- 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
- Hexadecanoic acid (palmitic acid)
- Hexadecylic acid
- Hydrofol
- Hystrene 8016
- Hystrene 9016
- Industrene 4516
- Kortacid 1695
- N-PALMITIC ACID
- NSC 5030
- Palmitic acid
- Palmitic acid (hexadecanoic acid)
- Palmitinic acid
- Pentadecanecarboxylic acid
- Prifac 2960
- n-Hexadecoic 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,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 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- 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).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 | 1.0402 | Relay (1.0) Calculated Property | |
| 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 |
| ΔfG° | -181.90 | kJ/mol | Joback Calculated Property |
| 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° | 116.71 | 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 ± 85.00 | kPa | NIST |
| 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 | 1965.00 | NIST | |
| Inp | 1981.00 | NIST | |
| Inp | 1951.00 | NIST | |
| Inp | 1963.00 | NIST | |
| Inp | 1968.00 | NIST | |
| Inp | 1943.00 | NIST | |
| Inp | 1984.00 | NIST | |
| Inp | 1960.00 | NIST | |
| Inp | 2001.00 | NIST | |
| Inp | 1936.00 | NIST | |
| Inp | 1970.00 | NIST | |
| Inp | 1974.00 | NIST | |
| Inp | 1967.00 | NIST | |
| Inp | 1969.00 | NIST | |
| Inp | 1959.00 | NIST | |
| Inp | 1978.00 | NIST | |
| Inp | 1971.00 | NIST | |
| Inp | 1975.00 | NIST | |
| Inp | 1973.00 | NIST | |
| Inp | 1977.00 | NIST | |
| Inp | 1976.00 | NIST | |
| Inp | 1937.00 | NIST | |
| Inp | 1957.00 | NIST | |
| Inp | 1968.20 | NIST | |
| Inp | 1956.00 | NIST | |
| Inp | 1964.00 | NIST | |
| Inp | 1953.00 | NIST | |
| Inp | 1940.00 | NIST | |
| Inp | 1962.00 | NIST | |
| Inp | Outlier 324.00 | NIST | |
| Inp | 1961.00 | NIST | |
| Inp | 1946.00 | NIST | |
| Inp | 1958.00 | NIST | |
| Inp | 1972.00 | NIST | |
| Inp | 1966.00 | NIST | |
| Inp | 1952.00 | NIST | |
| Inp | 1939.00 | 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 | 2931.00 | NIST | |
| I | Outlier 2871.00 | NIST | |
| I | 2890.00 | NIST | |
| I | 2880.00 | NIST | |
| I | 2922.00 | NIST | |
| I | 2940.00 | NIST | |
| I | 2910.00 | NIST | |
| I | 2930.00 | 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 ± 6.00 | K | NIST |
| Tc | 785.22 ± 3.00 | K | NIST |
| Tfus | [334.85; 337.22] | K |
|
| Tfus | 334.92 | K | Aq. Solubility Prediction |
| 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 |
| 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 ± 0.02 | K | NIST |
| Ttriple | 335.05 ± 0.50 | K | NIST |
| Vc | 0.946 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [719.80; 805.28] | J/mol×K | [711.53; 880.17] |
|
| Cp,gas | 719.80 | J/mol×K | 711.53 | Joback Calculated Property |
| Cp,gas | 735.78 | J/mol×K | 739.64 | Joback Calculated Property |
| Cp,gas | 751.03 | J/mol×K | 767.74 | Joback Calculated Property |
| Cp,gas | 765.59 | J/mol×K | 795.85 | Joback Calculated Property |
| Cp,gas | 779.46 | J/mol×K | 823.96 | Joback Calculated Property |
| Cp,gas | 792.69 | J/mol×K | 852.07 | Joback Calculated Property |
| Cp,gas | 805.28 | J/mol×K | 880.17 | Joback Calculated Property |
| 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 |
| η | [0.0000353; 0.0035737] | Pa×s | [380.83; 711.53] |
|
| η | 0.0035737 | Pa×s | 380.83 | Joback Calculated Property |
| η | 0.0010179 | Pa×s | 435.95 | Joback Calculated Property |
| η | 0.0003844 | Pa×s | 491.06 | Joback Calculated Property |
| η | 0.0001767 | Pa×s | 546.18 | Joback Calculated Property |
| η | 0.0000936 | Pa×s | 601.30 | Joback Calculated Property |
| η | 0.0000552 | Pa×s | 656.41 | Joback Calculated Property |
| η | 0.0000353 | Pa×s | 711.53 | Joback Calculated Property |
| 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 |
| 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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [481.72; 642.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | [3.22e-04; 1407.25] | kPa | [335.66; 776.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | -4.22801e+00 | |||
| Coefficient B | -8.29052e+03 | |||
| Coefficient C | 3.66210e+00 | |||
| Coefficient D | -3.66517e-06 | |||
| 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 |
Similar Compounds
Find more compounds similar to n-Hexadecanoic acid.
Mixtures
- Tetramethylammonium chloride + n-Hexadecanoic acid
- Tripalmitin + n-Hexadecanoic acid
- n-Hexadecanoic acid + Octadecane
- n-Decanoic acid + n-Hexadecanoic acid
- Formamide, N,N-dimethyl- + n-Hexadecanoic acid
- Hexadecane + n-Hexadecanoic acid
- 1-Dodecanol + n-Hexadecanoic acid
- Isopropyl Alcohol + n-Hexadecanoic acid
- 1-Propanol + n-Hexadecanoic acid
- Ethanol + n-Hexadecanoic acid
- Dodecanoic acid + n-Hexadecanoic acid
- Oleic Acid + n-Hexadecanoic acid
- Triolein + n-Hexadecanoic acid
- 9,12-Octadecadienoic acid (Z,Z)- + n-Hexadecanoic acid
- Trilinolein + n-Hexadecanoic acid
- Tristearin + n-Hexadecanoic acid
- Carbon dioxide + n-Hexadecanoic acid
- n-Hexadecanoic acid + Acetone
- n-Hexadecanoic acid + Heptane
- n-Hexane + n-Hexadecanoic acid
Find more mixtures with n-Hexadecanoic acid.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- 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
- 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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