Simulation Of Three-Phase Distillation Column Using Bubble Point And (^-0 Approach

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Simulation Of Three-Phase Distillation Column Using Bubble Point And (^-0 Approach

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dc.contributor.author Lashkari, Siamak en_US
dc.date.accessioned 2009-11-25T13:04:18Z
dc.date.available 2009-11-25T13:04:18Z
dc.date.issued 1995 en_US
dc.identifier.citation Engineering Journal of Qatar University, 1995, Vol. 8, Pages 43-64. en_US
dc.identifier.uri http://hdl.handle.net/10576/7874
dc.description.abstract Most of organic compounds are partially miscible in water and due to their solubility criteria split into two liquid phases. So design of equipments that separate two liquid phase systems differ from one liquid phase system equipments. A mathematical model and a computer program have been developed to simulate three-phase distillation columns. The proposed procedure is based on linearization of equations and solving them by Newton-Raphson method. Average liquid compositions are chosen as independent variables and temperature, vapor compositions and two liquid phase compositions are obtained by three-phase bubble point calculations on each tray. For predicting thermodynamic properties, equation of state is used en_US
dc.language.iso en en_US
dc.publisher Qatar University en_US
dc.subject Engineering: Research & Technology en_US
dc.title Simulation Of Three-Phase Distillation Column Using Bubble Point And (^-0 Approach en_US
dc.type Article en_US
dc.identifier.pagination 43-64 en_US
dc.identifier.volume 8 en_US

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