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Study of gas‐to‐liquid mass transfer by dynamic methods in trickle beds

1989; Wiley; Volume: 35; Issue: 1 Linguagem: Inglês

10.1002/aic.690350117

1547-5905

Alberto Goenaga, J. M. Smith, B. J. McCoy,

Heat and Mass Transfer in Porous Media

AIChE JournalVolume 35, Issue 1 p. 159-163 R & D Note Study of gas-to-liquid mass transfer by dynamic methods in trickle beds A. Goenaga, A. Goenaga Department of Chemical Engineering, University of California, Davis, CA 95616Search for more papers by this authorJ. M. Smith, J. M. Smith Department of Chemical Engineering, University of California, Davis, CA 95616Search for more papers by this authorB. J. McCoy, B. J. McCoy Department of Chemical Engineering, University of California, Davis, CA 95616Search for more papers by this author A. Goenaga, A. Goenaga Department of Chemical Engineering, University of California, Davis, CA 95616Search for more papers by this authorJ. M. Smith, J. M. Smith Department of Chemical Engineering, University of California, Davis, CA 95616Search for more papers by this authorB. J. McCoy, B. J. McCoy Department of Chemical Engineering, University of California, Davis, CA 95616Search for more papers by this author First published: January 1989 https://doi.org/10.1002/aic.690350117Citations: 5AboutPDF 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 Share a linkShare onEmailFacebookTwitterLinkedInRedditWechat Literature Cited Bird, R. B., W. E., Stewart and E. N. Lightfoot, Transport Phenomena, 400, John Wiley, New York, (1960). Burghardt, A., and J. M., Smith, “Dynamic Response of a Single Catalyst Pellet,” Chem. Eng. Sci., 34, 267 (1979). Chou, T. S., F. L., Worley, and D. Luss, “Local Particle-Liquid Mass Transfer Fluctuations in Mixed-Phase Cocurrent Downflow through a Fixed Bed in the Pulsing Regime,” Ind. Eng. Chem. Fund., 18, 279 (1979). Eroglu, I., and T., Dogu, “Dynamic Analysis of a Trickle Bed Reactor by Moment Technique,” Chem. Eng. Sci., 38, 801 (1983). Fukushima, S., and K., Kusaka, “Liquid Phase Volumetric and Mass Transfer Coefficient and Boundary of Hydrodynamic Flow Region in Packed Bed Column with Cocurrent Downward Flow,” J. Chem. Eng. Japan, 10, 468 (1977). Goto, S., and J. M., Smith, “Performance of Trickle-Bed Reactors,” AIChE J., 21, No. 4, 714 (July, 1975). Goto, S., J., Levec, and J. M. Smith, “Trickle-Bed Oxidation Reactors,” Ind. Eng. Chem. Proc. Dev., 14, 473 (1975). Herskowitz, M., and J. M., Smith, “Trickle-Bed Reactors: A Review,” AIChE J., 29, 1 (Jan., 1983). Komiyama, H., and J. M., Smith, “Sulfur Dioxide Oxidation in Slurries of Activated Carbon. Part II. Mass Transfer Studies,” AIChE J., No. 4, 670 (July, 1975). Mata, A. R., Mass Transfer and Reactor Studies in a Trickle Bed Reactor, Ph.D. Thesis, U. of CA., Davis, (1980). McCabe, W. L., J. C. Smith, P. Harriott, Unit Operations of Chemical Engineering, 4th Ed., McGraw Hill (1985). Ramachandran, P. A., and J. M., Smith, “Dynamic Behavior of Trickle-Bed Reactors,” Chem. Eng. Sci., 34, 75 (1979). Ramachandran, P. A., and R. V., Chaudhari, Three Phase Catalytic Reactors, Gordon and Breach, New York (1983). Seirafi, H. A., and J. M., Smith, “Mass Transfer and Adsorption in Liquid-Full and Trickle Beds,” AIChE J., 26, No. 5, 711 (Sept., 1980). Shah, Y. T., Gas-Liquid-Solid Reactor Design, McGraw-Hill, New York, (1979). Sylvester, N. D., and P., Pitayagulsarn, “Mass Transfer for Two-Phase Cocurrent Downflow in a Packed Bed,” Ind. Eng. Chem. Proc. Des. Dev., 14, 421 (1975). Tan, C. S., and J. M., Smith, “A Dynamic Method for Liquid-Particle Mass Transfer in Trickle-Beds,” AIChE J., 28, No. 2, 190 (March, 1982). Tosun, G., “A Study of Cocurrent Downflow of Nonfoaming Gas-Liquid Systems in a Packed Bed. Part I. Flow Regimes: Search for a Generalized Flow Map,” Ind. Eng. Chem. Proc. Des. Dev., 23, 29 (1984). Turek, F., and R., Lange, “Mass Transfer in Trickle-Bed Reactors at Low Reynolds Number,” Chem. Eng. Sci., 36, 569 (1981). Ufford, R. C., and J. J., Perona, “Liquid Phase Mass Transfer with Cocurrent Downflow through Packed Towers,” AIChE J., 19, No. 6, 1223 (Nov., 1973). Citing Literature Volume35, Issue1January 1989Pages 159-163 ReferencesRelatedInformation