Article ID Journal Published Year Pages File Type
9626006 Fluid Phase Equilibria 2005 8 Pages PDF
Abstract
Isothermal vapour-liquid equilibrium was measured for ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane at 318.4 K with an automated static total pressure measurement apparatus. The experimental data was correlated with the Wilson activity coefficient model. A good agreement between the experiments and the model was achieved. All six binary systems exhibited positive deviation from Raoult's law.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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