4.7 Review

Integrated butanol recovery for an advanced biofuel: current state and prospects

Journal

APPLIED MICROBIOLOGY AND BIOTECHNOLOGY
Volume 98, Issue 8, Pages 3463-3474

Publisher

SPRINGER
DOI: 10.1007/s00253-014-5561-6

Keywords

Butanol; ABE fermentation; Clostridium; Butanol recovery; Hybrid process

Funding

  1. National Natural Science Foundation of China (NSFC) [21306020, 21376044]
  2. Specialized Research Fund for the Doctoral Program of Higher Education of China [20130041120027]
  3. Liaoning Provincial Education Department [L2013022]
  4. China Postdoctoral Science Foundation [2013M530904]
  5. Biofuels Key Laboratory of Chinese Academy of Sciences in Qingdao Institute of Bioenergy and Bioprocess Technology [CASKLB201303]
  6. Scientific Research Foundation for the Returned Overseas Chinese Scholars of State Education Ministry

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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.

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