Effects of Decrease in Gas Volume due to Reactions on the Fluidization Quality in a Fluidized Catalyst Bed
Author:
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/kakoronbunshu/30/3/30_3_256/_pdf
Reference13 articles.
1. Defluidization phenomena during the pyrolysis of two plastic wastes
2. Methanation of carbon dioxide and fluidization quality in a fluid bed reactor—the influence of a decrease in gas volume
3. Emulsion phase expansion and sedimentation velocity in fluidized beds of fine particles.
4. A model for predicting the relationship between maximum voidage in homogeneous fluidization and emulsion phase voidage in bubbling fluidization.
5. Relationship between apparent bed viscosity and fluidization quality in a fluidized bed with fine particles.
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1. 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
2. An emulsion phase condensation model to describe the defluidization behavior for reactions involving gas-volume reduction;Chemical Engineering Journal;2012-08
3. Prevention of Defluidization by Recycling Unreacted Gas for Reactions Involving Gas Volume Reduction in a Fluidized Bed;KAGAKU KOGAKU RONBUNSHU;2012
4. Prevention of defluidization by gas dilution for reactions involving gas–volume reduction;Chemical Engineering Journal;2011-02
5. Analysis of fluidization quality of a fluidized bed with staged gas feed for reactions involving gas-volume reduction;AIChE Journal;2010
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