L. Bretschneider, Ingeborg Heuschkel, Martin Wegner, M. Lindmeyer, Katja Bühler, R. Karande, B. Bühler
{"title":"Conversion of Cyclohexane to 6-Hydroxyhexanoic Acid Using Recombinant Pseudomonas taiwanensis in a Stirred-Tank Bioreactor","authors":"L. Bretschneider, Ingeborg Heuschkel, Martin Wegner, M. Lindmeyer, Katja Bühler, R. Karande, B. Bühler","doi":"10.3389/fctls.2021.683248","DOIUrl":null,"url":null,"abstract":"6-hydroxyhexanoic acid (6HA) represents a polymer building block for the biodegradable polymer polycaprolactone. Alternatively to energy- and emission-intensive multistep chemical synthesis, it can be synthesized directly from cyclohexane in one step by recombinant Pseudomonas taiwanensis harboring a 4-step enzymatic cascade without the accumulation of any intermediate. In the present work, we performed a physiological characterization of this strain in different growth media and evaluated the resulting whole-cell activities. RB and M9* media led to reduced gluconate accumulation from glucose compared to M9 medium and allowed specific activities up to 37.5 ± 0.4 U gCDW −1 for 6HA synthesis. However, 50% of the specific activity was lost within 1 h in metabolically active resting cells, specifying growing cells, or induced resting cells as favored options for long-term biotransformation. Furthermore, the whole-cell biocatalyst was evaluated in a stirred-tank bioreactor setup with a continuous cyclohexane supply via the gas phase. At cyclohexane feed rates of 0.276 and 1.626 mmol min−1 L−1, whole-cell biotransformation occurred at first-order and zero-order rates, respectively. A final 6HA concentration of 25 mM (3.3 g L−1) and a specific product yield of 0.4 g gCDW −1 were achieved with the higher feed rate. Product inhibition and substrate toxification were identified as critical factors limiting biocatalytic performance. Future research efforts on these factors and the precise adjustment of the cyclohexane feed combined with an in situ product removal strategy are discussed as promising strategies to enhance biocatalyst durability and product titer and thus to enable the development of a sustainable multistep whole-cell process.","PeriodicalId":73071,"journal":{"name":"Frontiers in catalysis","volume":" ","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2021-05-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"9","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Frontiers in catalysis","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.3389/fctls.2021.683248","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 9
Abstract
6-hydroxyhexanoic acid (6HA) represents a polymer building block for the biodegradable polymer polycaprolactone. Alternatively to energy- and emission-intensive multistep chemical synthesis, it can be synthesized directly from cyclohexane in one step by recombinant Pseudomonas taiwanensis harboring a 4-step enzymatic cascade without the accumulation of any intermediate. In the present work, we performed a physiological characterization of this strain in different growth media and evaluated the resulting whole-cell activities. RB and M9* media led to reduced gluconate accumulation from glucose compared to M9 medium and allowed specific activities up to 37.5 ± 0.4 U gCDW −1 for 6HA synthesis. However, 50% of the specific activity was lost within 1 h in metabolically active resting cells, specifying growing cells, or induced resting cells as favored options for long-term biotransformation. Furthermore, the whole-cell biocatalyst was evaluated in a stirred-tank bioreactor setup with a continuous cyclohexane supply via the gas phase. At cyclohexane feed rates of 0.276 and 1.626 mmol min−1 L−1, whole-cell biotransformation occurred at first-order and zero-order rates, respectively. A final 6HA concentration of 25 mM (3.3 g L−1) and a specific product yield of 0.4 g gCDW −1 were achieved with the higher feed rate. Product inhibition and substrate toxification were identified as critical factors limiting biocatalytic performance. Future research efforts on these factors and the precise adjustment of the cyclohexane feed combined with an in situ product removal strategy are discussed as promising strategies to enhance biocatalyst durability and product titer and thus to enable the development of a sustainable multistep whole-cell process.
6-羟基己酸(6HA)代表可生物降解聚合物聚己内酯的聚合物构建块。作为能量和排放密集型多步化学合成的替代方案,它可以由含有4步酶级联的重组黄山假单胞菌直接从环己烷一步合成,而无需任何中间体的积累。在目前的工作中,我们在不同的生长培养基中对该菌株进行了生理学表征,并评估了由此产生的全细胞活性。与M9培养基相比,RB和M9*培养基减少了葡萄糖中葡萄糖酸盐的积累,并允许6HA合成的比活性高达37.5±0.4 U gCDW−1。然而,在代谢活跃的静息细胞中,50%的比活性在1小时内丧失,将生长细胞或诱导的静息细胞指定为长期生物转化的有利选择。此外,在通过气相连续供应环己烷的搅拌槽生物反应器装置中对全细胞生物催化剂进行了评估。在0.276和1.626 mmol min−1 L−1的环己烷进料速率下,全细胞生物转化分别以一级和零级速率发生。在较高的进料速率下,6HA的最终浓度为25 mM(3.3 g L−1),比产物产率为0.4 g gCDW−1。产物抑制和底物毒性被确定为限制生物催化性能的关键因素。未来对这些因素的研究工作以及环己烷进料的精确调整与原位产物去除策略相结合,被讨论为提高生物催化剂耐久性和产物滴度的有前景的策略,从而能够开发可持续的多步骤全细胞工艺。