4.7 Article

Continuous butanol production with reduced byproducts formation from glycerol by a hyper producing mutant of Clostridium pasteurianum

期刊

APPLIED MICROBIOLOGY AND BIOTECHNOLOGY
卷 93, 期 4, 页码 1485-1494

出版社

SPRINGER
DOI: 10.1007/s00253-011-3629-0

关键词

Anaerobic fermentation; Butanol; Clostridium pasteurianum; Glycerol; Acetone-butanol-ethanol fermentation

资金

  1. Advanced Biomass R&D Center of Korea through Ministry of Education, Science and Technology (MEST) [ABC-2010-0029799]
  2. BioFuelChem
  3. KAIST
  4. MEST [R32-2008-000-10142-0]
  5. Ministry of Education, Science & Technology (MoST), Republic of Korea [N01120030] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)
  6. National Research Foundation of Korea [R32-2012-000-10142-0, 2010-0029799] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

向作者/读者索取更多资源

Butanol, a four-carbon primary alcohol (C4H10O), is an important industrial chemical and has a good potential to be used as a superior biofuel. Bio-based production of butanol from renewable feedstock is a promising and sustainable alternative to substitute petroleum-based fuels. Here, we report the development of a process for butanol production from glycerol, which is abundantly available as a byproduct of biodiesel production. First, a hyper butanol producing strain of Clostridium pasteurianum was isolated by chemical mutagenesis. The best mutant strain, C. pasteurianum MBEL_GLY2, was able to produce 10.8 g l(-1) butanol from 80 g l(-1) glycerol as compared to 7.6 g l(-1) butanol produced by the parent strain. Next, the process parameters were optimized to maximize butanol production from glycerol. Under the optimized batch condition, the butanol concentration, yield, and productivity of 17.8 g l(-1), 0.30 g g(-1), and 0.43 g l(-1) h(-1) could be achieved. Finally, continuous fermentation of C. pasteurianum MBEL_GLY2 with cell recycling was carried out using glycerol as a major carbon source at several different dilution rates. The continuous fermentation was run for 710 h without strain degeneration. The acetone-butanol-ethanol productivity and the butanol productivity of 8.3 and 7.8 g l(-1) h(-1), respectively, could be achieved at the dilution rate of 0.9 h(-1). This study reports continuous production of butanol with reduced byproducts formation from glycerol using C. pasteurianum, and thus could help design a bioprocess for the improved production of butanol.

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