- 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
- 186.29
- CAS
- 110-42-9
- Other Names
-
- Capric acid methyl ester
- Metholene 2095
- Methyl caprate
- Methyl caprinate
- Methyl decanoate
- Methyl n-decanoate
- Methyl tridecanoate
- Methyl-n-caprate
- Uniphat A30
- capric acid, methyl ester
- n-Capric acid methyl ester
- 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).
- 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).
- 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).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×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.
Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| 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 |
| ΔfG° | -192.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -515.17 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 35.92 | kJ/mol | Heat Ca... |
| 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 |
| log10WS | [-4.69; -4.63] |
|
|
| log10WS | -4.63 | Aq. Sol... | |
| log10WS | -4.69 | Estimat... | |
| logPoct/wat | 3.300 | Crippen Calculated Property | |
| McVol | 173.290 | ml/mol | McGowan Calculated Property |
| Pc | 2014.51 | kPa | Joback Calculated Property |
| 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 | |
| I | [1550.00; 1636.00] |
|
|
| I | 1597.00 | NIST | |
| I | Outlier 1636.00 | NIST | |
| I | 1624.00 | NIST | |
| I | 1570.00 | NIST | |
| I | 1598.30 | NIST | |
| I | 1603.00 | NIST | |
| I | 1605.20 | NIST | |
| I | 1616.30 | NIST | |
| I | 1592.50 | NIST | |
| I | 1600.70 | NIST | |
| I | 1606.90 | NIST | |
| I | 1613.20 | NIST | |
| I | 1581.00 | NIST | |
| I | 1581.00 | NIST | |
| I | 1592.00 | NIST | |
| I | 1593.00 | NIST | |
| I | 1615.00 | NIST | |
| I | 1586.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1614.00 | NIST | |
| I | 1597.00 | NIST | |
| I | 1603.00 | NIST | |
| I | 1586.00 | NIST | |
| I | 1590.00 | NIST | |
| I | 1613.00 | NIST | |
| I | 1585.00 | NIST | |
| I | 1594.00 | NIST | |
| I | 1604.00 | NIST | |
| I | 1599.00 | NIST | |
| I | Outlier 1550.00 | NIST | |
| I | Outlier 1552.00 | NIST | |
| I | 1590.00 | NIST | |
| I | 1586.00 | NIST | |
| I | 1596.00 | NIST | |
| I | 1581.00 | NIST | |
| I | 1602.00 | NIST | |
| I | 1583.00 | NIST | |
| I | 1584.00 | NIST | |
| I | 1595.00 | NIST | |
| I | 1593.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1585.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1593.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1585.00 | NIST | |
| I | 1581.00 | NIST | |
| I | 1573.00 | NIST | |
| I | 1600.00 | NIST | |
| I | 1586.00 | NIST | |
| Tboil | [497.05; 497.20] | K |
|
| Tboil | 497.20 | K | NIST |
| Tboil | 497.05 ± 1.00 | K | NIST |
| Tc | 698.36 | K | Joback Calculated Property |
| Tfus | 260.40 ± 0.05 | K | NIST |
| Vc | 0.675 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [415.24; 496.57] | J/mol×K | [527.37; 698.36] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 420 440 460 480 500 550 600 650 700 | ||||
| Cp,gas | 415.24 | J/mol×K | 527.37 | Joback Calculated Property |
| Cp,gas | 430.19 | J/mol×K | 555.87 | Joback Calculated Property |
| Cp,gas | 444.58 | J/mol×K | 584.37 | Joback Calculated Property |
| Cp,gas | 458.41 | J/mol×K | 612.87 | Joback Calculated Property |
| Cp,gas | 471.67 | J/mol×K | 641.36 | Joback Calculated Property |
| Cp,gas | 484.39 | J/mol×K | 669.86 | Joback Calculated Property |
| Cp,gas | 496.57 | J/mol×K | 698.36 | Joback Calculated Property |
| Cp,liquid | [382.80; 417.20] | J/mol×K | [298.15; 373.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 380 390 400 410 420 300 320 340 360 | ||||
| Cp,liquid | 382.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 384.70 | J/mol×K | 303.15 | Heat ca... |
| Cp,liquid | 387.60 | J/mol×K | 313.15 | Heat ca... |
| Cp,liquid | 391.80 | J/mol×K | 323.15 | Heat ca... |
| Cp,liquid | 396.70 | J/mol×K | 333.15 | Heat ca... |
| Cp,liquid | 401.90 | J/mol×K | 343.15 | Heat ca... |
| Cp,liquid | 407.30 | J/mol×K | 353.15 | Heat ca... |
| Cp,liquid | 412.40 | J/mol×K | 363.15 | Heat ca... |
| Cp,liquid | 417.20 | J/mol×K | 373.15 | Heat ca... |
| η | [0.0007421; 0.0029888] | Pa×s | [278.15; 363.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 300 350 | ||||
| η | 0.0029888 | Pa×s | 278.15 | Densiti... |
| η | 0.0026543 | Pa×s | 283.15 | Densiti... |
| η | 0.0023733 | Pa×s | 288.15 | Densiti... |
| η | 0.0021360 | Pa×s | 293.15 | Densiti... |
| η | 0.0019335 | Pa×s | 298.15 | Densiti... |
| η | 0.0017601 | Pa×s | 303.15 | Densiti... |
| η | 0.0016091 | Pa×s | 308.15 | Densiti... |
| η | 0.0014773 | Pa×s | 313.15 | Densiti... |
| η | 0.0013613 | Pa×s | 318.15 | Densiti... |
| η | 0.0012589 | Pa×s | 323.15 | Densiti... |
| η | 0.0011675 | Pa×s | 328.15 | Densiti... |
| η | 0.0010864 | Pa×s | 333.15 | Densiti... |
| η | 0.0010133 | Pa×s | 338.15 | Densiti... |
| η | 0.0009477 | Pa×s | 343.15 | Densiti... |
| η | 0.0008886 | Pa×s | 348.15 | Densiti... |
| η | 0.0008342 | Pa×s | 353.15 | Densiti... |
| η | 0.0007859 | Pa×s | 358.15 | Densiti... |
| η | 0.0007421 | Pa×s | 363.15 | Densiti... |
| ΔvapH | [49.90; 63.05] | kJ/mol | [293.00; 498.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 50 52 54 56 58 60 62 64 300 400 500 | ||||
| ΔvapH | 63.05 | kJ/mol | 293.00 | NIST |
| ΔvapH | 62.90 ± 0.10 | kJ/mol | 337.00 | NIST |
| ΔvapH | 63.00 | kJ/mol | 347.00 | NIST |
| ΔvapH | 62.00 | kJ/mol | 350.00 | NIST |
| ΔvapH | 57.10 | kJ/mol | 439.50 | NIST |
| ΔvapH | 49.90 | kJ/mol | 498.00 | NIST |
| Pvap | [4.73e-04; 12.80] | kPa | [273.35; 432.65] |
|
|
T(K) Vapor pressure (kPa) 0 2 4 6 8 10 12 14 300 350 400 | ||||
| Pvap | 4.73e-04 | kPa | 273.35 | Fatty a... |
| Pvap | 4.98e-04 | kPa | 273.84 | Fatty a... |
| Pvap | 5.25e-04 | kPa | 274.32 | Fatty a... |
| Pvap | 5.54e-04 | kPa | 274.80 | Fatty a... |
| Pvap | 5.88e-04 | kPa | 275.29 | Fatty a... |
| Pvap | 6.15e-04 | kPa | 275.77 | Fatty a... |
| Pvap | 6.49e-04 | kPa | 276.26 | Fatty a... |
| Pvap | 6.85e-04 | kPa | 276.74 | Fatty a... |
| Pvap | 7.23e-04 | kPa | 277.23 | Fatty a... |
| Pvap | 7.60e-04 | kPa | 277.71 | Fatty a... |
| Pvap | 8.03e-04 | kPa | 278.20 | Fatty a... |
| Pvap | 8.44e-04 | kPa | 278.69 | Fatty a... |
| Pvap | 8.87e-04 | kPa | 279.18 | Fatty a... |
| Pvap | 9.34e-04 | kPa | 279.66 | Fatty a... |
| Pvap | 9.82e-04 | kPa | 280.15 | Fatty a... |
| Pvap | 1.03e-03 | kPa | 280.64 | Fatty a... |
| Pvap | 1.09e-03 | kPa | 281.12 | Fatty a... |
| Pvap | 1.13e-03 | kPa | 281.47 | Fatty a... |
| Pvap | 1.31e-03 | kPa | 282.96 | Fatty a... |
| Pvap | 1.39e-03 | kPa | 283.48 | Fatty a... |
| Pvap | 1.53e-03 | kPa | 284.46 | Fatty a... |
| Pvap | 1.61e-03 | kPa | 284.96 | Fatty a... |
| Pvap | 1.69e-03 | kPa | 285.43 | Fatty a... |
| Pvap | 1.73e-03 | kPa | 285.64 | Fatty a... |
| Pvap | 1.74e-03 | kPa | 285.74 | Fatty a... |
| Pvap | 1.78e-03 | kPa | 285.95 | Fatty a... |
| Pvap | 1.87e-03 | kPa | 286.44 | Fatty a... |
| Pvap | 1.97e-03 | kPa | 286.95 | Fatty a... |
| Pvap | 2.06e-03 | kPa | 287.44 | Fatty a... |
| Pvap | 2.17e-03 | kPa | 287.94 | Fatty a... |
| Pvap | 2.17e-03 | kPa | 287.94 | Fatty a... |
| Pvap | 2.39e-03 | kPa | 288.93 | Fatty a... |
| Pvap | 2.49e-03 | kPa | 289.31 | Fatty a... |
| Pvap | 2.51e-03 | kPa | 289.43 | Fatty a... |
| Pvap | 2.76e-03 | kPa | 290.42 | Fatty a... |
| Pvap | 2.79e-03 | kPa | 290.53 | Fatty a... |
| Pvap | 2.89e-03 | kPa | 290.92 | Fatty a... |
| Pvap | 3.15e-03 | kPa | 291.81 | Fatty a... |
| Pvap | 3.18e-03 | kPa | 291.92 | Fatty a... |
| Pvap | 3.34e-03 | kPa | 292.42 | Fatty a... |
| Pvap | 3.49e-03 | kPa | 292.87 | Experim... |
| Pvap | 3.50e-03 | kPa | 292.90 | Fatty a... |
| Pvap | 3.67e-03 | kPa | 293.41 | Fatty a... |
| Pvap | 3.84e-03 | kPa | 293.91 | Fatty a... |
| Pvap | 3.99e-03 | kPa | 294.30 | Fatty a... |
| Pvap | 4.22e-03 | kPa | 294.90 | Fatty a... |
| Pvap | 4.41e-03 | kPa | 295.40 | Fatty a... |
| Pvap | 4.44e-03 | kPa | 295.51 | Fatty a... |
| Pvap | 4.62e-03 | kPa | 295.90 | Fatty a... |
| Pvap | 4.84e-03 | kPa | 296.39 | Fatty a... |
| Pvap | 4.99e-03 | kPa | 296.77 | Fatty a... |
| Pvap | 5.30e-03 | kPa | 297.39 | Fatty a... |
| Pvap | 5.53e-03 | kPa | 297.89 | Fatty a... |
| Pvap | 5.57e-03 | kPa | 297.98 | Fatty a... |
| Pvap | 6.06e-03 | kPa | 298.88 | Fatty a... |
| Pvap | 6.34e-03 | kPa | 299.38 | Fatty a... |
| Pvap | 6.92e-03 | kPa | 300.37 | Fatty a... |
| Pvap | 6.95e-03 | kPa | 300.46 | Fatty a... |
| Pvap | 7.24e-03 | kPa | 300.87 | Fatty a... |
| Pvap | 7.89e-03 | kPa | 301.87 | Fatty a... |
| Pvap | 8.24e-03 | kPa | 302.37 | Fatty a... |
| Pvap | 8.52e-03 | kPa | 302.84 | Fatty a... |
| Pvap | 8.63e-03 | kPa | 302.94 | Fatty a... |
| Pvap | 8.40e-03 | kPa | 302.97 | Experim... |
| Pvap | 8.98e-03 | kPa | 303.36 | Fatty a... |
| Pvap | 9.24e-03 | kPa | 303.76 | Fatty a... |
| Pvap | 9.30e-03 | kPa | 303.81 | Fatty a... |
| Pvap | 9.29e-03 | kPa | 303.82 | Fatty a... |
| Pvap | 9.29e-03 | kPa | 303.82 | Fatty a... |
| Pvap | 9.37e-03 | kPa | 303.86 | Fatty a... |
| Pvap | 0.01 | kPa | 304.85 | Fatty a... |
| Pvap | 0.01 | kPa | 304.85 | Fatty a... |
| Pvap | 0.01 | kPa | 305.24 | Fatty a... |
| Pvap | 0.01 | kPa | 305.26 | Fatty a... |
| Pvap | 0.01 | kPa | 305.29 | Fatty a... |
| Pvap | 0.01 | kPa | 305.35 | Fatty a... |
| Pvap | 0.01 | kPa | 305.42 | Fatty a... |
| Pvap | 0.02 | kPa | 313.01 | Experim... |
| Pvap | 0.04 | kPa | 323.04 | Experim... |
| Pvap | 0.09 | kPa | 333.13 | Experim... |
| Pvap | 0.17 | kPa | 343.30 | Experim... |
| Pvap | 0.31 | kPa | 352.40 | Experim... |
| Pvap | 0.56 | kPa | 362.72 | Experim... |
| Pvap | 0.93 | kPa | 372.54 | Experim... |
| Pvap | 1.56 | kPa | 382.62 | Experim... |
| Pvap | 2.00 | kPa | 389.10 | Isobari... |
| Pvap | 2.00 | kPa | 389.10 | Isobari... |
| Pvap | 2.52 | kPa | 392.75 | Experim... |
| Pvap | 3.92 | kPa | 402.71 | Experim... |
| Pvap | 4.00 | kPa | 404.15 | Isobari... |
| Pvap | 6.01 | kPa | 412.79 | Experim... |
| Pvap | 6.00 | kPa | 412.93 | Isobari... |
| Pvap | 6.00 | kPa | 413.57 | Isobari... |
| Pvap | 8.89 | kPa | 422.71 | Experim... |
| Pvap | 10.00 | kPa | 424.43 | Isobari... |
| Pvap | 12.80 | kPa | 432.65 | Experim... |
| n0 | [1.39819; 1.43209] | [278.15; 358.15] |
|
|
|
T(K) Refractive Index 1.4 1.41 1.42 1.43 300 350 | ||||
| n0 | 1.43209 | 278.15 | Thermop... | |
| n0 | 1.42995 | 283.15 | Thermop... | |
| n0 | 1.42783 | 288.15 | Thermop... | |
| n0 | 1.42571 | 293.15 | Thermop... | |
| n0 | 1.42359 | 298.15 | Thermop... | |
| n0 | 1.42350 | 298.15 | Measure... | |
| n0 | 1.42148 | 303.15 | Thermop... | |
| n0 | 1.41938 | 308.15 | Thermop... | |
| n0 | 1.41726 | 313.15 | Thermop... | |
| n0 | 1.41510 | 318.15 | Thermop... | |
| n0 | 1.41295 | 323.15 | Thermop... | |
| n0 | 1.41083 | 328.15 | Thermop... | |
| n0 | 1.40871 | 333.15 | Thermop... | |
| n0 | 1.40659 | 338.15 | Thermop... | |
| n0 | 1.40448 | 343.15 | Thermop... | |
| n0 | 1.40237 | 348.15 | Thermop... | |
| n0 | 1.40028 | 353.15 | Thermop... | |
| n0 | 1.39819 | 358.15 | Thermop... | |
| ρl | [847.62; 872.25] | kg/m3 | [293.15; 323.15] |
|
|
T(K) Liquid Density (kg/m3) 850 855 860 865 870 300 310 320 | ||||
| ρl | 872.25 | kg/m3 | 293.15 | Measure... |
| ρl | 868.16 | kg/m3 | 298.15 | Measure... |
| ρl | 864.06 | kg/m3 | 303.15 | Measure... |
| ρl | 859.96 | kg/m3 | 308.15 | Measure... |
| ρl | 855.85 | kg/m3 | 313.15 | Measure... |
| ρl | 851.74 | kg/m3 | 318.15 | Measure... |
| ρl | 847.62 | kg/m3 | 323.15 | Measure... |
| λ | [0.12; 0.15] | W/m×K | [267.10; 399.95] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.13 0.13 0.14 0.14 0.15 0.15 300 350 400 | ||||
| λ | 0.15 | W/m×K | 267.10 | Experim... |
| λ | 0.15 | W/m×K | 267.11 | Experim... |
| λ | 0.15 | W/m×K | 277.00 | Experim... |
| λ | 0.15 | W/m×K | 277.07 | Experim... |
| λ | 0.14 | W/m×K | 288.82 | Experim... |
| λ | 0.14 | W/m×K | 288.84 | Experim... |
| λ | 0.14 | W/m×K | 300.83 | Experim... |
| λ | 0.14 | W/m×K | 300.86 | Experim... |
| λ | 0.14 | W/m×K | 311.66 | Experim... |
| λ | 0.14 | W/m×K | 311.87 | Experim... |
| λ | 0.14 | W/m×K | 324.72 | Experim... |
| λ | 0.14 | W/m×K | 324.92 | Experim... |
| λ | 0.13 | W/m×K | 336.71 | Experim... |
| λ | 0.13 | W/m×K | 336.71 | Experim... |
| λ | 0.13 | W/m×K | 348.66 | Experim... |
| λ | 0.13 | W/m×K | 348.81 | Experim... |
| λ | 0.13 | W/m×K | 354.58 | Experim... |
| λ | 0.13 | W/m×K | 354.59 | Experim... |
| λ | 0.13 | W/m×K | 360.11 | Experim... |
| λ | 0.13 | W/m×K | 360.61 | Experim... |
| λ | 0.13 | W/m×K | 368.98 | Experim... |
| λ | 0.13 | W/m×K | 369.47 | Experim... |
| λ | 0.12 | W/m×K | 379.50 | Experim... |
| λ | 0.12 | W/m×K | 379.65 | Experim... |
| λ | 0.12 | W/m×K | 389.35 | Experim... |
| λ | 0.12 | W/m×K | 389.39 | Experim... |
| λ | 0.12 | W/m×K | 399.87 | Experim... |
| λ | 0.12 | W/m×K | 399.95 | Experim... |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [381.00; 520.45] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| 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 |
Similar Compounds
Find more compounds similar to Decanoic acid, methyl ester.
Mixtures
- 1-Propanol + Decanoic acid, methyl ester
- 1-Butanol + Decanoic acid, methyl ester
- 1-Pentanol + Decanoic acid, methyl ester
- Octanoic acid, methyl ester + Decanoic acid, methyl ester
- Dodecanoic acid, methyl ester + Decanoic acid, methyl ester
- Decanoic acid, methyl ester + Cyclohexane, methyl-
- Heptane + Decanoic 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
- Butanoic acid, methyl ester + Dodecane + Decanoic acid, methyl ester
- Ethane + Decanoic acid, methyl ester
Sources
- 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
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility 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.