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A Review on Established and Emerging Fermentation Schemes for Microbial Production of Polyhydroxyalkanoate (PHA) Biopolyesters

机译:建立和新兴的微生物生产聚羟基链烷酸酯(PHA)生物聚酯发酵方案的综述。

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Polyhydroxyalkanoates (PHA) are microbial biopolyesters utilized as “green plastics”. Their production under controlled conditions resorts to bioreactors operated in different modes. Because PHA biosynthesis constitutes a multiphase process, both feeding strategy and bioreactor operation mode need smart adaptation. Traditional PHA production setups based on batch, repeated batch, fed-batch or cyclic fed-batch processes are often limited in productivity, or display insufficient controllability of polyester composition. For highly diluted substrate streams like is the case of (agro) industrial waste streams, fed-batch enhanced by cell recycling has recently been reported as a viable tool to increase volumetric productivity. As an emerging trend, continuous fermentation processes in single-, two- and multi-stage setups are reported, which bring the kinetics of both microbial growth and PHA accumulation into agreement with process engineering and allow tailoring PHA’s molecular structure. Moreover, we currently witness an increasing number of CO 2 -based PHA production processes using cyanobacteria; these light-driven processes resort to photobioreactors similar to those used for microalgae cultivation and can be operated both discontinuously and continuously. This development is parallel to the emerging use of methane and syngas as abundantly available gaseous substrates, which also calls for bioreactor systems with optimized gas transfer. The review sheds light on the challenges of diverse PHA production processes in different bioreactor types and operational regimes using miscellaneous microbial production strains such as extremophilic Archaea, chemoheterotrophic eubacteria and phototrophic cyanobacteria. Particular emphasis is dedicated to the limitations and promises of different bioreactor–strain combinations and to efforts devoted to upscaling these processes to industrially relevant scales.
机译:聚羟基链烷酸酯(PHA)是用作“绿色塑料”的微生物生物聚酯。它们在受控条件下的生产依赖于以不同模式运行的生物反应器。由于PHA生物合成是一个多相过程,因此进料策略和生物反应器操作模式都需要进行智能调整。基于分批,重复分批,进料分批或循环进料分批工艺的传统PHA生产设置通常在生产率上受到限制,或者聚酯组合物的可控性不足。对于高度稀释的底物流,如(农业)工业废水的情况,最近已报道了通过细胞再循环提高补料分批量的方法是提高容积生产率的可行工具。作为一种新兴趋势,据报道,在单阶段,两阶段和多阶段设置中进行连续发酵过程,使微生物生长和PHA积累的动力学与过程工程相一致,并可以定制PHA的分子结构。此外,我们目前目睹使用蓝细菌的基于CO 2的PHA生产工艺的数量不断增加;这些光驱动过程依赖于光生物反应器,类似于用于微藻培养的光生物反应器,并且可以间断和连续运行。这种发展与甲烷和合成气作为大量可利用的气态底物的新兴应用平行,这也要求生物反应器系统具有优化的气体传输。这篇综述揭示了使用不同的微生物生产菌株(如极端嗜热古生菌,化学营养型真细菌和光养性蓝细菌)在不同的生物反应器类型和操作方案中,不同的PHA生产工艺所面临的挑战。特别强调的是不同生物反应器-菌株组合的局限性和前景,以及致力于将这些过程升级至与工业相关的规模的努力。

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