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Selective hydrogenation and mass transfer in a fixed-bed catalytic reactor with gas-liquid concurrent upflow

✍ Scribed by Satoshi Mochizuki; Tatsuro Matsui


Publisher
American Institute of Chemical Engineers
Year
1976
Tongue
English
Weight
528 KB
Volume
22
Category
Article
ISSN
0001-1541

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✦ Synopsis


Abstract

Reaction rates of selective hydrogenation of phenylacetylene (PA) and styrene were studied in a packed‐bed reactor with concurrent gas and liquid upflow. The surface reaction rates were expressed by the reaction between adsorbed PA or styrene and dissociated hydrogen atoms competing for the same active sites. The contributions of mass transfer rate were determined, and better selectivity conditions were discussed.


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Gas-Liquid Mass Transfer in Fibrous Bed
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## Abstract In this work, the gas‐liquid mass transfer in a lab‐scale fibrous bed reactor with liquid recycle was studied. The volumetric gas‐liquid mass transfer coefficient, __k__~L~__a__, is determined over a range of the superficial liquid velocity (0.0042–0.0126Β m.s^–1^), gas velocity (0.006–0