Synthesis of 1-cyanocyclohexaneacetic acid in a partial-mixed recirculating bed reactor with resin-immobilized nitrilase.

IF 3.6 3区 生物学 Q2 BIOTECHNOLOGY & APPLIED MICROBIOLOGY
Neng Xiong, Jia-Yu Chen, Pei-Qi Lei, Teng-Teng Fu, Rui Xu, Ya-Ping Xue, Yu-Guo Zheng
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Abstract

Immobilized enzyme bioreactors provide a controlled reaction environment and integrated reaction-separation processes for biocatalysis. In this study, a biocatalytic process based on resin-immobilized nitrilase and a partial-mixed recirculating bed bioreactor was developed for the synthesis of 1-cyanocyclohexaneacetic acid, a gabapentin intermediate. The resin catalyst prepared by immobilizing the regioselective nitrilase AcN-S on the activated amino resin LX-1000EPHA achieved 99.12% immobilization yield, 73.40 U/g specific activity, and 95.42% activity recovery when loaded with 10 mg/g crude enzyme. The resin catalyst (100 g/L) could convert 1 M (148.2 g/L) substrate 1-cyanocyclohexaneacetonitrile to 1-cyanocyclohexaneacetic acid within 18 h, achieving a conversion of 95.40%. At a substrate concentration of 0.5 M, > 85% conversion could still be achieved after 15 batches. In a partial-mixed recirculating bed reactor, the resin catalyst (100 g/L) could completely convert 500 mM substrate within 10 h, and achieve > 90% conversion after 20 batches, with residual activity of 93.23%. Resin activation and cross-linking treatment after immobilization were found to improve operational stability, reduce protein leakage, and ensure high immobilization yield and activity recovery. The reactor provided a low-shear environment and recirculating flow, which together improve catalyst reusability and reduce product inhibition. The constructed reaction system provides a solution for the efficient conversion of slightly soluble/insoluble substrates and the integration of reaction and separation.

树脂固定化硝化酶在部分混合循环床反应器中合成1-氰环己乙酸。
固定化酶生物反应器为生物催化提供了可控的反应环境和一体化的反应分离过程。本研究以树脂固定化硝化酶和部分混合循环床生物反应器为基础,研究了加巴喷丁中间体1-氰环己乙酸的生物催化合成工艺。将区域选择性腈酶AcN-S固定在活化的氨基树脂LX-1000EPHA上制备的树脂催化剂,负载10 mg/g粗酶时,固定化率为99.12%,比活性为73.40 U/g,活性回收率为95.42%。树脂催化剂(100 g/L)可在18 h内将1 M (148.2 g/L)底物1-氰环己烷乙腈转化为1-氰环己烷乙酸,转化率达95.40%。在底物浓度为0.5 M时,15批后仍可实现> 85%的转化率。在部分混合循环床反应器中,树脂催化剂(100 g/L)可在10 h内完全转化500 mM底物,20批次后转化率达到90%,剩余活性为93.23%。固定化后树脂活化和交联处理提高了操作稳定性,减少了蛋白质泄漏,确保了高固定化收率和活性恢复。反应器提供了低剪切环境和再循环流量,提高了催化剂的可重复使用性,减少了产物抑制。所构建的反应体系为微溶性/不溶性底物的高效转化和反应分离一体化提供了解决方案。
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来源期刊
Bioprocess and Biosystems Engineering
Bioprocess and Biosystems Engineering 工程技术-工程:化工
CiteScore
7.90
自引率
2.60%
发文量
147
审稿时长
2.6 months
期刊介绍: Bioprocess and Biosystems Engineering provides an international peer-reviewed forum to facilitate the discussion between engineering and biological science to find efficient solutions in the development and improvement of bioprocesses. The aim of the journal is to focus more attention on the multidisciplinary approaches for integrative bioprocess design. Of special interest are the rational manipulation of biosystems through metabolic engineering techniques to provide new biocatalysts as well as the model based design of bioprocesses (up-stream processing, bioreactor operation and downstream processing) that will lead to new and sustainable production processes. Contributions are targeted at new approaches for rational and evolutive design of cellular systems by taking into account the environment and constraints of technical production processes, integration of recombinant technology and process design, as well as new hybrid intersections such as bioinformatics and process systems engineering. Manuscripts concerning the design, simulation, experimental validation, control, and economic as well as ecological evaluation of novel processes using biosystems or parts thereof (e.g., enzymes, microorganisms, mammalian cells, plant cells, or tissue), their related products, or technical devices are also encouraged. The Editors will consider papers for publication based on novelty, their impact on biotechnological production and their contribution to the advancement of bioprocess and biosystems engineering science. Submission of papers dealing with routine aspects of bioprocess engineering (e.g., routine application of established methodologies, and description of established equipment) are discouraged.
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