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- W102443648 abstract "This chapter describes process integration for butanol fermentation and simultaneous recovery. In unintegrated butanol fermentation, the concentration of the biofuel rarely exceeds 30 g/L due to its toxic nature. Such a low butanol concentration results in low reactor productivities of 0.30 g/L h, as well as low acetone-butanol-ethanol (ABE) yields that result in an uneconomic process. In an effort to improve productivity and yield, researchers have employed alternative product recovery techniques to remove butanol from the fermentation broth as it is produced, thus never allowing the biofuel to reach a toxic level. As a result, integrated bioreactor systems have used glucose to produce ABE in excess of 461-690 g/L. The product recovery techniques used in these integrated systems include adsorption, liquid-liquid extraction, perstraction, pervaporation, gas stripping, vacuum fermentation, and reverse osmosis. High-productivity reactors (up to 5.0 g/L h) employing product removal systems have resulted in integrated processes that could be commercialized for butanol fermentation. Some of the involved product recovery techniques have been studied for butanol production from whey permeate and agricultural residues through simultaneous hydrolysis, fermentation, and recovery (SSFR). The butanol-producing cultures in such reactors can hydrolyze lactose present in whey permeate during the fermentation and recovery processes. However, for the hydrolysis of agricultural residues, hydrolytic enzymes are added to the system, with hydrolysis, fermentation, and recovery performed as components of a single system." @default.
- W102443648 created "2016-06-24" @default.
- W102443648 creator A5074307519 @default.
- W102443648 date "2014-01-01" @default.
- W102443648 modified "2023-09-26" @default.
- W102443648 title "Integrated Bioprocessing and Simultaneous Product Recovery for Butanol Production" @default.
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- W102443648 doi "https://doi.org/10.1016/b978-0-444-59498-3.00010-5" @default.
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