2019
DOI: 10.1016/j.biortech.2018.11.002
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Evaluation of inhibitory effect and feasible utilization of dilute acid-pretreated rice straws on succinate production by metabolically engineered Escherichia coli AS1600a

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Cited by 20 publications
(16 citation statements)
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“…The total inhibitors increased from 5.56 g/L to 14.20 g/L when the dry biomass loading range from 5% (w/v) to 35% (w/v). The rice straw pretreated with H 3 PO 4 showed signi cantly lower total inhibitors when compared to those of the pretreatments with H 2 SO 4 and HCl [17]. The total inhibitors of 5.10 g/L were obtained when 1 N H 2 SO 4 pretreated rice straw with a dry biomass loading of 10% (w/v) for 60 min.…”
Section: Sugars and Inhibitors Liberated During Pretreatment Of Cs By Dilute H 2 Somentioning
confidence: 92%
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“…The total inhibitors increased from 5.56 g/L to 14.20 g/L when the dry biomass loading range from 5% (w/v) to 35% (w/v). The rice straw pretreated with H 3 PO 4 showed signi cantly lower total inhibitors when compared to those of the pretreatments with H 2 SO 4 and HCl [17]. The total inhibitors of 5.10 g/L were obtained when 1 N H 2 SO 4 pretreated rice straw with a dry biomass loading of 10% (w/v) for 60 min.…”
Section: Sugars and Inhibitors Liberated During Pretreatment Of Cs By Dilute H 2 Somentioning
confidence: 92%
“…A high xylose concentration of 45.22 g/L with glucose concentration of 8.30 g/L and arabinose concentration of 6.07 g/L was obtained at a dry biomass loading of 35% (w/v). This may be due to hemicellulose has a lower molecular weight and is less ligni ed and highly amorphous compared to cellulose, thus it is easily hydrolyzed by acids [17]. The percentages of hemicellulose sacchari cation and cellulose sacchari cation decreased as the increase of corn stover loading during diluted acid pretreatment.…”
Section: Sugars and Inhibitors Liberated During Pretreatment Of Cs By Dilute H 2 Somentioning
confidence: 99%
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“…Numerous techniques, such as hot water, dilute sulphuric etc., have been utilized to eliminate the recalcitrant lignin in lignocellulosic waste focusing on the feedstock being beneficiated to mitigate environmental pollution. Several lignocellulosic waste pretreatment approaches have been impractical and wasteful due to some technical challenges, which include the low yield and the formation of inhibitory by-products, e.g., furfural (up to 34.5 g/Kg), hydroxymethyl furfural (up to 29.5 g/Kg), total phenolics compounds (up to 4.1 g/Kg) and weak organic acids (up to 114.9 g/Kg), including total furans (up to 34.5 g/Kg) [51,52]. The processes involved bio-physico-chemical ligninolysis and holocellulolysis of lignocellulosic waste include physical (milling), thermal (hot water), chemical (dilute acid, caustic) and microbial-based processes [53,54].…”
Section: Current Beneficiation Of Lignocellulosic Waste Using Different Pretreatment Techniquesmentioning
confidence: 99%
“…The processes involved bio-physico-chemical ligninolysis and holocellulolysis of lignocellulosic waste include physical (milling), thermal (hot water), chemical (dilute acid, caustic) and microbial-based processes [53,54]. Formation of by-product toxicants is usually observed during dilute acid and alkaline pretreatment as lignin is being partially degraded [48,51]; however, it is still assumed to be the ideal pretreatment method for an industrialized approach to date. Some common types of acid used in pretreating lignocellulosic waste from agriculture and forestry include dilute sulphuric (H 2 SO 4 ), phosphoric (H 3 PO 4 ), hydrochloric (HCl), and nitric (HNO 3 ) acid [55].…”
Section: Current Beneficiation Of Lignocellulosic Waste Using Different Pretreatment Techniquesmentioning
confidence: 99%