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February 16, 20260 citationsOpen Access

Chiral Separation of Menthol Enantiomers by Simulated Moving Bed Chromatography: Mathematical Modeling and Experimental Study

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LSLinhe SunYYYing YangJYJianguo Yu

Key Points

  • The study aims to achieve chiral separation of menthol enantiomers using advanced chromatography techniques.
  • Simulated moving bed chromatography for separation of menthol enantiomers
  • Use of six preparative columns packed with amylose coated on silica gel
  • Measurement of binary adsorption isotherm and evaluation of adsorption kinetics
  • Mathematical modeling to describe chromatographic dynamics
  • Purities for both extract and raffinate exceeded 99.0%
  • Achieved productivity of 0.267 gracemate/(LCSP·min)
  • Solvent consumption was 0.431 L/gracemate

Abstract

l-menthol is one of the most popular flavors in the world. The separation of menthol enantiomers is crucial because of the unpleasant taste of d-menthol. This work presents the chiral separation of racemic menthol by simulated moving bed chromatography for the first time. Six preparative columns packed with amylose 3,5-dimethylphenylcarbamate coated on silica gel were used for separation, and a mixture of n-hexane/isopropanol was selected as the mobile phase. The hydrodynamic properties of the SMB columns were studied to minimize the packing asymmetry in the SMB experiment. The binary adsorption isotherm of menthol enantiomers was measured by the adsorption–desorption method. Fixed-bed batch chromatography was carried out to evaluate the adsorption kinetic behavior. Mathematical models, considering the mass transfer resistance and axial dispersion, were applied to describe the dynamics of the chromatographic separation process. The SMB process for chiral separation of racemic menthol was designed by evaluating the separation region using simulations. Reasonable agreements were achieved between the predicted results and the experimental results. Purities for both the extract and raffinate were above 99.0%, and a productivity of 0.267 gracemate/(LCSP∙min) and a solvent consumption of 0.431 L/gracemate were achieved.

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Cite This Study

Sun et al. (2026) studied this question.

synapsesocial.com/papers/69926503eb1f82dc367a0d50https://doi.org/10.3390/separations13020067
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