Rate-Based Model in Bubble Cap Batch Distillation Column - S. Ibrahim, Salah
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The dynamic behavior of trayed batch distillation column has been studied theoretically and experimentally. The experimental work was performed through using a batch distillation column consisting of eight bubble-cup trays. A zeotropic (nonazeotropic) system of Benzene, Toluene, and Ethylbenzene (B-T-EB) had been used. The theoretical study was performed through modeling that including of coupling mass and energy transfer between vapor and liquid phases so-called ¿Nonequilibrium (or Rate)-Based modeling¿. This study will be useful for researchers whose work on transport phenomena modeling.

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Produktbeschreibung
The dynamic behavior of trayed batch distillation column has been studied theoretically and experimentally. The experimental work was performed through using a batch distillation column consisting of eight bubble-cup trays. A zeotropic (nonazeotropic) system of Benzene, Toluene, and Ethylbenzene (B-T-EB) had been used. The theoretical study was performed through modeling that including of coupling mass and energy transfer between vapor and liquid phases so-called ¿Nonequilibrium (or Rate)-Based modeling¿. This study will be useful for researchers whose work on transport phenomena modeling.
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Autorenporträt
Ph.D.Chemical Engineering University of Technology Iraq 2007.M.Sc.Chemical Engineering University of Technology Iraq 2000.B.Sc.Chemical Engineering University of Technology Iraq 1997.Academic Positions in Chem.Eng.Dept.University of Technology.Iraq.2002-2007. Assistant Lecturer. 2007 - 2015. Lecturer. 2015 - present. Assistant Professor.