Article ID Journal Published Year Pages File Type
9626025 Fluid Phase Equilibria 2005 8 Pages PDF
Abstract
The isothermal P, x, y data are well represented with the Redlich and Kwong equation of state using the Mathias-Copeman alpha function and the Huron-Vidal mixing rules involving the NRTL model.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
Authors
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