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Process engineering and scale-up of autotrophic Clostridium strain P11 syngas fermentation.

机译:自养梭状芽胞杆菌菌株P11合成气发酵的工艺工程和规模放大。

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摘要

Scope and Method of Study. Biomass gasification followed by fermentation of syngas to ethanol is a potential process to produce bioenergy. The process is currently being researched under laboratory- and pilot-scale in an effort to optimize the process conditions and make the process feasible for commercial production of ethanol and other biofuels such as butanol and propanol. The broad research objectives for the research were to improve ethanol yields during syngas fermentation and to design a economical fermentation process. The research included four statistically designed experimental studies in serum bottles, bench-scale and pilot-scale fermentors to screen alternate fermentation media components, to determine the effect of process parameters such as pH, temperature and buffer on syngas fermentation, to determine the effect of key limiting nutrients of the acetyl-CoA pathway in a continuous series reactor design, and to scale-up the syngas fermentation in a 100-L pilot scale fermentor.;Findings and Conclusions. The first experimental study identified cotton seed extract (CSE) as a feasible medium for Clostridium strain P11 fermentation. The study showed that CSE at 0.5 g L-1 can potentially replace all the standard Clostridium strain P11 fermentation media components while using a media buffer did not significantly improve the ethanol production when used in fermentation with CSE. Scale-up of the CSE fermentation in 2-L and 5-L stirred tank fermentors showed 25% increase in ethanol yield. The second experimental study showed that syngas fermentation at 32°C without buffer was associated with higher ethanol concentration and reduced lag time in switching to solventogenesis. Conducting fermentation at 40°C or by lowering incubation pH to 5.0 resulted in reduced cell growth and no production of ethanol or acetic acid. The third experiment studied the effect of three limiting nutrients, calcium pantothenate, vitamin B12 and CoCl2 on syngas fermentation. Results indicated that it is possible to modulate the product formation by limiting key nutrients of acetyl-CoA pathway and using a continuous fermentation in two-stage fermentor design to improve ethanol yields. The last experimental study was conducted to commission a pilot scale fermentor, and subsequently scale-up the Clostridium strain P11 fermentation from a bench-scale to a pilot scale 100-L fermentor. Results indicated a six-fold improvement in ethanol concentration (25.3 g L-1 at the end of 59 d) compared to previous Clostridium strain P11 and Clostridium carboxidivorans fermentations plus the formation of other compounds such as isopropyl alcohol, acetic acid and butanol, which are of commercial importance.
机译:研究范围和方法。生物质气化,然后将合成气发酵成乙醇是产生生物能的潜在过程。目前正在实验室和中试规模下对该工艺进行研究,以优化工艺条件并使该工艺对于乙醇和其他生物燃料(如丁醇和丙醇)的商业化生产可行。该研究的广泛研究目标是在合成气发酵过程中提高乙醇产量,并设计一种经济的发酵工艺。该研究包括在血清瓶,台式规模和中试规模的发酵罐中进行的四项经过统计学设计的实验研究,以筛选替代的发酵培养基成分,以确定pH,温度和缓冲液等工艺参数对合成气发酵的影响,从而确定合成气的影响。连续串联反应器设计中乙酰辅酶A途径的关键限制性营养素,以及在100升中试规模发酵罐中扩大合成气发酵的规模;发现和结论。首次实验研究确定了棉籽提取物(CSE)是梭菌P11发酵的可行培养基。研究表明,0.5 g L-1的CSE可以潜在地取代所有标准的梭状芽胞杆菌P11发酵培养基成分,而使用培养基缓冲液在与CSE一起发酵时不能显着提高乙醇产量。在2升和5升搅拌釜发酵罐中进行CSE发酵的规模放大表明,乙醇收率提高了25%。第二项实验研究表明,在没有缓冲液的情况下,在32°C下进行合成气发酵,与乙醇浓度较高和切换到溶剂生成的滞后时间减少有关。在40°C或通过将孵育pH降低至5.0进行发酵导致细胞生长减少,并且不产生乙醇或乙酸。第三个实验研究了三种限制性营养素泛酸钙,维生素B12和CoCl2对合成气发酵的影响。结果表明,可以通过限制乙酰辅酶A途径的关键营养素并在两阶段发酵罐设计中使用连续发酵来提高乙醇产量来调节产物的形成。进行了最后的实验研究,以调试中试规模的发酵罐,然后将梭状芽胞杆菌菌株P11发酵从实验室规模扩大到中试规模的100 L发酵罐。结果表明,与以前的梭状芽胞杆菌菌株P11和羧氧化梭菌发酵相比,乙醇浓度提高了6倍(59 d末为25.3 g L-1),另外还形成了其他化合物,例如异丙醇,乙酸和丁醇具有商业重要性。

著录项

  • 作者单位

    Oklahoma State University.;

  • 授予单位 Oklahoma State University.;
  • 学科 Engineering Agricultural.;Energy.;Engineering Chemical.
  • 学位 M.S.
  • 年度 2010
  • 页码 147 p.
  • 总页数 147
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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