Journal of Zhejiang University SCIENCE A
ISSN 1673-565X(Print), 1862-1775(Online), Monthly
2009 Vol. 10 No. 5 p. 758~766
On-line Access Date: May 11, 2009Simulated moving bed separation of tocopherol homologues: simulation and experiments
Yu-bin L܆1,2, Bao-gen SU†‡1, Yi-wen YANG1, Qi-long REN1, Ping-dong WU1
(1National Laboratory of Secondary Resources Chemical Engineering, Zhejiang University, Hangzhou 310027, China)
(2Hangzhou Zhongmei Huadong Pharmaceutical Co., Ltd., Hangzhou 310011, China)
‡ Corresponding Author
†E-mail: lvyubin2001@zju.edu.cn; subg@zju.edu.cn
Received June 1, 2008; revision accepted Nov. 11, 2008; Crosschecked Feb. 25, 2009
Abstract: Chromatograms of tocopherol homologues were obtained by a column of analytical size (inner diameter (ID) 0.46 cm cm×10 cm) packed with silica gel. Adsorption isotherms and film mass-transfer coefficient were estimated from the chromatograms by using a general rate model, which considers axial dispersion, external mass-transfer and intraparticle diffusion. Based on the obtained isotherms and mass-transfer coefficient, the separation process of tocopherol homologues on simulated moving bed (SMB) was simulated using the same model. According to the simulated results, a mixture of α-, γ-, δ-tocopherols and other impurities was separated on an SMB equipment. The SMB equipment was composed of 8 columns of ID 2 cm×10 cm, with 2 columns in each section. The solid phase was silica gel, and the mobile phase was n-hexane/2-propanol (99/1 by volume). γ- and δ-tocopherols of purity greater than 98% were obtained with recovery greater than 98%. The effects of operating conditions (flow rates and switching time) on the performance of SMB were studied by both simulation and experiments. It was found that all the simulation results were quite close to the experimental results. We conclude that process development and optimization of operating conditions of SMB by simulation are feasible.
Key words: Simulated moving bed (SMB), Separation, Modeling, Simulation, Tocopherol homologues
doi:10.1631/jzus.A0850108 CLC number: TQ028.3
References:
[1] Bruce, P., 1998. Simulated moving bed processing: escape from the high-cost box. Journal of Chromatography A, 827(2):143-160.
[2] Chung, S.F., Wen, C.Y., 1968. Longitudinal dispersion of liquid flowing through fixed and fluidized beds. AIChE Journal, 14(6):857-866.
[3] Dunnebier, G., Klatt, K.U., 2000. Modeling and simulation of nonlinear chromatographic separation process: a comparison of different modeling approaches. Chemical Engineering Science, 55(21):373-380.
[4] Gu, T., 1995. Mathematical Model and Scale-up of Liquid Chromatography. Springer, Berlin.
[5] Gu, T., Zheng, Y., 1999. A study of the scale-up of reversed-phase liquid chromatography. Separation and Purification Technology, 15(1):41-58.
[6] Jupke, A., Epping, A., Schmidt-Traub, H., 2002. Optimal design of batch and simulated moving bed chromatographic separation processes. Journal of Chromatography A, 944(1-2):93-117.
[7] LÜ, Y.B., 2006. Study on Separating Natural Products with Simulated Moving Bed. PhD Thesis, Zhejiang University, Hangzhou, China (in Chinese).
[8] LÜ, Y.B., Wei, F., Shen, B., Ren, Q.L., Wu, P.D., 2006. Modeling, simulation of a simulated moving bed for separation of phosphatidylcholine from soybean phospholipids. Chinese Journal of Chemical Engineering, 14(2):171-177.
[9] Ma, Z., Wang, N.H.L., 1997. Design of simulated moving bed chromatography using standing wave analysis: linear systems. AIChE Journal, 43(10):2488-2508.
[10] Mackie, J.S., Meares, P., 1955. The Diffusion of Electrolytes in a Cation Exchange Resin Membrane. Proceedings of the Royal Society of London. Series A, 232:498-509.
[11] Mazzotti, M., Storti, G., Morbidelli, M., 1997. Optimal operation of simulated moving bed units for nonlinear chromatographic separations. Journal of Chromatography A, 769(1):3-24.
[12] Migliorini, C., Mazzotti, M., Morbidelli, M., 1998. Continuous chromatographic separation through simulated moving beds under linear and nonlinear conditions. Journal of Chromatography A, 827(2):161-173.
[13] Minceva, M., Rodrigues, A.E., 2002. Modeling and simulation of a simulated moving bed for the separation of p-xylene. Industrial & Engineering Chemistry Research, 41(14): 3454-3461.
[14] Ruthven, D.M., Ching, C.B., 1989. Counter-current and simulated counter-current adsorption separation process. Chemical Engineering Science, 44(5):1011-1038.
[15] Schulte, M., Strube, J., 2001. Preparative enantioseparation by simulated moving bed chromatography. Journal of Chromatography A, 906(1-2):399-416.
[16] Wilke, C.R., Chang, P.C., 1955. Correlations of diffusion coefficients in dilute solutions. AIChE Journal, 1(2):264.
[17] Xie, Y., Hritzko, B., Chin, C.Y., Wang, N.H.L., 2003. Separation of FTC-ester enantiomers using a simulated moving bed. Industrial & Engineering Chemistry Research, 42(17):4055-4067.
[18] Yang, Y.W., Wen, G.D., Wu, C.J., Ren, Q.L., Wu, P.D., 2004. Preparation of natural α-tocopherol from non-α-tocopherols. Journal of Zhejiang University SCIENCE, 5(12):1524-1527.
[19] Zhong, G.M., Guiochon, G., 1998. Steady-state analysis of simulated moving bed chromatography using the linear, ideal model. Chemical Engineering Science, 53(6):1121- 1130.