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Ozone transfer with optimal design of a new gas-induced reactor

✍ Scribed by Yung-Chien Hsu; Chyuan-Jih Huang


Publisher
American Institute of Chemical Engineers
Year
1997
Tongue
English
Weight
643 KB
Volume
43
Category
Article
ISSN
0001-1541

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## 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