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Syngas fermentation in a 100-L pilot scale fermentor: Design and process considerations

机译:100 L中型发酵罐中的合成气发酵:设计和工艺考虑

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摘要

Fermentation of syngas offers several advantages compared to chemical catalysts such as higher specificity of biocatalysts, lower energy costs, and higher carbon efficiency. Scale-up of syngas fermentation from a bench scale to a pilot scale fermentor is a critical step leading to commercialization. The primary objective of this research was to install and commission a pilot scale fermentor, and subsequently scale-up the Clostridium strain P11 fermentation from a 7.5-L fermentor to a pilot scale 100-L fermentor. Initial preparation and fermentations were conducted in strictly anaerobic conditions. The fermentation system was maintained in a batch mode with continuous syngas supply. The effect of anaerobic fermentation in a pilot scale fermentor was evaluated. In addition, the impact of improving the syngas mass transfer coefficient on the utilization and product formation was studied. Results indicate a six fold improvement in ethanol concentration compared to serum bottle fermentation, and formation of other compounds such as isopropyl alcohol, acetic acid and butanol, which are of commercial importance.
机译:与化学催化剂相比,合成气的发酵具有多种优势,例如更高的生物催化剂特异性,更低的能源成本和更高的碳效率。将合成气发酵从实验室规模扩大到中试规模的发酵罐是实现商业化的关键步骤。这项研究的主要目的是安装并调试中试规模的发酵罐,然后将梭状芽胞杆菌菌株P11发酵从7.5 L发酵罐扩大到中试规模100 L发酵罐。初始制备和发酵均在严格的厌氧条件下进行。发酵系统以连续供应合成气的方式保持在间歇模式下。评估了中型发酵罐中厌氧发酵的效果。此外,研究了提高合成气传质系数对利用率和产物形成的影响。结果表明,与血清瓶发酵相比,乙醇浓度提高了六倍,并且形成了其他具有商业意义的化合物,例如异丙醇,乙酸和丁醇。

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