Article ID Journal Published Year Pages File Type
202511 Fluid Phase Equilibria 2011 4 Pages PDF
Abstract

The liquid–liquid and vapor–liquid equilibrium data for the binary system of ethane + methanol were measured at ambient temperature over a wide range of pressures using a designed PVT apparatus. The experimental liquid–liquid and vapor–liquid equilibrium data were compared with the modeling results obtained using the Peng Robinson and Soave–Redlich–Kwong equations of state.

Research highlights► Liquid–liquid and vapor–liquid equilibrium data. ► Binary system of ethane + methanol at ambient temperature. ► Experimental study over a wide range of pressures using a designed PVT apparatus. ► The experimental data were modeled using the Peng Robinson and Soave–Redlich–Kwong equations of state.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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