Sarchami Tahereh, Rehmann Lars
Department of Chemical and Biochemical Engineering, Thompson Engineering Building, Western University, London, Ontario N6A 5B9, Canada.
ACS Omega. 2019 Sep 12;4(13):15521-15529. doi: 10.1021/acsomega.9b00879. eCollection 2019 Sep 24.
DSM 525 can produce butanol, 1,3-propanediol, and ethanol from glycerol. The product distribution can be tilted toward butanol when adding butyric acid. The strain predominantly produces acetic and butyric acids when grown on saccharides. Hence, butyrate formed from saccharide conversion can be used to stimulate butanol production from glycerol under cosubstrate cultivation. The optimal cosubstrate ratio was determined, and under optimal conditions, a butanol yield and a productivity of 0.27 ± 0.01 g g and 0.74 ± 0.02 g L h were obtained. On the basis of these results, batch fermentation in a 5 L bioreactor was performed using Jerusalem artichoke hydrolysate (carbohydrate source) and crude glycerol (residue from biodiesel production) at the previously determined optimal condition. A butanol yield and a productivity of 0.28 ± 0.007 g g and 0.55 ± 0.008 g L h were achieved after 27 h fermentation, indicating the suitability of those low-cost carbon sources as cosubstrates for butanol production via .
DSM 525能够从甘油生产丁醇、1,3 - 丙二醇和乙醇。添加丁酸时,产物分布可向丁醇倾斜。该菌株在糖类上生长时主要产生乙酸和丁酸。因此,在共底物培养条件下,由糖类转化形成的丁酸盐可用于刺激从甘油生产丁醇。确定了最佳共底物比例,在最佳条件下,丁醇产量和生产率分别为0.27±0.01 g/g和0.74±0.02 g/(L·h)。基于这些结果,在先前确定的最佳条件下,使用菊芋水解物(碳水化合物来源)和粗甘油(生物柴油生产的残余物)在5 L生物反应器中进行分批发酵。发酵27 h后,丁醇产量和生产率分别达到0.28±0.007 g/g和0.55±0.008 g/(L·h),表明这些低成本碳源作为共底物通过……生产丁醇的适用性。