A MATHEMATICAL MODEL OF THE PROCESS WITH PHASE TRANSITION ON THE POROUS CATALYST PELLET
Author:
Affiliation:
1. a Computing Center, Siberian Branch, the USSR Academy of Sciences , Novosibirsk, USSR
2. b Institute of Catalysis, Siberian Branch, the USSR Academy of Sciences , Novosibirsk, USSR
Publisher
Informa UK Limited
Subject
General Chemical Engineering,General Chemistry
Link
https://www.tandfonline.com/doi/pdf/10.1080/00986448308940053
Reference9 articles.
1. Catalyst effectiveness factor and contacting efficiency in trickle-bed reactors
2. Effectiveness factors and mass transfer in trickle-bed reactors
3. Partial wetting in trickle bed reactors — the reduction of crotonaldehyde over a palladium catalyst
4. Catalyst areas wetted by flowing and semistagnant liquid in trickle-bed reactors
5. Mass Transfer and Contacting Efficiency in a Trickle-Bed Reactor
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1. HYSTERESIS AND PHASE TRANSITIONS IN A SINGLE PARTIALLY INTERNALLY WETTED CATALYST PELLET: THERMOGRAVIMETRIC STUDIES;Chemical Engineering Communications;1997-03
2. Reaction rate hysteresis in a single partially internally wetted catalyst pellet: Experiment and modellng;Chemical Engineering Science;1996-04
3. Bimolecular exothermic reaction with vaporization in the half-wetted slab catalyst;Chemical Engineering Science;1993
4. TRANSPORT OF GASES CONTAINING CONDENSABLES IN POROUS SOLIDS;Advances in Transport Processes;1993
5. Partial internal wetting of catalyst particles with a distribution of pore size;AIChE Journal;1989-08
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