- InChI
- InChI=1S/C17H34O2/c1-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17(18)19-2/h3-16H2,1-2H3
- InChI Key
- FLIACVVOZYBSBS-UHFFFAOYSA-N
- Formula
- C17H34O2
- SMILES
- CCCCCCCCCCCCCCCC(=O)OC
- Molecular Weight1
- 270.45
- CAS
- 112-39-0
- Other Names
-
- Acide hexadecanoique methyl ester
- Emery 2216
- Metholene 2216
- Methyl n-hexadecanoate
- Radia 7120
- Uniphat A60
- methyl hexadecanoate
- methyl palmitate
- n-Hexadecanoic acid methyl ester
- palmitic acid, methyl ester
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- Cp,solid : Solid 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).
- ΔfH°liquid : Liquid phase 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.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : 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 | 0.7765 | ChemSep v8.3 pure component data | |
| ΔcH°liquid | -10107.00 ± 3.80 | kJ/mol | NIST |
| ΔcH°solid | -10669.00 ± 0.40 | kJ/mol | NIST |
| μ | 1.64 | debye | ChemSep v8.3 pure component data |
| ΔfG° | -254.00 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | -700.70 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°liquid | -1441.80 ± 3.80 | kJ/mol | NIST |
| ΔfusH° | 60.04 | kJ/mol | Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K |
| ΔvapH° | [93.20; 96.80] | kJ/mol |
|
| ΔvapH° | 96.80 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 96.40 | kJ/mol | NIST |
| ΔvapH° | 93.20 | kJ/mol | NIST |
| IE | 9.77 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.17 | Relay (1.0) Calculated Property | |
| logPoct/wat | 5.641 | Crippen Calculated Property | |
| McVol | 257.830 | ml/mol | McGowan Calculated Property |
| Pc | 1235.00 | kPa | ChemSep v8.3 pure component data |
| Ptriple | 4.00e-06 | kPa | ChemSep v8.3 pure component data |
| Inp | [319.52; 1939.00] |
|
|
| Inp | 1904.10 | NIST | |
| Inp | 1905.20 | NIST | |
| Inp | 1906.40 | NIST | |
| Inp | 1907.60 | NIST | |
| Inp | 1908.90 | NIST | |
| Inp | 1910.20 | NIST | |
| Inp | 1911.50 | NIST | |
| Inp | 1912.00 | NIST | |
| Inp | 1915.00 | NIST | |
| Inp | 1902.00 | NIST | |
| Inp | 1902.00 | NIST | |
| Inp | 1913.00 | NIST | |
| Inp | 1913.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1921.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1918.00 | NIST | |
| Inp | 1917.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1933.00 | NIST | |
| Inp | 1915.00 | NIST | |
| Inp | 1916.00 | NIST | |
| Inp | 1928.10 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1920.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1916.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.30 | NIST | |
| Inp | 1927.70 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1898.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1920.00 | NIST | |
| Inp | 1929.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1907.00 | NIST | |
| Inp | 1907.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1908.78 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1904.00 | NIST | |
| Inp | 1905.00 | NIST | |
| Inp | 1907.32 | NIST | |
| Inp | 1908.17 | NIST | |
| Inp | 1908.87 | NIST | |
| Inp | 1915.75 | NIST | |
| Inp | 1909.61 | NIST | |
| Inp | 1914.72 | NIST | |
| Inp | 1908.65 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1925.90 | NIST | |
| Inp | 1926.40 | NIST | |
| Inp | 1929.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1913.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1914.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1920.00 | NIST | |
| Inp | 1917.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1920.00 | NIST | |
| Inp | 1928.00 | NIST | |
| Inp | 1928.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1912.00 | NIST | |
| Inp | 1921.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1931.00 | NIST | |
| Inp | 1939.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1934.00 | NIST | |
| Inp | 1929.00 | NIST | |
| Inp | 1907.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1900.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1902.00 | NIST | |
| Inp | 1923.00 | NIST | |
| Inp | 1923.00 | NIST | |
| Inp | 1928.00 | NIST | |
| Inp | 1931.00 | NIST | |
| Inp | 1930.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1930.00 | NIST | |
| Inp | 1928.10 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1906.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1913.00 | NIST | |
| Inp | 1915.00 | NIST | |
| Inp | 1916.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1929.00 | NIST | |
| Inp | 1928.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1904.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1922.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1914.00 | NIST | |
| Inp | 1929.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1905.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1928.00 | NIST | |
| Inp | 1916.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1906.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1907.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1913.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1912.00 | NIST | |
| Inp | 1905.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1933.00 | NIST | |
| Inp | 1903.00 | NIST | |
| Inp | 1904.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1930.00 | NIST | |
| Inp | 1933.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1922.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1919.00 | NIST | |
| Inp | 1922.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1894.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1922.00 | NIST | |
| Inp | 1939.00 | NIST | |
| Inp | 1933.00 | NIST | |
| Inp | 1922.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1928.00 | NIST | |
| Inp | 1911.00 | NIST | |
| Inp | 1938.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1917.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1935.00 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1907.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | Outlier 319.52 | NIST | |
| Inp | Outlier 322.66 | NIST | |
| Inp | Outlier 331.20 | NIST | |
| Inp | Outlier 331.20 | NIST | |
| Inp | Outlier 331.30 | NIST | |
| Inp | Outlier 321.19 | NIST | |
| Inp | Outlier 321.34 | NIST | |
| Inp | Outlier 321.34 | NIST | |
| Inp | 1920.00 | NIST | |
| Inp | 1909.00 | NIST | |
| Inp | 1928.00 | NIST | |
| Inp | 1927.00 | NIST | |
| Inp | 1934.00 | NIST | |
| Inp | 1923.00 | NIST | |
| Inp | 1910.00 | NIST | |
| Inp | 1925.00 | NIST | |
| Inp | 1906.00 | NIST | |
| Inp | 1908.00 | NIST | |
| Inp | 1924.00 | NIST | |
| Inp | 1907.00 | NIST | |
| Inp | 1912.00 | NIST | |
| Inp | 1925.90 | NIST | |
| Inp | Outlier 321.34 | NIST | |
| Inp | 1926.00 | NIST | |
| Inp | 1927.30 | NIST | |
| Inp | 1898.00 | NIST | |
| Inp | 1904.00 | NIST | |
| Inp | 1915.75 | NIST | |
| Inp | 1911.00 | NIST | |
| I | [2170.00; 2254.00] |
|
|
| I | 2205.00 | NIST | |
| I | 2243.00 | NIST | |
| I | 2191.00 | NIST | |
| I | 2202.00 | NIST | |
| I | 2177.00 | NIST | |
| I | 2202.00 | NIST | |
| I | 2205.00 | NIST | |
| I | 2223.00 | NIST | |
| I | 2190.00 | NIST | |
| I | Outlier 2170.00 | NIST | |
| I | 2210.00 | NIST | |
| I | 2213.00 | NIST | |
| I | 2217.00 | NIST | |
| I | 2217.00 | NIST | |
| I | 2191.00 | NIST | |
| I | Outlier 2251.00 | NIST | |
| I | 2218.00 | NIST | |
| I | 2223.00 | NIST | |
| I | 2218.00 | NIST | |
| I | 2210.00 | NIST | |
| I | 2233.00 | NIST | |
| I | 2233.00 | NIST | |
| I | Outlier 2171.00 | NIST | |
| I | 2190.00 | NIST | |
| I | 2202.00 | NIST | |
| I | 2213.00 | NIST | |
| I | 2202.00 | NIST | |
| I | 2206.00 | NIST | |
| I | 2220.00 | NIST | |
| I | Outlier 2170.00 | NIST | |
| I | 2182.00 | NIST | |
| I | 2218.00 | NIST | |
| I | 2245.00 | NIST | |
| I | 2226.00 | NIST | |
| I | 2198.00 | NIST | |
| I | 2198.00 | NIST | |
| I | 2202.00 | NIST | |
| I | 2202.00 | NIST | |
| I | 2205.00 | NIST | |
| I | 2198.00 | NIST | |
| I | 2220.00 | NIST | |
| I | 2213.00 | NIST | |
| I | 2198.00 | NIST | |
| I | 2225.00 | NIST | |
| I | 2178.00 | NIST | |
| I | 2210.00 | NIST | |
| I | 2180.00 | NIST | |
| I | Outlier 2254.00 | NIST | |
| I | 2203.00 | NIST | |
| I | 2208.00 | NIST | |
| I | 2208.00 | NIST | |
| I | 2226.00 | NIST | |
| I | 2216.00 | NIST | |
| I | 2207.00 | NIST | |
| I | 2226.00 | NIST | |
| I | 2204.00 | NIST | |
| I | 2226.00 | NIST | |
| I | 2226.00 | NIST | |
| I | 2175.00 | NIST | |
| I | 2207.00 | NIST | |
| I | 2214.00 | NIST | |
| I | 2216.00 | NIST | |
| I | 2238.00 | NIST | |
| I | 2205.00 | NIST | |
| I | 2202.00 | NIST | |
| S°solid,1 bar | 495.09 | J/mol×K | NIST |
| Tboil | 469.15 | K | ChemSep v8.3 pure component data |
| Tc | [760.00; 762.20] | K |
|
| Tc | 760.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tc | 762.20 | K | ChemSep v8.3 pure component data |
| Tfus | [302.00; 304.00] | K |
|
| Tfus | 303.10 | K | ChemSep v8.3 pure component data |
| Tfus | 304.00 ± 1.00 | K | NIST |
| Tfus | 303.05 ± 0.35 | K | NIST |
| Tfus | 302.74 ± 0.10 | K | NIST |
| Tfus | 302.00 ± 2.00 | K | NIST |
| Tfus | 302.74 ± 0.10 | K | NIST |
| Ttriple | 301.85 | K | ChemSep v8.3 pure component data |
| UQi | 10.14 | ChemSep v8.3 pure component data | |
| URi | 12.25 | ChemSep v8.3 pure component data | |
| Vc | 1.150 | m3/kmol | ChemSep v8.3 pure component data |
| Zc | 0.2240000 | ChemSep v8.3 pure component data |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 436.70 | K | 0.50 | NIST |
Datasets
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 100.00 | 313.15 | 1317.2 |
| 10000.00 | 313.15 | 1365.4 |
| 20000.00 | 313.15 | 1411.5 |
| 30000.00 | 313.15 | 1454.4 |
| 40000.00 | 313.15 | 1494.8 |
| 100.00 | 323.15 | 1283.4 |
| 10000.00 | 323.15 | 1333.7 |
| 20000.00 | 323.15 | 1381.1 |
| 30000.00 | 323.15 | 1425.2 |
| 40000.00 | 323.15 | 1467.4 |
| 50000.00 | 323.15 | 1506.9 |
| 100.00 | 343.15 | 1215.3 |
| 10000.00 | 343.15 | 1270.1 |
| 20000.00 | 343.15 | 1319.7 |
| 30000.00 | 343.15 | 1366.8 |
| 40000.00 | 343.15 | 1410.5 |
| 50000.00 | 343.15 | 1450.6 |
| 100.00 | 363.15 | 1150.1 |
| 10000.00 | 363.15 | 1208.9 |
| 20000.00 | 363.15 | 1262.5 |
| 30000.00 | 363.15 | 1311.1 |
| 40000.00 | 363.15 | 1355.7 |
| 50000.00 | 363.15 | 1400.9 |
| 100.00 | 383.15 | 1087.2 |
| 10000.00 | 383.15 | 1150.3 |
| 20000.00 | 383.15 | 1207.5 |
| 30000.00 | 383.15 | 1259.3 |
| 40000.00 | 383.15 | 1310.8 |
| 50000.00 | 383.15 | 1358.3 |
| 100.00 | 393.15 | 1056.9 |
| 10000.00 | 393.15 | 1121.2 |
| 20000.00 | 393.15 | 1180.4 |
| 30000.00 | 393.15 | 1234.2 |
| 40000.00 | 393.15 | 1284.7 |
| 50000.00 | 393.15 | 1334.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [411.99; 1045.48] | J/mol×K | [298.15; 1500.00] |
ChemSep v8.3 pure component data
|
| 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 | 3.27170e+02 | |||
| Coefficient B | 6.30350e+02 | |||
| Coefficient C | 8.02120e+02 | |||
| Coefficient D | 3.83110e+02 | |||
| Coefficient E | 2.44830e+03 | |||
| Comment | ChemSep eq 107, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 411.99 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 550.21 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 667.44 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 757.75 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 830.63 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 891.70 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 943.03 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 985.34 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 1019.23 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 1045.48 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [565.27; 765.31] | J/mol×K | [303.05; 597.70] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 3.59530e+02 | |||
| Coefficient B | 6.78900e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidHeatCapacityCp | |||
| Temperature range, min. | 303.05 | |||
| Temperature range, max. | 597.70 | |||
| Cp,liquid | 565.27 | J/mol×K | 303.05 | Calculated Property |
| Cp,liquid | 587.50 | J/mol×K | 335.79 | Calculated Property |
| Cp,liquid | 609.72 | J/mol×K | 368.53 | Calculated Property |
| Cp,liquid | 631.95 | J/mol×K | 401.27 | Calculated Property |
| Cp,liquid | 654.18 | J/mol×K | 434.01 | Calculated Property |
| Cp,liquid | 676.40 | J/mol×K | 466.74 | Calculated Property |
| Cp,liquid | 698.63 | J/mol×K | 499.48 | Calculated Property |
| Cp,liquid | 720.86 | J/mol×K | 532.22 | Calculated Property |
| Cp,liquid | 743.08 | J/mol×K | 564.96 | Calculated Property |
| Cp,liquid | 765.31 | J/mol×K | 597.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0046686; 0.0002141] | Pa×s | [303.05; 597.70] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.16190e+01 | |||
| Coefficient B | 1.89470e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 303.05 | |||
| Temperature range, max. | 597.70 | |||
| η | 0.0046686 | Pa×s | 303.05 | Calculated Property |
| η | 0.0025378 | Pa×s | 335.79 | Calculated Property |
| η | 0.0015373 | Pa×s | 368.53 | Calculated Property |
| η | 0.0010106 | Pa×s | 401.27 | Calculated Property |
| η | 0.0007078 | Pa×s | 434.01 | Calculated Property |
| η | 0.0005211 | Pa×s | 466.74 | Calculated Property |
| η | 0.0003993 | Pa×s | 499.48 | Calculated Property |
| η | 0.0003162 | Pa×s | 532.22 | Calculated Property |
| η | 0.0002573 | Pa×s | 564.96 | Calculated Property |
| η | 0.0002141 | Pa×s | 597.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [90.27; 0.00] | kJ/mol | [303.05; 762.20] |
ChemSep v8.3 pure component data
|
| 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 | 1.30010e+02 | |||
| Coefficient B | 1.12830e+00 | |||
| Coefficient C | -1.30170e+00 | |||
| Coefficient D | 6.89490e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.62200e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 303.05 | |||
| Temperature range, max. | 762.20 | |||
| ΔvapH | 90.27 | kJ/mol | 303.05 | Calculated Property |
| ΔvapH | 85.42 | kJ/mol | 354.07 | Calculated Property |
| ΔvapH | 80.56 | kJ/mol | 405.08 | Calculated Property |
| ΔvapH | 75.46 | kJ/mol | 456.10 | Calculated Property |
| ΔvapH | 69.86 | kJ/mol | 507.12 | Calculated Property |
| ΔvapH | 63.41 | kJ/mol | 558.13 | Calculated Property |
| ΔvapH | 55.66 | kJ/mol | 609.15 | Calculated Property |
| ΔvapH | 45.87 | kJ/mol | 660.17 | Calculated Property |
| ΔvapH | 32.39 | kJ/mol | 711.18 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 762.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [459.57; 640.62] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50314e+01 | |||
| Coefficient B | -5.16468e+03 | |||
| Coefficient C | -1.09270e+02 | |||
| Temperature range, min. | 459.57 | |||
| Temperature range, max. | 640.62 | |||
| Pvap | 1.33 | kPa | 459.57 | Calculated Property |
| Pvap | 2.97 | kPa | 479.69 | Calculated Property |
| Pvap | 6.09 | kPa | 499.80 | Calculated Property |
| Pvap | 11.64 | kPa | 519.92 | Calculated Property |
| Pvap | 20.95 | kPa | 540.04 | Calculated Property |
| Pvap | 35.76 | kPa | 560.15 | Calculated Property |
| Pvap | 58.33 | kPa | 580.27 | Calculated Property |
| Pvap | 91.40 | kPa | 600.39 | Calculated Property |
| Pvap | 138.24 | kPa | 620.50 | Calculated Property |
| Pvap | 202.65 | kPa | 640.62 | Calculated Property |
| Pvap | [1.84e-05; 1244.80] | kPa | [303.05; 762.20] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.04082e+02 | |||
| Coefficient B | -1.44400e+04 | |||
| Coefficient C | -1.17850e+01 | |||
| Coefficient D | 1.00660e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 303.05 | |||
| Temperature range, max. | 762.20 | |||
| Pvap | 1.84e-05 | kPa | 303.05 | Calculated Property |
| Pvap | 2.82e-03 | kPa | 354.07 | Calculated Property |
| Pvap | 0.10 | kPa | 405.08 | Calculated Property |
| Pvap | 1.32 | kPa | 456.10 | Calculated Property |
| Pvap | 9.20 | kPa | 507.12 | Calculated Property |
| Pvap | 40.66 | kPa | 558.13 | Calculated Property |
| Pvap | 129.33 | kPa | 609.15 | Calculated Property |
| Pvap | 323.20 | kPa | 660.17 | Calculated Property |
| Pvap | 676.56 | kPa | 711.18 | Calculated Property |
| Pvap | 1244.80 | kPa | 762.20 | Calculated Property |
| Pvap | [0.27; 2.67] | kPa | [421.70; 475.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.89885e+01 | |||
| Coefficient B | -8.54184e+03 | |||
| Coefficient C | -1.06200e+00 | |||
| Reference | Bonhorst, Althouse, et al., 1948 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 421.70 | |||
| Temperature range, max. | 475.40 | |||
| Pvap | 0.27 | kPa | 421.70 | Calculated Property |
| Pvap | 0.36 | kPa | 427.67 | Calculated Property |
| Pvap | 0.47 | kPa | 433.63 | Calculated Property |
| Pvap | 0.61 | kPa | 439.60 | Calculated Property |
| Pvap | 0.80 | kPa | 445.57 | Calculated Property |
| Pvap | 1.03 | kPa | 451.53 | Calculated Property |
| Pvap | 1.32 | kPa | 457.50 | Calculated Property |
| Pvap | 1.68 | kPa | 463.47 | Calculated Property |
| Pvap | 2.12 | kPa | 469.43 | Calculated Property |
| Pvap | 2.67 | kPa | 475.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [857.57; 236.13] | kg/m3 | [303.05; 762.20] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 5.27055e+01 | |||
| Coefficient B | 2.23210e-01 | |||
| Coefficient C | 7.62200e+02 | |||
| Coefficient D | 2.97500e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 303.05 | |||
| Temperature range, max. | 762.20 | |||
| ρl | 857.57 | kg/m3 | 303.05 | Calculated Property |
| ρl | 820.32 | kg/m3 | 354.07 | Calculated Property |
| ρl | 781.48 | kg/m3 | 405.08 | Calculated Property |
| ρl | 740.66 | kg/m3 | 456.10 | Calculated Property |
| ρl | 697.28 | kg/m3 | 507.12 | Calculated Property |
| ρl | 650.44 | kg/m3 | 558.13 | Calculated Property |
| ρl | 598.56 | kg/m3 | 609.15 | Calculated Property |
| ρl | 538.52 | kg/m3 | 660.17 | Calculated Property |
| ρl | 461.83 | kg/m3 | 711.18 | Calculated Property |
| ρl | 236.13 | kg/m3 | 762.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.02; 0.05] | W/m×K | [597.70; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.80300e-06 | |||
| Coefficient B | 1.48570e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 597.70 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.02 | W/m×K | 597.70 | Calculated Property |
| λ | 0.03 | W/m×K | 642.40 | Calculated Property |
| λ | 0.03 | W/m×K | 687.10 | Calculated Property |
| λ | 0.03 | W/m×K | 731.80 | Calculated Property |
| λ | 0.04 | W/m×K | 776.50 | Calculated Property |
| λ | 0.04 | W/m×K | 821.20 | Calculated Property |
| λ | 0.04 | W/m×K | 865.90 | Calculated Property |
| λ | 0.04 | W/m×K | 910.60 | Calculated Property |
| λ | 0.05 | W/m×K | 955.30 | Calculated Property |
| λ | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.14; 0.08] | W/m×K | [303.05; 597.70] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.98230e-01 | |||
| Coefficient B | -1.91700e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidThermalConductivity | |||
| Temperature range, min. | 303.05 | |||
| Temperature range, max. | 597.70 | |||
| λ | 0.14 | W/m×K | 303.05 | Calculated Property |
| λ | 0.13 | W/m×K | 335.79 | Calculated Property |
| λ | 0.13 | W/m×K | 368.53 | Calculated Property |
| λ | 0.12 | W/m×K | 401.27 | Calculated Property |
| λ | 0.12 | W/m×K | 434.01 | Calculated Property |
| λ | 0.11 | W/m×K | 466.74 | Calculated Property |
| λ | 0.10 | W/m×K | 499.48 | Calculated Property |
| λ | 0.10 | W/m×K | 532.22 | Calculated Property |
| λ | 0.09 | W/m×K | 564.96 | Calculated Property |
| λ | 0.08 | W/m×K | 597.70 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexadecanoic acid, methyl ester.
Mixtures
- Glycerin + Hexadecanoic acid, methyl ester + Methyl Alcohol
- Hexadecanoic acid, methyl ester + Water
- Benzene + Hexadecanoic acid, methyl ester + Water
- Toluene + Hexadecanoic acid, methyl ester + Water
- Hexadecanoic acid, methyl ester + Phenol + Water
- Hexadecanoic acid, methyl ester + Methyl tetradecanoate
- Ethane + Hexadecanoic acid, methyl ester
- Glycerin + Hexadecanoic acid, methyl ester + Water
- Hexadecanoic acid, methyl ester + Methyl Alcohol
- Methyl stearate + Hexadecanoic acid, methyl ester
- Sucrose + Hexadecanoic acid, methyl ester
- Tetradecane + Hexadecanoic acid, methyl ester
- 9-Octadecenoic acid (Z)-, methyl ester + Hexadecanoic acid, methyl ester + Methyl tetradecanoate
- Thiophene + Hexadecanoic acid, methyl ester + Water
- Pyridine + Hexadecanoic acid, methyl ester + Water
- Hexadecanoic acid, methyl ester + Naphthalene + Water
- Phenanthrene + Hexadecanoic acid, methyl ester + Water
- Anthracene + Hexadecanoic acid, methyl ester + Water
Sources
- 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
- Isobaric vapor liquid equilibrium for binary system of methyl myristate + methyl palmitate at 0.5, 1.0 and 1.4 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
- Tar removal from biosyngas in the biomass gasification process. (Liquid + liquid) equilibrium {water + solvent (paraxylene and methyl hexadecanoate) + model molecules of tar (benzene, toluene, phenol)}
- 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
- Measurement and correlation of the density, viscosity and vapor pressure of fatty acid 2-ethyhexyl esters
- 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
- Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
- 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
- Measurements and Correlations of the Density, Viscosity, and Vapor Pressure for Methyl Ricinoleate
- Vapor Liquid Equilibrium for Methanol + Methyl Palmitate near the Critical Temperature of Methanol
- Elimination of Tar in Biomass Gasification Process: Liquid Liquid Equilibrium of Ternary Systems {Water + Solvent (p-Xylene and Methyl Hexadecanoate) + Model Molecules of Tar (Thiophene, Pyridine, Naphthalene, Phenathrene, and Anthracene)}
- Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
- Solid-Liquid Equilibria and Characterization of the Reaction Mixture To Produce Sucrose Palmitate in Solvent-Free Media
- 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
- Density and Speed of Sound Measurements on Five Fatty Acid Methyl Esters at 83 kPa and Temperatures from (278.15 to 338.15) K
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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