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发布时间：2019-03-12

论文类型：期刊论文

发表时间：2016-11-01

发表刊物：BIORESOURCE TECHNOLOGY

收录刊物：Scopus、PubMed、EI、SCIE

卷号：219

页面范围：158-168

ISSN号：0960-8524

关键字：Acetone-butanol-ethanol fermentation; Activated carbon; Adsorption; Butanol; In situ product recovery

摘要：Activated carbon Norit ROW 0.8, zeolite CBV901, and polymeric resins Dowex Optipore L-493 and SD-2 with high specific loadings and partition coefficients were studied for n-butanol adsorption. Adsorption isotherms were found to follow Langmuir model, which can be used to estimate the amount of butanol adsorbed in acetone-butanol-ethanol (ABE) fermentation. In serum-bottle fermentation with in situ adsorption, activated carbon showed the best performance with 21.9 g/L of butanol production. When operated in a fermentor, free-and immobilized-cell fermentations with adsorption produced 31.6 g/L and 54.6 g/L butanol with productivities of 0.30 g/L.h and 0.45 g/L.h, respectively. Thermal desorption produced a condensate containing similar to 167 g/L butanol, which resulted in a highly concentrated butanol solution of similar to 640 g/L after spontaneous phase separation. This in situ product recovery process with activated carbon is energy efficient and can be easily integrated with ABE fermentation for n-butanol production. (C) 2016 Elsevier Ltd. All rights reserved.