Design of SMB for a nonlinear amino acid system with mass‐transfer effects

A standing wave design (SWD) method and an experimental shortcut design method are developed in this study for SMB systems with nonlinear isotherms and mass-transfer effects (nonideal systems). In the SWD, the mass-transfer correction terms derived in a previous study for linear, nonideal systems are incorporated into the design equations for nonlinear, nonideal systems. The SWD requires accurate isotherm and mass-transfer parameters to ensure high product purity and high yield. If these parameters are unknown, the experimental shortcut design can be applied. Frontal experiments with a binary mixture at a fixed feed concentration and three or more different flow rates are needed to formulate a series of empirical correlations for the SMB design. The two methods were tested for the binary separation of phenylalanine and tryptophan. Both rated model simulations and experimental data showed that high product purity (99.1%–100%) and high yield (96.3%–100%) were achieved in both methods. The experimental shortcut design method is simpler than the SWD, but is limited to a fixed feed concentration. A dimensionless number is derived to quantify the deviation of an actual nonideal system from a system without mass-transfer effects (ideal system). If the dimensionless number has a value greater than 0.005 for the binary amino acid separation, the system deviates from its corresponding ideal system and the design considering mass-transfer effects gives significantly higher purity and yield than the ideal design.

[1]  N.-H. Linda Wang,et al.  Extended Standing Wave Design Method for Simulated Moving Bed Chromatography: Linear Systems , 2000 .

[2]  Luís S. Pais,et al.  Separation of 1,1'-bi-2-naphthol enantiomers by continuous chromatography in simulated moving bed , 1997 .

[3]  Massimo Morbidelli,et al.  Design of Simulated Moving Bed Units under Nonideal Conditions , 1999 .

[4]  Massimo Morbidelli,et al.  Optimal design of multicomponent countercurrent adsorption separation processes involving nonlinear equilibria , 1989 .

[5]  Massimo Morbidelli,et al.  Robust design of binary countercurrent adsorption separation processes , 1993 .

[6]  Bruce W. Pynnonen Simulated moving bed processing: escape from the high-cost box , 1998 .

[7]  Alírio E. Rodrigues,et al.  Design of a simulated moving bed in the presence of mass‐transfer resistances , 1999 .

[8]  N.-H. Linda Wang,et al.  Design of a carousel process for cesium removal using crystalline silicotitanate , 2000 .

[9]  Sungyong Mun,et al.  Standing Wave Design and Experimental Validation of a Tandem Simulated Moving Bed Process for Insulin Purification , 2002, Biotechnology progress.

[10]  M. Morbidelli,et al.  Design and optimisation of a simulated moving bed unit: role of deviations from equilibrium theory. , 2000, Journal of chromatography. A.

[11]  G. Guiochon,et al.  Effect of column efficiency on the internal concentration profiles and the performance of a simulated moving-bed unit in the case of a linear isotherm , 1997 .

[12]  M. Morbidelli,et al.  Simulated moving-bed chromatography and its application to chirotechnology. , 2000, Trends in biotechnology.

[13]  D. Ruthven,et al.  Counter-current and simulated counter-current adsorption separation processes , 1989 .

[14]  Alírio E. Rodrigues,et al.  Fructose–glucose separation in a SMB pilot unit: Modeling, simulation, design, and operation , 2001 .

[15]  Rutherford Aris,et al.  Multicomponent adsorption in continuous countercurrent exchangers , 1971, Philosophical Transactions of the Royal Society of London. Series A, Mathematical and Physical Sciences.

[16]  Kus Hidajat,et al.  Experimental study of a simulated counter-current adsorption system. III: Sorbex operation , 1985 .

[17]  J. Strube,et al.  Preparative enantioseparation by simulated moving bed chromatography. , 2001, Journal of chromatography. A.

[18]  E. J. Wilson,et al.  Liquid Mass Transfer at Very Low Reynolds Numbers in Packed Beds , 1966 .

[19]  Massimo Morbidelli,et al.  Optimal operation of simulated moving bed units for nonlinear chromatographic separations , 1997 .

[20]  Massimo Morbidelli,et al.  Shortcut experimental method for designing chiral SMB separations , 2002 .

[21]  Nien-Hwa Linda Wang,et al.  Standing wave design of nonlinear SMB systems for fructose purification , 1998 .

[22]  Nien-Hwa Linda Wang,et al.  Design of Simulated Moving Bed Chromatography for Amino Acid Separations , 1998 .

[23]  G. Ganetsos,et al.  Preparative and Production Scale Chromatography , 1992 .

[24]  Nien-Hwa Linda Wang,et al.  Standing wave analysis of SMB chromatography: Linear systems , 1997 .

[25]  G. Guiochon,et al.  Simulated moving bed chromatography. Effects of axial dispersion and mass transfer under linear conditions , 1997 .

[26]  C. Wen,et al.  Longitudinal dispersion of liquid flowing through fixed and fluidized beds , 1968 .

[27]  Robert J. Wooley,et al.  Standing‐wave design of tandem SMB for linear multicomponent systems , 2002 .