Gao Kai, Rehmann Lars
Department of Chemical &Biochemical Engineering, The University of Western Ontario, 1151 Richmond St., London, Ontario N6A 3K7, Canada.
Department of Biochemical Engineering, AVT - Aachener Verfahrenstechnik, RWTH Aachen University, Worringer Weg 1, 52074 Aachen, Germany.
Sci Rep. 2016 Jul 27;6:30533. doi: 10.1038/srep30533.
Phragmites australis (an invasive plant in North America) was used as feedstock for ABE (acetone-butanol-ethanol) fermentation by Clostridium saccharobutylicum. Sulphuric acid pretreated phragmites hydrolysate (SAEH) without detoxification inhibited butanol production (0.73 g/L butanol from 30 g/L sugars). The treatment of SAEH with resin L-493 prior the fermentation resulted in no inhibitory effects and an ABE titer of 14.44 g/L, including 5.49 g/L butanol was obtained, corresponding to an ABE yield and productivity of 0.49 g/g and 0.60 g/L/h, respectively. Dual functionality of the resin was realized by also using it as an in-situ product removal agent. Integrating in-situ product removal allowed for the use of high substrate concentrations without the typical product inhibition. Resin-detoxified SAEH was supplemented with neat glucose and an effective ABE titer of 33 g/L (including 13.7 g/L acetone, 16.4 g/L butanol and 1.9 g/L ethanol) was achieved with resin-based in-situ product removal, corresponding to an ABE yield and productivity of 0.41 g/g and 0.69 g/L/h, respectively. Both detoxification of the substrate and the products was achieved by the same resin, which was added prior the fermentation. Integrating hydrolysate detoxification and in-situ butanol removal in a batch process through single resin can potentially simplify cellulosic butanol production.
芦苇(北美一种入侵植物)被用作产丁醇梭菌进行丙酮-丁醇-乙醇(ABE)发酵的原料。未经解毒处理的硫酸预处理芦苇水解物(SAEH)会抑制丁醇的产生(30 g/L糖仅产生0.73 g/L丁醇)。在发酵前用树脂L-493处理SAEH没有产生抑制作用,获得了14.44 g/L的ABE滴度,其中包括5.49 g/L丁醇,相应的ABE产率和生产率分别为0.49 g/g和0.60 g/L/h。该树脂的双重功能还通过将其用作原位产物去除剂得以实现。集成原位产物去除使得可以使用高底物浓度而不会出现典型的产物抑制现象。用纯葡萄糖补充经树脂解毒的SAEH,通过基于树脂的原位产物去除实现了33 g/L的有效ABE滴度(包括13.7 g/L丙酮、16.4 g/L丁醇和1.9 g/L乙醇),相应的ABE产率和生产率分别为0.41 g/g和0.69 g/L/h。底物和产物的解毒均通过在发酵前添加的同一种树脂实现。通过单一树脂在分批过程中集成水解物解毒和原位丁醇去除可能会简化纤维素丁醇的生产。