2016
DOI: 10.1007/s13399-016-0218-6
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Bioethanol production from Eucalyptus grandis hemicellulose recovered before kraft pulping using an integrated biorefinery concept

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Cited by 6 publications
(5 citation statements)
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“…In general, hydrolysates from lignocellulosic byproducts, such as palm press fiber [51], sugarcane bagasse [52], sorghum stalks [53], or cotton stalks [54] achieved ethanol yields between 0.30 and 0.46 g ethanol/g sugar. However, fermentation from E. grandis hydrolysate enabled an ethanol yield of 0.21 g ethanol/g sugar [14]. In contrast, López-Linares et al [55] reached ethanol yields of 0.46-0.47 g/g when employing exhausted olive pomace hydrolysate with the bacteria E. coli SL100, with a maximum ethanol concentration of 13.6-14.5 g/L.…”
Section: Hydrolysates Fermentation For Ethanol Productionmentioning
confidence: 94%
See 1 more Smart Citation
“…In general, hydrolysates from lignocellulosic byproducts, such as palm press fiber [51], sugarcane bagasse [52], sorghum stalks [53], or cotton stalks [54] achieved ethanol yields between 0.30 and 0.46 g ethanol/g sugar. However, fermentation from E. grandis hydrolysate enabled an ethanol yield of 0.21 g ethanol/g sugar [14]. In contrast, López-Linares et al [55] reached ethanol yields of 0.46-0.47 g/g when employing exhausted olive pomace hydrolysate with the bacteria E. coli SL100, with a maximum ethanol concentration of 13.6-14.5 g/L.…”
Section: Hydrolysates Fermentation For Ethanol Productionmentioning
confidence: 94%
“…In order to overcome these difficulties, the removal of inhibitory compounds from the hemicellulosic hydrolysates by chemical, biological or physical methods is essential [6,13]. Detoxification strategies are the most employed and efficient procedures to tackle inhibition problems, namely evaporation, overliming, and liquid-solid extraction (activated charcoal, ion exchange) [13,14]. The main disadvantage of employing these procedures is the increase in the cost due to the additional separation steps to be made, and therefore, alternative strategies to surpass the inhibitory effect of degradation compounds have to be considered.…”
Section: Introductionmentioning
confidence: 99%
“…As compiled in Table 6, each organism presents some advantages and disadvantages for their industrial implementation [158]. Among these alternative organisms, Escherichia coli, Zymomonas mobilis and Pichia stipitis are worth mentioning, but others can be cited, such as Candida shehatae, Pachysolen tannophilus, Klebsiella oxytoca and Fusarium oxysporum [182][183][184]. Nevertheless, despite extensive research in this field, the majority of the studies concerning xylose (as the most relevant pentose) conversion to ethanol have been performed with only these few yeast species.…”
Section: Chemicals From Hemicellulosementioning
confidence: 99%
“…The extract obtained was highly concentrated in xylose and it was fermented by S. stipitis. After the removal of inhibitory compounds by using ethyl acetate extraction, the fermentation of the concentrated hydrolysates generated an ethanol concentration of 5.0 g•L −1 , and an ethanol yield of 0.21 g•g −1 [189]. During the Kraft cooking process, a fraction of hemicelluloses is dissolved in the black liquor and burned in the recovery boiler together with lignin.…”
Section: Converting Pulp and Paper Mills Into Biorefineriesmentioning
confidence: 99%
“…However, the removal method chosen should not affect the quality of the pulp [190][191][192]. Therefore, this process seems a promising approach for ethanol production by the conversion of Kraft pulping mills into forest-based biorefineries producing ethanol from hemicelluloses fraction and Kraft pulp from cellulose, as proposed and studied by several authors [189,190,[193][194][195]. Sugars from hemicelluloses can also be used as substrates to produce acetone and butanol, succinic acid, lactic acid, xylooligosaccharides, furfural, and xylitol.…”
Section: Converting Pulp and Paper Mills Into Biorefineriesmentioning
confidence: 99%