Elimination of Defluidization Caused by Reactions Involving a Volume Reduction in a Fluidized Catalyst Bed and Improvement of Fluidization by Two-Stage Feeding-Reference-Cited by-同舟云学术

Elimination of Defluidization Caused by Reactions Involving a Volume Reduction in a Fluidized Catalyst Bed and Improvement of Fluidization by Two-Stage Feeding

Published:2009 Issue:10 Volume:42 Page:733-738
ISSN:0021-9592
Container-title:JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
language:en
Short-container-title:J. Chem. Eng. Japan

Author:

Kai Takami¹,Furukawa Mitsunobu¹,Toriyama Kei-ich¹,Nakazato Tsutomu¹,Nakajima Mitsuyuki²

Affiliation:

1. Department of Applied Chemistry and Chemical Engineering, Kagoshima University

2. Ishikawajima Plant Engineering & Construction Co., Ltd.

Publisher

Society of Chemical Engineers, Japan

Subject

General Chemical Engineering,General Chemistry

Link

http://www.jstage.jst.go.jp/article/jcej/42/10/42_08we235/_pdf

Reference10 articles.

1. Methanation of carbon dioxide and fluidization quality in a fluid bed reactor—the influence of a decrease in gas volume

2. Formation of particle agglomerates after switching fluidizing gases

3. Kinetics of the methanation of carbon dioxide over a supported Ni-La2O3catalyst

4. Effect of gas adsorption on defluidization after switching fluidizing gases

5. Effects of Decrease in Gas Volume due to Reactions on the Fluidization Quality in a Fluidized Catalyst Bed

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1. Effect of Gas Volume Expansion on Bubble Behavior in Fluidized Catalyst Beds;Journal of Chemical Engineering of Japan;2024-06-28

2. Range of Particle Properties Inducing Defluidization after Gas Switching in a Fluidized Bed;KAGAKU KOGAKU RONBUNSHU;2018-07-20

3. Pressure Fluctuation Analysis of the Defluidization Caused by a Reaction Involving Gas-Volume Reduction in a Fluidized Catalyst Bed;Journal of Chemical Engineering of Japan;2015

4. Visualization of defluidization phenomena caused by gas switching in a two-dimensional fluidized bed;Powder Technology;2013-03

5. Gas recycling in fluidized bed to avoid defluidization for reactions accompanied by decrease in the number of moles;Chemical Engineering Journal;2013-01