- InChI
- InChI=1S/C11H22O2/c1-3-4-5-6-7-8-9-10-11(12)13-2/h3-10H2,1-2H3
- InChI Key
- YRHYCMZPEVDGFQ-UHFFFAOYSA-N
- Formula
- C11H22O2
- SMILES
- CCCCCCCCCC(=O)OC
- Molecular Weight1
- 186.30
- CAS
- 110-42-9
- Other Names
-
- Capric acid methyl ester
- Decanoic acid methyl ester
- Metholene 2095
- Methyl n-decanoate
- Methyl tridecanoate
- Methyl-n-caprate
- Uniphat A30
- capric acid, methyl ester
- methyl caprate
- methyl caprinate
- methyl decanoate
- n-Capric acid methyl ester
- 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).
- μ : Dipole Moment (debye).
- 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.5491; 0.6030] |
|
|
| ω | 0.6030 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.5491 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | [-6831.90; -6799.00] | kJ/mol |
|
| ΔcH°liquid | -6799.00 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -6831.90 ± 1.70 | kJ/mol | NIST |
| μ | 2.08 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -256.27 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -573.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 35.92 | kJ/mol | Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K |
| ΔvapH° | [66.10; 66.90] | kJ/mol |
|
| ΔvapH° | 66.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 66.90 | kJ/mol | NIST |
| ΔvapH° | 66.30 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 66.75 ± 0.57 | kJ/mol | NIST |
| ΔvapH° | 66.80 ± 0.60 | kJ/mol | NIST |
| IE | 9.68 | eV | Relay (1.0) Calculated Property |
| log10WS | [-4.69; -4.63] |
|
|
| log10WS | -4.63 | Aq. Solubility Prediction | |
| log10WS | -4.69 | Estimated Solubility | |
| logPoct/wat | 3.300 | Crippen Calculated Property | |
| McVol | 173.290 | ml/mol | McGowan Calculated Property |
| Pc | [1889.71; 1890.00] | kPa |
|
| Pc | 1889.71 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 1890.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 5.68e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [224.56; 1333.00] |
|
|
| Inp | 1323.80 | NIST | |
| Inp | 1319.30 | NIST | |
| Inp | 1313.00 | NIST | |
| Inp | 1321.00 | NIST | |
| Inp | 1312.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1328.00 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1327.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1325.10 | NIST | |
| Inp | 1328.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1312.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1311.40 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1306.20 | NIST | |
| Inp | 1306.60 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1303.76 | NIST | |
| Inp | 1309.67 | NIST | |
| Inp | 1309.08 | NIST | |
| Inp | 1320.62 | NIST | |
| Inp | 1311.06 | NIST | |
| Inp | 1313.09 | NIST | |
| Inp | 1306.48 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1322.60 | NIST | |
| Inp | 1328.60 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1321.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1316.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1333.00 | NIST | |
| Inp | 1327.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1327.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1313.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1323.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1328.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1322.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1302.00 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1329.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1328.00 | NIST | |
| Inp | 1328.00 | NIST | |
| Inp | 1314.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | Outlier 224.56 | NIST | |
| Inp | Outlier 226.16 | NIST | |
| Inp | Outlier 230.80 | NIST | |
| Inp | Outlier 226.04 | NIST | |
| Inp | Outlier 226.04 | NIST | |
| Inp | 1324.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1311.40 | NIST | |
| Inp | 1303.76 | NIST | |
| Inp | 1313.09 | NIST | |
| Inp | 1321.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1323.00 | NIST | |
| Inp | 1328.00 | NIST | |
| Inp | Outlier 226.04 | NIST | |
| Ip | [1550.00; 1636.00] |
|
|
| Ip | 1597.00 | NIST | |
| Ip | Outlier 1636.00 | NIST | |
| Ip | 1624.00 | NIST | |
| Ip | 1570.00 | NIST | |
| Ip | 1598.30 | NIST | |
| Ip | 1603.00 | NIST | |
| Ip | 1605.20 | NIST | |
| Ip | 1616.30 | NIST | |
| Ip | 1592.50 | NIST | |
| Ip | 1600.70 | NIST | |
| Ip | 1606.90 | NIST | |
| Ip | 1613.20 | NIST | |
| Ip | 1581.00 | NIST | |
| Ip | 1581.00 | NIST | |
| Ip | 1592.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1615.00 | NIST | |
| Ip | 1586.00 | NIST | |
| Ip | 1583.00 | NIST | |
| Ip | 1614.00 | NIST | |
| Ip | 1597.00 | NIST | |
| Ip | 1603.00 | NIST | |
| Ip | 1586.00 | NIST | |
| Ip | 1590.00 | NIST | |
| Ip | 1613.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1594.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | Outlier 1550.00 | NIST | |
| Ip | Outlier 1552.00 | NIST | |
| Ip | 1590.00 | NIST | |
| Ip | 1586.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1581.00 | NIST | |
| Ip | 1602.00 | NIST | |
| Ip | 1583.00 | NIST | |
| Ip | 1584.00 | NIST | |
| Ip | 1595.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1628.00 | NIST | |
| Ip | 1628.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1628.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1581.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1586.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1597.00 | NIST | |
| Ip | 1603.00 | NIST | |
| Ip | 1606.90 | NIST | |
| Tboil | [497.05; 505.00] | K |
|
| Tboil | 505.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 497.20 | K | NIST |
| Tboil | 497.05 ± 1.00 | K | NIST |
| Tc | [681.00; 681.00] | K |
|
| Tc | 681.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 681.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [255.15; 260.40] | K |
|
| Tfus | 255.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 255.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 260.40 ± 0.05 | K | NIST |
| Ttriple | 255.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 6.90 | ChemSep v8.3 pure component data Compiled value | |
| URi | 8.20 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.671; 0.714] | m3/kmol |
|
| Vc | 0.671 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.714 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2430000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [381.20; 387.20] | K | [1.30; 2.00] |
|
| Tboilr | 381.20 | K | 1.30 | NIST |
| Tboilr | 387.20 | K | 2.00 | NIST |
Datasets
- Molar heat capacity at constant pressure, J/K/mol (1)
- Viscosity, Pa*s (1)
- Mass density, kg/m3 (1)
- Speed of sound, m/s (1)
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 100.00 | 313.71 | 383.90 |
| 4070.00 | 313.82 | 382.10 |
| 8030.00 | 313.83 | 380.50 |
| 12010.00 | 313.99 | 378.50 |
| 16140.00 | 314.01 | 376.60 |
| 100.00 | 324.79 | 387.60 |
| 4070.00 | 324.79 | 386.00 |
| 8030.00 | 325.01 | 384.40 |
| 12010.00 | 325.06 | 382.50 |
| 16140.00 | 325.20 | 379.30 |
| 100.00 | 334.12 | 393.20 |
| 4070.00 | 334.53 | 390.30 |
| 8030.00 | 334.33 | 388.30 |
| 12010.00 | 334.60 | 386.20 |
| 16140.00 | 334.84 | 384.20 |
| Reference | ||
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 101.30 | 293.15 | 0.0022 |
| 20000.00 | 293.15 | 0.0027 |
| 40000.00 | 293.15 | 0.0032 |
| 60000.00 | 293.15 | 0.0039 |
| 80000.00 | 293.15 | 0.0047 |
| 100000.00 | 293.15 | 0.0055 |
| 120000.00 | 293.15 | 0.0065 |
| 140000.00 | 293.15 | 0.0077 |
| 160000.00 | 293.15 | 0.0090 |
| 101.30 | 313.15 | 0.0015 |
| 20000.00 | 313.15 | 0.0018 |
| 40000.00 | 313.15 | 0.0022 |
| 60000.00 | 313.15 | 0.0027 |
| 80000.00 | 313.15 | 0.0031 |
| 100000.00 | 313.15 | 0.0036 |
| 120000.00 | 313.15 | 0.0042 |
| 140000.00 | 313.15 | 0.0049 |
| 160000.00 | 313.15 | 0.0056 |
| 180000.00 | 313.15 | 0.0063 |
| 200000.00 | 313.15 | 0.0072 |
| 101.30 | 333.15 | 0.0011 |
| 20000.00 | 333.15 | 0.0013 |
| 40000.00 | 333.15 | 0.0016 |
| 60000.00 | 333.15 | 0.0019 |
| 80000.00 | 333.15 | 0.0022 |
| 100000.00 | 333.15 | 0.0025 |
| 120000.00 | 333.15 | 0.0029 |
| 140000.00 | 333.15 | 0.0033 |
| 160000.00 | 333.15 | 0.0037 |
| 180000.00 | 333.15 | 0.0042 |
| 200000.00 | 333.15 | 0.0047 |
| 101.30 | 353.15 | 0.0008 |
| 20000.00 | 353.15 | 0.0010 |
| 40000.00 | 353.15 | 0.0012 |
| 60000.00 | 353.15 | 0.0014 |
| 80000.00 | 353.15 | 0.0016 |
| 100000.00 | 353.15 | 0.0019 |
| 120000.00 | 353.15 | 0.0021 |
| 140000.00 | 353.15 | 0.0024 |
| 160000.00 | 353.15 | 0.0027 |
| 180000.00 | 353.15 | 0.0030 |
| 200000.00 | 353.15 | 0.0034 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 868.0 |
| 298.15 | 3000.00 | 870.0 |
| 298.15 | 6000.00 | 872.0 |
| 298.15 | 9000.00 | 874.0 |
| 298.15 | 12000.00 | 877.0 |
| 298.15 | 15000.00 | 878.0 |
| 308.15 | 100.00 | 860.0 |
| 308.15 | 3010.00 | 862.0 |
| 308.15 | 6000.00 | 864.0 |
| 308.15 | 9000.00 | 866.0 |
| 308.15 | 12000.00 | 869.0 |
| 308.15 | 15000.00 | 871.0 |
| 318.15 | 100.00 | 853.0 |
| 318.15 | 3000.00 | 854.0 |
| 318.15 | 6000.00 | 856.0 |
| 318.15 | 9000.00 | 859.0 |
| 318.15 | 12000.00 | 861.0 |
| 318.15 | 15000.00 | 863.0 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 283.15 | 101.30 | 1362.6 |
| 283.15 | 10000.00 | 1408.9 |
| 283.15 | 20000.00 | 1452.2 |
| 283.15 | 30000.00 | 1493.2 |
| 283.15 | 40000.00 | 1531.7 |
| 283.15 | 50000.00 | 1568.0 |
| 283.15 | 60000.00 | 1602.6 |
| 283.15 | 70000.00 | 1634.5 |
| 283.15 | 80000.00 | 1666.4 |
| 283.15 | 90000.00 | 1696.9 |
| 283.15 | 100000.00 | 1726.9 |
| 283.15 | 110000.00 | 1755.2 |
| 283.15 | 120000.00 | 1783.4 |
| 283.15 | 130000.00 | 1809.5 |
| 283.15 | 140000.00 | 1835.9 |
| 303.15 | 101.30 | 1287.7 |
| 303.15 | 10000.00 | 1339.2 |
| 303.15 | 20000.00 | 1385.8 |
| 303.15 | 30000.00 | 1429.6 |
| 303.15 | 40000.00 | 1470.3 |
| 303.15 | 50000.00 | 1508.7 |
| 303.15 | 60000.00 | 1544.9 |
| 303.15 | 70000.00 | 1580.2 |
| 303.15 | 80000.00 | 1614.1 |
| 303.15 | 90000.00 | 1646.1 |
| 303.15 | 100000.00 | 1676.9 |
| 303.15 | 110000.00 | 1706.8 |
| 303.15 | 120000.00 | 1735.1 |
| 303.15 | 130000.00 | 1762.8 |
| 303.15 | 140000.00 | 1789.2 |
| 303.15 | 150000.00 | 1815.2 |
| 303.15 | 170000.00 | 1864.9 |
| 303.15 | 190000.00 | 1912.7 |
| 303.15 | 210000.00 | 1957.6 |
| 323.15 | 101.30 | 1214.8 |
| 323.15 | 10000.00 | 1269.1 |
| 323.15 | 20000.00 | 1319.3 |
| 323.15 | 30000.00 | 1365.7 |
| 323.15 | 40000.00 | 1409.0 |
| 323.15 | 50000.00 | 1449.5 |
| 323.15 | 60000.00 | 1487.8 |
| 323.15 | 70000.00 | 1524.0 |
| 323.15 | 80000.00 | 1558.3 |
| 323.15 | 90000.00 | 1591.2 |
| 323.15 | 100000.00 | 1623.3 |
| 323.15 | 110000.00 | 1653.9 |
| 323.15 | 120000.00 | 1684.6 |
| 323.15 | 130000.00 | 1711.9 |
| 323.15 | 140000.00 | 1739.6 |
| 323.15 | 150000.00 | 1765.9 |
| 323.15 | 170000.00 | 1817.0 |
| 323.15 | 190000.00 | 1864.8 |
| 323.15 | 210000.00 | 1910.9 |
| 343.15 | 101.30 | 1142.8 |
| 343.15 | 10000.00 | 1202.4 |
| 343.15 | 20000.00 | 1255.9 |
| 343.15 | 30000.00 | 1304.9 |
| 343.15 | 40000.00 | 1350.5 |
| 343.15 | 50000.00 | 1393.5 |
| 343.15 | 60000.00 | 1433.7 |
| 343.15 | 70000.00 | 1471.7 |
| 343.15 | 80000.00 | 1508.2 |
| 343.15 | 90000.00 | 1541.7 |
| 343.15 | 100000.00 | 1574.1 |
| 343.15 | 110000.00 | 1606.0 |
| 343.15 | 120000.00 | 1636.2 |
| 343.15 | 130000.00 | 1665.9 |
| 343.15 | 140000.00 | 1694.0 |
| 343.15 | 150000.00 | 1721.2 |
| 343.15 | 170000.00 | 1773.2 |
| 343.15 | 190000.00 | 1822.0 |
| 343.15 | 210000.00 | 1868.7 |
| 363.15 | 10000.00 | 1138.5 |
| 363.15 | 20000.00 | 1195.9 |
| 363.15 | 30000.00 | 1247.9 |
| 363.15 | 40000.00 | 1296.3 |
| 363.15 | 50000.00 | 1341.1 |
| 363.15 | 60000.00 | 1382.7 |
| 363.15 | 70000.00 | 1421.6 |
| 363.15 | 80000.00 | 1458.4 |
| 363.15 | 90000.00 | 1493.8 |
| 363.15 | 100000.00 | 1527.4 |
| 363.15 | 110000.00 | 1559.7 |
| 363.15 | 120000.00 | 1590.9 |
| 363.15 | 130000.00 | 1620.7 |
| 363.15 | 140000.00 | 1649.4 |
| 363.15 | 150000.00 | 1677.2 |
| 363.15 | 170000.00 | 1730.6 |
| 363.15 | 190000.00 | 1780.4 |
| 363.15 | 210000.00 | 1827.2 |
| 383.15 | 10000.00 | 1077.4 |
| 383.15 | 20000.00 | 1138.6 |
| 383.15 | 30000.00 | 1193.5 |
| 383.15 | 40000.00 | 1244.5 |
| 383.15 | 50000.00 | 1291.3 |
| 383.15 | 60000.00 | 1334.9 |
| 383.15 | 70000.00 | 1375.4 |
| 383.15 | 80000.00 | 1414.2 |
| 383.15 | 90000.00 | 1450.6 |
| 383.15 | 100000.00 | 1485.3 |
| 383.15 | 110000.00 | 1518.9 |
| 383.15 | 120000.00 | 1550.9 |
| 383.15 | 130000.00 | 1581.2 |
| 383.15 | 140000.00 | 1610.8 |
| 383.15 | 150000.00 | 1641.0 |
| 383.15 | 170000.00 | 1692.7 |
| 383.15 | 190000.00 | 1743.0 |
| 383.15 | 210000.00 | 1791.1 |
| 403.15 | 10000.00 | 1017.7 |
| 403.15 | 20000.00 | 1083.2 |
| 403.15 | 30000.00 | 1141.7 |
| 403.15 | 40000.00 | 1194.7 |
| 403.15 | 50000.00 | 1242.9 |
| 403.15 | 60000.00 | 1288.1 |
| 403.15 | 70000.00 | 1330.6 |
| 403.15 | 80000.00 | 1370.3 |
| 403.15 | 90000.00 | 1407.7 |
| 403.15 | 100000.00 | 1442.8 |
| 403.15 | 110000.00 | 1476.6 |
| 403.15 | 120000.00 | 1509.7 |
| 403.15 | 130000.00 | 1541.7 |
| 403.15 | 140000.00 | 1571.6 |
| 403.15 | 150000.00 | 1600.1 |
| 403.15 | 170000.00 | 1655.5 |
| 403.15 | 190000.00 | 1706.6 |
| 403.15 | 210000.00 | 1754.5 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [271.79; 687.64] | J/mol×K | [298.15; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.09900e+02 | |||
| Coefficient B | 4.13910e+02 | |||
| Coefficient C | 7.77290e+02 | |||
| Coefficient D | 2.61610e+02 | |||
| Coefficient E | 2.44530e+03 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 271.79 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 365.14 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 441.66 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 499.95 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 547.08 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 586.82 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 620.38 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 648.15 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 670.41 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 687.64 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [346.77; 488.59] | J/mol×K | [255.15; 505.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 2.01940e+02 | |||
| Coefficient B | 5.67630e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.15 | |||
| Temperature range, max. | 505.00 | |||
| Cp,liquid | 346.77 | J/mol×K | 255.15 | Calculated Property |
| Cp,liquid | 362.53 | J/mol×K | 282.91 | Calculated Property |
| Cp,liquid | 378.29 | J/mol×K | 310.67 | Calculated Property |
| Cp,liquid | 394.04 | J/mol×K | 338.43 | Calculated Property |
| Cp,liquid | 409.80 | J/mol×K | 366.19 | Calculated Property |
| Cp,liquid | 425.56 | J/mol×K | 393.96 | Calculated Property |
| Cp,liquid | 441.32 | J/mol×K | 421.72 | Calculated Property |
| Cp,liquid | 457.08 | J/mol×K | 449.48 | Calculated Property |
| Cp,liquid | 472.84 | J/mol×K | 477.24 | Calculated Property |
| Cp,liquid | 488.59 | J/mol×K | 505.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0049544; 0.0002018] | Pa×s | [255.15; 505.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.17770e+01 | |||
| Coefficient B | 1.65070e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.15 | |||
| Temperature range, max. | 505.00 | |||
| η | 0.0049544 | Pa×s | 255.15 | Calculated Property |
| η | 0.0026260 | Pa×s | 282.91 | Calculated Property |
| η | 0.0015590 | Pa×s | 310.67 | Calculated Property |
| η | 0.0010083 | Pa×s | 338.43 | Calculated Property |
| η | 0.0006966 | Pa×s | 366.19 | Calculated Property |
| η | 0.0005070 | Pa×s | 393.96 | Calculated Property |
| η | 0.0003848 | Pa×s | 421.72 | Calculated Property |
| η | 0.0003022 | Pa×s | 449.48 | Calculated Property |
| η | 0.0002440 | Pa×s | 477.24 | Calculated Property |
| η | 0.0002018 | Pa×s | 505.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [69.13; 0.00] | kJ/mol | [255.15; 681.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 8.78330e+01 | |||
| Coefficient B | 5.92850e-01 | |||
| Coefficient C | -2.70010e-01 | |||
| Coefficient D | 1.31770e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.81000e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 686.9 K. | |||
| Temperature range, min. | 255.15 | |||
| Temperature range, max. | 681.00 | |||
| ΔvapH | 69.13 | kJ/mol | 255.15 | Calculated Property |
| ΔvapH | 65.53 | kJ/mol | 302.47 | Calculated Property |
| ΔvapH | 61.75 | kJ/mol | 349.78 | Calculated Property |
| ΔvapH | 57.70 | kJ/mol | 397.10 | Calculated Property |
| ΔvapH | 53.28 | kJ/mol | 444.42 | Calculated Property |
| ΔvapH | 48.33 | kJ/mol | 491.73 | Calculated Property |
| ΔvapH | 42.58 | kJ/mol | 539.05 | Calculated Property |
| ΔvapH | 35.57 | kJ/mol | 586.37 | Calculated Property |
| ΔvapH | 26.06 | kJ/mol | 633.68 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 681.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [381.00; 520.45] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.61003e+01 | |||
| Coefficient B | -4.73527e+03 | |||
| Coefficient C | -8.15400e+01 | |||
| Temperature range, min. | 381.00 | |||
| Temperature range, max. | 520.45 | |||
| Pvap | 1.33 | kPa | 381.00 | Calculated Property |
| Pvap | 2.90 | kPa | 396.49 | Calculated Property |
| Pvap | 5.87 | kPa | 411.99 | Calculated Property |
| Pvap | 11.16 | kPa | 427.48 | Calculated Property |
| Pvap | 20.07 | kPa | 442.98 | Calculated Property |
| Pvap | 34.39 | kPa | 458.47 | Calculated Property |
| Pvap | 56.47 | kPa | 473.97 | Calculated Property |
| Pvap | 89.30 | kPa | 489.46 | Calculated Property |
| Pvap | 136.56 | kPa | 504.96 | Calculated Property |
| Pvap | 202.67 | kPa | 520.45 | Calculated Property |
| Pvap | [5.69e-05; 1814.95] | kPa | [255.15; 681.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.59832e+01 | |||
| Coefficient B | -1.07940e+04 | |||
| Coefficient C | -9.64540e+00 | |||
| Coefficient D | 2.93910e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 686.9 K. | |||
| Temperature range, min. | 255.15 | |||
| Temperature range, max. | 681.00 | |||
| Pvap | 5.69e-05 | kPa | 255.15 | Calculated Property |
| Pvap | 8.27e-03 | kPa | 302.47 | Calculated Property |
| Pvap | 0.25 | kPa | 349.78 | Calculated Property |
| Pvap | 2.98 | kPa | 397.10 | Calculated Property |
| Pvap | 18.40 | kPa | 444.42 | Calculated Property |
| Pvap | 73.13 | kPa | 491.73 | Calculated Property |
| Pvap | 213.48 | kPa | 539.05 | Calculated Property |
| Pvap | 500.28 | kPa | 586.37 | Calculated Property |
| Pvap | 1004.28 | kPa | 633.68 | Calculated Property |
| Pvap | 1814.95 | kPa | 681.00 | Calculated Property |
| Pvap | [1.41; 31.13] | kPa | [380.50; 461.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53721e+01 | |||
| Coefficient B | -4.69188e+03 | |||
| Coefficient C | -6.82460e+01 | |||
| Reference | Rose and Supina, 1961 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 380.50 | |||
| Temperature range, max. | 461.40 | |||
| Pvap | 1.41 | kPa | 380.50 | Calculated Property |
| Pvap | 2.15 | kPa | 389.49 | Calculated Property |
| Pvap | 3.20 | kPa | 398.48 | Calculated Property |
| Pvap | 4.67 | kPa | 407.47 | Calculated Property |
| Pvap | 6.67 | kPa | 416.46 | Calculated Property |
| Pvap | 9.36 | kPa | 425.44 | Calculated Property |
| Pvap | 12.93 | kPa | 434.43 | Calculated Property |
| Pvap | 17.57 | kPa | 443.42 | Calculated Property |
| Pvap | 23.55 | kPa | 452.41 | Calculated Property |
| Pvap | 31.13 | kPa | 461.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [900.39; 375.06] | kg/m3 | [255.15; 681.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 6.33445e+01 | |||
| Coefficient B | 2.42920e-01 | |||
| Coefficient C | 6.86900e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 686.9 K. | |||
| Temperature range, min. | 255.15 | |||
| Temperature range, max. | 681.00 | |||
| ρl | 900.39 | kg/m3 | 255.15 | Calculated Property |
| ρl | 864.72 | kg/m3 | 302.47 | Calculated Property |
| ρl | 827.37 | kg/m3 | 349.78 | Calculated Property |
| ρl | 787.94 | kg/m3 | 397.10 | Calculated Property |
| ρl | 745.84 | kg/m3 | 444.42 | Calculated Property |
| ρl | 700.16 | kg/m3 | 491.73 | Calculated Property |
| ρl | 649.36 | kg/m3 | 539.05 | Calculated Property |
| ρl | 590.39 | kg/m3 | 586.37 | Calculated Property |
| ρl | 515.42 | kg/m3 | 633.68 | Calculated Property |
| ρl | 375.06 | kg/m3 | 681.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.01] | N/m | [255.15; 496.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.52413e-02 | |||
| Coefficient B | -9.12000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.15 | |||
| Temperature range, max. | 496.15 | |||
| γ | 0.03 | N/m | 255.15 | Calculated Property |
| γ | 0.03 | N/m | 281.93 | Calculated Property |
| γ | 0.03 | N/m | 308.71 | Calculated Property |
| γ | 0.02 | N/m | 335.48 | Calculated Property |
| γ | 0.02 | N/m | 362.26 | Calculated Property |
| γ | 0.02 | N/m | 389.04 | Calculated Property |
| γ | 0.02 | N/m | 415.82 | Calculated Property |
| γ | 0.01 | N/m | 442.59 | Calculated Property |
| γ | 0.01 | N/m | 469.37 | Calculated Property |
| γ | 0.01 | N/m | 496.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.06] | W/m×K | [505.00; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.20890e-06 | |||
| Coefficient B | 1.47900e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 505.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 505.00 | Calculated Property |
| λgas | 0.03 | W/m×K | 560.00 | Calculated Property |
| λgas | 0.03 | W/m×K | 615.00 | Calculated Property |
| λgas | 0.03 | W/m×K | 670.00 | Calculated Property |
| λgas | 0.04 | W/m×K | 725.00 | Calculated Property |
| λgas | 0.04 | W/m×K | 780.00 | Calculated Property |
| λgas | 0.05 | W/m×K | 835.00 | Calculated Property |
| λgas | 0.05 | W/m×K | 890.00 | Calculated Property |
| λgas | 0.06 | W/m×K | 945.00 | Calculated Property |
| λgas | 0.06 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.09] | W/m×K | [255.15; 537.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 1.97420e-01 | |||
| Coefficient B | -2.07730e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.15 | |||
| Temperature range, max. | 537.00 | |||
| λliquid | 0.14 | W/m×K | 255.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 286.47 | Calculated Property |
| λliquid | 0.13 | W/m×K | 317.78 | Calculated Property |
| λliquid | 0.12 | W/m×K | 349.10 | Calculated Property |
| λliquid | 0.12 | W/m×K | 380.42 | Calculated Property |
| λliquid | 0.11 | W/m×K | 411.73 | Calculated Property |
| λliquid | 0.11 | W/m×K | 443.05 | Calculated Property |
| λliquid | 0.10 | W/m×K | 474.37 | Calculated Property |
| λliquid | 0.09 | W/m×K | 505.68 | Calculated Property |
| λliquid | 0.09 | W/m×K | 537.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Decanoic acid, methyl ester.
Mixtures
- Dodecanoic acid, methyl ester + Decanoic acid, methyl ester
- Octanoic acid, methyl ester + Decanoic acid, methyl ester
- Decanoic acid, methyl ester + Cyclohexane, methyl-
- 1-Propanol + Decanoic acid, methyl ester
- 1-Butanol + Decanoic acid, methyl ester
- 1-Pentanol + Decanoic acid, methyl ester
- Ethane + Decanoic acid, methyl ester
- Heptane + Decanoic acid, methyl ester
- Dodecane + Decanoic acid, methyl ester
- Butanoic acid, methyl ester + Dodecane + Decanoic acid, methyl ester
- Decanoic acid, methyl ester + Tetradecane
- Hexadecane + Decanoic acid, methyl ester
- n-Hexane + Decanoic acid, methyl ester
- Octane + Decanoic acid, methyl ester
- Decane + Decanoic acid, methyl ester
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).
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Phase behaviour of high molecular mass methyl esters in supercritical ethane
- Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
- Experimental vapor pressures (from 1 Pa to 100 kPa) of six saturated Fatty Acid Methyl Esters (FAMEs): Methyl hexanoate, methyl octanoate, methyl decanoate, methyl dodecanoate, methyl tetradecanoate and methyl hexadecanoate
- Isobaric vapor-liquid equilibrium for binary system of methyl caprylate + methyl caprate at 2, 6 and 10 kPa
- Isobaric vapor-liquid equilibrium for binary system of methyl caprate + methyl laurate at 2, 4 and 6 kPa
- Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
- Heat capacities and thermal diffusivities of some n-alkanoic acid methyl esters
- Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
- Thermophysical properties of fatty acid methyl and ethyl esters
- Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
- Isobaric molar heat capacities of binary mixtures containing methyl caprate and methyl laurate at pressures up to 16.2 MPa
- Temperature and pressure dependence of densities and viscosities for binary mixtures of methyl decanoate plus n-heptane
- Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
- Experimental Investigation of the Thermophysical Properties of the Bio-Aviation Fuel Surrogates: Binary and Ternary Mixtures of n-Dodecane, Methyl Butyrate, and Methyl Decanoate
- Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K
- Densities and Viscosities of Fatty Acid Methyl and Ethyl Esters
- Speed of Sound, Density, and Derivative Properties of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Caprate and Ethyl Caprate
- Viscosities of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Caprate and Ethyl Caprate
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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