Gas−Liquid Interfacial Area and Holdup in a Cocurrent Upflow Packed Bed Bubble Column Reactor at Elevated Pressures
Author:
Affiliation:
1. Department of Chemical Engineering, Chemical Reaction Engineering Laboratories, Twente University, P.O. Box 217, 7500 AE Enschede, The Netherlands
Publisher
American Chemical Society (ACS)
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/ie960188o
Reference29 articles.
1. Gas-liquid mass transfer coefficients for cocurrent upflow in packed beds - effect of packing shape at low flow rates
2. Mass Transfer in Packed Beds with Two-Phase Flow
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