- 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
- 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).
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| 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-l... |
| ΔfusH° | 53.50 | kJ/mol | Solid-L... |
| ΔsubH° | 194.00 ± 11.00 | kJ/mol | NIST |
| ΔvapH° | 74.64 | kJ/mol | Joback Calculated Property |
| log10WS | -6.81 | Aq. Sol... | |
| 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. Sol... |
| Tfus | 336.84 | K | Measure... |
| Tfus | 337.17 | K | Solid-l... |
| Tfus | 337.22 | K | The sol... |
| Tfus | 334.85 | K | Predict... |
| Tfus | 335.75 | K | Nano-in... |
| Tfus | 335.90 | K | Solid L... |
| Tfus | 335.44 | K | Solid-L... |
| Tfus | 336.70 | K | Solid-L... |
| Tfus | 335.02 | K | Solid L... |
| Tfus | 336.00 | K | Study o... |
| Tfus | 335.80 | K | Solubil... |
| Ttriple | [335.05; 336.25] | K |
|
| Ttriple | 336.25 | K | Form-st... |
| Ttriple | 336.13 | K | Solubil... |
| Ttriple | 335.66 ± 0.02 | K | NIST |
| Ttriple | 335.05 ± 0.50 | K | NIST |
| Vc | 0.957 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [719.80; 805.28] | J/mol×K | [711.53; 880.17] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 720 740 760 780 800 750 800 850 | ||||
| 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] |
|
|
T(K) Solid phase heat capacity (J/mol×K) 450 500 550 600 650 700 300 320 340 360 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 400 500 600 700 | ||||
| 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] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 48 50 52 54 333 334 335 336 | ||||
| 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 P... |
| 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] |
|
|
T(K) Vapor pressure (kPa) 2 4 6 8 10 500 520 | ||||
| Pvap | 1.33 | kPa | 483.30 | Vapor p... |
| Pvap | 2.67 | kPa | 498.60 | Vapor p... |
| Pvap | 4.00 | kPa | 509.00 | Vapor p... |
| Pvap | 5.33 | kPa | 517.30 | Vapor p... |
| Pvap | 6.67 | kPa | 523.40 | Vapor p... |
| Pvap | 8.00 | kPa | 527.90 | Vapor p... |
| Pvap | 9.33 | kPa | 533.40 | Vapor p... |
| 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 ... |
| Tboil | 498.35 | K | 2.50 | Vapour ... |
| 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 Yaw...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 | ||||
| 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 Vap...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 400 500 600 700 | ||||
| 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
- 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.