- 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 hexadecanoate
- Methyl n-hexadecanoate
- Methyl palmitate
- Palmitic acid, methyl ester
- Radia 7120
- Uniphat A60
- n-Hexadecanoic 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,solid : Solid 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).
- 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).
- Pvap : Vapor pressure (kPa).
- 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).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.8575 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -10107.00 ± 3.80 | kJ/mol | NIST |
| ΔcH°solid | -10669.00 ± 0.40 | kJ/mol | NIST |
| ΔfG° | -141.66 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -706.93 | kJ/mol | Relay (1.0) Calculated Property |
| 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 | 1271.87 | kPa | Joback Calculated Property |
| 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 | 2202.00 | NIST | |
| I | 2205.00 | NIST | |
| S°solid,1 bar | 495.09 | J/mol×K | NIST |
| Tboil | 566.70 | K | Relay (1.0) Calculated Property |
| Tc | 760.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tfus | [302.00; 304.00] | K |
|
| 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 |
| Vc | 1.011 | m3/kmol | Relay (1.0) Calculated Property |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [459.57; 640.62] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 |
Similar Compounds
Find more compounds similar to Hexadecanoic acid, methyl ester.
Mixtures
- Hexadecanoic acid, methyl ester + Methyl tetradecanoate
- Tetradecane + Hexadecanoic acid, methyl ester
- Methyl stearate + Hexadecanoic acid, methyl ester
- Ethane + Hexadecanoic acid, methyl ester
- Glycerin + Hexadecanoic acid, methyl ester + Methyl Alcohol
- Hexadecanoic acid, methyl ester + Methyl Alcohol
- Sucrose + Hexadecanoic acid, methyl ester
- 9-Octadecenoic acid (Z)-, methyl ester + Hexadecanoic acid, methyl ester + Methyl tetradecanoate
- Hexadecanoic acid, methyl ester + Water
- Benzene + Hexadecanoic acid, methyl ester + Water
- Toluene + Hexadecanoic acid, methyl ester + Water
- Hexadecanoic acid, methyl ester + Phenol + Water
- 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
- Glycerin + Hexadecanoic acid, methyl ester + Water
Sources
- Cheméo Relay (1.0)
- 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
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.