- InChI
- InChI=1S/C16H32O2/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16(17)18/h2-15H2,1H3,(H,17,18)
- InChI Key
- IPCSVZSSVZVIGE-UHFFFAOYSA-N
- Formula
- C16H32O2
- SMILES
- CCCCCCCCCCCCCCCC(=O)O
- Molecular Weight1
- 256.42
- CAS
- 57-10-3
- Other Names
-
- 1-Pentadecanecarboxylic acid
- Cetylic acid
- Emersol 140
- Emersol 143
- Glycon P-45
- Hexadecanoic (palmitic) acid
- Hexadecanoic acid (palmitic acid)
- Hexadecylic acid
- Hydrofol
- Hystrene 8016
- Hystrene 9016
- Industrene 4516
- Kortacid 1695
- N-PALMITIC ACID
- NSC 5030
- Palmitic acid (hexadecanoic acid)
- Palmitinic acid
- Pentadecanecarboxylic acid
- Prifac 2960
- hexadecanoic acid
- n-Hexadecoic acid
- palmitic acid
- 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 standard conditions (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.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (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 | 0.9919 | ChemSep v8.3 pure component data | |
| ΔcH°liquid | [-10028.60; -9977.20] | kJ/mol |
|
| ΔcH°liquid | -9977.20 ± 1.60 | kJ/mol | NIST |
| ΔcH°liquid | -10028.60 ± 1.90 | kJ/mol | NIST |
| ΔcH°solid | -9977.60 ± 8.80 | kJ/mol | NIST |
| μ | 0.76 | debye | ChemSep v8.3 pure component data |
| ΔfG° | -260.00 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | [-730.00; -723.00] | kJ/mol |
|
| ΔfH°gas | -723.00 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | -730.00 ± 5.50 | kJ/mol | NIST |
| ΔfH°liquid | -848.40 ± 2.20 | kJ/mol | NIST |
| ΔfusH° | [52.55; 53.50] | kJ/mol |
|
| ΔfusH° | 52.55 | kJ/mol | Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs) |
| ΔfusH° | 53.50 | kJ/mol | Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry |
| ΔsubH° | 194.00 ± 11.00 | kJ/mol | NIST |
| ΔvapH° | 116.50 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.99 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.81 | Aq. Solubility Prediction | |
| logPoct/wat | 5.552 | Crippen Calculated Property | |
| McVol | 243.740 | ml/mol | McGowan Calculated Property |
| Pc | [1468.41; 1490.00] | kPa |
|
| Pc | 1490.00 | kPa | ChemSep v8.3 pure component data |
| Pc | 1468.41 ± 85.00 | kPa | NIST |
| Ptriple | [8.27e-06; 1.83e-05] | kPa |
|
| Ptriple | 1.83e-05 | kPa | ChemSep v8.3 pure component data |
| Ptriple | 8.27e-06 ± 4.00e-06 | kPa | NIST |
| Inp | [321.57; 2010.00] |
|
|
| Inp | 1961.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 2009.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1938.00 | NIST | |
| Inp | 1940.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1940.00 | NIST | |
| Inp | 1974.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1946.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1961.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1942.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 2010.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 2003.00 | NIST | |
| Inp | 1995.50 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1991.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1979.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1994.00 | NIST | |
| Inp | 1949.00 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | 1966.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1954.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1966.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1938.00 | NIST | |
| Inp | 1938.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1952.00 | NIST | |
| Inp | 1952.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1941.00 | NIST | |
| Inp | 1952.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1998.93 | NIST | |
| Inp | 1999.89 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1966.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1950.00 | NIST | |
| Inp | 1982.00 | NIST | |
| Inp | 1939.00 | NIST | |
| Inp | 1942.00 | NIST | |
| Inp | 1942.00 | NIST | |
| Inp | 1943.00 | NIST | |
| Inp | 1938.97 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 2001.00 | NIST | |
| Inp | 2000.00 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | 1950.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1968.20 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1963.50 | NIST | |
| Inp | 2010.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1941.00 | NIST | |
| Inp | 1966.00 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1945.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1943.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1953.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1943.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1942.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1945.00 | NIST | |
| Inp | 1991.00 | NIST | |
| Inp | 1944.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1974.00 | NIST | |
| Inp | 2001.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1933.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1954.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1959.60 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1936.00 | NIST | |
| Inp | 1936.00 | NIST | |
| Inp | 1949.00 | NIST | |
| Inp | 1940.00 | NIST | |
| Inp | 1935.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1931.00 | NIST | |
| Inp | 1931.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1955.00 | NIST | |
| Inp | 1974.00 | NIST | |
| Inp | 1993.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1983.00 | NIST | |
| Inp | 1959.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 2009.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1997.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 1940.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1939.00 | NIST | |
| Inp | 1959.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1972.20 | NIST | |
| Inp | 1959.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1936.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1949.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1955.00 | NIST | |
| Inp | 1950.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1946.00 | NIST | |
| Inp | 1946.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1945.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1986.00 | NIST | |
| Inp | 1983.00 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | 1974.00 | NIST | |
| Inp | 1944.00 | NIST | |
| Inp | 1953.00 | NIST | |
| Inp | 1946.00 | NIST | |
| Inp | 1936.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1946.00 | NIST | |
| Inp | 1941.00 | NIST | |
| Inp | 1944.00 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1961.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1947.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1944.00 | NIST | |
| Inp | 1950.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1992.00 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1961.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1953.00 | NIST | |
| Inp | 1929.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1952.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1987.00 | NIST | |
| Inp | 1949.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1942.00 | NIST | |
| Inp | 1917.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1940.00 | NIST | |
| Inp | 1953.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 2010.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 2010.00 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1948.00 | NIST | |
| Inp | 1948.00 | NIST | |
| Inp | 1961.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1983.00 | NIST | |
| Inp | 1942.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1943.00 | NIST | |
| Inp | 1944.00 | NIST | |
| Inp | 1945.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1980.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | Outlier 324.00 | NIST | |
| Inp | Outlier 336.70 | NIST | |
| Inp | Outlier 336.70 | NIST | |
| Inp | Outlier 336.90 | NIST | |
| Inp | Outlier 322.20 | NIST | |
| Inp | Outlier 321.88 | NIST | |
| Inp | Outlier 321.57 | NIST | |
| Inp | Outlier 325.15 | NIST | |
| Inp | 1968.20 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | Outlier 321.88 | NIST | |
| Inp | 1974.00 | NIST | |
| Inp | 1946.00 | NIST | |
| Inp | 1961.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1965.00 | NIST | |
| Inp | 1940.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1953.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | Outlier 324.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1966.00 | NIST | |
| Inp | 1952.00 | NIST | |
| Inp | 1939.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1943.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 2001.00 | NIST | |
| Inp | 1936.00 | NIST | |
| Inp | 1959.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1937.00 | NIST | |
| I | [2871.00; 2954.00] |
|
|
| I | 2910.00 | NIST | |
| I | 2890.00 | NIST | |
| I | 2886.00 | NIST | |
| I | 2919.00 | NIST | |
| I | 2923.00 | NIST | |
| I | 2888.00 | NIST | |
| I | 2880.00 | NIST | |
| I | 2928.00 | NIST | |
| I | 2899.00 | NIST | |
| I | 2900.00 | NIST | |
| I | 2954.00 | NIST | |
| I | 2922.00 | NIST | |
| I | 2899.00 | NIST | |
| I | 2900.00 | NIST | |
| I | 2910.00 | NIST | |
| I | 2946.00 | NIST | |
| I | 2940.00 | NIST | |
| I | 2886.00 | NIST | |
| I | Outlier 2871.00 | NIST | |
| I | 2930.00 | NIST | |
| I | 2886.00 | NIST | |
| I | 2886.00 | NIST | |
| I | 2916.00 | NIST | |
| I | 2903.00 | NIST | |
| I | 2912.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2892.00 | NIST | |
| I | 2900.00 | NIST | |
| I | 2911.00 | NIST | |
| I | 2920.00 | NIST | |
| I | 2906.00 | NIST | |
| I | 2913.00 | NIST | |
| I | 2905.00 | NIST | |
| I | 2894.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2886.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2913.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2929.00 | NIST | |
| I | Outlier 2875.00 | NIST | |
| I | 2887.00 | NIST | |
| I | 2917.00 | NIST | |
| I | 2880.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2912.00 | NIST | |
| I | 2876.00 | NIST | |
| I | 2886.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | Outlier 2871.00 | NIST | |
| I | Outlier 2871.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | Outlier 2871.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2890.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2931.00 | NIST | |
| I | 2917.00 | NIST | |
| I | 2876.00 | NIST | |
| I | 2930.00 | NIST | |
| I | 2910.00 | NIST | |
| I | 2890.00 | NIST | |
| I | 2880.00 | NIST | |
| I | 2922.00 | NIST | |
| I | 2940.00 | NIST | |
| I | 2931.00 | NIST | |
| I | Outlier 2871.00 | NIST | |
| S°solid,1 bar | [438.65; 543.50] | J/mol×K |
|
| S°solid,1 bar | 452.37 | J/mol×K | NIST |
| S°solid,1 bar | 438.65 | J/mol×K | NIST |
| S°solid,1 bar | 475.70 | J/mol×K | NIST |
| S°solid,1 bar | 543.50 | J/mol×K | NIST |
| Tboil | [612.15; 624.15] | K |
|
| Tboil | 624.15 | K | ChemSep v8.3 pure component data |
| Tboil | 612.15 ± 6.00 | K | NIST |
| Tc | [785.00; 785.22] | K |
|
| Tc | 785.00 | K | ChemSep v8.3 pure component data |
| Tc | 785.22 ± 3.00 | K | NIST |
| Tfus | [328.15; 337.22] | K |
|
| Tfus | 336.84 | K | Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids |
| Tfus | 337.17 | K | Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry |
| Tfus | 337.22 | K | The solid liquid phase diagrams of binary mixtures of even saturated fatty acids differing by six carbon atoms |
| Tfus | 334.85 | K | Prediction of the properties of eutectic fatty acid phase change materials |
| Tfus | 335.75 | K | Nano-inclusion aided thermal conductivity enhancement in palmitic acid/di-methyl formamide phase change material for latent heat thermal energy storage |
| Tfus | 335.90 | K | Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane |
| Tfus | 335.44 | K | Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures |
| Tfus | 336.70 | K | Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems |
| Tfus | 335.02 | K | Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols |
| Tfus | 336.00 | K | Study of the Effect of Pressure on Melting Behavior of Saturated Fatty Acids in Liquid or Supercritical Carbon Dioxide |
| Tfus | 335.80 | K | Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures |
| Tfus | 335.66 | K | ChemSep v8.3 pure component data |
| Tfus | 334.92 | K | Aq. Solubility Prediction |
| Tfus | 336.15 ± 0.30 | K | NIST |
| Tfus | 334.60 ± 0.40 | K | NIST |
| Tfus | 334.60 ± 0.40 | K | NIST |
| Tfus | 334.60 ± 0.40 | K | NIST |
| Tfus | 336.00 ± 2.00 | K | NIST |
| Tfus | 335.80 ± 0.05 | K | NIST |
| Tfus | 335.65 ± 0.30 | K | NIST |
| Tfus | 335.50 ± 0.60 | K | NIST |
| Tfus | 335.83 ± 0.10 | K | NIST |
| Tfus | 336.70 ± 2.00 | K | NIST |
| Tfus | 335.70 ± 0.10 | K | NIST |
| Tfus | 336.00 ± 2.00 | K | NIST |
| Tfus | 334.00 ± 2.00 | K | NIST |
| Tfus | 335.33 ± 0.30 | K | NIST |
| Tfus | 335.55 ± 0.30 | K | NIST |
| Tfus | 335.49 ± 0.30 | K | NIST |
| Tfus | 335.25 ± 0.30 | K | NIST |
| Tfus | 335.50 ± 1.00 | K | NIST |
| Tfus | 336.00 ± 3.00 | K | NIST |
| Tfus | 334.90 ± 1.00 | K | NIST |
| Tfus | Outlier 328.15 ± 0.50 | K | NIST |
| Tfus | 335.20 ± 3.00 | K | NIST |
| Ttriple | [335.05; 336.25] | K |
|
| Ttriple | 336.25 | K | Form-stable phase change nanocomposites for thermal energy storage based on hypercrosslinked polymer nanospheres |
| Ttriple | 336.13 | K | Solubility Measurement of Lauric, Palmitic, and Stearic Acids in Ethanol, n-Propanol, and 2-Propanol Using Differential Scanning Calorimetry |
| Ttriple | 335.66 | K | ChemSep v8.3 pure component data |
| Ttriple | 335.66 ± 0.02 | K | NIST |
| Ttriple | 335.05 ± 0.50 | K | NIST |
| Ttriple | 335.66 ± 0.02 | K | NIST |
| UQi | 9.63 | ChemSep v8.3 pure component data | |
| URi | 11.64 | ChemSep v8.3 pure component data | |
| Vc | 1.015 | m3/kmol | ChemSep v8.3 pure component data |
| Zc | 0.2320000 | ChemSep v8.3 pure component data |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | [448.00; 678.00] | J/mol×K | [292.50; 373.00] |
|
| Cp,solid | 462.30 | J/mol×K | 292.50 | NIST |
| Cp,solid | 448.00 | J/mol×K | 298.00 | NIST |
| Cp,solid | 463.36 | J/mol×K | 298.15 | NIST |
| Cp,solid | 460.66 | J/mol×K | 298.15 | NIST |
| Cp,solid | 678.00 | J/mol×K | 373.00 | NIST |
| ΔfusH | [47.00; 54.94] | kJ/mol | [332.70; 336.50] |
|
| ΔfusH | 51.37 | kJ/mol | 332.70 | NIST |
| ΔfusH | 53.00 | kJ/mol | 334.70 | NIST |
| ΔfusH | 53.90 | kJ/mol | 335.40 | NIST |
| ΔfusH | 54.81 | kJ/mol | 335.70 | NIST |
| ΔfusH | 54.81 | kJ/mol | 335.70 | NIST |
| ΔfusH | 54.89 | kJ/mol | 335.73 | NIST |
| ΔfusH | 54.94 | kJ/mol | 336.00 | NIST |
| ΔfusH | 47.00 | kJ/mol | 336.50 | NIST |
| ΔsubH | [134.00; 154.40] | kJ/mol | [288.00; 326.50] |
|
| ΔsubH | 134.00 | kJ/mol | 288.00 | NIST |
| ΔsubH | 154.00 | kJ/mol | 305.00 | NIST |
| ΔsubH | 154.00 ± 4.20 | kJ/mol | 319.64 | NIST |
| ΔsubH | 154.40 ± 4.20 | kJ/mol | 326.50 | NIST |
| ΔsubH | 154.40 ± 4.20 | kJ/mol | 326.50 | NIST |
| ΔvapH | [90.10; 121.60] | kJ/mol | [298.00; 532.50] |
|
| ΔvapH | 121.60 | kJ/mol | 298.00 | Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids |
| ΔvapH | 110.20 ± 2.00 | kJ/mol | 360.50 | NIST |
| ΔvapH | 90.10 | kJ/mol | 475.00 | NIST |
| ΔvapH | 97.50 | kJ/mol | 532.50 | NIST |
| Pvap | [1.33; 9.33] | kPa | [483.30; 533.40] |
|
| Pvap | 1.33 | kPa | 483.30 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 2.67 | kPa | 498.60 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 4.00 | kPa | 509.00 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 5.33 | kPa | 517.30 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 6.67 | kPa | 523.40 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 8.00 | kPa | 527.90 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| Pvap | 9.33 | kPa | 533.40 | Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique |
| ΔfusS | [163.50; 163.50] | J/mol×K | [335.73; 336.00] |
|
| ΔfusS | 163.50 | J/mol×K | 335.73 | NIST |
| ΔfusS | 163.50 | J/mol×K | 336.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [483.15; 498.35] | K | [1.20; 2.50] |
|
| Tboil | 483.15 | 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 | 498.35 | 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 | 544.70 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [381.01; 985.76] | J/mol×K | [300.00; 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 | 2.84750e+02 | |||
| Coefficient B | 8.64940e+02 | |||
| Coefficient C | 1.68780e+03 | |||
| Coefficient D | 6.11070e+02 | |||
| Coefficient E | 7.67350e+02 | |||
| Comment | ChemSep eq 107, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 300.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 381.01 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 516.19 | J/mol×K | 433.33 | Calculated Property |
| Cp,gas | 627.16 | J/mol×K | 566.67 | Calculated Property |
| Cp,gas | 714.64 | J/mol×K | 700.00 | Calculated Property |
| Cp,gas | 785.49 | J/mol×K | 833.33 | Calculated Property |
| Cp,gas | 843.32 | J/mol×K | 966.67 | Calculated Property |
| Cp,gas | 890.45 | J/mol×K | 1100.00 | Calculated Property |
| Cp,gas | 928.82 | J/mol×K | 1233.33 | Calculated Property |
| Cp,gas | 960.12 | J/mol×K | 1366.67 | Calculated Property |
| Cp,gas | 985.76 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [573.01; 1041.04] | J/mol×K | [335.66; 624.15] |
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 | 3.53400e+02 | |||
| Coefficient B | 1.33660e-01 | |||
| Coefficient C | 1.55100e-03 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidHeatCapacityCp | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 624.15 | |||
| Cp,liquid | 573.01 | J/mol×K | 335.66 | Calculated Property |
| Cp,liquid | 612.27 | J/mol×K | 367.71 | Calculated Property |
| Cp,liquid | 654.71 | J/mol×K | 399.77 | Calculated Property |
| Cp,liquid | 700.33 | J/mol×K | 431.82 | Calculated Property |
| Cp,liquid | 749.15 | J/mol×K | 463.88 | Calculated Property |
| Cp,liquid | 801.15 | J/mol×K | 495.93 | Calculated Property |
| Cp,liquid | 856.34 | J/mol×K | 527.99 | Calculated Property |
| Cp,liquid | 914.72 | J/mol×K | 560.04 | Calculated Property |
| Cp,liquid | 976.28 | J/mol×K | 592.10 | Calculated Property |
| Cp,liquid | 1041.04 | J/mol×K | 624.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0090415; 0.0003087] | Pa×s | [335.66; 624.15] |
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 | -2.27470e+01 | |||
| Coefficient B | 3.12810e+03 | |||
| Coefficient C | 1.49960e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 624.15 | |||
| η | 0.0090415 | Pa×s | 335.66 | Calculated Property |
| η | 0.0046008 | Pa×s | 367.71 | Calculated Property |
| η | 0.0026365 | Pa×s | 399.77 | Calculated Property |
| η | 0.0016558 | Pa×s | 431.82 | Calculated Property |
| η | 0.0011175 | Pa×s | 463.88 | Calculated Property |
| η | 0.0007989 | Pa×s | 495.93 | Calculated Property |
| η | 0.0005984 | Pa×s | 527.99 | Calculated Property |
| η | 0.0004657 | Pa×s | 560.04 | Calculated Property |
| η | 0.0003741 | Pa×s | 592.10 | Calculated Property |
| η | 0.0003087 | Pa×s | 624.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [112.93; 0.00] | kJ/mol | [335.66; 785.00] |
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 | 1.41400e+02 | |||
| Coefficient B | -2.11250e-01 | |||
| Coefficient C | 2.07070e+00 | |||
| Coefficient D | -1.48350e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.85000e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 785.00 | |||
| ΔvapH | 112.93 | kJ/mol | 335.66 | Calculated Property |
| ΔvapH | 104.47 | kJ/mol | 385.59 | Calculated Property |
| ΔvapH | 95.81 | kJ/mol | 435.51 | Calculated Property |
| ΔvapH | 87.18 | kJ/mol | 485.44 | Calculated Property |
| ΔvapH | 78.74 | kJ/mol | 535.37 | Calculated Property |
| ΔvapH | 70.55 | kJ/mol | 585.29 | Calculated Property |
| ΔvapH | 62.49 | kJ/mol | 635.22 | Calculated Property |
| ΔvapH | 54.10 | kJ/mol | 685.15 | Calculated Property |
| ΔvapH | 43.61 | kJ/mol | 735.07 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 785.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [481.72; 642.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.68013e+01 | |||
| Coefficient B | -6.05915e+03 | |||
| Coefficient C | -1.14803e+02 | |||
| Temperature range, min. | 481.72 | |||
| Temperature range, max. | 642.15 | |||
| Pvap | 1.33 | kPa | 481.72 | Calculated Property |
| Pvap | 2.87 | kPa | 499.55 | Calculated Property |
| Pvap | 5.75 | kPa | 517.37 | Calculated Property |
| Pvap | 10.89 | kPa | 535.20 | Calculated Property |
| Pvap | 19.58 | kPa | 553.02 | Calculated Property |
| Pvap | 33.61 | kPa | 570.85 | Calculated Property |
| Pvap | 55.41 | kPa | 588.67 | Calculated Property |
| Pvap | 88.09 | kPa | 606.50 | Calculated Property |
| Pvap | 135.56 | kPa | 624.32 | Calculated Property |
| Pvap | 202.63 | kPa | 642.15 | Calculated Property |
| Pvap | [1.83e-05; 1490.10] | kPa | [335.66; 785.00] |
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 | 1.78292e+02 | |||
| Coefficient B | -2.09250e+04 | |||
| Coefficient C | -2.18130e+01 | |||
| Coefficient D | 4.56820e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 785.00 | |||
| Pvap | 1.83e-05 | kPa | 335.66 | Calculated Property |
| Pvap | 2.87e-03 | kPa | 385.59 | Calculated Property |
| Pvap | 0.10 | kPa | 435.51 | Calculated Property |
| Pvap | 1.39 | kPa | 485.44 | Calculated Property |
| Pvap | 9.63 | kPa | 535.37 | Calculated Property |
| Pvap | 41.67 | kPa | 585.29 | Calculated Property |
| Pvap | 130.39 | kPa | 635.22 | Calculated Property |
| Pvap | 328.00 | kPa | 685.15 | Calculated Property |
| Pvap | 721.41 | kPa | 735.07 | Calculated Property |
| Pvap | 1490.10 | kPa | 785.00 | Calculated Property |
| Pvap | [3.22e-04; 1407.25] | kPa | [335.66; 776.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | -4.22801e+00 | |||
| Coefficient B | -8.29052e+03 | |||
| Coefficient C | 3.66210e+00 | |||
| Coefficient D | -3.66517e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 776.00 | |||
| Pvap | 3.22e-04 | kPa | 335.66 | Calculated Property |
| Pvap | 0.01 | kPa | 384.59 | Calculated Property |
| Pvap | 0.16 | kPa | 433.51 | Calculated Property |
| Pvap | 1.44 | kPa | 482.44 | Calculated Property |
| Pvap | 8.30 | kPa | 531.37 | Calculated Property |
| Pvap | 34.98 | kPa | 580.29 | Calculated Property |
| Pvap | 115.04 | kPa | 629.22 | Calculated Property |
| Pvap | 309.73 | kPa | 678.15 | Calculated Property |
| Pvap | 707.34 | kPa | 727.07 | Calculated Property |
| Pvap | 1407.25 | kPa | 776.00 | Calculated Property |
| Pvap | [0.13; 100.81] | kPa | [426.80; 626.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.69408e+01 | |||
| Coefficient B | -7.04918e+03 | |||
| Coefficient C | -5.50770e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 426.80 | |||
| Temperature range, max. | 626.90 | |||
| Pvap | 0.13 | kPa | 426.80 | Calculated Property |
| Pvap | 0.39 | kPa | 449.03 | Calculated Property |
| Pvap | 1.00 | kPa | 471.27 | Calculated Property |
| Pvap | 2.37 | kPa | 493.50 | Calculated Property |
| Pvap | 5.15 | kPa | 515.73 | Calculated Property |
| Pvap | 10.41 | kPa | 537.97 | Calculated Property |
| Pvap | 19.79 | kPa | 560.20 | Calculated Property |
| Pvap | 35.65 | kPa | 582.43 | Calculated Property |
| Pvap | 61.22 | kPa | 604.67 | Calculated Property |
| Pvap | 100.81 | kPa | 626.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [853.60; 250.69] | kg/m3 | [335.66; 785.00] |
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 | 5.95776e+01 | |||
| Coefficient B | 2.37650e-01 | |||
| Coefficient C | 7.85000e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 785.00 | |||
| ρl | 853.60 | kg/m3 | 335.66 | Calculated Property |
| ρl | 819.68 | kg/m3 | 385.59 | Calculated Property |
| ρl | 784.13 | kg/m3 | 435.51 | Calculated Property |
| ρl | 746.53 | kg/m3 | 485.44 | Calculated Property |
| ρl | 706.31 | kg/m3 | 535.37 | Calculated Property |
| ρl | 662.54 | kg/m3 | 585.29 | Calculated Property |
| ρl | 613.63 | kg/m3 | 635.22 | Calculated Property |
| ρl | 556.39 | kg/m3 | 685.15 | Calculated Property |
| ρl | 482.14 | kg/m3 | 735.07 | Calculated Property |
| ρl | 250.69 | kg/m3 | 785.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [335.66; 785.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K | |||
| Coefficient A | 5.69270e-02 | |||
| Coefficient B | 1.21910e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.85000e+02 | |||
| Comment | ChemSep eq 106, SurfaceTension | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 785.00 | |||
| γ | 0.03 | N/m | 335.66 | Calculated Property |
| γ | 0.02 | N/m | 385.59 | Calculated Property |
| γ | 0.02 | N/m | 435.51 | Calculated Property |
| γ | 0.02 | N/m | 485.44 | Calculated Property |
| γ | 0.01 | N/m | 535.37 | Calculated Property |
| γ | 0.01 | N/m | 585.29 | Calculated Property |
| γ | 0.01 | N/m | 635.22 | Calculated Property |
| γ | 0.00 | N/m | 685.15 | Calculated Property |
| γ | 0.00 | N/m | 735.07 | Calculated Property |
| γ | 0.00 | N/m | 785.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.03; 0.11] | W/m×K | [624.15; 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 | 2.07730e-08 | |||
| Coefficient B | 2.32030e+00 | |||
| Coefficient C | 7.87000e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 624.15 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.03 | W/m×K | 624.15 | Calculated Property |
| λ | 0.03 | W/m×K | 665.91 | Calculated Property |
| λ | 0.04 | W/m×K | 707.67 | Calculated Property |
| λ | 0.05 | W/m×K | 749.43 | Calculated Property |
| λ | 0.06 | W/m×K | 791.19 | Calculated Property |
| λ | 0.06 | W/m×K | 832.96 | Calculated Property |
| λ | 0.07 | W/m×K | 874.72 | Calculated Property |
| λ | 0.08 | W/m×K | 916.48 | Calculated Property |
| λ | 0.09 | W/m×K | 958.24 | Calculated Property |
| λ | 0.11 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.16; 0.10] | W/m×K | [335.66; 624.15] |
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 | 2.23000e-01 | |||
| Coefficient B | -2.00000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidThermalConductivity | |||
| Temperature range, min. | 335.66 | |||
| Temperature range, max. | 624.15 | |||
| λ | 0.16 | W/m×K | 335.66 | Calculated Property |
| λ | 0.15 | W/m×K | 367.71 | Calculated Property |
| λ | 0.14 | W/m×K | 399.77 | Calculated Property |
| λ | 0.14 | W/m×K | 431.82 | Calculated Property |
| λ | 0.13 | W/m×K | 463.88 | Calculated Property |
| λ | 0.12 | W/m×K | 495.93 | Calculated Property |
| λ | 0.12 | W/m×K | 527.99 | Calculated Property |
| λ | 0.11 | W/m×K | 560.04 | Calculated Property |
| λ | 0.10 | W/m×K | 592.10 | Calculated Property |
| λ | 0.10 | W/m×K | 624.15 | Calculated Property |
Similar Compounds
Find more compounds similar to n-Hexadecanoic acid.
Mixtures
- TETRAMETHYLAMMONIUM CHLORIDE + n-Hexadecanoic acid
- n-Hexane + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE + 1-Hexanol
- n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE + 1-Pentanol
- 1-Butanol + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- 1-Propanol + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- 2-Propanol + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- Tetradecanoic acid + n-Hexadecanoic acid
- Octadecanoic acid + n-Hexadecanoic acid
- Ethanol + n-Hexadecanoic acid + Water
- n-Hexadecanoic acid + Octadecane
- Carbon dioxide + n-Hexadecanoic acid
- Carbon dioxide + Ethanol + n-Hexadecanoic acid
- 2-Propanol + Carbon dioxide + n-Hexadecanoic acid
- Tripalmitin + n-Hexadecanoic acid
- Formamide, N,N-dimethyl- + n-Hexadecanoic acid
- n-Decanoic acid + n-Hexadecanoic acid
- n-Hexane + n-Hexadecanoic acid
- n-Hexadecanoic acid + Heptane
- n-Hexadecanoic acid + Pentane, 2,2,4-trimethyl-
Find more mixtures with n-Hexadecanoic acid.
Sources
- KDB Vapor Pressure Data
- 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
- Solubility and density measurements of palmitic acid in supercritical carbon dioxide + alcohol mixtures
- LLE for the systems ethyl palmitate (palmiticacid)(1) + ethanol(2) + glycerol (water)(3)
- Measurement and PC-SAFT modeling of solid-liquid equilibrium of deep eutectic solvents of quaternary ammonium chlorides and carboxylic acids
- Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry
- Experimental determination of the (vapor + liquid) equilibrium data of binary mixtures of fatty acids by differential scanning calorimetry
- Solubilities of palmitic and stearic fatty acids in supercritical carbon dioxide
- Phase equilibrium measurements and modelling of ternary system (carbon dioxide + ethanol + palmitic acid)
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Vapour liquid equilibria of monocaprylin plus palmitic acid or methyl stearate at P = (1.20 and 2.50) kPa by using DSC technique
- Solid-liquid phase equilibria of (n-octadecane with myristic, and palmitic acid) binary mixtures used as phase change materials (PCMs)
- Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
- The solid liquid phase diagrams of binary mixtures of even saturated fatty acids differing by six carbon atoms
- Vapor pressure data for fatty acids obtained using an adaptation of the DSC technique
- Prediction of the properties of eutectic fatty acid phase change materials
- Form-stable phase change nanocomposites for thermal energy storage based on hypercrosslinked polymer nanospheres
- Nano-inclusion aided thermal conductivity enhancement in palmitic acid/di-methyl formamide phase change material for latent heat thermal energy storage
- Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
- Solubility of Vitamin E Acetate in Supercritical Carbon Dioxide: Measurement and Correlation
- Solubilities of Palmitic Acid + Capsaicin in Supercritical Carbon Dioxide
- Solubility of Squalene and Fatty Acids in Carbon Dioxide at Supercritical Conditions: Binary and Ternary Systems
- Solubilities of Binary Systems alpha-Tocopherol + Capsaicin and alpha-Tocopherol + Palmitic Acid in Supercritical Carbon Dioxide
- Solid-Liquid Equilibrium of Binary Systems Containing Fatty Acids and Fatty Alcohols Using Differential Scanning Calorimetry
- Solubility Measurement of Lauric, Palmitic, and Stearic Acids in Ethanol, n-Propanol, and 2-Propanol Using Differential Scanning Calorimetry
- Apparent Molar Volumes and Viscosities of Lauric, Palmitic, and Stearic Acids in 2-Butanol at (20, 30, 40, and 60) C
- Solid-Liquid Equilibrium of Binary Fatty Acid Mixtures
- Phase Equilibria of Long-Chain Carboxylic Acids in Supercritical Propane
- Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems
- Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols
- Solubilities of Fatty Acids and Triglycerides in 1-Bromopropane
- Vapor Pressures and Vaporization, Sublimation, and Fusion Enthalpies of Some Fatty Acids
- Study of the Effect of Pressure on Melting Behavior of Saturated Fatty Acids in Liquid or Supercritical Carbon Dioxide
- Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
- Solubilities of Hexadecanoic and Octadecanoic Acids in Supercritical CO2 With and Without Cosolvents
- Joback Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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