## Abstract The pressure drop and mass transfer efficiency for twoβphase 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 0.073βm diameter column, with an element composed of a
Estimation of the Mass-Transfer Efficiency in Catalytic Distillation in a Packed Column
β Scribed by V. V. Dil'man; V. A. Lotkhov; A. A. Lipatova; S. Ya. Kvashnin; N. N. Kulov
- Publisher
- Springer
- Year
- 2005
- Tongue
- English
- Weight
- 78 KB
- Volume
- 39
- Category
- Article
- ISSN
- 0040-5795
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