Comparison of three-phase kinetic measurements between a coiled tubular flow reactor and an improved basket type batch reactor.
Author:
Affiliation:
1. Kinuura Research Center, JGC Corporation
2. Department of Chemical Engineering, Nagoya University
Publisher
Society of Chemical Engineers, Japan
Subject
General Chemical Engineering,General Chemistry
Link
http://www.jstage.jst.go.jp/article/jcej/28/3/28_3_329/_pdf
Reference7 articles.
1. 1) Collins, G. M., R. K. Hess and A. Akgerman; Chem. Eng. Comm., 35, 281–291 (1985)
2. Kimetic studies on liquid-phase hydrogenation of 1-methylnaphthalene using an improved basket reactor.
3. 3) Ramachandran, P. A. and R. V. Chaudhari; Three-Phase Catalytic Reactors, p. 359–380, Gordon and Breach Science Publishers, New York (1983)
4. 4) Shah, Y. T.; Gas-Liquid-Solid Reactor Design, p. 9–18, McGraw-Hill, New York (1979)
5. Equilibrium constants from a modified Redlich-Kwong equation of state
Cited by 2 articles. 订阅此论文施引文献 订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献
1. Trickle bed reactor diluted with fine particles and coiled tubular flow-type reactor for kinetic measurements without external effects;Catalysis Today;1999-01
2. Vapor-phase kinetics and its contribution to global three-phase reaction rate in hydrogenation of 1-methylnaphthalene;Catalysis Today;1999-01
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