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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received October 15, 2013
Accepted February 1, 2014
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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Sequential simulation of packed distillation columns using rate-based model

Department of Chemical Engineering, Dong-A University, 840, Hadan-dong, Saha-gu, Busan 604-714, Korea
Korean Journal of Chemical Engineering, June 2014, 31(6), 944-948(5), 10.1007/s11814-014-0039-x
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Abstract

Though a packed column has continuous internal structure from top to bottom, the design procedure of the column handles it like the trayed column in both the equilibrium-stage design and the rate-based model design. The differential equation of material balance is good for the continuous phase of the packed column. But the counter flow of vapor and liquid streams makes solving the differential equation difficult. We propose a sequential solving procedure of the packed-column model using an iterative computation. The computed results for the systems of methanol/ethanol, ethanol/n-propanol and methanol/n-propanol were compared with the experimental results to examine the usefulness of the proposed procedure for the simulation of the packed column. The comparison indicates that the proposed procedure predicts satisfactory results of column profiles in the packed column.

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