## Abstract The pressure drop and mass transfer efficiency for twoโphase flow in a structured packed column were simulated using a commercial CFD package, CFX version 10. The distillation of the methanol/isopropanol system was carried out in a 0.073โm diameter column, with an element composed of a
โฆ LIBER โฆ
A study of mass transfer behaviour in a catalytic distillation column
โ Scribed by Chuncheng Huang; Gary G. Podrebarac; Flora T. T. Ng; Garry L. Rempel
- Publisher
- John Wiley and Sons
- Year
- 1998
- Tongue
- English
- Weight
- 902 KB
- Volume
- 76
- Category
- Article
- ISSN
- 0008-4034
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