Packed column distillation simulation with a rate-based method

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Abstract

A simulation algorithm using a rate-based model is proposed fer multicomponent packed column distillation. The packed column sections are divided into small segments for the modeling. For each packing segment, (6c + 7) MERQ equations are set up and solved by an equation-tearing method with two calculation loops. Calculation of the whole column consists of an iterative segment-wise algorithm with the correction of the bulk vapor composition by the overall normalized θ method for acceleration. The numerical characteristics of the proposed algorithm and some remarks on its application are illustrated using numerical examples and experimental data obtained from a pilot-scale plant.

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Mori, H., Oda, A., Aragaki, T., & Kunimoto, Y. (1996). Packed column distillation simulation with a rate-based method. Journal of Chemical Engineering of Japan, 29(2), 307–314. https://doi.org/10.1252/jcej.29.307

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