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使用固定化ω-转氨酶在可控水活度的有机溶剂中对酮进行连续流生物胺化反应。

Continuous Flow Bioamination of Ketones in Organic Solvents at Controlled Water Activity using Immobilized ω-Transaminases.

作者信息

Böhmer Wesley, Volkov Alexey, Engelmark Cassimjee Karim, Mutti Francesco G

机构信息

Van't Hoff Institute for Molecular Sciences, HIMS-Biocat University of Amsterdam Science Park 904 1098 XH Amsterdam The Netherlands.

EnginZyme AB Tomtebodavägen 6 171 65 Solna Sweden.

出版信息

Adv Synth Catal. 2020 Apr 27;362(9):1858-1867. doi: 10.1002/adsc.201901274. Epub 2020 Feb 17.

Abstract

Compared with biocatalysis in aqueous media, the use of enzymes in neat organic solvents enables increased solubility of hydrophobic substrates and can lead to more favorable thermodynamic equilibria, avoidance of possible hydrolytic side reactions and easier product recovery. ω-Transaminases from . (AsR-ωTA) and (Cv-ωTA) were immobilized on controlled porosity glass metal-ion affinity beads (EziG) and applied in neat organic solvents for the amination of 1-phenoxypropan-2-one with 2-propylamine. The reaction system was investigated in terms of type of carrier material, organic solvents and reaction temperature. Optimal conditions were found with more hydrophobic carrier materials and toluene as reaction solvent. The system's water activity (a) was controlled via salt hydrate pairs during both the biocatalyst immobilization step and the progress of the reaction in different non-polar solvents. Notably, the two immobilized ωTAs displayed different optimal values of a, namely 0.7 for EziG-AsR-ωTA and 0.2 for EziG-Cv-ωTA. In general, high catalytic activity was observed in various organic solvents even when a high substrate concentration (450-550 mM) and only one equivalent of 2-propylamine were applied. Under batch conditions, a chemical turnover (TTN) above 13000 was obtained over four subsequent reaction cycles with the same batch of EziG-immobilized ωTA. Finally, the applicability of the immobilized biocatalyst in neat organic solvents was further demonstrated in a continuous flow packed-bed reactor. The flow reactor showed excellent performance without observable loss of enzymatic catalytic activity over several days of operation. In general, ca. 70% conversion was obtained in 72 hours using a 1.82 mL flow reactor and toluene as flow solvent, thus affording a space-time yield of 1.99 g L h. Conversion reached above 90% when the reaction was run up to 120 hours.

摘要

与在水介质中的生物催化相比,在纯有机溶剂中使用酶能够提高疏水性底物的溶解度,并可导致更有利的热力学平衡,避免可能的水解副反应,且产物回收更容易。来自嗜热栖热放线菌(AsR-ωTA)和柱孢属(Cv-ωTA)的ω-转氨酶被固定在可控孔径玻璃金属离子亲和珠(EziG)上,并应用于纯有机溶剂中,用于1-苯氧基丙-2-酮与2-丙胺的胺化反应。从载体材料类型、有机溶剂和反应温度方面对反应体系进行了研究。发现使用疏水性更强的载体材料和甲苯作为反应溶剂时为最佳条件。在生物催化剂固定步骤以及在不同非极性溶剂中的反应过程中,通过水合盐对来控制系统的水活度(a)。值得注意的是,两种固定化的ω-转氨酶显示出不同的最佳a值,即EziG-AsR-ωTA为0.7,EziG-Cv-ωTA为0.2。一般来说,即使使用高底物浓度(450 - 550 mM)且仅使用一当量的2-丙胺,在各种有机溶剂中仍观察到高催化活性。在分批条件下,使用同一批固定有EziG的ω-转氨酶,在四个连续反应循环中获得了超过13000的化学转化数(TTN)。最后,在连续流填充床反应器中进一步证明了固定化生物催化剂在纯有机溶剂中的适用性。该流动反应器在运行数天期间表现出优异的性能,酶催化活性没有明显损失。一般来说,使用1.82 mL流动反应器并以甲苯作为流动溶剂,在72小时内可获得约70%的转化率,因此时空产率为1.99 g L⁻¹ h⁻¹。当反应进行到120小时时,转化率达到90%以上。

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