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Author:Howat, C.S.

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10 matching references were found.

Howat, J.N.; Howat, C.S., Infinite Dilution Activity Coefficients and Miscibility Using a Modified Static Total Pressure Method, J. Chem. Eng. Data, 1996, 41, 977-986. [all data]

Howat, J.N.; Howat, C.S., AIChE Annual Meeting, Florida, November, 1995. [all data]

Hartwick, R.P.; Howat, C.S., Infinite Dilution Activity Coefficients of Acetone in Water. A New Experimental Method and Verification, J. Chem. Eng. Data, 1995, 40, 738-45. [all data]

Laird, D.G.; Howat, C.S., Vapor - Liquid Phase Equilibria and Molar Volumes of the Butadiene - Acetonitrile System from 300 to 335 K., Fluid Phase Equilib., 1990, 60, 173-190. [all data]

Howat, C.S.; Swift, G.W., Vapor-liquid phase equilibria for the binaries isoprene-dicyclopentadiene and n-pentane-dicyclopentadiene at 313 and 323 K, J. Chem. Eng. Data, 1985, 30, 281. [all data]

Howat, C.S.; Swift, G.W., Vapor-Liquid Phase Equilibria for the Isoprene-n-Pentane Binary System from 300 to 330 K, Fluid Phase Equilib., 1985, 21, 113. [all data]

Howat, C.S.; Swift, G.W., Fluid Phase Equilb., 1984, 21, 113. [all data]

Shanker, G.; Howat, C.S.; Torres, R.R.; Swift, G.W., Vapor-liquid equilibria for 2-methylbutene-1 and 2-methyl-1,3-butadiene at 310.93, 316.48 and 322.03 k, Fluid Phase Equilib., 1981, 5, 305-21. [all data]

Ezekwe, J.N.; Howat, C.S.; Swift, G.W., Vapor-liquid equilibria for the binary system 2-methylbutene-2 and 2- methyl-1,3-butadiene at 310.93, 316.48 and 322.04 k., Fluid Phase Equilib., 1981, 7, 75. [all data]

Muir, R.F.; Howat, C.S., Predictiing Solid-liquid equilibrium Data from Vapor-liquid Data, Chem. Eng., 1982, 22, 89-92. [all data]