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Korean Journal of Chemical Engineering, Vol.17, No.5, 570-573, 2000
Design of a Fully Thermally Coupled Distillation Column Based on Dynamic Simulations
A dynamic simulation of a fully thermally coupled distillation column is conducted for the design of a possible operation schemer and its performance is examined with an example process of butanol isomer ternary system. The outcome of the dynamic simulation indicates that the column can be operated by using a 3x3 control structure. The structure consists of three controlled variables of the compositions of overhead, bottom and side products and three manipulated variables of the flow rates of reflux and steam and liquid split ratio between a main column and a prefractionator.
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[Cited By]
- Lee JC, Yeo YK, Song KH, Kim IW, Korean Journal of Chemical Engineering, 18(4), 428, 2001
- Kim YH, Nakaiwa M, Hwang KS, Korean Journal of Chemical Engineering, 19(3), 383, 2002
- Kim YH, Choi DW, Hwang KS, Korean Journal of Chemical Engineering, 20(4), 755, 2003
- Segovia-Hernandez JG, Bonilla-Petriciolet A, Salcedo-Estrada LI, Korean Journal of Chemical Engineering, 23(5), 689, 2006
- Cho J, Kim DM, Korean Journal of Chemical Engineering, 24(3), 438, 2007
- Lee SH, Shamsuzzoha M, Han M, Kim YH, Lee M, Korean Journal of Chemical Engineering, 28(2), 348, 2011
- Tian W, Guo Q, Sun S, Korean Journal of Chemical Engineering, 29(1), 9, 2012
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