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• W2088894115 abstract "Concentrated cassava bagasse hydrolysate (CBH) containing 584.4 g/L glucose was studied for acetone-butanol-ethanol (ABE) fermentation with a hyper-butanol-producing Clostridium acetobutylicum strain in a fibrous bed bioreactor with gas stripping for continuous butanol recovery. With periodical nutrient supplementation, stable production of n-butanol from glucose in the CBH was maintained in the fed-batch fermentation over 263 h with an average sugar consumption rate of 1.28 g/L h and butanol productivity of 0.32±0.03 g/L h. A total of 108.5 g/L ABE (butanol: 76.4 g/L, acetone: 27.0 g/L, ethanol: 5.1 g/L) was produced, with an overall yield of 0.32±0.03 g/g glucose for ABE and 0.23±0.01 g/g glucose for butanol. The gas stripping process generated a product containing 10-16% (w/v) of butanol, ~4% (w/v) of acetone, a small amount of ethanol (<0.8%) and almost no acids, resulting in a highly concentrated butanol solution of ~64% (w/v) after phase separation." @default.
• W2088894115 created "2016-06-24" @default.
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• W2088894115 date "2012-01-01" @default.
• W2088894115 modified "2023-10-18" @default.
• W2088894115 title "Fed-batch fermentation for n-butanol production from cassava bagasse hydrolysate in a fibrous bed bioreactor with continuous gas stripping" @default.
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• W2088894115 doi "https://doi.org/10.1016/j.biortech.2011.10.089" @default.
• W2088894115 hasPubMedId "https://pubmed.ncbi.nlm.nih.gov/22101071" @default.
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