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Methyl Alcohol

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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

Tboil (K) Reference Comment
337.65Arce, Martinez-Ageitos, et al., 1998Uncertainty assigned by TRC = 0.1 K; TRC
337.42Blanco and Ortega, 1998Uncertainty assigned by TRC = 0.3 K; TRC
337.70Comelli and Francesconi, 1997Uncertainty assigned by TRC = 0.1 K; TRC
337.75Arce, Blanco, et al., 1995Uncertainty assigned by TRC = 0.2 K; TRC
337.5Reddy, Rambabu, et al., 1995Uncertainty assigned by TRC = 0.3 K; TRC
337.69Hiaki, Yamato, et al., 1992Uncertainty assigned by TRC = 0.08 K; TRC
337.85Cabezas, Beltran, et al., 1991Uncertainty assigned by TRC = 0.3 K; TRC
337.69Kato, Tanaka, et al., 1991Uncertainty assigned by TRC = 0.08 K; TRC
337.72Arce, Dominguez, et al., 1990Uncertainty assigned by TRC = 0.1 K; TRC
337.60Gultekin, 1990Uncertainty assigned by TRC = 0.15 K; TRC
337.690Kato and Tanaka, 1989Uncertainty assigned by TRC = 0.2 K; TRC
337.690Kato and Tanaka, 1989, 2Uncertainty assigned by TRC = 0.2 K; TRC
338.05Rajendran, Renganarayanan, et al., 1989Uncertainty assigned by TRC = 0.3 K; TRC
337.35Manjeshwar and Aminabhavi, 1988Uncertainty assigned by TRC = 0.3 K; TRC
337.830Wisniak and Tamir, 1988Uncertainty assigned by TRC = 0.2 K; TRC
337.830Wisniak and Tamir, 1988, 2Uncertainty assigned by TRC = 0.15 K; TRC
337.830Wisniak and Tamir, 1988, 3Uncertainty assigned by TRC = 0.15 K; TRC
337.830Wisniak and Tamir, 1988, 4Uncertainty assigned by TRC = 0.15 K; TRC
337.35Aminabhavi, Manjeshwar, et al., 1987Uncertainty assigned by TRC = 0.3 K; TRC
337.35Manjeshwar and Aminabhavi, 1987Uncertainty assigned by TRC = 0.3 K; TRC
337.840Tamir and Wisniak, 1987Uncertainty assigned by TRC = 0.15 K; TRC
337.660Linek and Bernatova, 1986Uncertainty assigned by TRC = 0.1 K; TRC
337.830Tamir and Wisniak, 1986Uncertainty assigned by TRC = 0.1 K; TRC
337.75Choi, Park, et al., 1985Uncertainty assigned by TRC = 0.5 K; TRC
337.920Dribika, Rashed, et al., 1985Uncertainty assigned by TRC = 0.07 K; TRC
337.45Kovac, Svoboda, et al., 1985Uncertainty assigned by TRC = 0.2 K; TRC
337.7Majer and Svoboda, 1985 
337.85Mato and Benito, 1985Uncertainty assigned by TRC = 0.4 K; TRC
337.85Mato, Benito, et al., 1985Uncertainty assigned by TRC = 0.3 K; TRC
337.830Wisniak and Tamir, 1985Uncertainty assigned by TRC = 0.1 K; TRC
337.670Cervenkova and Boublik, 1984Uncertainty assigned by TRC = 0.06 K; TRC
337.85Dizechi and Marschell, 1982Uncertainty assigned by TRC = 0.3 K; TRC
337.660Aim and Ciprian, 1980Uncertainty assigned by TRC = 0.08 K; TRC
337.8Natarajan and Srinivasan, 1980Uncertainty assigned by TRC = 0.4 K; TRC
337.55Yoshikawa, Takagi, et al., 1980Uncertainty assigned by TRC = 0.3 K; TRC
337.65Ochi and Lu, 1978Uncertainty assigned by TRC = 0.05 K; TRC
341.8Schindler, Plank, et al., 1977Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
329.4Srinivasan and Kulkarni, 1976Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
337.71Svoboda, Vesely, et al., 1973Uncertainty assigned by TRC = 0.05 K; TRC
337.670Boublik and Aim, 1972Uncertainty assigned by TRC = 0.05 K; TRC
337.9Lesteva and Timofeev, 1972Uncertainty assigned by TRC = 0.4 K; TRC
337.85Nagata and Ohta, 1971Uncertainty assigned by TRC = 0.5 K; TRC
337.9Sagnes and Sanchez, 1971Uncertainty assigned by TRC = 0.3 K; TRC
337.74Kato, Konishi, et al., 1970Uncertainty assigned by TRC = 0.3 K; TRC
337.74Kirby and Van Winkle, 1970Uncertainty assigned by TRC = 0.25 K; TRC
337.85Strubl, Svoboda, et al., 1970Uncertainty assigned by TRC = 0.2 K; TRC
337.740Willock and Van Winkle, 1970Uncertainty assigned by TRC = 0.2 K; TRC
337.730Hudson and Van Winkle, 1969Uncertainty assigned by TRC = 0.08 K; TRC
337.9Nagata, 1969Uncertainty assigned by TRC = 0.3 K; TRC
337.65Anonymous, 1968TRC
337.8Bekarek and Hala, 1968Uncertainty assigned by TRC = 0.15 K; TRC
337.75Nakanishi, Shirai, et al., 1968Uncertainty assigned by TRC = 0.2 K; TRC
337.60Freshwater and Pike, 1967Uncertainty assigned by TRC = 0.1 K; TRC
337.60Freshwater, 1967Uncertainty assigned by TRC = 0.3 K; TRC
337.75Nakanishi, Nakasato, et al., 1967Uncertainty assigned by TRC = 0.3 K; TRC
337.95Nakanishi, Shirai, et al., 1967Uncertainty assigned by TRC = 0.3 K; TRC
337.75Katti and Prakash, 1966Uncertainty assigned by TRC = 0.08 K; TRC
337.80Fort and Moore, 1965Uncertainty assigned by TRC = 0.2 K; TRC
338.0Grove and Walden, 1965Uncertainty assigned by TRC = 0.4 K; TRC
337.25Baker, Fisher, et al., 1964Uncertainty assigned by TRC = 0.2 K; TRC; Data excluded from overall average
337.8Burke, Williams, et al., 1964Uncertainty assigned by TRC = 0.5 K; TRC
337.85Akita and Yoshida, 1963Uncertainty assigned by TRC = 0.2 K; TRC
337.6Raju, Ranganathan, et al., 1963Uncertainty assigned by TRC = 0.4 K; TRC
337.690Brown and Smith, 1962TRC
337.85Nagata, 1962Uncertainty assigned by TRC = 0.3 K; TRC
337.720Paraskevopoulos and Missen, 1962Uncertainty assigned by TRC = 0.05 K; Calculated from equation based on previous data; TRC
337.8Kiser, Johnson, et al., 1961Uncertainty assigned by TRC = 0.2 K; TRC
337.700Copp and Findlay, 1960Uncertainty assigned by TRC = 0.12 K; TRC
337.65Yen and Reed, 1959Uncertainty assigned by TRC = 0.2 K; TRC
337.65Anonymous, 1958TRC
337.85Costello and Bowden, 1958Uncertainty assigned by TRC = 0.5 K; TRC
337.900Ling and Van Winkle, 1958Uncertainty assigned by TRC = 0.1 K; TRC
337.65Murti and Van Winkle, 1958Uncertainty assigned by TRC = 0.3 K; TRC
337.2Bender and Kemp, 1957Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
337.75Amer, Paxton, et al., 1956Uncertainty assigned by TRC = 0.5 K; TRC
337.65McCracken and Smith, 1956Uncertainty assigned by TRC = 0.33 K; TRC
337.65Vandenheuvel and Vatcher, 1956Uncertainty assigned by TRC = 1. K; TRC
337.85Dever, Finch, et al., 1955Uncertainty assigned by TRC = 0.5 K; TRC
337.75Green and Vener, 1955Uncertainty assigned by TRC = 0.3 K; TRC
337.55Hammond and Stokes, 1955Uncertainty assigned by TRC = 0.5 K; TRC
337.960Hansen and Hansen, 1955Uncertainty assigned by TRC = 0.2 K; TRC
337.800Colmant, 1954Uncertainty assigned by TRC = 0.1 K; TRC
337.95Cropper, Spieth, et al., 1954Uncertainty assigned by TRC = 0.5 K; TRC
337.880Griffiths, 1954Uncertainty assigned by TRC = 0.1 K; TRC
337.75Purnell and Bowden, 1954TRC
337.75Amer, Paxton, et al., 1953Uncertainty assigned by TRC = 0.5 K; TRC
337.75McKenna, Tartar, et al., 1953Uncertainty assigned by TRC = 0.5 K; TRC
337.8100Ballard and Van Winkle, 1952Uncertainty assigned by TRC = 0.11 K; Apparatus : Cotrell; TRC
337.85Desseigne and Belliot, 1952Uncertainty assigned by TRC = 0.5 K; TRC
337.85Hill and Van Winkle, 1952Uncertainty assigned by TRC = 0.5 K; Cottrell app.-therm.grad. 0.2 Rep. to +- 0.1 -Cartesian manostat; TRC
337.80Hughes and Maloney, 1952TRC
337.6500Scatchard and Ticknor, 1952Uncertainty assigned by TRC = 0.01 K; TRC
337.740Staveley and Spice, 1952Uncertainty assigned by TRC = 0.05 K; TRC
337.50West, Senise, et al., 1952Uncertainty assigned by TRC = 0.6 K; TRC
337.75Alpert and Elving, 1951Uncertainty assigned by TRC = 0.2 K; Cu-constantan thermocouple., checked with thermomometer calibr. by NBS. All temps. corr., pressure regulating system; TRC
337.75Heyding and Winkler, 1951Uncertainty assigned by TRC = 0.5 K; TRC
337.65Lyubomilov and Terent'ev, 1951Uncertainty assigned by TRC = 1. K; TRC
338.2Pino, Ercoli, et al., 1951Uncertainty assigned by TRC = 1. K; TRC
337.740Lang, 1950Uncertainty assigned by TRC = 0.05 K; Cottrell app. - P +- 1/4 Torr, T 1/100 deg.; TRC
337.800Natta, Pino, et al., 1950Uncertainty assigned by TRC = 0.1 K; TRC
337.85Natta, Pino, et al., 1950Uncertainty assigned by TRC = 0.1 K; TRC
337.85Pichler, Ziesecke, et al., 1950Uncertainty assigned by TRC = 0.5 K; TRC
339.Gorin and Gorn, 1949Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
337.85Griswold and Buford, 1949Uncertainty assigned by TRC = 0.1 K; Cottrell app. - therm.grad. 0.2 - checked N.B.S.; TRC
338.Hatem, 1949Uncertainty assigned by TRC = 1. K; TRC
337.80Lecat, 1949Uncertainty assigned by TRC = 0.1 K; TRC
337.75McKenna, Tartar, et al., 1949Uncertainty assigned by TRC = 0.1 K; TRC
337.9Tschamler, Richter, et al., 1949Uncertainty assigned by TRC = 0.5 K; TRC
337.9Baron and Mishchenko, 1948Uncertainty assigned by TRC = 0.5 K; TRC
337.8Lauder, 1948Uncertainty assigned by TRC = 0.5 K; TRC
337.80Lecat, 1947Uncertainty assigned by TRC = 0.3 K; TRC
337.8Lecat, 1947, 2Uncertainty assigned by TRC = 0.4 K; TRC
337.8Woods, 1947Uncertainty assigned by TRC = 0.2 K; TRC
337.65Kretschmer, Nowakowska, et al., 1946Uncertainty assigned by TRC = 0.2 K; TRC
337.80Lecat, 1946Uncertainty assigned by TRC = 0.1 K; TRC
337.7Pollock, Collett, et al., 1946Uncertainty assigned by TRC = 0.3 K; Anshutz therm. cal. N.B.S.; TRC
337.66Scatchard, Wood, et al., 1946Uncertainty assigned by TRC = 0.05 K; calculated from v.p. equation fit to obs. data; TRC
337.Addison, 1945Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
337.9Briscoe and Rinehart, 1942Uncertainty assigned by TRC = 0.2 K; TRC
337.66Maryott, 1941Uncertainty assigned by TRC = 0.1 K; TRC
337.4Bennewitz and Rossner, 1938Uncertainty assigned by TRC = 0.5 K; TRC
337.7Ingle and Cady, 1938Uncertainty assigned by TRC = 0.5 K; TRC
337.65Wojciechowski, 1936Uncertainty assigned by TRC = 0.03 K; Apparatus: Swietoslawski meth. N.B.S. calibr. Pt. resis. thermometer; TRC
337.75De Brouckere and Gillet, 1935Uncertainty assigned by TRC = 0.1 K; TRC
337.78De Brouckere and Gillet, 1935Uncertainty assigned by TRC = 0.1 K; TRC
337.77De Brouckere and Gillet, 1935Uncertainty assigned by TRC = 0.1 K; TRC
337.90Keffler and MacLean, 1935Uncertainty assigned by TRC = 0.1 K; Thermometer grad. 0.1 - stand. - corr. for sten.; TRC
337.7Smith, 1934Uncertainty assigned by TRC = 0.5 K; TRC
337.61Butler, Thomson, et al., 1933Uncertainty assigned by TRC = 0.1 K; TRC
337.9Lecat, 1930Uncertainty assigned by TRC = 0.3 K; not clear that this is a new measurement; TRC
337.51Rakovskii and Frost, 1930Uncertainty assigned by TRC = 0.1 K; TRC
337.54Rakovskii and Frost, 1930Uncertainty assigned by TRC = 0.1 K; TRC
337.80Timmermans and Hennaut-Roland, 1930Uncertainty assigned by TRC = 0.05 K; TRC
337.87Lecat, 1928Uncertainty assigned by TRC = 0.2 K; TRC
337.9Lecat, 1927Uncertainty assigned by TRC = 0.5 K; TRC
337.9Lecat, 1927, 2Uncertainty assigned by TRC = 0.5 K; TRC
337.9Lecat, 1927, 3Uncertainty assigned by TRC = 0.5 K; TRC
337.9Lecat, 1926Uncertainty assigned by TRC = 0.2 K; TRC
337.820Mathews, 1926Uncertainty assigned by TRC = 0.15 K; TRC
339.6Munch, 1926Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
337.90Norris and Ashdown, 1925Uncertainty assigned by TRC = 0.2 K; TRC
338.40Dancaster, 1924Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
339.2Ormandy and Craven, 1923Uncertainty assigned by TRC = 0.6 K; TRC; Data excluded from overall average
337.980Willard and Smith, 1923Uncertainty assigned by TRC = 0.1 K; TRC
338.140Willard and Smith, 1923Uncertainty assigned by TRC = 0.1 K; TRC
337.65Barr and Bircumshaw, 1921Uncertainty assigned by TRC = 0.2 K; TRC
338.95Creighton and Way, 1918Uncertainty assigned by TRC = 0.2 K; TRC; Data excluded from overall average
337.660Richards and Shipley, 1916Uncertainty assigned by TRC = 0.2 K; TRC
337.85Willcox and Brunel, 1916Uncertainty assigned by TRC = 0.2 K; TRC
338.2Campbell, 1915Uncertainty assigned by TRC = 0.5 K; TRC
337.87Tyrer, 1914Uncertainty assigned by TRC = 0.05 K; TRC
337.8Atkins and Wallace, 1913Uncertainty assigned by TRC = 0.05 K; TRC
338.05Bingham, White, et al., 1913Uncertainty assigned by TRC = 0.4 K; TRC
337.90Bridgman, 1913Uncertainty assigned by TRC = 1. K; TRC
338.2Muendel, 1913Uncertainty assigned by TRC = 0.5 K; TRC
338.05N/AUncertainty assigned by TRC = 0.5 K; TRC
337.85Timmermans, 1912Uncertainty assigned by TRC = 0.02 K; TRC
337.85Timmermans, 1911Uncertainty assigned by TRC = 0.3 K; TRC
337.85Timmermans, 1910Uncertainty assigned by TRC = 0.2 K; TRC
337.85Young, 1910Uncertainty assigned by TRC = 0.2 K; TRC
337.680Doroshevskii, 1909Uncertainty assigned by TRC = 0.2 K; TRC
338.05Holmes and Sageman, 1909Uncertainty assigned by TRC = 0.5 K; TRC
337.71Gyr, 1908Uncertainty assigned by TRC = 0.1 K; TRC
339.2Richards and Mathews, 1908Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
337.85Young and Fortey, 1902Uncertainty assigned by TRC = 0.1 K; TRC
338.15Landolt and Jahn, 1892Uncertainty assigned by TRC = 1. K; TRC
338.95Perkin, 1884TRC; Data excluded from overall average
339.4Zander, 1884Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
338.85Prytz, 1880Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
339.93Regnault, 1863Uncertainty assigned by TRC = 0.5 K; TRC; Data excluded from overall average
338.65Kopp, 1854Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average
338.65Kopp, 1848Uncertainty assigned by TRC = 1. K; TRC; Data excluded from overall average

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.

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]

Blanco and Ortega, 1998
Blanco, A.M.; Ortega, J., Densities and Vapor-Liquid Equilibrium Values for Binary Mixtures Composed of Methanol + an Ethyl Ester 1t 141.3 kPa with Application of an Extended Correlation Equation for Isobaric VLE Data, J. Chem. Eng. Data, 1998, 43, 638-645. [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]

Reddy, Rambabu, et al., 1995
Reddy, V.K.; Rambabu, K.; Devarajulu, T.; Krishnaiah, A., Volume of Mixing, Speed of Sound, and Viscosity of Methyl Cellosolve with Aliphatic Alcohols at 308.15 K, J. Chem. Eng. Data, 1995, 40, 124-7. [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]

Arce, Dominguez, et al., 1990
Arce, A.; Dominguez, A.; Tojo, J., Vapor-liquid equilibrium of the system methanol + benzene + cyclohexane at 760 mmHg, J. Chem. Eng. Data, 1990, 35, 30. [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]

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]

Rajendran, Renganarayanan, et al., 1989
Rajendran, M.; Renganarayanan, S.; Madhavan, P.R.; Srinivasan, D., Effect of Dissolved Salts on the Heat of Mixing of Three Binary Systems, J. Chem. Eng. Data, 1989, 34, 375. [all data]

Manjeshwar and Aminabhavi, 1988
Manjeshwar, L.S.; Aminabhavi, T.M., Densities and Viscosities of Binary Liquid Mixtures Containing Bromoform at 45 deg C, J. Chem. Eng. Data, 1988, 33, 184-5. [all data]

Wisniak and Tamir, 1988
Wisniak, J.; Tamir, A., Vapor-Liquid Equilibrim at 760 mmHg in the System Methanol- 1,1-Dichloroethane, J. Chem. Eng. Data, 1988, 33, 109. [all data]

Wisniak and Tamir, 1988, 2
Wisniak, J.; Tamir, A., Vapor-Liquid Equilibria at 760 mmHg in the Ternary System Methanol- Propyl Bromide-Methyl Methacrylate, J. Chem. Eng. Data, 1988, 33, 376. [all data]

Wisniak and Tamir, 1988, 3
Wisniak, J.; Tamir, A., Vapor-Liquid Equilibria at 760 mmHg in the Ternary System Methanol- 1,1-Dichloroethane-Propyl Bromide, J. Chem. Eng. Data, 1988, 33, 429. [all data]

Wisniak and Tamir, 1988, 4
Wisniak, J.; Tamir, A., Association Effects in the Methanol-1-Pentanol System, J. Chem. Eng. Data, 1988, 33, 432. [all data]

Aminabhavi, Manjeshwar, et al., 1987
Aminabhavi, T.M.; Manjeshwar, L.S.; Balundgi, R.H., Viscosities of Binary Liquid Mixtures, J. Chem. Eng. Data, 1987, 32, 50-2. [all data]

Manjeshwar and Aminabhavi, 1987
Manjeshwar, L.S.; Aminabhavi, T.M., Densities and Viscosities of Binary Liquid Mixtures at 45 deg. C, J. Chem. Eng. Data, 1987, 32, 409-12. [all data]

Tamir and Wisniak, 1987
Tamir, A.; Wisniak, J., Vapor-Liquid Equilibria at 760 mm Hg in the Ternary System Methanol- Acetonitrile-Propyl Bromide, J. Chem. Eng. Data, 1987, 32, 291. [all data]

Linek and Bernatova, 1986
Linek, J.; Bernatova, S., Liquid-Liquid Equil. in the Sys. Methanol-Water-Tert-Amyl Methyl Ether, Collect. Czech. Chem. Commun., 1986, 51, 188. [all data]

Tamir and Wisniak, 1986
Tamir, A.; Wisniak, J., Liquid-Vapor Equilibria at 760 mmHg in the Systems Methanol-Aceto- nitrile and Acetonitrile-Propyl Bromide, J. Chem. Eng. Data, 1986, 31, 363. [all data]

Choi, Park, et al., 1985
Choi, J.S.; Park, D.W.; Rhim, J.N., Isothermal Phase Equilibria for the Ternary System (Methanol(1)-n-Hexane(2)-n-Heptane(3)), Hwahak Konghak, 1985, 23, 89. [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]

Wisniak and Tamir, 1985
Wisniak, J.; Tamir, A., Vapor-Liquid Equilibria at 760 mmHg in the Sys. Methanol-2-Propanol-Propyl Bromide and Its Binaries, J. Chem. Eng. Data, 1985, 30, 339. [all data]

Cervenkova and Boublik, 1984
Cervenkova, I.; Boublik, T., Vapor pressures, refractive indexes, and densities at 20.0 .degree.C, and vapor-liquid equilibrium at 101.325 kPa, in the tert-amyl methyl ether-methanol system, J. Chem. Eng. Data, 1984, 29, 425. [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]

Aim and Ciprian, 1980
Aim, K.; Ciprian, M., Vapor Pressures, Refractive Index at 20.0 deg C, and Vapor-Liquid Equilibrium at 101.325 kPa in thee Methyl tert-Butyl Ether Methanol System,, J. Chem. Eng. Data, 1980, 25, 100. [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]

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]

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]

Schindler, Plank, et al., 1977
Schindler, L.E.; Plank, C.A.; Christopher, P.M.; Laukhuf, W.L.S., Vapor-liquid equilibria of the ternary system methyl borate + methyl alcohol + carbon tetrachloride, J. Chem. Eng. Data, 1977, 22, 294-6. [all data]

Srinivasan and Kulkarni, 1976
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Notes

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