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In relation to this article, we declare that there is no conflict of interest.
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Received March 27, 2006
Accepted June 19, 2006
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Simulation of protein adsorption in a batchwise affinity chromatography with a modified rate model

Nuclear Research Center for Agriculture & Medicine, AEOI, P.O. Box 31585-4395, Karaj, Iran 1Chemical Engineering Research Center, East China University of Science and Technology, Shanghai, 200237, China
Korean Journal of Chemical Engineering, November 2006, 23(6), 997-1002(6), 10.1007/s11814-006-0020-4
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Abstract

A rate model was adapted to simulate the dynamics of protein adsorption. This model takes axial dispersion and film mass transfer into account where there is a nonlinear adsorption isotherm for protein. The model equations were solved with the application of orthogonal collocation method on finite elements. The model is validated with experimental adsorption of urokinase in a batchwise column chromatographic process. Adsorption kinetics and isotherm were measured in a batchwise operation. With the assumption of back mixing at the column inlet, the effect of the different flow pattern on the concentration change inside the column can be simulated with the rate model.

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