Research Article
Dec 1972
Sorption Kinetics in Finite-Bath Systems
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VIEW THE REPLYPublication: Journal of the Sanitary Engineering Division
Volume 98, Issue 6
Abstract
Rates of sorption on activated carbon in rapidly agitated batch reactors can be influenced by both surface mass transfer and internal pore diffusion mechanisms. Mathematic interpretation of kinetic data is further complicated by the characteristic nonlinear equilibrium behavior of many sorbates. A conceptual kinetic model is developed using simplifying assumptions of irreversible adsorption and quasi-steady state. The model in its final form allows for straightforward calculation of diffusion and mass transfer coefficients. Experimental design was found to be critical for successful application of rate data to the model. Molecular size and shape were significant factors in predicting rate-limiting step behavior.
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Published In
Journal of the Sanitary Engineering Division
Volume 98 • Issue 6 • December 1972
Pages: 1021 - 1036
Copyright
© 1972 American Society of Civil Engineers.
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Published in print: Dec 1972
Published online: Feb 12, 2021
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Authors
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Francis A. DiGiano
Asst. Prof., Dept. of Civ. Engrg., Univ. of Massachusetts, Amherst, Mass., USA
Walter J. Weber Jr., M.ASCE
Prof., Dept. of Civ. and Water Resources Engrg., Univ. of Michigan, Ann Arbor, Mich., USA
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