Simulation Of Three-Phase Distillation Column Using Bubble Point And Φ-Φ Approach

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contributor.author Lashkari, Siamak en_US
contributor.author Moshfeghian, Mahmood en_US
date.accessioned 2009-11-25T13:04:18Z en_US
date.available 2009-11-25T13:04:18Z en_US
date.issued 1995 en_US
identifier.citation Engineering Journal of Qatar University, 1995, Vol. 8, Pages 43-64. en_US
identifier.uri http://hdl.handle.net/10576/7874 en_US
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
language.iso en en_US
publisher Qatar University en_US
subject Engineering: Research & Technology en_US
title Simulation Of Three-Phase Distillation Column Using Bubble Point And Φ-Φ Approach en_US
type Article en_US
identifier.pagination 43-64 en_US
identifier.volume 8 en_US


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