Articles & Issues
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received August 5, 2002
Accepted September 27, 2002
-
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
unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.
All issues
Continuous Separation of Glucose and Fructose at High Concentration Using Two-Section Simulated Moving Bed Process
Department of Chemical Engineering, Hankyong National University, 67, Sukjung-dong, Ansung-si, Kyonggi-do 456-749, Korea
Korean Journal of Chemical Engineering, May 2003, 20(3), 532-537(6), 10.1007/BF02705561
Download PDF
Abstract
A two-section simulated moving bed (SMB) modified from a three-section SMB [Barker et al., 1975] was applied to the separation of an aqueous mixture of glucose and fructose at high concentration up to 500 kg/m(3). Dowex 50W-X12 resin of Ca(++) form was used as an adsorbent and water as an isocratic eluent. The equilibrium isotherms in terms of a quadratic expression and a plug flow model with mass transfer effect were used to predict both the products and on-concentrations in the two-section SMB process. The two-section SMB process suggested in this work was successful in obtaining high fructose corn syrup (fructose with 55-90% w/w) at the high concentration of 500 kg/m(3).
References
Barker PE, Critcher D, Chem. Eng. Sci., 13, 82 (1960)
Barker PE, Deeble RE, Chromatographia, 8(2), 67 (1975)
Barker PE, Huntington DH, J. Gas. Chromatogra., 4, 9 (1966)
Broughton DB, Chem. Eng. Prog., 64(8), 60 (1968)
Ching CB, Ruthven DM, Chem. Eng. Sci., 40(6), 877 (1985)
Finlayson BA, "Nonlinear Analysis in Chemical Engineering," McGraw-Hill, New York (1980)
Ganetsos G, Barker PE, "Semicontinuous Countercurrent Chromatographic Refiner," In Preparative and Production Scale Chromatography; Ganetsos, G. and Barker, P.E., Eds., Marcel Dekker, Inc., New York (1993)
Gerald CF, Wheatley PO, "Applied Numerical Analysis," Addison-Wesley Co. (1984)
Hidajat K, Ching CB, Ruthven DM, Chem. Eng. Sci., 41(11), 2953 (1986)
Kim YD, Lee JK, Cho YS, Korean J. Chem. Eng., 18(6), 971 (2001)
Lee KN, Lee WK, Sep. Sci. Technol., 27(3), 295 (1992)
Liapis AI, Rippen DWT, AIChE J., 25, 455 (1979)
Lu ZP, Ching CB, Sep. Sci. Technol., 32(12), 1993 (1997)
Michael S, Jochen S, J. Chromatogr. A, 906, 399 (2001)
Ruthven DM, Ching CB, Chem. Eng. Sci., 44(5), 1011 (1989)
Villadsen J, Michelson ML, "Solution of Differential Equation Models by Polynomial Approximation," Prentice Hall, Englewood Cliffs, NJ (1980)
Won JH, Cho YS, Kim YD, Ahn DJ, HWAHAK KONGHAK, 39(6), 685 (2001)
Barker PE, Deeble RE, Chromatographia, 8(2), 67 (1975)
Barker PE, Huntington DH, J. Gas. Chromatogra., 4, 9 (1966)
Broughton DB, Chem. Eng. Prog., 64(8), 60 (1968)
Ching CB, Ruthven DM, Chem. Eng. Sci., 40(6), 877 (1985)
Finlayson BA, "Nonlinear Analysis in Chemical Engineering," McGraw-Hill, New York (1980)
Ganetsos G, Barker PE, "Semicontinuous Countercurrent Chromatographic Refiner," In Preparative and Production Scale Chromatography; Ganetsos, G. and Barker, P.E., Eds., Marcel Dekker, Inc., New York (1993)
Gerald CF, Wheatley PO, "Applied Numerical Analysis," Addison-Wesley Co. (1984)
Hidajat K, Ching CB, Ruthven DM, Chem. Eng. Sci., 41(11), 2953 (1986)
Kim YD, Lee JK, Cho YS, Korean J. Chem. Eng., 18(6), 971 (2001)
Lee KN, Lee WK, Sep. Sci. Technol., 27(3), 295 (1992)
Liapis AI, Rippen DWT, AIChE J., 25, 455 (1979)
Lu ZP, Ching CB, Sep. Sci. Technol., 32(12), 1993 (1997)
Michael S, Jochen S, J. Chromatogr. A, 906, 399 (2001)
Ruthven DM, Ching CB, Chem. Eng. Sci., 44(5), 1011 (1989)
Villadsen J, Michelson ML, "Solution of Differential Equation Models by Polynomial Approximation," Prentice Hall, Englewood Cliffs, NJ (1980)
Won JH, Cho YS, Kim YD, Ahn DJ, HWAHAK KONGHAK, 39(6), 685 (2001)
