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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.
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.