- InChI
- InChI=1S/C15H30O2/c1-3-4-5-6-7-8-9-10-11-12-13-14-15(16)17-2/h3-14H2,1-2H3
- InChI Key
- ZAZKJZBWRNNLDS-UHFFFAOYSA-N
- Formula
- C15H30O2
- SMILES
- CCCCCCCCCCCCCC(=O)OC
- Molecular Weight1
- 242.40
- CAS
- 124-10-7
- Other Names
-
- Acide myristique methyl ester
- Emery 2214
- Metholeneat 2495
- Methyl myristylate
- Methyl n-tetradecanoate
- Uniphat A50
- methyl myristate
- myristic acid, methyl ester
- tetradecanoic 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).
- 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).
- 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.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | [-9445.60; -9430.70] | kJ/mol |
|
| ΔcH°liquid | -9430.70 ± 0.40 | kJ/mol | NIST |
| ΔcH°liquid | -9445.60 ± 2.10 | kJ/mol | NIST |
| ΔfG° | -158.50 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -597.73 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 52.01 | kJ/mol | Heat Ca... |
| ΔvapH° | [85.90; 87.00] | kJ/mol |
|
| ΔvapH° | 86.98 | kJ/mol | NIST |
| ΔvapH° | 85.90 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 86.60 | kJ/mol | NIST |
| ΔvapH° | 86.20 ± 1.00 | kJ/mol | NIST |
| ΔvapH° | 86.98 ± 0.94 | kJ/mol | NIST |
| ΔvapH° | 87.00 ± 0.90 | kJ/mol | NIST |
| log10WS | -4.96 | Crippen Calculated Property | |
| logPoct/wat | 4.861 | Crippen Calculated Property | |
| McVol | 229.650 | ml/mol | McGowan Calculated Property |
| Pc | 1465.73 | kPa | Joback Calculated Property |
| Inp | [286.80; 1738.00] |
|
|
| Inp | 1710.60 | NIST | |
| Inp | 1710.00 | NIST | |
| Inp | 1718.00 | NIST | |
| Inp | 1712.00 | NIST | |
| Inp | 1713.00 | NIST | |
| Inp | 1713.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1726.00 | NIST | |
| Inp | 1706.00 | NIST | |
| Inp | 1726.00 | NIST | |
| Inp | 1726.00 | NIST | |
| Inp | 1727.00 | NIST | |
| Inp | 1713.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1714.00 | NIST | |
| Inp | 1727.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1719.00 | NIST | |
| Inp | 1706.00 | NIST | |
| Inp | 1706.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1707.44 | NIST | |
| Inp | 1708.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1715.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1714.00 | NIST | |
| Inp | 1722.20 | NIST | |
| Inp | 1728.00 | NIST | |
| Inp | 1726.00 | NIST | |
| Inp | 1728.00 | NIST | |
| Inp | 1699.00 | NIST | |
| Inp | 1699.00 | NIST | |
| Inp | 1708.00 | NIST | |
| Inp | 1727.00 | NIST | |
| Inp | 1724.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1738.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1726.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1727.40 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1727.00 | NIST | |
| Inp | 1706.00 | NIST | |
| Inp | 1722.00 | NIST | |
| Inp | 1710.00 | NIST | |
| Inp | 1724.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1709.00 | NIST | |
| Inp | 1729.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1727.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1705.00 | NIST | |
| Inp | 1708.00 | NIST | |
| Inp | 1708.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1712.00 | NIST | |
| Inp | 1722.00 | NIST | |
| Inp | 1726.00 | NIST | |
| Inp | 1735.00 | NIST | |
| Inp | 1684.00 | NIST | |
| Inp | 1735.00 | NIST | |
| Inp | 1708.00 | NIST | |
| Inp | 1727.00 | NIST | |
| Inp | 1727.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1723.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1717.00 | NIST | |
| Inp | 1706.00 | NIST | |
| Inp | 1725.00 | NIST | |
| Inp | 1707.00 | NIST | |
| Inp | 1708.00 | NIST | |
| Inp | 1714.00 | NIST | |
| Inp | 1715.00 | NIST | |
| Inp | Outlier 288.78 | NIST | |
| Inp | Outlier 291.18 | NIST | |
| Inp | Outlier 297.60 | NIST | |
| Inp | Outlier 297.60 | NIST | |
| Inp | Outlier 297.70 | NIST | |
| Inp | Outlier 286.80 | NIST | |
| Inp | Outlier 290.52 | NIST | |
| Inp | Outlier 290.32 | NIST | |
| Inp | Outlier 290.32 | NIST | |
| Inp | Outlier 290.32 | NIST | |
| Inp | 1722.20 | NIST | |
| I | [1978.00; 2037.00] |
|
|
| I | 2005.00 | NIST | |
| I | 2037.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 1998.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 2006.00 | NIST | |
| I | 2034.00 | NIST | |
| I | 1988.00 | NIST | |
| I | 2028.00 | NIST | |
| I | 2008.00 | NIST | |
| I | 2008.00 | NIST | |
| I | 2000.00 | NIST | |
| I | 1998.00 | NIST | |
| I | 2032.00 | NIST | |
| I | 2036.00 | NIST | |
| I | 2014.00 | NIST | |
| I | 2006.00 | NIST | |
| I | 1987.00 | NIST | |
| I | 2021.00 | NIST | |
| I | 2034.00 | NIST | |
| I | 2014.00 | NIST | |
| I | 2009.00 | NIST | |
| I | 1999.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 1990.00 | NIST | |
| I | 2020.00 | NIST | |
| I | 1978.00 | NIST | |
| I | 2000.00 | NIST | |
| I | 1998.00 | NIST | |
| I | 2028.00 | NIST | |
| Tboil | 596.20 | K | NIST |
| Tc | 730.00 | K | Vapor-l... |
| Tfus | [290.00; 292.00] | K |
|
| Tfus | 290.00 ± 1.00 | K | NIST |
| Tfus | 291.85 ± 0.30 | K | NIST |
| Tfus | 292.00 ± 2.00 | K | NIST |
| Vc | 0.899 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [620.74; 714.65] | J/mol×K | [618.89; 786.41] |
|
| Cp,gas | 620.74 | J/mol×K | 618.89 | Joback Calculated Property |
| Cp,gas | 638.14 | J/mol×K | 646.81 | Joback Calculated Property |
| Cp,gas | 654.83 | J/mol×K | 674.73 | Joback Calculated Property |
| Cp,gas | 670.81 | J/mol×K | 702.65 | Joback Calculated Property |
| Cp,gas | 686.10 | J/mol×K | 730.57 | Joback Calculated Property |
| Cp,gas | 700.70 | J/mol×K | 758.49 | Joback Calculated Property |
| Cp,gas | 714.65 | J/mol×K | 786.41 | Joback Calculated Property |
| Cp,liquid | 505.40 | J/mol×K | 298.15 | NIST |
| η | [0.0014233; 0.0044420] | Pa×s | [293.15; 353.15] |
|
| η | 0.0044420 | Pa×s | 293.15 | Group C... |
| η | 0.0039821 | Pa×s | 298.15 | Densiti... |
| η | 0.0034960 | Pa×s | 303.15 | Group C... |
| η | 0.0035430 | Pa×s | 303.15 | Densiti... |
| η | 0.0031651 | Pa×s | 308.15 | Densiti... |
| η | 0.0028447 | Pa×s | 313.15 | Densiti... |
| η | 0.0028410 | Pa×s | 313.15 | Group C... |
| η | 0.0025709 | Pa×s | 318.15 | Densiti... |
| η | 0.0023343 | Pa×s | 323.15 | Densiti... |
| η | 0.0022520 | Pa×s | 323.15 | Group C... |
| η | 0.0021295 | Pa×s | 328.15 | Densiti... |
| η | 0.0018190 | Pa×s | 333.15 | Group C... |
| η | 0.0019498 | Pa×s | 333.15 | Densiti... |
| η | 0.0017932 | Pa×s | 338.15 | Densiti... |
| η | 0.0016549 | Pa×s | 343.15 | Densiti... |
| η | 0.0015210 | Pa×s | 343.15 | Group C... |
| η | 0.0015321 | Pa×s | 348.15 | Densiti... |
| η | 0.0014233 | Pa×s | 353.15 | Densiti... |
| ΔfusH | [50.21; 50.21] | kJ/mol | [291.60; 291.60] |
|
| ΔfusH | 50.21 | kJ/mol | 291.60 | NIST |
| ΔfusH | 50.21 | kJ/mol | 291.60 | NIST |
| ΔsubH | 137.70 ± 2.10 | kJ/mol | 281.00 | NIST |
| ΔvapH | [65.30; 87.00] | kJ/mol | [293.00; 498.00] |
|
| ΔvapH | 75.06 | kJ/mol | 293.00 | NIST |
| ΔvapH | 86.10 | kJ/mol | 298.15 | the vap... |
| ΔvapH | 87.00 | kJ/mol | 313.00 | NIST |
| ΔvapH | 79.80 | kJ/mol | 350.00 | NIST |
| ΔvapH | 76.00 ± 0.20 | kJ/mol | 382.00 | NIST |
| ΔvapH | 77.40 | kJ/mol | 390.50 | NIST |
| ΔvapH | 75.60 | kJ/mol | 454.00 | NIST |
| ΔvapH | 65.30 | kJ/mol | 498.00 | NIST |
| Pvap | [1.13e-04; 4.00] | kPa | [302.71; 459.62] |
|
| Pvap | 1.13e-04 | kPa | 302.71 | Fatty a... |
| Pvap | 1.50e-04 | kPa | 305.30 | Fatty a... |
| Pvap | 1.66e-04 | kPa | 306.14 | Fatty a... |
| Pvap | 1.95e-04 | kPa | 307.76 | Fatty a... |
| Pvap | 2.14e-04 | kPa | 308.58 | Fatty a... |
| Pvap | 2.54e-04 | kPa | 310.23 | Fatty a... |
| Pvap | 2.81e-04 | kPa | 311.21 | Fatty a... |
| Pvap | 3.26e-04 | kPa | 312.71 | Fatty a... |
| Pvap | 3.62e-04 | kPa | 313.70 | Fatty a... |
| Pvap | 4.20e-04 | kPa | 315.17 | Fatty a... |
| Pvap | 4.65e-04 | kPa | 316.16 | Fatty a... |
| Pvap | 5.36e-04 | kPa | 317.65 | Fatty a... |
| Pvap | 5.91e-04 | kPa | 318.63 | Fatty a... |
| Pvap | 6.86e-04 | kPa | 320.12 | Fatty a... |
| Pvap | 7.62e-04 | kPa | 321.26 | Fatty a... |
| Pvap | 8.69e-04 | kPa | 322.58 | Fatty a... |
| Pvap | 9.62e-04 | kPa | 323.72 | Fatty a... |
| Pvap | 1.11e-03 | kPa | 325.20 | Fatty a... |
| Pvap | 1.22e-03 | kPa | 326.19 | Fatty a... |
| Pvap | 1.39e-03 | kPa | 327.67 | Fatty a... |
| Pvap | 1.52e-03 | kPa | 328.66 | Fatty a... |
| Pvap | 1.74e-03 | kPa | 330.13 | Fatty a... |
| Pvap | 1.91e-03 | kPa | 331.13 | Fatty a... |
| Pvap | 2.76e-03 | kPa | 332.40 | Experim... |
| Pvap | 2.17e-03 | kPa | 332.60 | Fatty a... |
| Pvap | 2.38e-03 | kPa | 333.60 | Fatty a... |
| Pvap | 2.75e-03 | kPa | 335.34 | Fatty a... |
| Pvap | 2.94e-03 | kPa | 336.07 | Fatty a... |
| Pvap | 3.41e-03 | kPa | 337.83 | Fatty a... |
| Pvap | 3.63e-03 | kPa | 338.55 | Fatty a... |
| Pvap | 4.21e-03 | kPa | 340.31 | Fatty a... |
| Pvap | 4.47e-03 | kPa | 341.01 | Fatty a... |
| Pvap | 5.98e-03 | kPa | 342.28 | Experim... |
| Pvap | 5.88e-03 | kPa | 342.28 | Experim... |
| Pvap | 5.17e-03 | kPa | 342.80 | Fatty a... |
| Pvap | 5.47e-03 | kPa | 343.48 | Fatty a... |
| Pvap | 6.33e-03 | kPa | 345.28 | Fatty a... |
| Pvap | 6.70e-03 | kPa | 345.96 | Fatty a... |
| Pvap | 7.72e-03 | kPa | 347.76 | Fatty a... |
| Pvap | 8.13e-03 | kPa | 348.43 | Fatty a... |
| Pvap | 9.38e-03 | kPa | 350.25 | Fatty a... |
| Pvap | 9.87e-03 | kPa | 350.91 | Fatty a... |
| Pvap | 0.01 | kPa | 352.35 | Experim... |
| Pvap | 0.01 | kPa | 352.35 | Experim... |
| Pvap | 0.01 | kPa | 352.73 | Fatty a... |
| Pvap | 0.01 | kPa | 353.15 | Isother... |
| Pvap | 0.03 | kPa | 362.59 | Experim... |
| Pvap | 0.03 | kPa | 363.15 | Isother... |
| Pvap | 0.05 | kPa | 372.73 | Experim... |
| Pvap | 0.05 | kPa | 373.15 | Isother... |
| Pvap | 0.09 | kPa | 382.82 | Experim... |
| Pvap | 0.10 | kPa | 383.15 | Isother... |
| Pvap | 0.17 | kPa | 392.86 | Experim... |
| Pvap | 0.17 | kPa | 392.87 | Experim... |
| Pvap | 0.17 | kPa | 393.15 | Isother... |
| Pvap | 0.30 | kPa | 402.76 | Experim... |
| Pvap | 0.30 | kPa | 403.15 | Isother... |
| Pvap | 0.51 | kPa | 412.80 | Experim... |
| Pvap | 0.51 | kPa | 413.15 | Isother... |
| Pvap | 0.83 | kPa | 422.64 | Experim... |
| Pvap | 0.84 | kPa | 423.15 | Isother... |
| Pvap | 1.31 | kPa | 432.57 | Experim... |
| Pvap | 1.31 | kPa | 432.57 | Experim... |
| Pvap | 1.31 | kPa | 432.58 | Experim... |
| Pvap | 1.35 | kPa | 433.15 | Isother... |
| Pvap | 1.72 | kPa | 437.72 | Vapor-L... |
| Pvap | 2.06 | kPa | 442.36 | Experim... |
| Pvap | 2.05 | kPa | 442.37 | Experim... |
| Pvap | 2.05 | kPa | 442.38 | Experim... |
| Pvap | 2.12 | kPa | 443.15 | Isother... |
| Pvap | 3.12 | kPa | 452.24 | Experim... |
| Pvap | 3.13 | kPa | 452.25 | Experim... |
| Pvap | 3.13 | kPa | 452.26 | Experim... |
| Pvap | 3.27 | kPa | 453.15 | Isother... |
| Pvap | 4.00 | kPa | 459.62 | Vapor l... |
| n0 | [1.41083; 1.43704] | [293.15; 358.15] |
|
|
| n0 | 1.43704 | 293.15 | Thermop... | |
| n0 | 1.43499 | 298.15 | Thermop... | |
| n0 | 1.43490 | 298.15 | Liquid-... | |
| n0 | 1.43296 | 303.15 | Thermop... | |
| n0 | 1.43093 | 308.15 | Thermop... | |
| n0 | 1.42890 | 313.15 | Thermop... | |
| n0 | 1.42681 | 318.15 | Thermop... | |
| n0 | 1.42472 | 323.15 | Thermop... | |
| n0 | 1.42254 | 328.15 | Thermop... | |
| n0 | 1.42020 | 333.15 | Thermop... | |
| n0 | 1.41783 | 338.15 | Thermop... | |
| n0 | 1.41630 | 343.15 | Thermop... | |
| n0 | 1.41474 | 348.15 | Thermop... | |
| n0 | 1.41282 | 353.15 | Thermop... | |
| n0 | 1.41083 | 358.15 | Thermop... | |
| ρl | [844.34; 867.17] | kg/m3 | [293.15; 323.15] |
|
| ρl | 867.17 | kg/m3 | 293.15 | Measure... |
| ρl | 863.35 | kg/m3 | 298.15 | Measure... |
| ρl | 859.54 | kg/m3 | 303.15 | Measure... |
| ρl | 855.74 | kg/m3 | 308.15 | Measure... |
| ρl | 851.94 | kg/m3 | 313.15 | Measure... |
| ρl | 848.14 | kg/m3 | 318.15 | Measure... |
| ρl | 844.34 | kg/m3 | 323.15 | Measure... |
| λ | [0.13; 0.15] | W/m×K | [304.02; 402.41] |
|
| λ | 0.15 | W/m×K | 304.02 | Experim... |
| λ | 0.15 | W/m×K | 304.33 | Experim... |
| λ | 0.14 | W/m×K | 320.10 | Experim... |
| λ | 0.14 | W/m×K | 320.81 | Experim... |
| λ | 0.14 | W/m×K | 327.18 | Experim... |
| λ | 0.14 | W/m×K | 327.53 | Experim... |
| λ | 0.14 | W/m×K | 338.31 | Experim... |
| λ | 0.14 | W/m×K | 338.55 | Experim... |
| λ | 0.14 | W/m×K | 342.21 | Experim... |
| λ | 0.14 | W/m×K | 342.28 | Experim... |
| λ | 0.14 | W/m×K | 354.31 | Experim... |
| λ | 0.14 | W/m×K | 354.58 | Experim... |
| λ | 0.14 | W/m×K | 359.14 | Experim... |
| λ | 0.14 | W/m×K | 359.27 | Experim... |
| λ | 0.13 | W/m×K | 369.45 | Experim... |
| λ | 0.13 | W/m×K | 369.47 | Experim... |
| λ | 0.13 | W/m×K | 377.12 | Experim... |
| λ | 0.13 | W/m×K | 377.13 | Experim... |
| λ | 0.13 | W/m×K | 386.13 | Experim... |
| λ | 0.13 | W/m×K | 386.27 | Experim... |
| λ | 0.13 | W/m×K | 394.31 | Experim... |
| λ | 0.13 | W/m×K | 394.48 | Experim... |
| λ | 0.13 | W/m×K | 402.41 | Experim... |
| λ | 0.13 | W/m×K | 402.41 | Experim... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 429.20 | K | 0.90 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0035 |
| 303.15 | 20000.00 | 0.0044 |
| 303.15 | 40000.00 | 0.0055 |
| 313.15 | 101.30 | 0.0028 |
| 313.15 | 20000.00 | 0.0035 |
| 313.15 | 40000.00 | 0.0043 |
| 313.15 | 60000.00 | 0.0052 |
| 313.15 | 80000.00 | 0.0063 |
| 313.15 | 100000.00 | 0.0075 |
| 333.15 | 101.30 | 0.0019 |
| 333.15 | 20000.00 | 0.0024 |
| 333.15 | 40000.00 | 0.0029 |
| 333.15 | 60000.00 | 0.0035 |
| 333.15 | 80000.00 | 0.0041 |
| 333.15 | 100000.00 | 0.0048 |
| 353.15 | 101.30 | 0.0014 |
| 353.15 | 20000.00 | 0.0017 |
| 353.15 | 40000.00 | 0.0021 |
| 353.15 | 60000.00 | 0.0025 |
| 353.15 | 80000.00 | 0.0029 |
| 353.15 | 100000.00 | 0.0034 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 100.00 | 303.15 | 1335.8 |
| 10000.00 | 303.15 | 1382.9 |
| 20000.00 | 303.15 | 1426.9 |
| 30000.00 | 303.15 | 1468.1 |
| 40000.00 | 303.15 | 1507.6 |
| 50000.00 | 303.15 | 1544.9 |
| 60000.00 | 303.15 | 1580.2 |
| 70000.00 | 303.15 | 1614.2 |
| 100.00 | 323.15 | 1264.0 |
| 10000.00 | 323.15 | 1316.4 |
| 20000.00 | 323.15 | 1364.8 |
| 30000.00 | 323.15 | 1409.6 |
| 40000.00 | 323.15 | 1451.9 |
| 50000.00 | 323.15 | 1492.5 |
| 60000.00 | 323.15 | 1530.5 |
| 70000.00 | 323.15 | 1566.8 |
| 80000.00 | 323.15 | 1601.2 |
| 100.00 | 343.15 | 1195.7 |
| 10000.00 | 343.15 | 1251.2 |
| 20000.00 | 343.15 | 1302.9 |
| 30000.00 | 343.15 | 1350.8 |
| 40000.00 | 343.15 | 1396.0 |
| 50000.00 | 343.15 | 1437.4 |
| 60000.00 | 343.15 | 1477.5 |
| 70000.00 | 343.15 | 1515.0 |
| 80000.00 | 343.15 | 1550.8 |
| 100.00 | 363.15 | 1130.9 |
| 10000.00 | 363.15 | 1190.4 |
| 20000.00 | 363.15 | 1245.2 |
| 30000.00 | 363.15 | 1295.9 |
| 40000.00 | 363.15 | 1342.5 |
| 50000.00 | 363.15 | 1385.7 |
| 60000.00 | 363.15 | 1426.7 |
| 70000.00 | 363.15 | 1465.5 |
| 80000.00 | 363.15 | 1502.6 |
| 100.00 | 383.15 | 1066.7 |
| 10000.00 | 383.15 | 1131.3 |
| 20000.00 | 383.15 | 1189.6 |
| 30000.00 | 383.15 | 1242.9 |
| 40000.00 | 383.15 | 1291.7 |
| 50000.00 | 383.15 | 1338.0 |
| 60000.00 | 383.15 | 1380.3 |
| 70000.00 | 383.15 | 1420.4 |
| 80000.00 | 383.15 | 1457.6 |
| 100.00 | 393.15 | 1036.2 |
| 10000.00 | 393.15 | 1103.6 |
| 20000.00 | 393.15 | 1163.5 |
| 30000.00 | 393.15 | 1217.8 |
| 40000.00 | 393.15 | 1267.7 |
| 50000.00 | 393.15 | 1314.4 |
| 60000.00 | 393.15 | 1357.8 |
| 70000.00 | 393.15 | 1397.8 |
| 80000.00 | 393.15 | 1436.8 |
| Reference | ||
Similar Compounds
Find more compounds similar to Methyl tetradecanoate.
Mixtures
- Cyclohexane, methyl- + Methyl tetradecanoate
- Hexadecanoic acid, methyl ester + Methyl tetradecanoate
- Tetradecane + Methyl tetradecanoate
- 1-Hexadecanol + Methyl tetradecanoate
- Methyl tetradecanoate + Methyl Alcohol
- Ethane + Methyl tetradecanoate
- Pentadecane + Methyl tetradecanoate
- Hexadecane + Methyl tetradecanoate
- Glycerin + Methyl tetradecanoate + Methyl Alcohol
- 9-Octadecenoic acid (Z)-, methyl ester + Hexadecanoic acid, methyl ester + Methyl tetradecanoate
- Ethanol + Glycerin + Methyl tetradecanoate
- Glycerin + Methyl tetradecanoate + Water
Sources
- Crippen Method
- Crippen Method
- Measurement and correlation of vapor liquid equilibria for methanol + methyl laurate and methanol + methyl myristate systems near critical temperature of methanol
- Phase behaviour of high molecular mass methyl esters in supercritical ethane
- Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
- Isobaric vapor liquid equilibrium for binary system of methyl myristate + methyl palmitate at 0.5, 1.0 and 1.4 kPa
- Isobaric vapor-liquid equilibrium for the three binary systems of C14 - C16 n-alkane + methyl myristate at 5.00 kPa
- Measurement and correlation of ternary vapor-liquid equilibria for methanol + glycerol + fatty acid methyl ester (methyl laurate, methyl myristate, methyl palmitate) systems at elevated temperatures and pressures
- 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
- Experimental studies on the liquid thermal conductivity of three saturated fatty acid methyl esters components of biodiesel
- 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)
- the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
- Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
- Viscosities of Fatty Acid Methyl and Ethyl Esters under High Pressure: Methyl Myristate and Ethyl Myristate
- Liquid Liquid Equilibrium for the Ternary System of Methyl Laurate/Methyl Myristate + Ethanol + Glycerol at 318.15 and 333.15 K
- Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
- Vapor-Liquid Equilibria of Binary Systems with Long-Chain Organic Compounds (Fatty Alcohol, Fatty Ester, Acylglycerol, and n-Paraffin) at Subatmospheric Pressures
- Liquid-Liquid Equilibria for Ternary Mixtures of gamma-Valerolactone + n-Tetradecane + (Butanoic Acid or Hexanoic Acid or Methyl Myristate) at 298.15 K
- 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
- Isobaric Vapor Liquid Equilibrium of the Mixture of Methyl Palmitate and Methyl Stearate at 0.1 kPa, 1 kPa, 5 kPa, and 10 kPa
- Article Ternary Liquid Liquid Equilibrium of Biodiesel Compounds for Systems Consisting of a Methyl Ester + Glycerin + Water
- Speed of Sound, Density, and Derivative Properties of Ethyl Myristate, Methyl Myristate, and Methyl Palmitate under High Pressure
- Group Contribution Model for Predicting Viscosity of Fatty Compounds
- Viscosities of Fatty Mixtures: Experimental Data and Prediction
- Joback Method
- McGowan Method
- NIST Webbook
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