Article ID Journal Published Year Pages File Type
204386 Fluid Phase Equilibria 2007 11 Pages PDF
Abstract

Isothermal vapour–liquid equilibrium measurements for the systems of butane with methanol, 2-propanol, 1-butanol, 2-butanol and 2-methyl-2-propanol were made at 364.5 K using a static total pressure apparatus. The obtained pressure–temperature–total composition (PTz) data were converted into pressure–temperature–liquid–vapour composition (PTxy) form by means of the Barker method. Error analysis was performed on measured and calculated variables. The systems of butane with methanol and 2-propanol showed azeotropic behaviour at 364.5 K. Wilson and NRTL parameters were regressed. The VLE measurements were compared with predictions obtained using the UNIFAC, UNIFAC-Dortmund and COSMO-RS models.

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Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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