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Rate-Based Model in Bubble Cap Batch Distillation Column - Salah S. Ibrahim

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2017-04-03
91,74 € 141,14 €

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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 ... Visas aprašymas

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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.

Daugiau informacijos

Autorius Salah S. Ibrahim
Leidėjas Scholars' Press
Išleidimo metai 2017
Viršelio tipas Minkšti viršeliai
EAN 9783330651265
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91,74 € 141,14 €