Modelling Approach for the Continuous Biocatalytic Synthesis of N-Acetylneuraminic Acid in Packed Bed Reactors

被引:0
作者
Hoelting, Kristin [1 ,2 ]
Assmann, Miriam [1 ]
Bubenheim, Paul [2 ]
Liese, Andreas [2 ]
Kuballa, Juergen [1 ]
机构
[1] GALAB Labs GmbH, Schleusengraben 7, D-21029 Hamburg, Germany
[2] Hamburg Univ Technol, Inst Tech Biocatalysis, Denickestr 15, D-21073 Hamburg, Germany
关键词
immobilisation; continuous biocatalysis; N-acetylneuraminic acid; packed bed reactor; flow tube; GlcNAc; 2-epimerase; Neu5Ac lyase; D-GLUCOSAMINE; 2-EPIMERASE; ACETYL-D-GLUCOSAMINE; SIALIC-ACID; EXTINCTION COEFFICIENTS; PURIFICATION; LYASE; IMMOBILIZATION; ALDOLASE; PERFORMANCE;
D O I
10.3390/pr12102191
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Continuous flow technologies have become increasingly important for biocatalytic processes. In this study, we present the application and modelling of covalently immobilised N-acetylglucosamine 2-epimerase and N-acetylneuraminic acid lyase in packed bed reactors for the synthesis of N-acetylneuraminic acid. The immobilised enzymes were stable under continuous flow process conditions with half-life times of >28 d (epimerase immobilised on hexamethylamino methacrylate HA403/M) or 58 d (lyase immobilised on dimenthylamino methacrylate ECR8309M), suitable for continuous flow applications. Kinetic studies revealed Michaelis-Menten kinetic behaviour for both enzymes. The kinetic parameters and the inhibitions were analysed under continuous flow conditions and were integrated into a process model using Python. The model was validated by varying flow rates, the mass of immobilised enzymes and the reactor dimensions and shows a low error compared to the measured data. An error accuracy of 6% (epimerase) or 9% (lyase) was achieved. The product concentrations of the enzyme cascade at the end of the packed bed reactor can be predicted with an accuracy of 9% for the calculation of a large column (84.5 mL) or of 24% if several small columns (2.5 mL, 0.8 mL) are connected in series. The developed model has proved to be valid and will be used to optimise the process with respect to substrate concentrations, reactor dimensions and flow rate.
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页数:25
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