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- W199423786 abstract "Currently, fermentation industries are structured around individual unit operations for the production of biofuels such as ethanol, butanol, and 2,3-butanediol. This structure is associated with increased capital and operational costs, and increased costs result in low profitability and increased prices for the consumer. The development of novel technologies allows the unit operations of fermentation facilities to be combined or integrated, thus reducing overall operation costs. This chapter discusses the potential of various product recovery technologies that operate at fermentation temperatures, as opposed to the distillative recovery of biofuels, because these technologies can lead to combined fermentation and recovery. The technologies to be discussed include adsorption, liquid-liquid extraction, perstraction, pervaporation, gas stripping, vacuum fermentation, salt-induced phase separation, and ionic liquid separation. The chapter also describes the use of feedstocks such as cellulosic wastes as economically viable alternatives to sugarcane juice, molasses, corn, and corn starch. The cost of agricultural residues is about $60 per ton, as opposed to the cost of corn at $275 per ton. However, these residues require hydrolysis prior to fermentation and recovery. In order to address the need for additional processing of the feedstock, simultaneous hydrolysis, fermentation, and recovery might be carried out using one of these product separation techniques." @default.
- W199423786 created "2016-06-24" @default.
- W199423786 creator A5074307519 @default.
- W199423786 date "2014-01-01" @default.
- W199423786 modified "2023-09-29" @default.
- W199423786 title "Integrated Processes for Product Recovery" @default.
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- W199423786 doi "https://doi.org/10.1016/b978-0-444-59498-3.00005-1" @default.
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