Rate-Based Model in Bubble Cap Batch Distillation Column - Salah S. Ibrahim
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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 ... Pilns apraksts
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Aprašymas
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.
Vairāk informācijas
| Autors | Salah S. Ibrahim |
|---|---|
| Izdevējs | Scholars' Press |
| Izlaides gads | 2017 |
| Vāka tips | Mīkstais vāks |
| EAN | 9783330651265 |