- InChI
- InChI=1S/C19H38O2/c1-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19(20)21-2/h3-18H2,1-2H3
- InChI Key
- HPEUJPJOZXNMSJ-UHFFFAOYSA-N
- Formula
- C19H38O2
- SMILES
- CCCCCCCCCCCCCCCCCC(=O)OC
- Molecular Weight1
- 298.50
- CAS
- 112-61-8
- Other Names
-
- 28:0, Me ester
- Emery 2218
- Kemester 4516
- Kemester 9018
- Kemester 9718
- Metholene 2218
- Methyl ester of octadecanoic acid
- Methyl n-octadecanoate
- NSC 9418
- Octadecanoic acid methyl ester
- methyl octadecanoate
- n-Octadecanoic acid, methyl ester
- octadecanoic acid, methyl ester
- stearic acid, methyl ester
- ω : Acentric Factor.
- ΔcH°solid : Standard solid 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- 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).
- Tboil(P) : Boiling point at given pressure (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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.8595; 0.8645] |
|
|
| ω | 0.8645 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.8595 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | -11962.00 ± 0.40 | kJ/mol | NIST |
| μ | 1.67 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -201.27 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -741.90 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 66.35 | kJ/mol | Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K |
| ΔvapH° | [105.90; 109.50] | kJ/mol |
|
| ΔvapH° | 109.50 ± 2.70 | kJ/mol | NIST |
| ΔvapH° | 105.90 ± 1.40 | kJ/mol | NIST |
| ΔvapH° | 106.20 | kJ/mol | NIST |
| IE | 9.83 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.84 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.421 | Crippen Calculated Property | |
| McVol | 286.010 | ml/mol | McGowan Calculated Property |
| Pc | [1084.00; 1165.24] | kPa |
|
| Pc | 1165.24 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 1084.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 5.33e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [349.48; 2141.00] |
|
|
| Inp | 2099.80 | NIST | |
| Inp | 2101.00 | NIST | |
| Inp | 2102.10 | NIST | |
| Inp | 2103.30 | NIST | |
| Inp | 2104.50 | NIST | |
| Inp | 2105.80 | NIST | |
| Inp | 2107.10 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2113.00 | NIST | |
| Inp | 2114.00 | NIST | |
| Inp | 2102.00 | NIST | |
| Inp | 2113.00 | NIST | |
| Inp | 2113.00 | NIST | |
| Inp | 2126.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2140.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2116.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2135.00 | NIST | |
| Inp | 2112.00 | NIST | |
| Inp | 2117.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2110.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2133.00 | NIST | |
| Inp | 2138.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2141.00 | NIST | |
| Inp | 2135.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2109.49 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2116.00 | NIST | |
| Inp | 2108.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2098.00 | NIST | |
| Inp | 2123.10 | NIST | |
| Inp | 2127.10 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2111.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2139.00 | NIST | |
| Inp | 2110.00 | NIST | |
| Inp | 2114.00 | NIST | |
| Inp | 2106.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2127.00 | NIST | |
| Inp | 2137.00 | NIST | |
| Inp | 2122.00 | NIST | |
| Inp | 2138.00 | NIST | |
| Inp | 2126.00 | NIST | |
| Inp | 2141.00 | NIST | |
| Inp | 2133.00 | NIST | |
| Inp | 2124.00 | NIST | |
| Inp | 2109.20 | NIST | |
| Inp | 2137.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2110.00 | NIST | |
| Inp | 2124.00 | NIST | |
| Inp | 2129.30 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2110.00 | NIST | |
| Inp | 2111.00 | NIST | |
| Inp | 2112.00 | NIST | |
| Inp | 2117.00 | NIST | |
| Inp | 2111.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2139.00 | NIST | |
| Inp | 2104.00 | NIST | |
| Inp | 2125.00 | NIST | |
| Inp | 2126.00 | NIST | |
| Inp | 2127.00 | NIST | |
| Inp | 2133.00 | NIST | |
| Inp | 2111.00 | NIST | |
| Inp | 2108.00 | NIST | |
| Inp | 2105.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2110.00 | NIST | |
| Inp | 2107.00 | NIST | |
| Inp | 2111.00 | NIST | |
| Inp | 2112.00 | NIST | |
| Inp | 2102.00 | NIST | |
| Inp | 2116.00 | NIST | |
| Inp | 2116.00 | NIST | |
| Inp | 2112.00 | NIST | |
| Inp | 2126.00 | NIST | |
| Inp | 2134.00 | NIST | |
| Inp | 2125.00 | NIST | |
| Inp | 2123.00 | NIST | |
| Inp | 2123.00 | NIST | |
| Inp | 2108.00 | NIST | |
| Inp | 2121.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2125.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2101.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2127.00 | NIST | |
| Inp | 2127.00 | NIST | |
| Inp | 2128.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2134.00 | NIST | |
| Inp | 2119.00 | NIST | |
| Inp | 2127.00 | NIST | |
| Inp | 2140.00 | NIST | |
| Inp | 2129.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2109.00 | NIST | |
| Inp | 2098.00 | NIST | |
| Inp | 2112.00 | NIST | |
| Inp | 2115.00 | NIST | |
| Inp | Outlier 349.48 | NIST | |
| Inp | Outlier 352.84 | NIST | |
| Inp | Outlier 362.20 | NIST | |
| Inp | Outlier 362.20 | NIST | |
| Inp | Outlier 362.20 | NIST | |
| Inp | Outlier 351.30 | NIST | |
| Inp | Outlier 351.38 | NIST | |
| Inp | Outlier 351.38 | NIST | |
| Inp | 2106.00 | NIST | |
| Inp | 2138.00 | NIST | |
| Inp | 2109.20 | NIST | |
| Inp | 2129.30 | NIST | |
| Inp | 2112.00 | NIST | |
| Inp | 2104.00 | NIST | |
| Inp | 2111.00 | NIST | |
| Inp | 2110.00 | NIST | |
| Inp | 2116.00 | NIST | |
| Inp | 2126.00 | NIST | |
| Inp | 2130.00 | NIST | |
| Inp | 2099.80 | NIST | |
| Inp | 2105.80 | NIST | |
| Inp | 2102.00 | NIST | |
| Inp | Outlier 351.38 | NIST | |
| Inp | 2123.10 | NIST | |
| Inp | 2128.00 | NIST | |
| Ip | [2386.00; 2445.00] |
|
|
| Ip | 2419.00 | NIST | |
| Ip | 2410.00 | NIST | |
| Ip | 2445.00 | NIST | |
| Ip | 2396.00 | NIST | |
| Ip | 2389.00 | NIST | |
| Ip | 2409.00 | NIST | |
| Ip | 2415.00 | NIST | |
| Ip | Outlier 2386.00 | NIST | |
| Ip | 2417.00 | NIST | |
| Ip | Outlier 2386.00 | NIST | |
| Ip | 2426.00 | NIST | |
| Ip | 2431.00 | NIST | |
| Ip | 2445.00 | NIST | |
| Ip | 2445.00 | NIST | |
| Ip | 2424.00 | NIST | |
| Ip | 2419.00 | NIST | |
| Ip | 2422.00 | NIST | |
| Ip | 2412.00 | NIST | |
| Ip | 2433.00 | NIST | |
| Ip | 2405.00 | NIST | |
| Ip | 2409.00 | NIST | |
| Ip | 2415.00 | NIST | |
| Ip | 2405.00 | NIST | |
| Ip | 2434.00 | NIST | |
| Ip | 2418.00 | NIST | |
| Ip | 2429.00 | NIST | |
| Ip | 2418.00 | NIST | |
| Ip | 2442.00 | NIST | |
| Ip | 2409.00 | NIST | |
| Ip | 2426.00 | NIST | |
| Ip | 2429.00 | NIST | |
| Tboil | 451.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | [781.10; 788.00] | K |
|
| Tc | 785.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tc | 788.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 781.10 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [310.00; 312.70] | K |
|
| Tfus | 312.70 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 312.40 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 310.00 ± 0.50 | K | NIST |
| Tfus | 312.15 ± 0.35 | K | NIST |
| Tfus | 311.20 ± 1.00 | K | NIST |
| Tfus | 312.10 ± 0.50 | K | NIST |
| Ttriple | 310.55 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 11.22 | ChemSep v8.3 pure component data Compiled value | |
| URi | 13.59 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [1.112; 1.310] | m3/kmol |
|
| Vc | 1.112 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 1.310 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2190000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil(P) | [475.97; 493.38] | K | [1.20; 2.50] |
|
| Tboil(P) | 475.97 | K | 1.20 | Vapour liquid equilibria of monocaprylin plus palmitic acid or methyl stearate at P = (1.20 and 2.50) kPa by using DSC technique |
| Tboil(P) | 493.38 | K | 2.50 | Vapour liquid equilibria of monocaprylin plus palmitic acid or methyl stearate at P = (1.20 and 2.50) kPa by using DSC technique |
| Tboilr | 488.20 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [457.83; 1164.72] | 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 | 3.63430e+02 | |||
| Coefficient B | 7.03170e+02 | |||
| Coefficient C | 8.02660e+02 | |||
| Coefficient D | 4.26690e+02 | |||
| Coefficient E | 2.44330e+03 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 457.83 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 611.93 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 742.78 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 843.67 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 925.11 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 993.32 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 1050.61 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 1097.78 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 1135.52 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 1164.72 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [632.01; 893.06] | J/mol×K | [312.15; 623.70] |
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 | 3.70460e+02 | |||
| Coefficient B | 8.37900e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 312.15 | |||
| Temperature range, max. | 623.70 | |||
| Cp,liquid | 632.01 | J/mol×K | 312.15 | Calculated Property |
| Cp,liquid | 661.02 | J/mol×K | 346.77 | Calculated Property |
| Cp,liquid | 690.02 | J/mol×K | 381.38 | Calculated Property |
| Cp,liquid | 719.03 | J/mol×K | 416.00 | Calculated Property |
| Cp,liquid | 748.03 | J/mol×K | 450.62 | Calculated Property |
| Cp,liquid | 777.04 | J/mol×K | 485.23 | Calculated Property |
| Cp,liquid | 806.04 | J/mol×K | 519.85 | Calculated Property |
| Cp,liquid | 835.05 | J/mol×K | 554.47 | Calculated Property |
| Cp,liquid | 864.05 | J/mol×K | 589.08 | Calculated Property |
| Cp,liquid | 893.06 | J/mol×K | 623.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0050857; 0.0002093] | Pa×s | [312.15; 623.70] |
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 | -1.16680e+01 | |||
| Coefficient B | 1.99360e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 312.15 | |||
| Temperature range, max. | 623.70 | |||
| η | 0.0050857 | Pa×s | 312.15 | Calculated Property |
| η | 0.0026882 | Pa×s | 346.77 | Calculated Property |
| η | 0.0015953 | Pa×s | 381.38 | Calculated Property |
| η | 0.0010326 | Pa×s | 416.00 | Calculated Property |
| η | 0.0007146 | Pa×s | 450.62 | Calculated Property |
| η | 0.0005212 | Pa×s | 485.23 | Calculated Property |
| η | 0.0003964 | Pa×s | 519.85 | Calculated Property |
| η | 0.0003120 | Pa×s | 554.47 | Calculated Property |
| η | 0.0002526 | Pa×s | 589.08 | Calculated Property |
| η | 0.0002093 | Pa×s | 623.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [96.73; 0.00] | kJ/mol | [312.15; 781.10] |
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 | 1.45680e+02 | |||
| Coefficient B | 1.35910e+00 | |||
| Coefficient C | -1.76850e+00 | |||
| Coefficient D | 9.41210e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.81100e+02 | |||
| Temperature range, min. | 312.15 | |||
| Temperature range, max. | 781.10 | |||
| ΔvapH | 96.73 | kJ/mol | 312.15 | Calculated Property |
| ΔvapH | 91.59 | kJ/mol | 364.26 | Calculated Property |
| ΔvapH | 86.54 | kJ/mol | 416.36 | Calculated Property |
| ΔvapH | 81.30 | kJ/mol | 468.47 | Calculated Property |
| ΔvapH | 75.51 | kJ/mol | 520.57 | Calculated Property |
| ΔvapH | 68.75 | kJ/mol | 572.68 | Calculated Property |
| ΔvapH | 60.45 | kJ/mol | 624.78 | Calculated Property |
| ΔvapH | 49.75 | kJ/mol | 676.89 | Calculated Property |
| ΔvapH | 34.84 | kJ/mol | 728.99 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 781.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [8.04e-06; 1088.27] | kPa | [312.15; 781.10] |
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 | 1.06212e+02 | |||
| Coefficient B | -1.53720e+04 | |||
| Coefficient C | -1.19610e+01 | |||
| Coefficient D | 5.66720e-19 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 312.15 | |||
| Temperature range, max. | 781.10 | |||
| Pvap | 8.04e-06 | kPa | 312.15 | Calculated Property |
| Pvap | 1.46e-03 | kPa | 364.26 | Calculated Property |
| Pvap | 0.06 | kPa | 416.36 | Calculated Property |
| Pvap | 0.86 | kPa | 468.47 | Calculated Property |
| Pvap | 6.55 | kPa | 520.57 | Calculated Property |
| Pvap | 30.99 | kPa | 572.68 | Calculated Property |
| Pvap | 104.00 | kPa | 624.78 | Calculated Property |
| Pvap | 270.72 | kPa | 676.89 | Calculated Property |
| Pvap | 582.78 | kPa | 728.99 | Calculated Property |
| Pvap | 1088.27 | kPa | 781.10 | Calculated Property |
| Pvap | [0.11; 1.73] | kPa | [427.16; 484.82] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.81486e+01 | |||
| Coefficient B | -7.48219e+03 | |||
| Coefficient C | -5.96590e+01 | |||
| Reference | Rose and Schrodt, 1964 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 427.16 | |||
| Temperature range, max. | 484.82 | |||
| Pvap | 0.11 | kPa | 427.16 | Calculated Property |
| Pvap | 0.16 | kPa | 433.57 | Calculated Property |
| Pvap | 0.22 | kPa | 439.97 | Calculated Property |
| Pvap | 0.30 | kPa | 446.38 | Calculated Property |
| Pvap | 0.41 | kPa | 452.79 | Calculated Property |
| Pvap | 0.56 | kPa | 459.19 | Calculated Property |
| Pvap | 0.75 | kPa | 465.60 | Calculated Property |
| Pvap | 1.00 | kPa | 472.01 | Calculated Property |
| Pvap | 1.32 | kPa | 478.41 | Calculated Property |
| Pvap | 1.73 | kPa | 484.82 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [850.11; 228.07] | kg/m3 | [312.15; 781.10] |
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 | 4.98233e+01 | |||
| Coefficient B | 2.18460e-01 | |||
| Coefficient C | 7.81100e+02 | |||
| Coefficient D | 2.84350e-01 | |||
| Temperature range, min. | 312.15 | |||
| Temperature range, max. | 781.10 | |||
| ρl | 850.11 | kg/m3 | 312.15 | Calculated Property |
| ρl | 814.05 | kg/m3 | 364.26 | Calculated Property |
| ρl | 776.36 | kg/m3 | 416.36 | Calculated Property |
| ρl | 736.63 | kg/m3 | 468.47 | Calculated Property |
| ρl | 694.26 | kg/m3 | 520.57 | Calculated Property |
| ρl | 648.34 | kg/m3 | 572.68 | Calculated Property |
| ρl | 597.26 | kg/m3 | 624.78 | Calculated Property |
| ρl | 537.81 | kg/m3 | 676.89 | Calculated Property |
| ρl | 461.30 | kg/m3 | 728.99 | Calculated Property |
| ρl | 228.07 | kg/m3 | 781.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.02] | N/m | [311.15; 488.15] |
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 | 5.33691e-02 | |||
| Coefficient B | -7.75000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 311.15 | |||
| Temperature range, max. | 488.15 | |||
| γ | 0.03 | N/m | 311.15 | Calculated Property |
| γ | 0.03 | N/m | 330.82 | Calculated Property |
| γ | 0.03 | N/m | 350.48 | Calculated Property |
| γ | 0.02 | N/m | 370.15 | Calculated Property |
| γ | 0.02 | N/m | 389.82 | Calculated Property |
| γ | 0.02 | N/m | 409.48 | Calculated Property |
| γ | 0.02 | N/m | 429.15 | Calculated Property |
| γ | 0.02 | N/m | 448.82 | Calculated Property |
| γ | 0.02 | N/m | 468.48 | Calculated Property |
| γ | 0.02 | N/m | 488.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.05] | W/m×K | [623.70; 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 | 2.21770e-06 | |||
| Coefficient B | 1.44860e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 623.70 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 623.70 | Calculated Property |
| λgas | 0.03 | W/m×K | 665.51 | Calculated Property |
| λgas | 0.03 | W/m×K | 707.32 | Calculated Property |
| λgas | 0.03 | W/m×K | 749.13 | Calculated Property |
| λgas | 0.04 | W/m×K | 790.94 | Calculated Property |
| λgas | 0.04 | W/m×K | 832.76 | Calculated Property |
| λgas | 0.04 | W/m×K | 874.57 | Calculated Property |
| λgas | 0.04 | W/m×K | 916.38 | Calculated Property |
| λgas | 0.05 | W/m×K | 958.19 | Calculated Property |
| λgas | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.08] | W/m×K | [312.15; 623.70] |
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 | 1.95310e-01 | |||
| Coefficient B | -1.85000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 312.15 | |||
| Temperature range, max. | 623.70 | |||
| λliquid | 0.14 | W/m×K | 312.15 | Calculated Property |
| λliquid | 0.13 | W/m×K | 346.77 | Calculated Property |
| λliquid | 0.12 | W/m×K | 381.38 | Calculated Property |
| λliquid | 0.12 | W/m×K | 416.00 | Calculated Property |
| λliquid | 0.11 | W/m×K | 450.62 | Calculated Property |
| λliquid | 0.11 | W/m×K | 485.23 | Calculated Property |
| λliquid | 0.10 | W/m×K | 519.85 | Calculated Property |
| λliquid | 0.09 | W/m×K | 554.47 | Calculated Property |
| λliquid | 0.09 | W/m×K | 589.08 | Calculated Property |
| λliquid | 0.08 | W/m×K | 623.70 | Calculated Property |
Similar Compounds
Find more compounds similar to Methyl stearate.
Mixtures
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
- Crippen Method
- Phase behaviour of high molecular mass methyl esters in supercritical ethane
- Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
- Vapour liquid equilibria of monocaprylin plus palmitic acid or methyl stearate at P = (1.20 and 2.50) kPa by using DSC technique
- Fatty acids methyl esters: Complementary measurements and comprehensive analysis of vaporization thermodynamics
- the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
- Express thermo-gravimetric method for the vaporization enthalpies appraisal for very low volatile molecular and ionic compounds.
- A Comparison of Results by Correlation Gas Chromatography with Another Gas Chromatographic Retention Time Technique. The Effects of Retention Time Coincidence on Vaporization Enthalpy and Vapor Pressure
- 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
- Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
- Joback Method
- McGowan Method
- NIST Webbook
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