Acetone
- Formula: C3H6O
- Molecular weight: 58.0791
- IUPAC Standard InChIKey: CSCPPACGZOOCGX-UHFFFAOYSA-N
- CAS Registry Number: 67-64-1
- Chemical structure:
This structure is also available as a 2d Mol file or as a computed 3d SD file
The 3d structure may be viewed using Java or Javascript. - Isotopologues:
- Other names: 2-Propanone; β-Ketopropane; Dimethyl ketone; Dimethylformaldehyde; Methyl ketone; Propanone; Pyroacetic ether; (CH3)2CO; Dimethylketal; Ketone propane; Ketone, dimethyl-; Chevron acetone; Rcra waste number U002; UN 1090; Sasetone; Propan-2-one; NSC 135802
- Permanent link for this species. Use this link for bookmarking this species for future reference.
- Information on this page:
- Other data available:
- Gas phase thermochemistry data
- Condensed phase thermochemistry data
- Phase change data
- Reaction thermochemistry data: reactions 1 to 50, reactions 51 to 85
- Henry's Law data
- Gas phase ion energetics data
- Ion clustering data
- IR Spectrum
- Mass spectrum (electron ionization)
- UV/Visible spectrum
- Vibrational and/or electronic energy levels
- Gas Chromatography
- Data at other public NIST sites:
- Options:
Data at NIST subscription sites:
- NIST / TRC Web Thermo Tables, "lite" edition (thermophysical and thermochemical data)
- NIST / TRC Web Thermo Tables, professional edition (thermophysical and thermochemical data)
NIST subscription sites provide data under the NIST Standard Reference Data Program, but require an annual fee to access. The purpose of the fee is to recover costs associated with the development of data collections included in such sites. Your institution may already be a subscriber. Follow the links above to find out more about the data in these sites and their terms of usage.
Normal boiling point
Go To: Top, References, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Data compiled as indicated in comments:
TRC - Thermodynamics Research Center, NIST Boulder Laboratories, Chris Muzny director
BS - Robert L. Brown and Stephen E. Stein
Tboil (K) | Reference | Comment |
---|---|---|
329.2 | Treszczanowicz, Kasprzycka-Guttman, et al., 1999 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.3 | Resa, Echebarria, et al., 1996 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.45 | Gultekin, 1990 | Uncertainty assigned by TRC = 0.15 K; TRC |
329.45 | Gultekin, 1989 | Uncertainty assigned by TRC = 0.3 K; TRC |
329. | American Tokyo Kasei, 1988 | BS |
329.21 | Takagi, Ishikawa, et al., 1986 | Uncertainty assigned by TRC = 0.04 K; TRC |
329.3 | Majer and Svoboda, 1985 | |
329.45 | Dizechi and Marschell, 1982 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.4 | Natarajan and Srinivasan, 1980 | Uncertainty assigned by TRC = 0.4 K; TRC |
329.25 | Chandak, Nageshwar, et al., 1979 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.47 | Gil'burd, Yurkevich, et al., 1979 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.23 | Ochi and Lu, 1978 | Uncertainty assigned by TRC = 0.05 K; TRC |
329.25 | Boublik and Aim, 1972 | Uncertainty assigned by TRC = 0.05 K; TRC |
329.26 | Willock and Van Winkle, 1970 | Uncertainty assigned by TRC = 0.3 K; TRC |
329. | Willock and Van Winkle, 1970 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.30 | Garrett and Van Winkle, 1969 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.3 | Hudson and Van Winkle, 1969 | Uncertainty assigned by TRC = 0.06 K; TRC |
329.25 | Bekarek and Hala, 1968 | Uncertainty assigned by TRC = 0.15 K; TRC |
329.38 | Freshwater and Pike, 1967 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.4 | Freshwater, 1967 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.15 | McConnell and Van Winkle, 1967 | Uncertainty assigned by TRC = 0.3 K; TRC |
329. | Serebryakov and Konoval'chukov, 1966 | Uncertainty assigned by TRC = 1. K; TRC |
329.3 | Subbarao and Rao, 1966 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.3 | Fort and Moore, 1965 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.4 | Grove and Walden, 1965 | Uncertainty assigned by TRC = 0.4 K; TRC |
329.25 | Sokolov, Zhilina, et al., 1963 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.25 | Jones, 1962 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.21 | Brown and Smith, 1960 | Uncertainty assigned by TRC = 0.1 K; TRC |
329.25 | Free and Hutchison, 1959 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.26 | Ling and Van Winkle, 1958 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.65 | Shenton and Smith, 1958 | Uncertainty assigned by TRC = 1. K; TRC |
330.95 | Murphy, Lastovica, et al., 1957 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.25 | Amer, Paxton, et al., 1956 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.26 | Canjar, Horni, et al., 1956 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.15 | Fitzpatrick and Gettler, 1956 | Uncertainty assigned by TRC = 1. K; TRC |
326.15 | Kornblum, Blackwood. R.K., et al., 1956 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.33 | Stutchbury, 1956 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.25 | Hatch, 1955 | Uncertainty assigned by TRC = 1. K; TRC |
329.75 | Kochi, 1955 | Uncertainty assigned by TRC = 1. K; TRC |
328.9 | Quinlan and Amis, 1955 | Uncertainty assigned by TRC = 0.4 K; TRC |
329.25 | Bayliss and McRae, 1954 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.35 | Doolittle, 1954 | Uncertainty assigned by TRC = 1. K; may not be an original measurement; TRC |
329.28 | Gjaldbaek and Andersen, 1954 | Uncertainty assigned by TRC = 0.15 K; TRC |
329.15 | Kishimoto and Nomoto, 1954 | Uncertainty assigned by TRC = 1. K; TRC |
329.25 | Amer, Paxton, et al., 1953 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.35 | Hellwig and Van Winkle, 1953 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.35 | McKenna, Tartar, et al., 1953 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.35 | Cook, 1952 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.35 | Griffiths, 1952 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.33 | Othmer, Chudgar, et al., 1952 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.28 | karr, Bowes, et al., 1951 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.5 | Elderfield and McCarthy, 1951 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.3 | Newitt and Weale, 1951 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.65 | Holub and Bigelow, 1950 | Uncertainty assigned by TRC = 0.5 K; TRC |
328.65 | Wender, Levine, et al., 1950 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.35 | Dreisbach and Martin, 1949 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.65 | Griswold and Buford, 1949 | Uncertainty assigned by TRC = 1. K; TRC |
329.3 | Lecat, 1949 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.15 | Schuerch and Huntress, 1949 | Uncertainty assigned by TRC = 1. K; TRC |
323.40 | Lecat, 1947 | Uncertainty assigned by TRC = 0.3 K; TRC; Data excluded from overall average |
329.27 | Kretschmer, Nowakowska, et al., 1946 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.3 | Lecat, 1946 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.4 | Milas and Perry, 1946 | Uncertainty assigned by TRC = 1. K; TRC |
329.25 | Treybal, Weber, et al., 1946 | Uncertainty assigned by TRC = 1. K; TRC |
330.15 | Beggerow and Harteck, 1944 | Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average |
329.75 | Brunjes and Bogart, 1943 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.25 | Othmer, 1943 | Uncertainty assigned by TRC = 1. K; TRC |
329.65 | Platt, Rusoff, et al., 1943 | Uncertainty assigned by TRC = 1. K; TRC |
329.2 | Ewell and Welch, 1941 | Uncertainty assigned by TRC = 1. K; probably not measured by authors; TRC |
329.15 | Whitmore, Wilson, et al., 1941 | Uncertainty assigned by TRC = 1. K; TRC |
329.26 | Clusius and Ringer, 1940 | Uncertainty assigned by TRC = 0.1 K; TRC |
331.15 | Schaad and Ipatieff, 1940 | Uncertainty assigned by TRC = 3. K; TRC; Data excluded from overall average |
328.85 | Bennewitz and Rossner, 1938 | Uncertainty assigned by TRC = 1. K; TRC |
329.15 | Magnani and McElvain, 1938 | Uncertainty assigned by TRC = 2. K; TRC |
328.57 | Albright, 1937 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.3 | McNeight and Smyth, 1936 | Uncertainty assigned by TRC = 1. K; TRC |
329.55 | Brunjes and Furnas, 1935 | Uncertainty assigned by TRC = 1. K; TRC |
329.65 | Earp and Glasstone, 1935 | Uncertainty assigned by TRC = 0.3 K; TRC |
328.75 | Kohlraush and Koppl, 1934 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
328.95 | Trew and Watkins, 1933 | Uncertainty assigned by TRC = 1. K; TRC |
329.4 | Young, 1933 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.39 | Ernst, Litkenhous, et al., 1932 | Uncertainty assigned by TRC = 0.5 K; TRC |
330. | Pfeiffer and Adkins, 1931 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.35 | Trew and Spencer, 1931 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.35 | Marti, 1930 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.45 | Jones, 1929 | Uncertainty assigned by TRC = 1. K; TRC |
329.35 | Prentiss, 1929 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.25 | Robinson, 1929 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.3 | Parks and Kelley, 1928 | Uncertainty assigned by TRC = 0.4 K; TRC |
329.35 | Timmermans and Martin, 1928 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.17 | Krchma and Williams, 1927 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.50 | Lecat, 1927 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.32 | Parks and Chaffee, 1927 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.65 | Suida and Poll, 1927 | Uncertainty assigned by TRC = 1. K; TRC |
329.15 | Mathews, 1926 | Uncertainty assigned by TRC = 1. K; TRC |
329.35 | Bonino, 1925 | Uncertainty assigned by TRC = 1. K; TRC |
329.22 | Williams and Daniels, 1925 | Uncertainty assigned by TRC = 0.2 K; TRC |
329.23 | Brunel, 1923 | Uncertainty assigned by TRC = 0.1 K; TRC |
329.3 | Grimm and Patrick, 1923 | Uncertainty assigned by TRC = 1. K; TRC |
329.2 | Herz and Neukirch, 1923 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.48 | Willard and Smith, 1923 | Uncertainty assigned by TRC = 1. K; TRC |
329.25 | Barr and Bircumshaw, 1921 | Uncertainty assigned by TRC = 1. K; TRC |
329.65 | Michael, 1919 | Uncertainty assigned by TRC = 1. K; TRC |
329.35 | Price, 1919 | Uncertainty assigned by TRC = 1. K; TRC |
329.45 | Reilly and Ralph, 1919 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.65 | Creighton and Way, 1918 | Uncertainty assigned by TRC = 1. K; TRC |
329.3 | Sameshima, 1918 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.15 | Jaeger, 1917 | Uncertainty assigned by TRC = 1. K; TRC |
329.65 | Worley, 1914 | Uncertainty assigned by TRC = 1. K; TRC |
329.7 | Bridgman, 1913 | Uncertainty assigned by TRC = 1.5 K; TRC |
329.3 | Shipsey and Werner, 1913 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.4 | N/A | Uncertainty assigned by TRC = 1. K; TRC |
329.25 | Timmermans, 1912 | Uncertainty assigned by TRC = 0.3 K; TRC |
329.3 | Timmermans, 1911 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.3 | Hubbard, 1910 | Uncertainty assigned by TRC = 1. K; TRC |
329.25 | Timmermans, 1910 | Uncertainty assigned by TRC = 0.3 K; TRC |
330.2 | Holmes and Sageman, 1909 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.34 | Rosanoff and Easley, 1909 | Uncertainty assigned by TRC = 0.5 K; TRC |
329.15 | Sabatier and Mailhe, 1909 | Uncertainty assigned by TRC = 1. K; TRC |
329.4 | Makovetzkii, 1908 | Uncertainty assigned by TRC = 1. K; TRC |
329.55 | Guttman, 1907 | Uncertainty assigned by TRC = 1. K; TRC |
330.15 | Nef, 1901 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.55 | McElroy and Krug, 1893 | Uncertainty assigned by TRC = 1. K; TRC |
328.9 | Perkin, 1884 | Uncertainty assigned by TRC = 1. K; TRC |
329.5 | Zander, 1882 | Uncertainty assigned by TRC = 1. K; TRC |
329.5 | Von Reis, 1881 | Uncertainty assigned by TRC = 0.5 K; TRC |
330.85 | Prytz, 1880 | Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average |
329.45 | Regnault, 1863 | Uncertainty assigned by TRC = 1. K; TRC |
329.45 | Kopp, 1854 | Uncertainty assigned by TRC = 1. K; TRC |
References
Go To: Top, Normal boiling point, Notes
Data compilation copyright by the U.S. Secretary of Commerce on behalf of the U.S.A. All rights reserved.
Treszczanowicz, Kasprzycka-Guttman, et al., 1999
Treszczanowicz, T.; Kasprzycka-Guttman, T.; Treszczanowicz, A.J.,
Distribution Coefficient of β-Carotene in Systems Composed of Hexan, Water, and 2-Propanone and Toluene, Water and 2-Propanone,
J. Chem. Eng. Data, 1999, 44, 970-3. [all data]
Resa, Echebarria, et al., 1996
Resa, J.M.; Echebarria, S.; Betolaza, M.A.; Ruiz, A.; Moradillo, B.,
Isobaric Vapor-Liquid Equilibria of 3-Pentanone with Acetone and Isopropyl Ether at 101.3 kPa,
J. Chem. Eng. Data, 1996, 41, 63-5. [all data]
Gultekin, 1990
Gultekin, N.,
Vapor-Liquid Equilibria at 1 atm. for Ternary and Quarternary Systems Composed of Acetone, Methanol, 2-Propanol, and 1-Propanol,
J. Chem. Eng. Data, 1990, 35, 132. [all data]
Gultekin, 1989
Gultekin, N.,
Vapor-Liquid Equilibria for Binary and Ternary Systems Comprosed of Acetone, 2-Propanol, and 1-Propanol,
J. Chem. Eng. Data, 1989, 34, 168. [all data]
American Tokyo Kasei, 1988
American Tokyo Kasei,
TCI American Organic Chemical 88/89 Catalog, American Tokyo Kasei, Portland, OR, 1988, 1610. [all data]
Takagi, Ishikawa, et al., 1986
Takagi, S.; Ishikawa, M.; Kumada, M.; Kimura, T.; Fujishiro, R.,
Vapor Pressure and Thermo. Prop. of Hexamethyldisilane at 305-387 K,
Thermochim. Acta, 1986, 109, 55. [all data]
Majer and Svoboda, 1985
Majer, V.; Svoboda, V.,
Enthalpies of Vaporization of Organic Compounds: A Critical Review and Data Compilation, Blackwell Scientific Publications, Oxford, 1985, 300. [all data]
Dizechi and Marschell, 1982
Dizechi, M.; Marschell, E.,
Viscosity of Some Binary and Ternary Liquid Mixtures,
J. Chem. Eng. Data, 1982, 27, 358. [all data]
Natarajan and Srinivasan, 1980
Natarajan, T.S.; Srinivasan, D.,
Vapor-liquid equilibrium data for the systems acetone + methanol and methanol + benzene in the presence of dissolved salts,
J. Chem. Eng. Data, 1980, 25, 215-8. [all data]
Chandak, Nageshwar, et al., 1979
Chandak, B.S.; Nageshwar, G.D.; Mene, P.S.,
Excess gibbs free energy, enthalpy, and volume and viscosity of acetone-methyl cellosolve mixtures,
J. Chem. Eng. Data, 1979, 24, 267. [all data]
Gil'burd, Yurkevich, et al., 1979
Gil'burd, M.M.; Yurkevich, B.P.; Politanskaya, T.I.,
Liquid-vapor phase equilibria in ethyl acetate + acetone and ethyl acetate + allyl alcohol systems.,
Zh. Prikl. Khim. (Leningrad), 1979, 52, 2372-74. [all data]
Ochi and Lu, 1978
Ochi, K.; Lu, B.C.Y.,
Determination and Correlation of Binary Vapor-Liquid Equilibrium Data,
Fluid Phase Equilib., 1978, 1, 185-200. [all data]
Boublik and Aim, 1972
Boublik, T.; Aim, K.,
Heats of Vaporization of Simple Non-spherical Molecule Compounds,
Collect. Czech. Chem. Commun., 1972, 37, 3513. [all data]
Willock and Van Winkle, 1970
Willock, J.M.; Van Winkle, M.,
Binary and Ternary Vapor-Liquid Equilibria of Methano-Acetone-2,3-Dimethyl- butane,
J. Chem. Eng. Data, 1970, 15, 281. [all data]
Garrett and Van Winkle, 1969
Garrett, G.R.; Van Winkle, M.,
Vapor-Liquid Equilibria of the Ternary System Acetone-Chloroform-2,3- Dimethylbutane,
J. Chem. Eng. Data, 1969, 14, 302. [all data]
Hudson and Van Winkle, 1969
Hudson, J.W.; Van Winkle, M.,
Multicomponent Vapor-Liquid Equilibria in Systems of Mixed Positive and Negative Deviations,
J. Chem. Eng. Data, 1969, 14, 310-8. [all data]
Bekarek and Hala, 1968
Bekarek, V.; Hala, E.,
Liquid-vapor equilibrium. XXXIX. Liquid-vapor equilibrium in systems of components with widley differing volatilities,
Collect. Czech. Chem. Commun., 1968, 33, 2598-607. [all data]
Freshwater and Pike, 1967
Freshwater, D.C.; Pike, K.A.,
Vapor-liquid equilibrium data for systems of acetone - methanol - isopropanol,
J. Chem. Eng. Data, 1967, 12, 179. [all data]
Freshwater, 1967
Freshwater, D.C.,
Vapor-Liquid Equilibrium Data for Systems Acetone-Methanol-Isopropanol,
J. Chem. Eng. Data, 1967, 12, 179. [all data]
McConnell and Van Winkle, 1967
McConnell, C.G.; Van Winkle, M.,
Vapor-Liquid Equilibria in the Acetone-2,3-Dimethylbutane and Chloroform-2,3-Dimethylbutane Systems,
J. Chem. Eng. Data, 1967, 12, 430-2. [all data]
Serebryakov and Konoval'chukov, 1966
Serebryakov, B.R.; Konoval'chukov, A.G.,
Zh. Fiz. Khim., 1966, 40, 1384. [all data]
Subbarao and Rao, 1966
Subbarao, B.V.; Rao, C.V.,
Isobaric Ternary Vapor-Liquid Equilibria System,
J. Chem. Eng. Data, 1966, 11, 158. [all data]
Fort and Moore, 1965
Fort, R.J.; Moore, W.R.,
Adiabatic compressibilities of binary liquid mixtures,
Trans. Faraday Soc., 1965, 61, 2102. [all data]
Grove and Walden, 1965
Grove, E.L.; Walden, G.E.,
Variation of Dielectric Constant with Temperature for SOme Five- and Six-Carbon Ketones,
J. Chem. Eng. Data, 1965, 10, 98. [all data]
Sokolov, Zhilina, et al., 1963
Sokolov, V.V.; Zhilina, L.P.; Mishchenko, K.P.,
Thermodynamics of Evaporation of Acetone at Different Temperatures,
Zh. Prikl. Khim. (Leningrad), 1963, 36, 750-4. [all data]
Jones, 1962
Jones, H.E.,
J. Chem. Eng. Data, 1962, 7, 13. [all data]
Brown and Smith, 1960
Brown, I.; Smith, F.,
Liquid-Vapour Equilibria X. The Systems Acetone + Nitromethane and Acetone + Acetonitrile at 45 deg C,
Aust. J. Chem., 1960, 13, 30. [all data]
Free and Hutchison, 1959
Free, K.W.; Hutchison, H.P.,
Isobaric Vapor-Liquid Equilibria for the Ternary System Acetone- Benzene-Chlorobenzene,
J. Chem. Eng. Data, 1959, 4, 193. [all data]
Ling and Van Winkle, 1958
Ling, T.D.; Van Winkle, M.,
Properties of Binary Mixtures as a Function of Composition point of binary mixtures,
Chem. Eng. Data Ser., 1958, 3, 88-95. [all data]
Shenton and Smith, 1958
Shenton, T.; Smith, J.C.,
Chem. Ind. (London), 1958, 1958, 1510. [all data]
Murphy, Lastovica, et al., 1957
Murphy, N.F.; Lastovica, J.E.; Fallis, J.G.,
Correlation of Interfacial Tension of Two-Phase Three-Component Systems,
Ind. Eng. Chem., 1957, 49, 1035. [all data]
Amer, Paxton, et al., 1956
Amer, H.H.; Paxton, R.R.; Van Winkle, M.,
Methanol - ethanol - acetone vapor-liquid equilibria,
Ind. Eng. Chem., 1956, 48, 142. [all data]
Canjar, Horni, et al., 1956
Canjar, L.N.; Horni, E.C.; Rothfus, R.R.,
Vapor-Liquid Equil. in the Acetone-Benzene-Ethylene Dichloride System,
Ind. Eng. Chem., 1956, 48, 427. [all data]
Fitzpatrick and Gettler, 1956
Fitzpatrick, F.W.; Gettler, J.D.,
J. Am. Chem. Soc., 1956, 78, 530. [all data]
Kornblum, Blackwood. R.K., et al., 1956
Kornblum, N.; Blackwood. R.K.; Mooberry, D.D.,
J. Am. Chem. Soc., 1956, 78, 1501. [all data]
Stutchbury, 1956
Stutchbury, J.E.,
Compressions of Organic Liquids and Their Mixtures with Water,
Aust. J. Chem., 1956, 9, 536-540. [all data]
Hatch, 1955
Hatch, L.F.,
Hydrocarbon Process., 1955, 34, 4, 160. [all data]
Kochi, 1955
Kochi, J.K.,
J. Am. Chem. Soc., 1955, 77, 5274. [all data]
Quinlan and Amis, 1955
Quinlan, J.E.; Amis, E.S.,
J. Am. Chem. Soc., 1955, 77, 4187. [all data]
Bayliss and McRae, 1954
Bayliss, N.S.; McRae, E.G.,
J. Phys. Chem., 1954, 58, 1006. [all data]
Doolittle, 1954
Doolittle, A.K.,
The Technology of Solvents and Plasticizers, Wiley-Inter- science, New York, 1954. [all data]
Gjaldbaek and Andersen, 1954
Gjaldbaek, J. Chr.; Andersen, E.K.,
The Solubility of Carbon Dioxide, Oxygen, Carbon Monoxide and Nitrogen in Polar Solvents,
Acta Chem. Scand., 1954, 8, 1398. [all data]
Kishimoto and Nomoto, 1954
Kishimoto, T.; Nomoto, O.,
J. Phys. Soc. Jpn., 1954, 9, 66. [all data]
Amer, Paxton, et al., 1953
Amer, H.H.; Paxton, R.R.; Van Winkle, M.,
Ternary methanol + ethanol + acetone and three related binary solutions refractive indices and bubble points,
Anal. Chem., 1953, 25, 1204. [all data]
Hellwig and Van Winkle, 1953
Hellwig, L.R.; Van Winkle, M.,
Vapour-liquid equilibria for ethyl alcohol binary systems.,
Ind. Eng. Chem., 1953, 45, 624. [all data]
McKenna, Tartar, et al., 1953
McKenna, F.E.; Tartar, H.V.; Lingafelter, E.C.,
Studies of hemiacetal formation in alcohol - aldehyde systems: II refraction studies,
J. Am. Chem. Soc., 1953, 75, 604-7. [all data]
Cook, 1952
Cook, N.C.,
, Unpublished, Final Rep. Stand. Proj. on Oxygenated Compounds, Penn. State Univ., College Park, PA, 1952. [all data]
Griffiths, 1952
Griffiths, V.S.,
Densities of SOme Binary Liquid Mixtures, Part I.,
J. Chem. Soc., 1952, 1952, 1326. [all data]
Othmer, Chudgar, et al., 1952
Othmer, D.F.; Chudgar, M.M.; Levy, S.L.,
Composition of vapors from boiling binary solutions: binary and ternary systems of acetone, methyl ethyl ketone, and water,
Ind. Eng. Chem., 1952, 44, 1872-81. [all data]
karr, Bowes, et al., 1951
karr, A.E.; Bowes, W.M.; Scheibel, E.G.,
Analysis of binary and ternary mixtures system acetone + chloroform + methyl isobutyl ketone,
Anal. Chem., 1951, 23, 459-63. [all data]
Elderfield and McCarthy, 1951
Elderfield, R.C.; McCarthy, J.R.,
The reaction of o-phenylenediamines with carbonyl compounds: II aliphatic ketones,
J. Am. Chem. Soc., 1951, 73, 975. [all data]
Newitt and Weale, 1951
Newitt, D.M.; Weale, K.E.,
Pressure-volume-temperature relations in liquids and liquid mixtures: II the compression isotherms of some organic liquids up to 1000 atmospheres, and the compressions of some aqueous and nonaqueous,
J. Chem. Soc., 1951, 1951, 3092-8. [all data]
Holub and Bigelow, 1950
Holub, R.; Bigelow, L.A.,
J. Am. Chem. Soc., 1950, 72, 4879. [all data]
Wender, Levine, et al., 1950
Wender, I.; Levine, R.; Orchin, M.,
Chemistry of the oxo and related reactions: II hydrogenation,
J. Am. Chem. Soc., 1950, 72, 4375. [all data]
Dreisbach and Martin, 1949
Dreisbach, R.R.; Martin, R.A.,
Physical Data on Some Organic Compounds,
Ind. Eng. Chem., 1949, 41, 2875-8. [all data]
Griswold and Buford, 1949
Griswold, J.; Buford, C.B.,
Separation of synthesis mixtures vapor-liquid equilibria of acetone - methanol - water,
Ind. Eng. Chem., 1949, 41, 2347. [all data]
Lecat, 1949
Lecat, M.,
Tables Azeotropiques, Vol. 1, 10th ed., Brussels, Belgium, 1949. [all data]
Schuerch and Huntress, 1949
Schuerch, C.; Huntress, E.H.,
The Schmidt Reaction II. A New Rearangement Obseved during Degradation of Triethylacetic Acid,
J. Am. Chem. Soc., 1949, 71, 2238. [all data]
Lecat, 1947
Lecat, M.,
Orthobaric Azeotropes of Sulfides,
Bull. Cl. Sci., Acad. R. Belg., 1947, 33, 160-82. [all data]
Kretschmer, Nowakowska, et al., 1946
Kretschmer, C.B.; Nowakowska, J.; Wiebe, R.,
Solubility of Oxygen and Nitrogen In Organic Solvents,
Ind. Eng. Chem., 1946, 38, 506. [all data]
Lecat, 1946
Lecat, M.,
Binary orthobaric azeotropes containing an alkyl halide,
C. R. Hebd. Seances Acad. Sci., 1946, 223, 478. [all data]
Milas and Perry, 1946
Milas, N.A.; Perry, L.H.,
J. Am. Chem. Soc., 1946, 68, 1938. [all data]
Treybal, Weber, et al., 1946
Treybal, R.E.; Weber, L.D.; Daley, J.F.,
The system acetone-water-1,1,2-trichloroethane - ternary liquid and binary vapour equilibria.,
Ind. Eng. Chem., 1946, 38, 817. [all data]
Beggerow and Harteck, 1944
Beggerow, G.; Harteck, P.,
On the Measurement of Adsorption Coefficient and Heat of Adsorption of Hydrocarbons,
Z. Phys. Chem. (Leipzig), 1944, 193, 265. [all data]
Brunjes and Bogart, 1943
Brunjes, A.S.; Bogart, M.J.P.,
Vapor-liquid equilibria for commercially important systems of organic solvents: the binary systems ethanol - n-butanol; acetone - water, and isopropanol - water,
Ind. Eng. Chem., 1943, 35, 255. [all data]
Othmer, 1943
Othmer, D.F.,
Composition of vapors from boiling binary solutions,
Ind. Eng. Chem., 1943, 35, 614-20. [all data]
Platt, Rusoff, et al., 1943
Platt, J.R.; Rusoff, I.I.; Klevens, H.B.,
J. Chem. Phys., 1943, 11, 535. [all data]
Ewell and Welch, 1941
Ewell, R.H.; Welch, L.M.,
Maximum Boiling Mixtures of chloroparaffins with Donor Liquids,
J. Am. Chem. Soc., 1941, 63, 2475. [all data]
Whitmore, Wilson, et al., 1941
Whitmore, F.C.; Wilson, C.D.; Capinjola, J.V.; Tongberg, C.O.; Fleming, G.H.; McGrew, R.V.; Cosby, J.N.,
J. Am. Chem. Soc., 1941, 63, 2035. [all data]
Clusius and Ringer, 1940
Clusius, K.; Ringer, W.,
Partial miscibility in the system acetone + carbon disulphide,
Z. Phys. Chem., Abt. A, 1940, 187, 186. [all data]
Schaad and Ipatieff, 1940
Schaad, R.E.; Ipatieff, V.N.,
Catalytic Hydration of Acetylene and Some Alkylacetylenes,
J. Am. Chem. Soc., 1940, 62, 178. [all data]
Bennewitz and Rossner, 1938
Bennewitz, K.; Rossner, W.,
The molar heat of organic vapors,
Z. Phys. Chem., Abt. B, 1938, 39, 126. [all data]
Magnani and McElvain, 1938
Magnani, A.; McElvain, S.M.,
The reaction of various alkyl benzoates with sodium alkoxides.,
J. Am. Chem. Soc., 1938, 60, 813. [all data]
Albright, 1937
Albright, P.S.,
Exper. Tests of Recent Theories Descriptive of the Salting-out Effect,
J. Am. Chem. Soc., 1937, 59, 2098. [all data]
McNeight and Smyth, 1936
McNeight, S.A.; Smyth, C.P.,
Non-Rotation of Molecules in a Number of Solids,
J. Am. Chem. Soc., 1936, 58, 1718. [all data]
Brunjes and Furnas, 1935
Brunjes, A.S.; Furnas, C.C.,
Vapor-Liquid Equilibrium Data for Commercially Important Sysems of Organic Solvents acetone,
Ind. Eng. Chem., 1935, 27, 396. [all data]
Earp and Glasstone, 1935
Earp, D.P.; Glasstone, S.,
Dielectric polarisation and molecular-compound formation in solution,
J. Chem. Soc., 1935, 1935, 1709. [all data]
Kohlraush and Koppl, 1934
Kohlraush, K.W.F.; Koppl, F.,
Z. Phys. Chem., Abt. B, 1934, 24, 370. [all data]
Trew and Watkins, 1933
Trew, V.C.G.; Watkins, G.M.C.,
Some Physical Properties of Mixtures of Certain Organic Liquids,
Trans. Faraday Soc., 1933, 29, 1310. [all data]
Young, 1933
Young, W.G.,
The Specific Gravity of Acetone-Water Mixtures,
J. Soc. Chem. Ind., London, Trans. Commun., 1933, 52, 449. [all data]
Ernst, Litkenhous, et al., 1932
Ernst, R.C.; Litkenhous, E.E.; Spanyer, J.W.,
The Physical Properties of the Ternary System Acetone-n-Butyl Alcohol-Water water,
J. Phys. Chem., 1932, 36, 842. [all data]
Pfeiffer and Adkins, 1931
Pfeiffer, G.J.; Adkins, H.,
The Relation of the Structure of Ketones to Their Reactivity and Affinity in Acetal Formation II.,
J. Am. Chem. Soc., 1931, 53, 1043. [all data]
Trew and Spencer, 1931
Trew, V.C.G.; Spencer, J.F.,
The Magnetic Susceptibility of Binary Systems of Organic Liquids,
Proc. R. Soc. London, A, 1931, 131, 209. [all data]
Marti, 1930
Marti, F.B.,
Methods and equipment used at the bureau of physico-chemical standards: 3 Physico-chemical properties of some solid organic compounds at normal temperatures,
Bull. Soc. Chim. Belg., 1930, 39, 590. [all data]
Jones, 1929
Jones, D.C.,
The systems n-butyl alcohol - water and n-butyl alcohol - acetone - water,
J. Chem. Soc., 1929, 1929, 799-813. [all data]
Prentiss, 1929
Prentiss, S.W.,
The reactivity of atoms and groups in organic compounds. IX. the vapor pressures, densities and refractive indices of certain binary mixtures,
J. Am. Chem. Soc., 1929, 51, 2825. [all data]
Robinson, 1929
Robinson, A.L.,
J. Phys. Chem., 1929, 33, 1193. [all data]
Parks and Kelley, 1928
Parks, G.S.; Kelley, K.K.,
The application of the third law of thermodynamics to some organic reactions,
J. Phys. Chem., 1928, 32, 734-50. [all data]
Timmermans and Martin, 1928
Timmermans, J.; Martin, F.,
Study of the Physical Constants of Twenty Organic Compounds of the Physical Constants of Twenty Organic Compounds,
J. Chim. Phys. Phys.-Chim. Biol., 1928, 25, 411. [all data]
Krchma and Williams, 1927
Krchma, I.J.; Williams, J.W.,
J. Am. Chem. Soc., 1927, 49, 2408. [all data]
Lecat, 1927
Lecat, M.,
New binary azeotropes: 6th list,
Ann. Soc. Sci. Bruxelles, Ser. B, 1927, 47, 63-71. [all data]
Parks and Chaffee, 1927
Parks, G.S.; Chaffee, C.S.,
Some Physical-Chemical Properties of Mixtures of Acetone and Isopropyl Alcohol,
J. Phys. Chem., 1927, 31, 439-47. [all data]
Suida and Poll, 1927
Suida, H.; Poll,
Angew. Chem., 1927, 40, 505. [all data]
Mathews, 1926
Mathews, J.H.,
The Accurate Measurement of Heats of Vaporization of Liquids,
J. Am. Chem. Soc., 1926, 48, 562. [all data]
Bonino, 1925
Bonino, G.B.,
Gazz. Chim. Ital., 1925, 55, 335. [all data]
Williams and Daniels, 1925
Williams, J.W.; Daniels, F.,
The specific heats of binary mixtures,
J. Am. Chem. Soc., 1925, 47, 1490-1503. [all data]
Brunel, 1923
Brunel, R.F.,
The Purification and Some Physical Properties of Certain Aliphatic Alcohols,
J. Am. Chem. Soc., 1923, 45, 1334. [all data]
Grimm and Patrick, 1923
Grimm, F.V.; Patrick, W.A.,
The Dielectric Constastants of Organic Liquids at the Boilin Point,
J. Am. Chem. Soc., 1923, 45, 2794. [all data]
Herz and Neukirch, 1923
Herz, W.; Neukirch, E.,
On Knowldge of the Critical State,
Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1923, 104, 433-50. [all data]
Willard and Smith, 1923
Willard, H.H.; Smith, G.F.,
The Perchalorates of the Alkali and A;kaline Earth Metals and Ammonium. Their Solubility in Water and Other Solvents,
J. Am. Chem. Soc., 1923, 45, 286. [all data]
Barr and Bircumshaw, 1921
Barr, G.; Bircumshaw, L.L.,
, Aeron. Res. Comm. Rep. Mem. No. 746 1921, 1921. [all data]
Michael, 1919
Michael, A.,
J. Am. Chem. Soc., 1919, 41, 393. [all data]
Price, 1919
Price, T.W.,
J. Chem. Soc., 1919, 115, 1116. [all data]
Reilly and Ralph, 1919
Reilly, J.; Ralph, E.W.,
Sci. Proc. R. Dublin Soc., 1919, 15, 597. [all data]
Creighton and Way, 1918
Creighton, H.J.M.; Way, D.H.,
J. Franklin Inst., 1918, 186, 675. [all data]
Sameshima, 1918
Sameshima, J.,
On the system acetone - ethyl ether,
J. Am. Chem. Soc., 1918, 40, 1482-1503. [all data]
Jaeger, 1917
Jaeger, F.M.,
Z. Anorg. Allg. Chem., 1917, 101, 130. [all data]
Worley, 1914
Worley, R.P.,
XXX. The Surface Tension of Mixtures. Part II. Mixtures of Perfectly Miscible Liquids and the Relation between Their Surface Tensions and Vapor Pressures,
J. Chem. Soc., 1914, 105, 273. [all data]
Bridgman, 1913
Bridgman, P.W.,
Thermodynamic properties of twelve liquids between 20!31 and 80!31 and up to 12,000 kgcu cm pressure,
Proc. Am. Acad. Arts Sci., 1913, 49, 1. [all data]
Shipsey and Werner, 1913
Shipsey, K.; Werner,
J. Chem. Soc., 1913, 103, 1255. [all data]
Timmermans, 1912
Timmermans, J.,
Experimental Research on the Density of Liquids Below 0 Degrees.,
Sci. Proc. R. Dublin Soc., 1912, 13, 310. [all data]
Timmermans, 1911
Timmermans, J.,
Researches on the freezing point of organic liquid compounds,
Bull. Soc. Chim. Belg., 1911, 25, 300. [all data]
Hubbard, 1910
Hubbard, J.C.,
Physical properties of binary liquid mixtures,
Z. Phys. Chem., Stoechiom. Verwandtschaftsl., 1910, 74, 207-32. [all data]
Timmermans, 1910
Timmermans, J.,
The Purification and Physical Constants of Several Organic Liquids,
Bull. Soc. Chim. Belg., 1910, 24, 244. [all data]
Holmes and Sageman, 1909
Holmes, J.; Sageman, P.J.,
CCXIII. Contributions to the Theory of Solutions.,
J. Chem. Soc., 1909, 95, 1919. [all data]
Rosanoff and Easley, 1909
Rosanoff, M.A.; Easley, C.W.,
Z. Phys. Chem. (Leipzig), 1909, 68, 641. [all data]
Sabatier and Mailhe, 1909
Sabatier, P.; Mailhe, A.,
New Applications of the General Method of Hydrogenation with Various Metals,
Ann. Chim. Phys., 1909, 16, 70. [all data]
Makovetzkii, 1908
Makovetzkii, A.E.,
Vapor pressure of aqueous acetone solutions,
Zh. Russ. Fiz.-Khim. O-va., Chast Khim., 1908, 40, 216. [all data]
Guttman, 1907
Guttman, L.F.,
The determination of melting points at low temperatures: II.,
J. Am. Chem. Soc., 1907, 29, 345-9. [all data]
Nef, 1901
Nef, J.V.,
Justus Liebigs Ann. Chem., 1901, 318, 137. [all data]
McElroy and Krug, 1893
McElroy, R.; Krug, S.,
J. Soc. Chem. Ind., London, 1893, 12, 177. [all data]
Perkin, 1884
Perkin, W.H.,
On the Magnetic Rotary Polarisation of Compounds in Relation to their Chemical Consitution; with Observations on the Preparation and Relative Densities of the Bodies Examined,
J. Chem. Soc., 1884, 45, 421-580. [all data]
Zander, 1882
Zander, A.,
The Specific Volume of Some Allyl-, Propyl-, and OTher COmpounds,
Justus Liebigs Ann. Chem., 1882, 214, 138-93. [all data]
Von Reis, 1881
Von Reis, M.A.,
IV. The Specific Heat of Liquid Organic Compounds and its Relation to Molecular Weight.,
Ann. Phys. (Leipzig), 1881, 13, 447. [all data]
Prytz, 1880
Prytz, K.,
Experimental investigations of the refractive index,
Ann. Phys. (Leipzig), 1880, 11, 104-20. [all data]
Regnault, 1863
Regnault, G.S.,
Jahresber. Fort. Chem., 1863, 16, 69. [all data]
Kopp, 1854
Kopp, H.,
Specific volumes of liquid compounds,
Justus Liebigs Ann. Chem., 1854, 92, 1-32. [all data]
Notes
Go To: Top, Normal boiling point, References
- Symbols used in this document:
Tboil Boiling point - Data from NIST Standard Reference Database 69: NIST Chemistry WebBook
- The National Institute of Standards and Technology (NIST) uses its best efforts to deliver a high quality copy of the Database and to verify that the data contained therein have been selected on the basis of sound scientific judgment. However, NIST makes no warranties to that effect, and NIST shall not be liable for any damage that may result from errors or omissions in the Database.
- Customer support for NIST Standard Reference Data products.