Abstract
An analysis of data on the vapor-liquid equilibrium of a mixture of C4 hydrocarbons in the pres-ence of an extractant - acetonitrile - was performed. The values of the binary interaction param-eters of the NRTL and UNIFAC models for the components of a mixture of C4 and acetonitrile are estimated
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Schedule a callMore From: Bulletin of the Angarsk State Technical University
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