Xiong Neng, Chen Jia-Yu, Lei Pei-Qi, Fu Teng-Teng, Xu Rui, Xue Ya-Ping, Zheng Yu-Guo
Key Laboratory of Bioorganic Synthesis of Zhejiang Province, College of Biotechnology and Bioengineering, Zhejiang University of Technology, Hangzhou, 310014, People's Republic of China.
Engineering Research Center of Bioconversion and Biopurification of Ministry of Education, Zhejiang University of Technology, Hangzhou, 310014, People's Republic of China.
Bioprocess Biosyst Eng. 2025 Aug 28. doi: 10.1007/s00449-025-03227-0.
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.
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集成的反应-分离过程。在本研究中,开发了一种基于树脂固定化腈水解酶和部分混合循环床生物反应器的生物催化过程,用于合成加巴喷丁中间体1-氰基环己烷乙酸。通过将区域选择性腈水解酶AcN-S固定在活化氨基树脂LX-1000EPHA上制备的树脂催化剂,在负载10 mg/g粗酶时,固定化产率达到99.12%,比活性为73.40 U/g,活性回收率为95.42%。该树脂催化剂(100 g/L)可在18小时内将1 M(148.2 g/L)底物1-氰基环己烷乙腈转化为1-氰基环己烷乙酸,转化率达到95.40%。在底物浓度为0.5 M时,经过15批次反应后仍可实现>85%的转化率。在部分混合循环床反应器中,该树脂催化剂(100 g/L)可在10小时内将500 mM底物完全转化,并在20批次反应后实现>90%的转化率,残余活性为93.23%。发现固定化后进行树脂活化和交联处理可提高操作稳定性,减少蛋白质泄漏,并确保高固定化产率和活性回收率。该反应器提供了低剪切环境和循环流动,共同提高了催化剂的可重复使用性并减少了产物抑制。构建的反应系统为微溶/不溶底物的高效转化以及反应和分离的集成提供了解决方案。