Gas Pressure Drop and Mass Transfer Characteristics in a Cross-flow Rotating Packed Bed with Porous Plate Packing-Reference-Cited by-同舟云学术

Gas Pressure Drop and Mass Transfer Characteristics in a Cross-flow Rotating Packed Bed with Porous Plate Packing

Published:2010-03-24 Issue:8 Volume:49 Page:3732-3740
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Jiao Wei Zhou¹,Liu You Zhi¹,Qi Gui Sheng¹

Affiliation:

1. Research Center of Shanxi Province for High Gravity Chemical Engineering and Technology, North University of China, Taiyuan 030051, People’s Republic of China

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/ie9009777

Reference28 articles.

1. Formaldehyde process intensification through gas heat capacity

2. Process intensification in trickle-bed reactors

3. Process intensification: spinning disk reactor for styrene polymerisation

4. Process intensification: Visual study of liquid maldistribution in rotating packed beds

5. Distillation Studies in a High-Gravity Contactor

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