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Amine transaminases (ATAs) are powerful biocatalysts for the stereoselective synthesis of chiral amines. However, wild-type ATAs usually show pH optima at slightly alkaline values and exhibit low catalytic activity under physiological conditions. For efficient asymmetric synthesis ATAs are commonly used in combination with lactate dehydrogenase (LDH, optimal pH: 7.5) and glucose dehydrogenase (GDH, optimal pH: 7.75) to shift the equilibrium towards the synthesis of the target chiral amine and hence their pH optima should fit to each other. Based on a protein structure alignment, variants of (R)-selective transaminases were rationally designed, produced in E. coli, purified and subjected to biochemical characterization. This resulted in the discovery of the variant E49Q of the ATA from Aspergillus fumigatus, for which the pH optimum was successfully shifted from pH 8.5 to 7.5 and this variant furthermore had a two times higher specific activity than the wild-type protein at pH 7.5. A possible mechanism for this shift of the optimal pH is proposed. Asymmetric synthesis of (R)-1-phenylethylamine from acetophenone in combination with LDH and GDH confirmed that the variant E49Q shows superior performance at pH 7.5 compared to the wild-type enzyme.
The synthesis of several bioactive compounds and active pharmaceutical ingredients relies on the development of general and efficient methods to prepare optically pure amines. Transaminases are industrially relevant enzymes and are useful for synthesizing a large number of compounds that contain a chiral amine functionality. Although the immense potential associated to the use of these biocatalysts, the equilibrium position is often unfavorable for amine synthesis. The use of an excess of amine donor, compared to the ketone substrate, combined with selective removal of the formed product, can help in overcoming this limitation. This work mainly focused on broadening the application of membrane-based in situ product recovery (ISPR) techniques for the transaminase-catalyzed synthesis of chiral amines. The
overall work was designed around the implementation of amine donors, possessing considerably larger molecular ‘size’ compared to commonly used amine donors. To clearly
distinguish these molecules from traditional donor amines, we designate them as High Molecular Weigh amine donors. With a molecular weight between 400 and 1500 g/mol, in contrast to traditional donor amines, HMW amine donors enable a size-based separation between amine donor and amine product molecules. HMW amines, provided in excess for thermodynamic equilibrium shifting can thus be simply retained by a size-exclusion mechanism by commercial membranes, while the smaller product amines are permeated. Therefore, a selective recovery of the desired chiral amine product is possible. The implementation of ISPR techniques using HMW amine donors can theoretically lead to (i) equilibrium shifting, (ii) alleviation of product inhibition, and (iii) a highly pure product stream.
The feasibility of using HMW amine donors in aqueous, organic solvent and solvent-free media for the transaminase-catalyzed synthesis of 1-methyl-3-phenylpropylamine (MPPA) was proven in this thesis. The latter two approaches were investigated with the aim to achieve higher product concentrations. Along with that, we demonstrated two membrane-assisted ISPR proof of concepts. Specifically, nanofiltration was coupled with the enzymatic reaction performed in aqueous media (Article I), while liquid-liquid (L-L) extraction in a contactor was applied for transamination in organic solvent media (Article II). As an alternative to membrane-based strategies we also designed a spinning reactor concept for the integrated chiral amine synthesis (in organic solvent) and recovery (Article III).
Abstract
A device for the transaminase‐catalysed synthesis combined with continuous recovery of chiral amines was designed. The system enabled the separation of the reaction components in three liquid phases: a reaction phase, an organic solvent phase (where the poorly water soluble ketone substrate was supplied), and an aqueous extraction phase for continuous product recovery. The transaminase‐mediated asymmetric synthesis of (S)‐1‐methyl‐3‐phenylpropylamine was employed as model reaction. Factors influencing the performance of the system, such as reactor geometry, working volumes and operating parameters, were investigated. Specifically, reaction yield and product recovery were enhanced by i) reducing the thickness of the reaction phase, while continuously stirring and ii) reducing the volume of the extraction phase. Under the optimal condition tested, 85 % of the product formed was extracted and a product concentration value of 9 g/L was reached. However, co‐extraction of the unreacted amine donor (17 %) was observed. Advantages and drawbacks of this process compared to existing technologies, as well as possible optimization strategies are discussed.