HYDROGENATION OF 1,5-CYCLOOCTADIENE IN A TRICKLE BED REACTOR ACCOMPANIED BY PHASE TRANSITION
作者:
JIŘÍ HANIKA,
BORISN. LUKJANOV,
VALERIJA. KIRILLOV,
VLADIMÍR STANĚK,
期刊:
Chemical Engineering Communications
(Taylor Available online 1986)
卷期:
Volume 40,
issue 1-6
页码: 183-194
ISSN:0098-6445
年代: 1986
DOI:10.1080/00986448608911696
出版商: Taylor & Francis Group
关键词: Trickle bed reactor;Phase transition;Mathematical model;1,5-Cyclooctadiene hydrogenation;Reaction mixture evaporation
数据来源: Taylor
摘要:
This paper examined the evaporation and condensation of the reaction mixture within the trickle bed reactor during 1,5-cyclooctadiene hydrogenation. The aim of study has been to formulate a mathematical model of heat and mass transfer influenced the exothermic reaction of a volatile reaction mixture apt to evaporation by the reaction heat in the system which is often accompanied by a hot spot temperature formation in the reactor followed by the enhancement of undesirable side reactions and/or catalyst deactivation. The numerical solution of the proposed model agreed quite well with the experimental temperature profiles in the trickle bed reactor.
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