教授 博士生导师 硕士生导师
主要任职: 生物工程学院副院长
性别: 男
毕业院校: 大连理工大学
学位: 博士
所在单位: 生物工程学院
学科: 生物化工. 膜科学与技术. 微生物学
联系方式: xue.1@dlut.edu.cn
电子邮箱: xue.1@dlut.edu.cn
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论文类型: 期刊论文
发表时间: 2014-04-01
发表刊物: APPLIED MICROBIOLOGY AND BIOTECHNOLOGY
收录刊物: SCIE、EI、PubMed
卷号: 98
期号: 8
页面范围: 3463-3474
ISSN号: 0175-7598
关键字: Butanol; ABE fermentation; Clostridium; Butanol recovery; Hybrid process
摘要: Butanol has recently gained increasing interest due to escalating prices in petroleum fuels and concerns on the energy crisis. However, the butanol production cost with conventional acetone-butanol-ethanol fermentation by Clostridium spp. was higher than that of petrochemical processes due to the low butanol titer, yield, and productivity in bioprocesses. In particular, a low butanol titer usually leads to an extremely high recovery cost. Conventional biobutanol recovery by distillation is an energy-intensive process, which has largely restricted the economic production of biobutanol. This article thus reviews the latest studies on butanol recovery techniques including gas stripping, liquid-liquid extraction, adsorption, and membrane-based techniques, which can be used for in situ recovery of inhibitory products to enhance butanol production. The productivity of the fermentation system is improved efficiently using the in situ recovery technology; however, the recovered butanol titer remains low due to the limitations from each one of these recovery technologies, especially when the feed butanol concentration is lower than 1 % (w/v). Therefore, several innovative multi-stage hybrid processes have been proposed and are discussed in this review. These hybrid processes including two-stage gas stripping and multi-stage pervaporation have high butanol selectivity, considerably higher energy and production efficiency, and should outperform the conventional processes using single separation step or method. The development of these new integrated processes will give a momentum for the sustainable production of industrial biobutanol.