Please use this identifier to cite or link to this item: https://scholarbank.nus.edu.sg/handle/10635/91392
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dc.titleA method for calculation of vapor-liquid and liquid-liquid equilibria
dc.contributor.authorHan, G.
dc.contributor.authorRangaiah, G.P.
dc.date.accessioned2014-10-09T08:17:35Z
dc.date.available2014-10-09T08:17:35Z
dc.date.issued1997
dc.identifier.citationHan, G.,Rangaiah, G.P. (1997). A method for calculation of vapor-liquid and liquid-liquid equilibria. Computers and Chemical Engineering 21 (8) : 905-913. ScholarBank@NUS Repository.
dc.identifier.issn00981354
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/91392
dc.description.abstractA new parameter, pseudo temperature (Tp) is introduced to solve two-phase equilibrium calculations. The resulting Tp-method has a single set of equations to describe different phase regions encountered in vapor-liquid equilibrium (VLE) and liquid-liquid equilibrium (LLE). It does not require a priori the number of phases existing at equilibrium, and involves a minimization problem having a linear objective function subject to nonlinear constraints, which can be solved by a version of successive linear programming method. Tp-method is tested on typical examples for VLE and LLE, and compared with pseudo pressure (Pp) method of Bullard and Biegler [Computers and Chemical Engineering 17, 95-109 (1993)] for VLE. In each example, several operating conditions are considered to cover both single- and two-phase situations. The results show that Tp-method is successful for both VLE and LLE, and that Tp-and Pp-methods are comparable for VLE. © 1997 Elsevier Science Ltd.
dc.sourceScopus
dc.typeArticle
dc.contributor.departmentCHEMICAL ENGINEERING
dc.description.sourcetitleComputers and Chemical Engineering
dc.description.volume21
dc.description.issue8
dc.description.page905-913
dc.description.codenCCEND
dc.identifier.isiutNOT_IN_WOS
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