State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China.
State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; University of the Chinese Academy of Sciences, Chinese Academy of Sciences, Beijing 100049, China.
Bioresour Technol. 2018 Oct;266:26-33. doi: 10.1016/j.biortech.2018.06.016. Epub 2018 Jun 15.
The aim of the present study is to develop an effective bioprocess for converting CO into succinic acid (SA) with Actinobacillus succinogenes by an integrated fermentation and membrane separation process. CO could be effectively converted into SA using NaOH as the neutralizer under the completely closed exhaust pipe case with self-circulation of CO in the bioreactor. Meanwhile, the optimal CO partial pressure was 0.4 bar. In addition, a 300 kDa ultrafiltration (UF) membrane was preferred for constructing the membrane bioreactor. Moreover, a high conductivity was toxic to the cells during SA biosynthesis. After removing the high concentration salts by in-situ membrane filtration, the SA productivity and CO fixation rate increased by 39.2% compared with the batch culture, reaching 1.39 g·L·h and 0.52 g·L·h respectively. Furthermore, nanofiltration (NF) was suitable for purifying the SA and recovering the residual substrates in the UF permeate for the next fermentation.
本研究旨在开发一种有效的生物过程,通过集成发酵和膜分离过程,将 CO 转化为琥珀酸 (SA),使用 Actinobacillus succinogenes。在生物反应器中 CO 自循环的完全封闭排气管情况下,使用 NaOH 作为中和剂,可以将 CO 有效地转化为 SA。同时,最优 CO 分压为 0.4 巴。此外,300kDa 超滤 (UF) 膜被优选用于构建膜生物反应器。此外,在 SA 生物合成过程中,高电导率对细胞有毒。通过原位膜过滤去除高浓度盐后,SA 生产力和 CO 固定率分别比分批培养提高了 39.2%,达到 1.39g·L·h 和 0.52g·L·h。此外,纳滤 (NF) 适合纯化 SA 并回收 UF 渗透物中的残留底物,以供下一次发酵使用。