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Received November 15, 2001
Accepted January 16, 2002
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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
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Approximate Design of Fully Thermally Coupled Distillation Columns
Dept. of Chem. Eng., Dong-A University, Busan 604-714, Korea 1Energy-Efficient Chemical Systems Group, National Institute of Advanced Industrial Science and Technology, Tsukuba 305-8565, Japan 2Dept. of Chemical Engineering, Pusan National University, Busan 609-735, Japan
Korean Journal of Chemical Engineering, May 2002, 19(3), 383-390(8), 10.1007/BF02697144
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Abstract
An approximate design procedure for fully thermally coupled distillation columns (FTCDCs) is proposed and applied to example ternary systems. The procedure gives a fast solution of structural and operation design for a preliminary study of the FTCDC. The structural information resolves the design difficulty, caused from the interlinking streams of the column, which is encountered when a conventional design procedure is implemented. The design outcome explains that how the thermodynamic efficiency of the FTCDC is higher than that of a conventional two-column system and how the system of a separate prefractionator is different from a dividing wall structure. From the design result of three example systems with three different feed compositions, the useful performance of the proposed scheme is proved. In addition, the structural design of the FTCDC gives better understanding of the system and_x000D_
leads to high efficiency design of the column.
Keywords
References
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Agrawal R, Fidkowski ZT, Ind. Eng. Chem. Res., 37(8), 3444 (1998)
Annakou O, Mizsey P, Ind. Eng. Chem. Res., 35(6), 1877 (1996)
Carlberg NA, Westerberg AW, Ind. Eng. Chem. Res., 28, 1386 (1989)
Cerda J, Westerberg AW, Ind. Eng. Chem. Process Des. Dev., 20, 546 (1981)
Chavez CR, Seader JD, Wayburn TL, Ind. Eng. Chem. Fundam., 25, 566 (1986)
Douglas JM, "Conceptual Design of Chemical Processes," McGraw-Hill Book Co., New York, U.S.A., 569 (1988)
Dunnebier G, Pantelides CC, Ind. Eng. Chem. Res., 38(1), 162 (1999)
Fidkowski Z, Krolikowski L, AIChE J., 32, 537 (1986)
Glinos KN, Malone MF, Ind. Eng. Chem. Process Des. Dev., 24, 822 (1985)
Glinos KN, Malone MF, Ind. Eng. Chem. Process Des. Dev., 24, 1087 (1985)
Glinos KN, Malone MF, Chem. Eng. Res. Des., 66, 229 (1988)
Gmehling J, Onken U, Arlt W, "Vapor-Liquid Equilibrium Data Collection," Dechema, Frankfurt/Main, Germany, Vol. I, Part 1, 2b and 6a, 562, 504, 649 (1980)
Kim YH, Luyben WL, Chem. Eng. Commun., 128, 65 (1994)
Kim YH, Korean J. Chem. Eng., 17(5), 570 (2000)
Kim YH, Ind. Eng. Chem. Res., 40(11), 2460 (2001)
Kim YH, Chem. Eng. J., 85(2-3), 289 (2002)
King CJ, "Separation Processes," 2nd ed., McGraw-Hill, New York, 235-237, 421 (1980)
Lee YS, Kim MG, Ha DM, Oda A, Ito C, Aragaki T, Mori H, Korean J. Chem. Eng., 14(5), 321 (1997)
Lestak F, Egenes D, Yoda H, Hamnett C, "Kellogg Divided Wall Column Technology for Ternary Separation," Proc. The 5th Int. Symposium on Sep. Tech. between Korea and Japan, 233 (1999)
McCabe WL, Smith JC, "Unit Operations of Chemical Engineering," 3rd ed., McGraw-Hill Book Co., New York, 568 (1976)
Midori S, Nakahashi A, "Industrial Application of Continuous Distillation Columns with Vertical Partition," Proc. The 5th Int. Symposium on Sep. Tech. Between Korea and Japan, 221 (1999)
Petlyuk FB, Platonov VM, Slavinskii DM, Ind. Eng. Chem., 5, 555 (1965)
Seader JD, Henley EJ, "Separation Process Principles," John Wiley & Sons, Inc., New York, 510 (1998)
Triantafyllou C, Smith R, Trans. IChemE, 70(A), 118 (1992)
Underwood AJV, Chem. Eng. Prog., 44, 603 (1948)
Underwood AJV, Chem. Eng. Prog., 45, 609 (1949)
Wang JC, Henke GE, Hydrocarb. Process., 45, 155 (1966)
Wolff EA, Skogestad S, Ind. Eng. Chem. Res., 34(6), 2094 (1995)
Yoo KP, Lee KS, Lee WH, Park HS, Korean J. Chem. Eng., 5(2), 123 (1988)
