Abstract: AIChE JournalVolume 30, Issue 3 p. 500-502 R & D Note Gas-particle mass transfer in trickle beds Pan Zheng Lu, Pan Zheng Lu University of California, Davis, CA 95616Search for more papers by this authorJ. M. Smith, J. M. Smith University of California, Davis, CA 95616Search for more papers by this authorMordechay Herskowitz, Mordechay Herskowitz Ben Gurien University of the Negev Beer, Sheva, IsraelSearch for more papers by this author Pan Zheng Lu, Pan Zheng Lu University of California, Davis, CA 95616Search for more papers by this authorJ. M. Smith, J. M. Smith University of California, Davis, CA 95616Search for more papers by this authorMordechay Herskowitz, Mordechay Herskowitz Ben Gurien University of the Negev Beer, Sheva, IsraelSearch for more papers by this author First published: May 1984 https://doi.org/10.1002/aic.690300326Citations: 9AboutPDF ToolsRequest permissionExport citationAdd to favoritesTrack citation ShareShare Give accessShare full text accessShare full-text accessPlease review our Terms and Conditions of Use and check box below to share full-text version of article.I have read and accept the Wiley Online Library Terms and Conditions of UseShareable LinkUse the link below to share a full-text version of this article with your friends and colleagues. Learn more.Copy URL No abstract is available for this article. Literature Cited Dwivedi, P. N., and S. N., Upadhyay, “Particle-Fluid Mass Transfer in Fixed and Fluidized Beds,” Ind. Eng. Chem., Process Design and Dev., 16, p. 157 (1977). Gianetto, A., V., Specchia, and G. Baldi, “Absorption in Packed Towers with Concurrent Downward High-Velocity Flow. II: Mass Transfer,” AIChE J., 19, 916 (1973). Goto, S., J., Levec, and J. M. Smith, “Mass Transfer in Packed Beds with Two-Phase Flow,” Ind. and Eng. Chem., Prog. Design and Dev., 14, 473 (1975). Herskowitz, M., R. G., Carbonell, and J. M. Smith, “Effectiveness Factors and Mass Transfer in Trickle-Bed Reactors,” AIChE J., 25, 272 (1979). Herskowitz, M., and S., Mosseri, “ Global Rate of Reaction in Trickle Bed Reactors; Effect of Gas and Liquid Flow Rates,” Ind. and Eng. Chem. Fund. (1982). Reiss, L. P., “Cocurrent Gas-Liquid Contacting in Packed Columns,” Ind. Eng. Chem. Proc. Design Dev., 6, p. 486 (1967). Satterfield, C. N., “Trickle-Bed Reactors,” AIChE J., 21, 209 (1975). Tan, C. S., and J. M., Smith, “Catalyst Particle Effectiveness with Unsymmetrical Boundary Conditions,” Chem. Eng. Sci., 35, 1601 (1980). Citing Literature Volume30, Issue3May 1984Pages 500-502 ReferencesRelatedInformation
Publication Year: 1984
Publication Date: 1984-05-01
Language: en
Type: article
Indexed In: ['crossref']
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Cited By Count: 11
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