K | Relay (... Calculated Property |
| Tfus | [295.20; 298.23] | K |
|
| Tfus | 298.23 | K | Solid-l... |
| Tfus | 297.40 | K | High pr... |
| Tfus | 297.70 | K | Influen... |
| Tfus | 297.70 ± 2.00 | K | NIST |
| Tfus | 297.15 ± 4.00 | K | NIST |
| Tfus | 298.20 ± 2.00 | K | NIST |
| Tfus | 295.20 ± 2.00 | K | NIST |
| Tfus | 295.20 ± 1.50 | K | NIST |
| Vc | 1.072 | m3/kmol | Relay (... Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [789.92; 890.54] | J/mol×K | [687.53; 855.83] |
|
| Cp,gas | 789.92 | J/mol×K | 687.53 | Joback Calculated Property |
| Cp,gas | 808.70 | J/mol×K | 715.58 | Joback Calculated Property |
| Cp,gas | 826.65 | J/mol×K | 743.63 | Joback Calculated Property |
| Cp,gas | 843.80 | J/mol×K | 771.68 | Joback Calculated Property |
| Cp,gas | 860.14 | J/mol×K | 799.73 | Joback Calculated Property |
| Cp,gas | 875.72 | J/mol×K | 827.78 | Joback Calculated Property |
| Cp,gas | 890.54 | J/mol×K | 855.83 | Joback Calculated Property |
| η | [0.0016233; 0.0050107] | Pa×s | [303.15; 363.15] |
|
| η | 0.0050107 | Pa×s | 303.15 | Densiti... |
| η | 0.0044399 | Pa×s | 308.15 | Densiti... |
| η | 0.0039558 | Pa×s | 313.15 | Densiti... |
| η | 0.0035472 | Pa×s | 318.15 | Densiti... |
| η | 0.0031973 | Pa×s | 323.15 | Densiti... |
| η | 0.0028969 | Pa×s | 328.15 | Densiti... |
| η | 0.0026373 | Pa×s | 333.15 | Densiti... |
| η | 0.0024121 | Pa×s | 338.15 | Densiti... |
| η | 0.0022140 | Pa×s | 343.15 | Densiti... |
| η | 0.0020391 | Pa×s | 348.15 | Densiti... |
| η | 0.0018842 | Pa×s | 353.15 | Densiti... |
| η | 0.0017464 | Pa×s | 358.15 | Densiti... |
| η | 0.0016233 | Pa×s | 363.15 | Densiti... |
| ΔfusH | [15.09; 53.14] | kJ/mol | [296.00; 296.40] |
|
| ΔfusH | 53.14 | kJ/mol | 296.00 | NIST |
| ΔfusH | 15.09 | kJ/mol | 296.35 | NIST |
| ΔfusH | 15.09 | kJ/mol | 296.40 | NIST |
| ΔfusH | 15.09 | kJ/mol | 296.40 | NIST |
| ΔsubH | 150.80 | kJ/mol | 290.00 | NIST |
| ΔvapH | [73.90; 100.70] | kJ/mol | [308.00; 447.50] |
|
| ΔvapH | 100.70 | kJ/mol | 308.00 | NIST |
| ΔvapH | 73.90 | kJ/mol | 447.50 | NIST |
| Pvap | [0.10; 9.33] | kPa | [412.63; 515.13] |
|
| Pvap | 0.10 | kPa | 412.63 | Isobari... |
| Pvap | 0.15 | kPa | 419.36 | Isobari... |
| Pvap | 0.20 | kPa | 425.07 | Isobari... |
| Pvap | 0.30 | kPa | 433.31 | Isobari... |
| Pvap | 0.40 | kPa | 438.71 | Isobari... |
| Pvap | 0.50 | kPa | 442.68 | Isobari... |
| Pvap | 0.65 | kPa | 448.35 | Isobari... |
| Pvap | 0.80 | kPa | 452.99 | Isobari... |
| Pvap | 1.00 | kPa | 457.98 | Isobari... |
| Pvap | 1.20 | kPa | 462.64 | Isobari... |
| Pvap | 1.33 | kPa | 464.49 | Determi... |
| Pvap | 1.50 | kPa | 468.07 | Isobari... |
| Pvap | 2.67 | kPa | 481.90 | Determi... |
| Pvap | 4.00 | kPa | 495.23 | Determi... |
| Pvap | 5.33 | kPa | 502.27 | Determi... |
| Pvap | 5.33 | kPa | 502.27 | Vapor l... |
| Pvap | 6.67 | kPa | 508.10 | Determi... |
| Pvap | 8.00 | kPa | 512.23 | Determi... |
| Pvap | 9.33 | kPa | 515.13 | Determi... |
| Pvap | 9.33 | kPa | 515.13 | Vapor l... |
| n0 | 1.43700 | 298.15 | (Vapor ... | |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [464.20; 465.70] | K | [1.30; 1.30] |
|
| Tboilr | 465.70 | K | 1.30 | NIST |
| Tboilr | 464.20 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [477.80; 647.67] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.60464e+01 | |||
| Coefficient B | -5.71995e+03 | |||
| Coefficient C | -1.14830e+02 | |||
| Temperature range, min. | 477.80 | |||
| Temperature range, max. | 647.67 | |||
| Pvap | 1.33 | kPa | 477.80 | Calculated Property |
| Pvap | 2.91 | kPa | 496.67 | Calculated Property |
| Pvap | 5.88 | kPa | 515.55 | Calculated Property |
| Pvap | 11.18 | kPa | 534.42 | Calculated Property |
| Pvap | 20.11 | kPa | 553.30 | Calculated Property |
| Pvap | 34.45 | kPa | 572.17 | Calculated Property |
| Pvap | 56.55 | kPa | 591.05 | Calculated Property |
| Pvap | 89.39 | kPa | 609.92 | Calculated Property |
| Pvap | 136.63 | kPa | 628.80 | Calculated Property |
| Pvap | 202.66 | kPa | 647.67 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexadecanoic acid, ethyl ester.
Mixtures
- Hexadecanoic acid, ethyl ester + Ethyl Oleate
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Ethyl Oleate
- Hexadecanoic acid, ethyl ester + Tetradecanoic acid, ethyl ester
- Hexadecanoic acid, ethyl ester + Octadecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Octadecanoic acid, ethyl ester
- Ethanol + Hexadecanoic acid, ethyl ester
- Hexadecanoic acid, ethyl ester + Linoleic acid ethyl ester
- Hexadecanoic acid, ethyl ester + Nonanoic acid, 3-methylbutyl ester
- Isoamyl laurate + Hexadecanoic acid, ethyl ester
- Dodecanoic acid, ethyl ester + Hexadecanoic acid, ethyl ester + Tetradecanoic acid, ethyl ester
- Carbon dioxide + Hexadecanoic acid, ethyl ester
- Carbon dioxide + Ethanol + Hexadecanoic acid, ethyl ester
- Ethanol + Hexadecanoic acid, ethyl ester + Water
- Ethanol + Hexadecanoic acid, ethyl ester + Glycerin
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Solid liquid equilibrium in ternary mixtures of ethyl oleate, ethyl laurate and ethyl palmitate
- Isobaric vapor liquid equilibrium for binary system of ethyl myristate + ethyl palmitate at 0.5, 1.0 and 1.5 kPa
- LLE for the systems ethyl palmitate (palmiticacid)(1) + ethanol(2) + glycerol (water)(3)
- 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
- Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
- (Vapor + liquid) equilibrium for the binary systems {water + glycerol} and {ethanol + glycerol, ethyl stearate, and ethyl palmitate} at low pressures
- Phase equilibrium measurements and thermodynamic modelling for the system (CO2 + ethyl palmitate + ethanol) at high pressures
- Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
- 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
- Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.