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论文类型： 期刊论文

发表时间： 2014-02-15

发表刊物： BIOCHEMICAL ENGINEERING JOURNAL

收录刊物： SCIE、EI、Scopus

卷号： 83

页面范围： 55-61

ISSN号： 1369-703X

关键字： Fermentation; Fed-batch culture; Separation; Bioprocess design; Gas stripping; Butanol production

摘要： Two-stage gas stripping coupled with acetone-butanol-ethanol fermentation in a fibrous bed bioreactor was established for energy-efficient butanol recovery. The impacts of process parameters including butanol concentration, temperature and cell density with feed, gas flow rate, and cooling temperature on the efficiency of the gas stripping system were studied. High butanol concentration, low cell density and cooling temperature increased butanol titer in the condensate. The butanol titer in the condensate increased when stripping temperature increased from 25 to 55 C, and decreased when temperature was above 55 C. The optimal gas flow rate was 1.6 L/min, above which more water was stripped off and the condensate was diluted. After process optimization, 48.5 g/L butanol (73.3 g/L ABE) was produced in the fed-batch fermentation with in situ gas stripping due to the reduced butanol inhibition on cells. The condensate containing 147.2 g/L butanol (199.0 g/L ABE) was produced by the first-stage gas stripping, while a highly concentrated condensate containing 515.3 g/L butanol (671.1 g/L ABE) was obtained from the second-stage gas stripping. This process can significantly reduce energy consumption in the final product recovery. (C) 2013 Elsevier B.V. All rights reserved.