Article ID Journal Published Year Pages File Type
9625980 Fluid Phase Equilibria 2005 6 Pages PDF
Abstract
The isothermal P, x, y data are well represented with the Peng and Robinson equation of state using the Mathias-Copeman alpha function and the Wong-Sandler mixing rules involving the NRTL gE model.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
Authors
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