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Analysis of Packed Distillation Columns with a Rate-based Model
Korean Journal of Chemical Engineering, September 1997, 14(5), 321-324(4), 10.1007/BF02707046
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Abstract
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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References
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Bravo JL, Rocha JA, Fair JR, Hydrocarb. Process., 64(1), 91 (1985)
Brunazzi E, Nadini G, Paglianti A, Petarca L, Chem. Eng. Technol., 18, 248 (1985)
Chilton TH, Colburn AP, Ind. Eng. Chem., 6, 1183 (1934)
Daubert TE, Danner RP, "Physical and Thermodynamic Properties of Pure Chemicals Data Compilation," Hemisphere Publishing Co., New York (1989)
Fair JR, Bravo JL, Chem. Eng. Prog., 86(1), 19 (1990)
Fair JR, Bravo JL, J. Chem. Eng. Symp. Ser., 104, A138 (1987)
HenriquesdeBrio M, VonStocker U, Bomio P, J. Chem. Eng. Symp. Ser., 128, B137 (1992)
Debrito MH, Vonstockar U, Bangerter AM, Bomio P, Laso M, Ind. Eng. Chem. Res., 33(3), 647 (1994)
Krishnamurthy R, Taylor R, AIChE J., 31, 449 (1985)
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Mori H, Oda A, Aragaki T, Kunimoto Y, J. Chem. Eng. Jpn., 29(2), 307 (1996)
Reid RC, Prausnitz JM, Poling B, "The Properties of Gases and Liquids," 4th ed., McGraw-Hill, New York (1987)
Tochigi K, Tiegs D, Gmehling J, Kojima K, J. Chem. Eng. Jpn., 23, 454 (1990)
Taylor R, Kooijman A, Chem. Eng. Commun., 102, 87 (1991)
Weiland RH, Ahlgren KR, Evans M, Ind. Eng. Chem. Res., 32, 1411 (1993)
