2018
DOI: 10.1016/j.biombioe.2017.10.044
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Improved n- butanol production from lignocellulosic hydrolysate by Clostridium strain screening and culture-medium optimization

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Cited by 40 publications
(17 citation statements)
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“…There is ongoing research on metabolic engineering to develop clostridial strains capable of simultaneously fermenting hexose and pentose for butanol production [71, 93, 94, 113, 114]. Even though Lee et al [23] stated metabolic engineering is necessary for simultaneous utilization of sugars, researchers have developed different feeding and pre-growth strategies achieving co-utilization without any strain manipulation [73, 115–120]. However, in the mixed sugar fermentation study of Zhang et al [121], transcriptional studies suggested that glucose inhibition on xylose metabolism-related genes was still present despite the simultaneous utilization of glucose and xylose.…”
Section: Fermentative Butanol Production From Mixed Sugarsmentioning
confidence: 99%
“…There is ongoing research on metabolic engineering to develop clostridial strains capable of simultaneously fermenting hexose and pentose for butanol production [71, 93, 94, 113, 114]. Even though Lee et al [23] stated metabolic engineering is necessary for simultaneous utilization of sugars, researchers have developed different feeding and pre-growth strategies achieving co-utilization without any strain manipulation [73, 115–120]. However, in the mixed sugar fermentation study of Zhang et al [121], transcriptional studies suggested that glucose inhibition on xylose metabolism-related genes was still present despite the simultaneous utilization of glucose and xylose.…”
Section: Fermentative Butanol Production From Mixed Sugarsmentioning
confidence: 99%
“…Since the 1960s, cellulase has been used increasingly in food, paper, pulp, textile industries, and pharmaceutical industries. However, there are limited studies that exploited the hydrolysis process of agricultural residues of lignocellulosic materials to produce high-value products with low cost [10][11][12]. Moreover, the problem with the biorefining process is that it is costly due to a lack of biocatalysts that are capable of withstanding a variety of environmental stressors such as low/high temperature, acidic/alkaline pH, high salinity, and expression of multi-enzyme complexes.…”
Section: Introductionmentioning
confidence: 99%
“…As a consequence, production of SCOAs was prevalent over solvents not only in experiments with glucose of this work, but also in those using synthetic vinasse. In fact, acidogenic fermentation tends to be the prevailing one especially at low concentrations of sugars in substrate (MONOT et al , 1982; MAGALHÃES et al , 2018). Additionally, it is noteworthy that even at 60 g Gli L −1 of initial concentration of carbon source, there are technical literature reports on cases of poor butanol generation (3.7 mg BuOH L −1 ) in a fermentation medium under pH controlled at 6.8 and 5.0 (GEORGE & CHEN, 1983).…”
Section: Resultsmentioning
confidence: 99%