Modelling and Simulation of the Monolithic Reactor for Gas-Liquid-Solid Reactions
A Mathematical Model and Process Simulations of a Monolith Reactor Operated in Film and Slug Flow Was Presented. the Three-Phase Hydrogenation of Alpha-Methylstyrene into Cumene and a Consecutive Reaction System Were Used as Model Reactions. Hydrogenation Kinetic Parameters Were Estimated by Experimental Data from a Laboratory Batch Reactor. the Simulations for Both Monolithic and Trickle-Bed Reactors Were Conducted under Optimum Operating Conditions of Each System. the Monolith Reactor Had Higher Selectivity and Increased Product Yield. the Improved Performance of Monolithic Reactors over Trickle-Bed Reactors Could Lead to a Justification for Replacing These Traditional Reactors in Many Industrial Applications. This is an Abstract of a Paper Presented at the 7th World Congress of Chemical Engineering (Glasgow, Scotland 7/10-14/2005).
T. Bauer et al., "Modelling and Simulation of the Monolithic Reactor for Gas-Liquid-Solid Reactions," 7th World Congress of Chemical Engineering, GLASGOW2005, incorporating the 5th European Congress of Chemical Engineering, p. 38, Elsevier, Dec 2005.
The definitive version is available at https://doi.org/10.1205/cherd.04335
Chemical and Biochemical Engineering
International Standard Book Number (ISBN)
Article - Conference proceedings
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01 Dec 2005
Technische Universität Dresden, Grant None