2016
DOI: 10.1186/s13068-016-0575-1
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Cellulolytic enzyme expression and simultaneous conversion of lignocellulosic sugars into ethanol and xylitol by a new Candida tropicalis strain

Abstract: BackgroundLignocellulosic ethanol production involves major steps such as thermochemical pretreatment of biomass, enzymatic hydrolysis of pre-treated biomass and the fermentation of released sugars into ethanol. At least two different organisms are conventionally utilized for producing cellulolytic enzymes and for ethanol production through fermentation, whereas in the present study a single yeast isolate with the capacity to simultaneously produce cellulases and xylanases and ferment the released sugars into … Show more

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Cited by 44 publications
(18 citation statements)
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“…Recent innovations about lignocellulosic biomass hydrolysis include acid or base treatments, which are not yet satisfactory because of the ecological waste issues [22, 23]. Hydrolysis with hemicellulolytic and cellulolytic enzymes had also been commonly used for lignocellulose degradation [2, 24]. However, enzymatic hydrolysis is time consuming and is not enough to break down the hemicellulose and cellulose complex structures to simple sugars [2, 25, 26].…”
Section: Introductionmentioning
confidence: 99%
“…Recent innovations about lignocellulosic biomass hydrolysis include acid or base treatments, which are not yet satisfactory because of the ecological waste issues [22, 23]. Hydrolysis with hemicellulolytic and cellulolytic enzymes had also been commonly used for lignocellulose degradation [2, 24]. However, enzymatic hydrolysis is time consuming and is not enough to break down the hemicellulose and cellulose complex structures to simple sugars [2, 25, 26].…”
Section: Introductionmentioning
confidence: 99%
“…The highest accumulation of furfural and HMF was found to be 110 mg g −1 DM in CS corresponding to ∼9.6 g L −1 which would be detrimental to bioconversion (van der Pol et al, 2014; Figure 3C). For WS, M and W the maximum individual inhibitor accumulation were below 4 g L −1 for HMF and furfural, which is important as up to 4 g L −1 of furfural or HMF has been shown to not inhibit microbial growth (Geddes et al, 2011;Mattam et al, 2016;Wang et al, 2016). Previous publications already mentioned have a range of inhibitors concentrations from 7.5 to 45.8 g kg −1 (Castro et al, 2014) 3.62 to 5.65 g L −1 (Negro et al, 2014) and 3.77 g Kg −1 (Zhang et al, 2014) for SE-PT biomass.…”
Section: Inhibitor Generationmentioning
confidence: 99%
“…Hasunuma and Kondo [30] presented a review of the development of yeast cells for second-generation bioethanol production through CBP. Within their study, they conclude that the combination of cell surface [31][32][33][34] review the possibilities of recombinant yeasts generation for second-generation bioethanol production through CBP.…”
Section: Process Configuration For Second-generation Bioethanol Produmentioning
confidence: 99%