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Ethanol

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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
352.2Fandary, Aljima, et al., 1999Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
351.44Arce, Martinez-Ageitos, et al., 1998Uncertainty assigned by TRC = 0.1 K; TRC
351.45Comelli and Francesconi, 1997Uncertainty assigned by TRC = 0.2 K; TRC
351.56Arce, Blanco, et al., 1995Uncertainty assigned by TRC = 0.2 K; TRC
351.44Hiaki, Takahashi, et al., 1995Uncertainty assigned by TRC = 0.2 K; TRC
351.44Hiaki, Takahashi, et al., 1994Uncertainty assigned by TRC = 0.2 K; TRC
351.42Hiaki, Yamato, et al., 1992Uncertainty assigned by TRC = 0.08 K; TRC
351.45Cabezas, Beltran, et al., 1991Uncertainty assigned by TRC = 0.4 K; TRC
351.48Kato, Tanaka, et al., 1991Uncertainty assigned by TRC = 0.05 K; TRC
351.46Ortega, Susial, et al., 1990Uncertainty assigned by TRC = 0.2 K; TRC
351.45Kaczmarek and Radecki, 1989Uncertainty assigned by TRC = 0.5 K; TRC
351.49Kato and Tanaka, 1989Uncertainty assigned by TRC = 0.2 K; TRC
351.45Kato and Tanaka, 1989, 2Uncertainty assigned by TRC = 0.2 K; TRC
351.46Susial, Ortega, et al., 1989Uncertainty assigned by TRC = 0.2 K; TRC
351.7Weast and Grasselli, 1989BS
351.6Ortega, Pena, et al., 1986Uncertainty assigned by TRC = 0.2 K; TRC
351.45Dribika, Rashed, et al., 1985Uncertainty assigned by TRC = 0.06 K; TRC
351.45Kovac, Svoboda, et al., 1985Uncertainty assigned by TRC = 0.2 K; TRC
351.5Majer and Svoboda, 1985 
351.5Mato and Benito, 1985Uncertainty assigned by TRC = 0.4 K; TRC
351.45Mato, Benito, et al., 1985Uncertainty assigned by TRC = 0.4 K; TRC
351.45Dizechi and Marschell, 1982Uncertainty assigned by TRC = 0.3 K; TRC
351.2Yoshikawa, Takagi, et al., 1980Uncertainty assigned by TRC = 0.3 K; TRC
351.45Thorat, Nageshwar, et al., 1979Uncertainty assigned by TRC = 0.3 K; TRC
310.45Marinichev and Vasil'eva, 1976Uncertainty assigned by TRC = 0.3 K; TRC; Data excluded from overall average
351.5Nagata and Ohta, 1971Uncertainty assigned by TRC = 0.5 K; TRC
351.5Sagnes and Sanchez, 1971Uncertainty assigned by TRC = 0.4 K; TRC
351.53Kato, Konishi, et al., 1970Uncertainty assigned by TRC = 0.15 K; TRC
351.4Suska, Holub, et al., 1970Uncertainty assigned by TRC = 0.1 K; TRC
351.45Anonymous, 1968TRC
351.8Grove and Walden, 1965Uncertainty assigned by TRC = 0.4 K; TRC
351.470Agarwal and Mene, 1963Uncertainty assigned by TRC = 0.4 K; TRC
351.49Deshpande and Lu, 1963Uncertainty assigned by TRC = 0.2 K; same as 1963 ho lu 0; TRC
351.49Ho and Lu, 1963Uncertainty assigned by TRC = 0.2 K; same as 1963 deslu 1; TRC
351.45Kudryavtseva and Susarev, 1963Uncertainty assigned by TRC = 0.3 K; TRC
351.45Kudryavtseva and Susarev, 1963, 2Uncertainty assigned by TRC = 0.3 K; TRC
351.45Waldo and Weber, 1963Uncertainty assigned by TRC = 0.3 K; TRC
351.44Brown and Smith, 1962Uncertainty assigned by TRC = 0.1 K; TRC
351.45Kaes and Weber, 1962Uncertainty assigned by TRC = 0.3 K; TRC
351.45Belknap and Weber, 1961Uncertainty assigned by TRC = 0.5 K; TRC
351.47Copp and Findlay, 1960Uncertainty assigned by TRC = 0.1 K; TRC
351.45Anonymous, 1958TRC
351.45Costello and Bowden, 1958Uncertainty assigned by TRC = 0.3 K; TRC
351.5Ling and Van Winkle, 1958Uncertainty assigned by TRC = 0.1 K; TRC
351.45Murti and Van Winkle, 1958Uncertainty assigned by TRC = 0.3 K; TRC
351.15Ogata and Takagi, 1958Uncertainty assigned by TRC = 1. K; TRC
351.45Wagner and Weber, 1958Uncertainty assigned by TRC = 0.5 K; TRC
351.45Amer, Paxton, et al., 1956Uncertainty assigned by TRC = 0.3 K; TRC
351.65Katz and Newman, 1956Uncertainty assigned by TRC = 0.3 K; TRC
351.15Omura, Higasi, et al., 1956Uncertainty assigned by TRC = 11. K; TRC
351.5Stutchbury, 1956Uncertainty assigned by TRC = 0.1 K; TRC
351.15Hammond and Stokes, 1955Uncertainty assigned by TRC = 0.4 K; TRC
351.75Hansen and Hansen, 1955Uncertainty assigned by TRC = 0.1 K; TRC
351.45Hassion and Cole, 1955Uncertainty assigned by TRC = 0.3 K; TRC
351.35Bayliss and McRae, 1954Uncertainty assigned by TRC = 0.3 K; TRC
351.44Brown and Smith, 1954Uncertainty assigned by TRC = 0.2 K; TRC
351.55Purnell and Bowden, 1954Uncertainty assigned by TRC = 0.3 K; TRC
352.15Sasa, 1954Uncertainty assigned by TRC = 2. K; TRC; Data excluded from overall average
351.45Amer, Paxton, et al., 1953Uncertainty assigned by TRC = 0.3 K; TRC
351.44Barker, Brown, et al., 1953Uncertainty assigned by TRC = 0.05 K; TRC
351.45Chang and Moulton, 1953Uncertainty assigned by TRC = 0.5 K; TRC
351.55Hellwig and Van Winkle, 1953Uncertainty assigned by TRC = 0.2 K; Cottrel. b.p. app. Fe & const. thermo.-cross.-checked NBS therm.; TRC
351.65McKenna, Tartar, et al., 1953Uncertainty assigned by TRC = 0.3 K; TRC
351.45Otsuki and Williams, 1953Uncertainty assigned by TRC = 0.2 K; TRC
351.65Wetzel, Miller, et al., 1953Uncertainty assigned by TRC = 0.5 K; TRC
351.65Ballard and Van Winkle, 1952Uncertainty assigned by TRC = 0.27 K; Cottrell apparatus; TRC
351.15Cook, 1952Uncertainty assigned by TRC = 0.5 K; TRC
351.45Griffiths, 1952Uncertainty assigned by TRC = 0.15 K; TRC
351.43Hughes and Maloney, 1952Uncertainty assigned by TRC = 0.1 K; TRC
351.4Kipling and Tester, 1952Uncertainty assigned by TRC = 0.4 K; TRC
351.51Staveley and Spice, 1952Uncertainty assigned by TRC = 0.1 K; TRC
350.9West, Senise, et al., 1952Uncertainty assigned by TRC = 0.25 K; TRC; Data excluded from overall average
351.45Heyding and Winkler, 1951Uncertainty assigned by TRC = 0.3 K; TRC
351.45Moeller, Englund, et al., 1951Uncertainty assigned by TRC = 0.3 K; TRC
351.42Dreisbach and Martin, 1949Uncertainty assigned by TRC = 0.02 K; TRC
351.5Hatem, 1949Uncertainty assigned by TRC = 0.2 K; TRC
351.45Lecat, 1949Uncertainty assigned by TRC = 0.3 K; TRC
351.35Tschamler, Richter, et al., 1949Uncertainty assigned by TRC = 0.5 K; TRC
351.5Vvedenskii, Ivannikov, et al., 1949Uncertainty assigned by TRC = 1. K; TRC
351.15Vogel, 1948Uncertainty assigned by TRC = 0.5 K; TRC
351.5Lecat, 1947Uncertainty assigned by TRC = 0.4 K; TRC
351.45Lecat, 1947, 2Uncertainty assigned by TRC = 0.4 K; TRC
351.4Shostakovskii and Prilezhaeva, 1947Uncertainty assigned by TRC = 0.5 K; TRC
351.45Lecat, 1946Uncertainty assigned by TRC = 0.3 K; TRC
351.55Pollock, Collett, et al., 1946Uncertainty assigned by TRC = 0.3 K; Anchuetz thermometer calibr. N.B.S; TRC
351.65Addison, 1945Uncertainty assigned by TRC = 0.5 K; TRC
351.15Beggerow and Harteck, 1944Uncertainty assigned by TRC = 0.5 K; TRC
351.49Maryott, 1941Uncertainty assigned by TRC = 0.1 K; TRC
351.25Bennewitz and Rossner, 1938Uncertainty assigned by TRC = 0.3 K; TRC
351.65Ingle and Cady, 1938Uncertainty assigned by TRC = 0.3 K; TRC
351.5Zepalova-Mikhailova, 1937Uncertainty assigned by TRC = 0.1 K; TRC
351.45Getman, 1936Uncertainty assigned by TRC = 0.5 K; TRC
351.97Pearce and McDowell, 1936Uncertainty assigned by TRC = 0.1 K; Thermocouple - stand. against Pt. resist. therm. - IPTS stand; TRC; Data excluded from overall average
351.47Wojciechowski, 1936Uncertainty assigned by TRC = 0.01 K; Sample: (td-tb) = 0.001 deg at 760 mm; Swietoslowski method; TRC
351.45De Brouckere and Gillet, 1935Uncertainty assigned by TRC = 0.3 K; TRC
351.4Keffler and MacLean, 1935Uncertainty assigned by TRC = 0.1 K; Thermometer grad. 0.1 deg - stand. - corr.for stem.; TRC
351.52Harris, 1933Uncertainty assigned by TRC = 0.05 K; TRC
351.47Swietoslawski and Usakiewicz, 1933Uncertainty assigned by TRC = 0.01 K; TRC
351.47Swietoslawski, Zmaczynski, et al., 1932Uncertainty assigned by TRC = 0.02 K; TRC
351.46Swietoslawski, Zmaczynski, et al., 1932Uncertainty assigned by TRC = 0.02 K; TRC
351.46Swietoslawski, Zmaczynski, et al., 1932Uncertainty assigned by TRC = 0.02 K; TRC
351.7Fiock, Ginnings, et al., 1931Uncertainty assigned by TRC = 0.4 K; TRC
351.45Longuinov and Pryanishinkov, 1931Uncertainty assigned by TRC = 0.5 K; TRC
351.47Frost, 1930Uncertainty assigned by TRC = 0.3 K; TRC
351.47Lecat, 1930Uncertainty assigned by TRC = 0.2 K; not clear that this is a new measurement; TRC
351.45Noyes, 1930Uncertainty assigned by TRC = 0.3 K; TRC
351.6Smyth and Engel, 1929Uncertainty assigned by TRC = 0.15 K; TRC
351.55Smyth and Stoops, 1929Uncertainty assigned by TRC = 0.3 K; TRC
351.05Adkins and Broderick, 1928Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
351.05Adkins and Broderick, 1928, 2Uncertainty assigned by TRC = 0.3 K; TRC; Data excluded from overall average
351.45Barbaudy, 1927Uncertainty assigned by TRC = 0.2 K; TRC
351.5Lecat, 1927Uncertainty assigned by TRC = 0.5 K; TRC
351.5Lecat, 1927, 2Uncertainty assigned by TRC = 0.5 K; TRC
351.5Lecat, 1927, 3Uncertainty assigned by TRC = 0.5 K; TRC
351.45Lecat, 1926Uncertainty assigned by TRC = 0.3 K; TRC
350.95Munch, 1926Uncertainty assigned by TRC = 0.3 K; TRC; Data excluded from overall average
351.5Norris and Ashdown, 1925Uncertainty assigned by TRC = 0.2 K; TRC
351.45Palmer and Constable, 1925Uncertainty assigned by TRC = 0.2 K; TRC
351.55Williams and Daniels, 1924Uncertainty assigned by TRC = 0.2 K; TRC
351.47Grimm and Patrick, 1923Uncertainty assigned by TRC = 0.1 K; TRC
350.65Ormandy and Craven, 1923Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
351.45Willard and Smith, 1923Uncertainty assigned by TRC = 0.15 K; TRC
351.45Maass and Boomer, 1922Uncertainty assigned by TRC = 0.5 K; may not be measured by authors; TRC
351.45Barr and Bircumshaw, 1921Uncertainty assigned by TRC = 0.5 K; TRC
351.55Paul and Schantz, 1919Uncertainty assigned by TRC = 0.4 K; TRC
351.55Creighton and Way, 1918Uncertainty assigned by TRC = 0.5 K; TRC
351.55Jaeger, 1917Uncertainty assigned by TRC = 0.5 K; TRC
351.15Willcox and Brunel, 1916Uncertainty assigned by TRC = 0.5 K; TRC
351.65Campbell, 1915Uncertainty assigned by TRC = 0.5 K; TRC
351.47Tyrer, 1914Uncertainty assigned by TRC = 0.05 K; TRC
351.6Bingham, White, et al., 1913Uncertainty assigned by TRC = 0.3 K; TRC
351.05Bridgman, 1913Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
351.55Muendel, 1913Uncertainty assigned by TRC = 0.5 K; TRC
351.25N/AUncertainty assigned by TRC = 0.3 K; TRC
351.45Wrewski, 1912Uncertainty assigned by TRC = 0.2 K; TRC
351.54Wade and Merriman, 1911Uncertainty assigned by TRC = 0.1 K; TRC
351.53Holmes and Sageman, 1909Uncertainty assigned by TRC = 0.2 K; TRC
351.2Richards and Mathews, 1908Uncertainty assigned by TRC = 1. K; TRC
351.45Young, 1902Uncertainty assigned by TRC = 0.3 K; TRC
351.45Noyes and Warfel, 1901Uncertainty assigned by TRC = 0.1 K; Beckman therm. 1/100 grad. - corr. 0 deg.; TRC
351.35Louguinine, 1898Uncertainty assigned by TRC = 0.2 K; Thermometer calibr. by the Charlottenburg Physical Institute 20 deg. long therm; TRC
351.25Landolt and Jahn, 1892Uncertainty assigned by TRC = 0.5 K; TRC
351.45Beckmann, 1890Uncertainty assigned by TRC = 0.5 K; TRC
351.45Kahlbaum, 1884Uncertainty assigned by TRC = 0.5 K; TRC
351.65Perkin, 1884Uncertainty assigned by TRC = 0.5 K; TRC
351.45Mendeleev, 1865Uncertainty assigned by TRC = 0.1 K; TRC
351.41Regnault, 1863Uncertainty assigned by TRC = 0.2 K; TRC
351.55Kopp, 1854Uncertainty assigned by TRC = 0.5 K; TRC
351.55Kopp, 1848Uncertainty assigned by TRC = 0.5 K; TRC

In addition to the Thermodynamics Research Center (TRC) data available from this site, much more physical and chemical property data is available from the following TRC products:


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.

Fandary, Aljima, et al., 1999
Fandary, M.S.H.; Aljima, A.S.; Al-Kandary, J.A., Liquid-Liquid Equilibria for the System Water + Ethanol + Ethyl tert-Butyl Ether, J. Chem. Eng. Data, 1999, 44, 1129-31. [all data]

Arce, Martinez-Ageitos, et al., 1998
Arce, A.; Martinez-Ageitos, J.; Soto, A., Vapor-Liquid Equilibria at 101.32 kPa of the Ternary Systems 2-Methoxy-2-methylpropane + Methano + Water and 2-Methoxy-2-methylprpane + Ethanol + Water, J. Chem. Eng. Data, 1998, 43, 708-13. [all data]

Comelli and Francesconi, 1997
Comelli, F.; Francesconi, R., Isothermal Vapor-Liquid Equilibria Measurements, Excess Molar Enthalpies, and Excess Molar Volumes of Dimethyl Carbonate + Methanol, + Ethanol, and + Propan-1-ol at 313.15 K, J. Chem. Eng. Data, 1997, 42, 705-9. [all data]

Arce, Blanco, et al., 1995
Arce, A.; Blanco, A.; Souza, P.; Vidal, I., Liquid-Liquid Equilibria of the Ternary Mixtures Water + Propanoic Acid + Methyl Ethyl Ketone and Water + Propanoic Acid + Methyl Propyl Ketone, J. Chem. Eng. Data, 1995, 40, 225-9. [all data]

Hiaki, Takahashi, et al., 1995
Hiaki, T.; Takahashi, K.; Tsuji, T.; Hongo, M.; Kojima, K., Vapor-Liquid Equilibria of Ethanol + Octane at 343.15 K and 1-Propanol + Octane at 358.15 K, J. Chem. Eng. Data, 1995, 40, 271-3. [all data]

Hiaki, Takahashi, et al., 1994
Hiaki, T.; Takahashi, K.; Tsuji, T.; Hongo, M.; Kojima, K., Vapor-Liquid Equilibria of Ethanol + 2,2,4-Trimethylpentane at 333.15 K and 1-Propanol + 2,2,4-Trimethylpentane at at 343.15 K, J. Chem. Eng. Data, 1994, 39, 605-7. [all data]

Hiaki, Yamato, et al., 1992
Hiaki, T.; Yamato, K.; Kojima, K., Vapor-liquid equilibria of 2,3-dimethylbutane + methanol or ethanol at 101. 3 kPa, J. Chem. Eng. Data, 1992, 37, 203-6. [all data]

Cabezas, Beltran, et al., 1991
Cabezas, J.L.; Beltran, S.; Coca, J., Isobaric vapor-liquid equilibrium data for the binary systems 1,2- dimethoxyethane + alcohols, J. Chem. Eng. Data, 1991, 36, 184-8. [all data]

Kato, Tanaka, et al., 1991
Kato, M.; Tanaka, H.; Yoshikawa, H., Vapor-liquid equilibria for four binary systems made of alcohol and icyclohexylamine at 100 kPa., J. Chem. Eng. Data, 1991, 36, 387. [all data]

Ortega, Susial, et al., 1990
Ortega, J.; Susial, P.; de Alfonso, C., Vapor-Liquid Equilibrium Measurements at 101.32 kPa for Binary Mixtures of Methyl Acetate + Ethanol or 1-Propanol, J. Chem. Eng. Data, 1990, 35, 350. [all data]

Kaczmarek and Radecki, 1989
Kaczmarek, B.; Radecki, A., Vapor-Liquid Equilibria in Binary Systems Containing Ethanol with Tetramethyldisiloxane and Dimethyl Sulfoxide, J. Chem. Eng. Data, 1989, 34, 195. [all data]

Kato and Tanaka, 1989
Kato, M.; Tanaka, H., Vapor-Liquid Equilibrium Determination with a Flow-Type Ebulliometer for Six Binary Systems Made of Alcohol and Amine, J. Chem. Eng. Data, 1989, 34, 203. [all data]

Kato and Tanaka, 1989, 2
Kato, M.; Tanaka, H., Ebulliometric Measurement of Vapor-Liquid Equilibria for Four Binary Systems: Methanol + Silicon Tetramethoxide, Methanol + Silicon Tetraethoxide, Ethanol + Silicon Tetramethoxide and Ethanol + Silic, J. Chem. Eng. Data, 1989, 34, 206. [all data]

Susial, Ortega, et al., 1989
Susial, P.; Ortega, J.; de Alfonso, C.; Alonso, C., Vapor-Liquid Equilibrium Measurements for Methyl Propanoate-Ethanol and Methyl Propanoate-Propan-1-ol at 101.32 kPa, J. Chem. Eng. Data, 1989, 34, 247. [all data]

Weast and Grasselli, 1989
CRC Handbook of Data on Organic Compounds, 2nd Editon, Weast,R.C and Grasselli, J.G., ed(s)., CRC Press, Inc., Boca Raton, FL, 1989, 1. [all data]

Ortega, Pena, et al., 1986
Ortega, J.; Pena, J.A.; de Alfonso, C., Isobaric Vapor-Liquid Equilibria of Ethyl Acetate + Ethanol Mixtures at 760 +- 0.5mmHg, J. Chem. Eng. Data, 1986, 31, 339. [all data]

Dribika, Rashed, et al., 1985
Dribika, M.M.; Rashed, I.G.; Biddulph, M.W., Vapor-Liquid Equilibria in the Ternary System Methyl Alcohol-Ethyl Alcohol-Isopropyl Alcohol at Atmospheric Pressure, J. Chem. Eng. Data, 1985, 30, 146. [all data]

Kovac, Svoboda, et al., 1985
Kovac, A.; Svoboda, J.; Ondrus, I., Vapor-liquid equilibrium of some binary systems containing 1,1-dichloroethylene, Chem. Zvesti, 1985, 39, 6, 729. [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]

Mato and Benito, 1985
Mato, F.; Benito, G.G., Liquid-Vapor Equilibrium of Binary Mixtures of Nitriles and Alcohols. I., An. Quim., Ser. A, 1985, 81, 116. [all data]

Mato, Benito, et al., 1985
Mato, F.; Benito, G.G.; Sobron, F., Liquid-Vapor Equilibrium of Binary Mixtures of Nitriles and Alcohols. II., An. Quim., Ser. A, 1985, 81, 400. [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]

Yoshikawa, Takagi, et al., 1980
Yoshikawa, Y.; Takagi, A.; Kato, M., Indirect Determination of Vapor-Liquid Equilibria by a Small Ebulliometer Tetrahydrofuran-Alcohol Binary Systems, J. Chem. Eng. Data, 1980, 25, 344. [all data]

Thorat, Nageshwar, et al., 1979
Thorat, R.T.; Nageshwar, G.D.; Mene, P.S., Excess thermodynamic properties of the ternary system ethyl acetate + ethanol + 2-ethoxyethanol, J. Chem. Eng. Data, 1979, 24, 270-2. [all data]

Marinichev and Vasil'eva, 1976
Marinichev, A.N.; Vasil'eva, I.I., Azeotropic Properties of the System Water-Ethyl Alcohol-Methyl Ethyl Ketone-n-Octane, Zh. Prikl. Khim. (Leningrad), 1976, 49, 2065-9. [all data]

Nagata and Ohta, 1971
Nagata, I.; Ohta, T., Isobaric vapor-liquid equilibria for three binary and two ternary systems, J. Chem. Eng. Data, 1971, 16, 164. [all data]

Sagnes and Sanchez, 1971
Sagnes, M.; Sanchez, V., Vapor-liquid equilibria for fourteen systems consisting of chlorinated hydrocarbons and alcohols, J. Chem. Eng. Data, 1971, 16, 351-4. [all data]

Kato, Konishi, et al., 1970
Kato, M.; Konishi, H.; Hirata, M., New apparatus for isobaric dew and bubble point method methanol + water, ethyl acetate + ethanol, water + 1-butanol, and ethyl acetate + water systems, J. Chem. Eng. Data, 1970, 15, 435-9. [all data]

Suska, Holub, et al., 1970
Suska, J.; Holub, R.; Vonka, P.; Pick, J., Liquid-Vapor Equilibrium XLII. Systems: Ethyl Alcohol-Water-tert- Butyl Alcohol and Ethyl Alcohol-Water-Isobutyl Alcohol, Collect. Czech. Chem. Commun., 1970, 35, 385-95. [all data]

Anonymous, 1968
Anonymous, X., Chemicals and Plastics Physical Properties, 1968, Union Carbide Corp., product bulletin, 1968. [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]

Agarwal and Mene, 1963
Agarwal, M.M.; Mene, P.S., Studies in Binary Vapor-Liquid Equilibria, Indian Chem. Eng., 1963, 5, 71. [all data]

Deshpande and Lu, 1963
Deshpande, A.K.; Lu, B.C.Y., Vapor-Liquid Equilibria Part III. System Ethanol-Cyclohexane at Atmospheric Pressure, J. Chem. Eng. Data, 1963, 8, 558. [all data]

Ho and Lu, 1963
Ho, J.C.K.; Lu, B.C.Y., Vapor-Liquid Equilibria Part II. System n-Hexane-Ethanol-Benzene at 55, J. Chem. Eng. Data, 1963, 8, 553. [all data]

Kudryavtseva and Susarev, 1963
Kudryavtseva, L.S.; Susarev, M.P., Liquid-vapor equilibrium in the systems acetone-hexane and hexane-ethyl alcohol at 35, 45, and 55 deg. and 760 mm of Hg., Zh. Prikl. Khim. (Leningrad), 1963, 36, 1471. [all data]

Kudryavtseva and Susarev, 1963, 2
Kudryavtseva, L.S.; Susarev, M.P., Liquid-vapor equilibrium in the ethyl alcohol + chloroform + hexane system at temperatures of 55, 45, and 35 c and a pressure of 760 mm hg, Zh. Prikl. Khim. (Leningrad), 1963, 36, 2025-2030. [all data]

Waldo and Weber, 1963
Waldo, R.A.; Weber, J.H., Vapor Liquid Equilibrium at Atmospheric Pressure: The Ternary System Benzene-Ethanol-n-Hexane, J. Chem. Eng. Data, 1963, 8, 349. [all data]

Brown and Smith, 1962
Brown, I.; Smith, F., Aust. J. Chem., 1962, 15, 3-8. [all data]

Kaes and Weber, 1962
Kaes, G.L.; Weber, J.H., Vapor-Liquid Equilibrium at Atmospheric Pressure. Systems Containing Ethyl Alcohol, n-Hexane, Benzene, and Methylcyclopentane, J. Chem. Eng. Data, 1962, 7, 344. [all data]

Belknap and Weber, 1961
Belknap, R.C.; Weber, J.H., Vapor-Liquid Equilibrium at Atmospheric Pressure. Systems Containing Ethyl Alcohol, n-Hexane, Benzene, and Methylcyclopentane, J. Chem. Eng. Data, 1961, 6, 485. [all data]

Copp and Findlay, 1960
Copp, J.L.; Findlay, T.J.V., Thermodynamics of Binary Systems Containing Amines. Part 4., Trans. Faraday Soc., 1960, 56, 13. [all data]

Anonymous, 1958
Anonymous, X., Am. Pet. Inst. Res. Proj. 50, 1958, Unpublished, 1958. [all data]

Costello and Bowden, 1958
Costello, J.M.; Bowden, S.T., The Temperature Variation of Orthobaric Density Difference in Liquid-Vapor Systems III. Alcohols, Recl. Trav. Chim. Pays-Bas, 1958, 77, 36-46. [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]

Murti and Van Winkle, 1958
Murti, P.S.; Van Winkle, M., Vapor-Liquid Equilibria for Binary Systems of Methanol, Ethyl Alcohol, 1-Propanol, and 2-Propanol with Ethyl Acetate and 1-Propanol-Water, Chem. Eng. Data Ser., 1958, 3, 72-81. [all data]

Ogata and Takagi, 1958
Ogata, Y.; Takagi, Y., J. Am. Chem. Soc., 1958, 80, 3591. [all data]

Wagner and Weber, 1958
Wagner, IrvenF.; Weber, J.H., Vapor-Liquid Equilibria at Atmosphereic Pressure for the Ternary System Benzene-Ethyl Alcohol-n-Heptane, J. Chem. Eng. Data, 1958, 3, 220. [all data]

Amer, Paxton, et al., 1956
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Notes

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