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dc.contributor.authorKhoo, Boo Kean
dc.contributor.authorVu, Trieu Minh
dc.date.accessioned2012-10-30T03:22:07Z
dc.date.available2012-10-30T03:22:07Z
dc.date.issued2010-10-16
dc.identifier.isbn978-967-5760-03-7
dc.identifier.urihttp://dspace.unimap.edu.my/123456789/21567
dc.descriptionInternational Postgraduate Conference On Engineering (IPCE 2010), 16th - 17th October 2010 organized by Centre for Graduate Studies, Universiti Malaysia Perlis (UniMAP) at School of Mechatronic Engineering, Pauh Putra Campus, Perlis, Malaysia.en_US
dc.description.abstractDistillation column processing is the most vital separation technology for today’s industry. An inclination to controlling distillation columns in a manner that is economically efficient depends much on the selection of reliable systems. This paper presents a detailed methodology to derive a mathematic modeling and simulation analysis for a distillation column based on continuous and non-linear model of the mass and energy balance. The mathematical modeling is then used as the reference model system to examine the ability of the developed distillate column tower dealing with the modelplant mismatch and feed disturbances inputsen_US
dc.language.isoenen_US
dc.publisherUniversiti Malaysia Perlis (UniMAP)en_US
dc.relation.ispartofseriesProceedings of the International Postgraduate Conference on Engineering (IPCE 2010)en_US
dc.subjectDistillation column processingen_US
dc.subjectMathematic modelingen_US
dc.subjectSimulation analysisen_US
dc.titleMathematical modeling and simulation of a distillation columnen_US
dc.typeWorking Paperen_US
dc.publisher.departmentCentre for Graduate Studiesen_US
dc.contributor.urlbkkhoo@yahoo.comen_US
dc.contributor.urlvutrieuminh@petronas.com.myen_US


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