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Synergy of municipal solid waste co-processing with lignocellulosic waste for improved biobutanol production.
Farmanbordar, Sara; Amiri, Hamid; Karimi, Keikhosro.
Affiliation
  • Farmanbordar S; Department of Chemical Engineering, Isfahan University of Technology, Isfahan 84156-83111, Iran. Electronic address: s.farmanbordar@ce.iut.ac.ir.
  • Amiri H; Department of Biotechnology, Faculty of Biological Science and Technology, University of Isfahan, Isfahan 81746-73441, Iran; Environmental Research Institute, University of Isfahan, Isfahan 81746-73441, Iran. Electronic address: h.amiri@ast.ui.ac.ir.
  • Karimi K; Department of Chemical Engineering, Isfahan University of Technology, Isfahan 84156-83111, Iran; Industrial Biotechnology Group, Research Institute for Biotechnology and Bioengineering, Isfahan University of Technology, Isfahan 84156-83111, Iran. Electronic address: karimi@cc.iut.ac.ir.
Waste Manag ; 118: 45-54, 2020 Dec.
Article in En | MEDLINE | ID: mdl-32889233
ABSTRACT
Co-processing of lignocellulosic wastes, e.g., garden and paper wastes, and the organic matters fraction of municipal solid waste (OMSW) in an integrated bioprocess is a possible approach to realize the potential of wastes for biobutanol production. Dilute acid pretreatment is a multi-functional stage for breaking the recalcitrant lignocellulose's structure, hydrolyzing hemicellulose, and hydrolyzing/solubilizing starch, leading to a pretreated solid and a rich hydrolysate. In this study, dilute-acid pretreatment of the combination of wastepaper and OMSW, composite I, as well as garden waste and OMSW, composite II, at severe conditions resulted in "pretreatment hydrolysates" containing 33.7 and 19.4 g/L sugar along with 18.9 and 33.2 g/L soluble starch, respectively. In addition, the hydrolysis of solid remained after the pretreatment of composite I and II resulted in "enzymatic hydrolysates" comprising 19.4 and 33 g/L sugar, respectively. The fermentation of the pretreatment hydrolysates and enzymatic hydrolysates resulted in 3.5 and 6.4 g/L ABE from composite I and 15 and 5.2 g/L ABE from composite II, respectively. In this process, 148 and 173 g ABE (60 and 100 g gasoline equivalent/kg) was obtained from each kg composite I and composite II, respectively, where co-processing of OMSW with lignocellulosic wastes resulted in 10 and 49% higher ABE than that produced from the individual substrates.
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Full text: 1 Collection: 01-internacional Database: MEDLINE Main subject: Solid Waste / Butanols Language: En Journal: Waste Manag Journal subject: SAUDE AMBIENTAL / TOXICOLOGIA Year: 2020 Type: Article

Full text: 1 Collection: 01-internacional Database: MEDLINE Main subject: Solid Waste / Butanols Language: En Journal: Waste Manag Journal subject: SAUDE AMBIENTAL / TOXICOLOGIA Year: 2020 Type: Article