Tracer Response in a Packed Bed Reactor
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Consider an isothermal packed bed reactor (PBR) of length . Assume that a tracer pulse enters at , with . For a closed-closed vessel, the Danckwerts boundary conditions apply: and . Initially, . The turbulent flow of the fluid in the pipe is characterized by the velocity .
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Contributed by: Housam Binous, Farrukh Shehzad, Mohammad Mozahar Hossain, Abdullah A. Shaikh, and Ahmed Bellagi (January 2016)
(King Fahd University of Petroleum and Minerals, KSA; ENIM, University of Monastir, Tunisia)
Open content licensed under CC BY-NC-SA
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The theoretical value of the variance was first derived by van der Laan [2] in 1958:
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References
[1] O. Levenspiel, Chemical Reaction Engineering, New York: John Wiley & Sons, 1999.
[2] E. T. van der Laan, Chemical Engineering Science, 7(3), 1958 pp. 187–191. doi:10.1016/0009-2509(58)80025-1.
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