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Korean Journal of Chemical Engineering, Vol.14, No.5, 321-324, 1997
Analysis of Packed Distillation Columns with a Rate-based Model
Multicomponent packed column distillation is simulated using a rate-based model and the simulation results are compared with the experimental results obtained from a 0.2 m diameter pilot-scale packed column. The simulation algorithm used is previously proposed by the authors, which based on an equation-tearing method for (6c+7) equations of one packing segment and the whole column is solved by an iterative segmentwise calculation with the overall normalized θ method for acceleration. The performance of two packings is examined by simulating the pilot-scale column experiments using the published correlations for estimating liquid and vapor phase mass transfer coefficients and a effective interfacial area.
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[Cited By]
- Kim YH, Nakaiwa M, Hwang KS, Korean Journal of Chemical Engineering, 19(3), 383, 2002
- Pradhan S, Kannan A, Korean Journal of Chemical Engineering, 22(3), 441, 2005
- Poortalari H, Sabet JK, Varaminian F, Korean Journal of Chemical Engineering, 35(5), 1151, 2018
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