Activation of mandelate racemase via immobilization in lyotropic liquid crystals for biocatalysis in organic solvents: application and modeling

• Published in: Journal of molecular catalysis. B, Enzymatic Vol. 16; no. 2; pp. 91 - 100
• Main Authors: Bauer, Christoph, Boy, Matthias, Faber, Kurt, Felfer, Ulfried, Voss, Harald
• Format: Journal Article
• Language: English
• Published: Amsterdam Elsevier B.V 05.12.2001; Elsevier Science
• Subjects: Bioconversions. Hemisynthesis; Biological and medical sciences; Biotechnology; Computer programming; Computer simulation; Enzymatic racemization; Enzymes; Finite element method; Fundamental and applied biological sciences. Psychology; Liquid crystals; Lyotropic liquid crystals; Mandelate racemase [EC 5.1.2.2]; Mass transfer; Methods. Procedures. Technologies; Organic solvents; Substrates; Finite element method; Lyotropic liquid crystals; Mandelate racemase [EC 5.1.2.2]; Enzymatic racemization; Pseudomonadales; Mandelate racemase; Enzyme; Immobilization; Racemization; Enzymatic catalysis; Liquid crystals; Modeling; Organic solvent; Isomerases; Bacteria; Pseudomonadaceae; Lyotropic state; Immobilized enzyme; Pseudomonas putida
• ISSN: 1381-1177; 1873-3158
• DOI: 10.1016/S1381-1177(01)00049-2

Mandelate racemase from Pseudomonas putida ATCC 12633 could be activated in an organic solvent by immobilization in lyotropic liquid crystals (LC). A theoretical model for a system, that consisted of an organic solvent phase to solve the nonpolar substrate and the LC phase with the immobilized enzyme was developed. The model included the biocatalytic reaction and the mass transfer in-between and within the phases. By means of the finite element method (FEM) this model was transferred into a computer program, which was used as a tool for the simulation of the racemization of d-mandelic acid by mandelate racemase in the organic solvent (di- n-butyl ether). The experimental results at temperatures ranging from 20 to 60°C and starting concentrations of d-mandelic acid between 40 and 80 mmol l −1 in the organic solvent phase could be simulated by the model with high accuracy. Furthermore, the model was used to vary the geometry of the system to minimize mass transfer limitations, which represent a crucial limitation for this system.