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首页> 外文期刊>Applied Microbiology and Biotechnology >Production of 1,3-propanediol by Clostridium butyricum growing on biodiesel-derived crude glycerol through a non-sterilized fermentation process
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Production of 1,3-propanediol by Clostridium butyricum growing on biodiesel-derived crude glycerol through a non-sterilized fermentation process

机译:通过未经灭菌的发酵过程,在生物柴油衍生的粗甘油上生长的丁酸梭菌生产1,3-丙二醇

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The aim of the present study was to investigate the production of 1,3-propanediol (PDO) under non-sterile fermentation conditions by employing the strain Clostridium butyricum VPI 1718. A series of batch cultures were performed by utilizing biodiesel-derived crude glycerol feedstocks of different origins as the sole carbon source, in various initial concentrations. The strain presented similarities in terms of PDO production when cultivated on crude glycerol of various origins, with final concentrations ranging between 11.1 and 11.5 g/L. Moreover, PDO fermentation was successfully concluded regardless of the initial crude glycerol concentration imposed (from 20 to 80 g/L), accompanied by sufficient PDO production yields (0.52–0.55 g per gram of glycerol consumed). During fed-batch operation under non-sterile culture conditions, 67.9 g/L of PDO were finally produced, with a yield of 0.55 g/g. Additionally, the sustainability of the bioprocess during a continuous operation was tested; indeed, the system was able to run at steady state for 16 days, during which PDO effluent level was 13.9 g/L. Furthermore, possible existence of a microbial community inside the chemostat was evaluated by operating a polymerase chain reaction-denaturing gradient gel electrophoresis (PCR-DGGE) analysis, and DGGE results revealed the presence of only one band corresponding to that of C. butyricum VPI 1718. Finally, non-sterile continuous cultures were carried out at different dilution rates (D), with inlet glycerol concentration at 80 g/L. Maximum PDO production was achieved at low D values (0.02 h−1) corresponding to 30.1 g/L, while the elaboration of kinetic data from continuous cultures revealed the stability of the bioprocess proposed, with global PDO production yield corresponding to 0.52 g/g.
机译:本研究的目的是研究使用丁酸梭状芽胞杆菌VPI 1718菌株在非无菌发酵条件下生产1,3-丙二醇(PDO)的过程。利用生物柴油衍生的粗甘油原料进行了一系列分批培养不同来源作为唯一碳源的各种初始浓度。当在各种来源的粗甘油上培养时,该菌株在PDO生产方面表现出相似性,最终浓度在11.1至11.5 g / L之间。此外,无论最初施加的粗甘油浓度如何(从20到80 g / L),伴随着足够的PDO产量(每克消耗的甘油0.52-0.55 g),PDO发酵都能成功完成。在非无菌培养条件下分批补料操作期间,最终生产了67.9 g / L的PDO,产量为0.55 g / g。此外,还测试了连续运行过程中生物过程的可持续性;实际上,该系统能够在稳定状态下运行16天,在此期间PDO出水水平为13.9 g / L。此外,通过进行聚合酶链反应-变性梯度凝胶电泳(PCR-DGGE)分析,评估了化学恒温器内部可能存在的微生物群落,DGGE结果显示仅存在一条与丁酸梭菌VPI 1718相对应的条带。最后,以不同的稀释率(D)进行非无菌连续培养,入口甘油浓度为80 g / L。在低D值(0.02 h −1 )对应于30.1 g / L的情况下实现了最大PDO产量,而对连续培养的动力学数据进行的详细分析显示了拟议的生物过程的稳定性,全球PDO产量产量对应于0.52g / g。

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