C. Howat

发表

Data reconciliation and parameter estimation in plant performance analysis

R. J. MacDonald, C. S. Howat, R. J. MacDonald, 1988 .

Vapor—liquid phase equilibria for the isoprene—n-pentane binary system from 300 to 330 K

G. Swift, C. Howat, 1985 .

Vapor-liquid equilibria for 2-methylbutene-1 and 2-methyl-1,3-butadiene at 310.93, 316.48 and 322.03 K

G. Swift, C. Howat, G. Shanker, 1981 .

Vapor—liquid phase equilibria and molar volumes of the butadiene-acetonitrile system from 300 to 335 K

D. G. Laird, C. Howat, 1990 .

Infinite Dilution Activity Coefficients of Acetone in Water. A New Experimental Method and Verification

C. Howat, Roger P. Hartwick, 1995 .

Cyclopentadiene-dicyclopentadiene phase equilibria and reaction rate behavior using the transient total pressure method

G. Swift, C. Howat, 1988 .

A New Correlation of Propene-Propane Vapor-Liquid Equilibrium Data and Application of the Correlation to Determine Optimum Fractionator Operating Pressure in the Manufacture of Polymerization-Grade Propene

George W. Swift, Colin S. Howat, G. Swift, 1980 .

Sector insights: skills and performance challenges in the health and social care sector

M. Lawrie, C. Howat, R. Sutton, 2015 .

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

G. Swift, C. Howat, J. N. Ezekwe, 1981 .

A procedure for the design of experiments in fluid phase equilibria

G. Swift, C. Howat, 1983 .