Improved Hydrodynamic Model for Wetting Efficiency, Pressure Drop, and Liquid Holdup in Trickle-Bed Reactors
Author:
Affiliation:
1. Chemical Engineering and Plant Design, Helsinki University of Technology, POB 6100, FIN-02015 HUT, Finland, VTT Technical Research Centre of Finland, POB 1000, FIN-02044 VTT, Finland, and Neste Jacobs Oy, POB 310, 06101 Porvoo, Finland
Publisher
American Chemical Society (ACS)
Subject
Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/ie8003754
Reference60 articles.
1. Modeling of Gas−Liquid Packed-Bed Reactors with Momentum Equations and Local Interaction Closures
2. Catalyst bed dilution for improving catalyst wetting in laboratory trickle-bed reactors
3. Evaluation of liquid-solid contacting in trickle-bed reactors by tracer methods
4. Solid-liquid contacting effectiveness in trickle bed reactors
5. Solid-Liquid Mass Transfer in Concurrent Two-Phase Flow through Packed Beds
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