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                }
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            "abstractNote": "BACKGROUND: Ethanolic fermentation of lignocellulosic biomass is a sustainable option for the production of bioethanol. This process would greatly benefit from recombinant Saccharomyces cerevisiae strains also able to ferment, besides the hexose sugar fraction, the pentose sugars, arabinose and xylose. Different pathways can be introduced in S. cerevisiae to provide arabinose and xylose utilisation. In this study, the bacterial arabinose isomerase pathway was combined with two different xylose utilisation pathways: the xylose reductase/xylitol dehydrogenase and xylose isomerase pathways, respectively, in genetically identical strains. The strains were compared with respect to aerobic growth in arabinose and xylose batch culture and in anaerobic batch fermentation of a mixture of glucose, arabinose and xylose. RESULTS: The specific aerobic arabinose growth rate was identical, 0.03 h-1, for the xylose reductase/xylitol dehydrogenase and xylose isomerase strain. The xylose reductase/xylitol dehydrogenase strain displayed higher aerobic growth rate on xylose, 0.14 h-1, and higher specific xylose consumption rate in anaerobic batch fermentation, 0.09 g (g cells)-1 h-1 than the xylose isomerase strain, which only reached 0.03 h-1 and 0.02 g (g cells)-1h-1, respectively. Whereas the xylose reductase/xylitol dehydrogenase strain produced higher ethanol yield on total sugars, 0.23 g g-1 compared with 0.18 g g-1 for the xylose isomerase strain, the xylose isomerase strain achieved higher ethanol yield on consumed sugars, 0.41 g g-1 compared with 0.32 g g-1 for the xylose reductase/xylitol dehydrogenase strain. Anaerobic fermentation of a mixture of glucose, arabinose and xylose resulted in higher final ethanol concentration, 14.7 g l-1 for the xylose reductase/xylitol dehydrogenase strain compared with 11.8 g l-1 for the xylose isomerase strain, and in higher specific ethanol productivity, 0.024 g (g cells)-1 h-1 compared with 0.01 g (g cells)-1 h-1 for the xylose reductase/xylitol dehydrogenase strain and the xylose isomerase strain, respectively. CONCLUSION: The combination of the xylose reductase/xylitol dehydrogenase pathway and the bacterial arabinose isomerase pathway resulted in both higher pentose sugar uptake and higher overall ethanol production than the combination of the xylose isomerase pathway and the bacterial arabinose isomerase pathway. Moreover, the flux through the bacterial arabinose pathway did not increase when combined with the xylose isomerase pathway. This suggests that the low activity of the bacterial arabinose pathway cannot be ascribed to arabitol formation via the xylose reductase enzyme.",
            "publicationTitle": "Biotechnology for Biofuels",
            "publisher": "",
            "place": "",
            "date": "2008",
            "volume": "1",
            "issue": "1",
            "section": "",
            "partNumber": "",
            "partTitle": "",
            "pages": "16",
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            "seriesTitle": "",
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            "journalAbbreviation": "Biotechnology for Biofuels",
            "DOI": "10.1186/1754-6834-1-16",
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            "url": "http://www.ncbi.nlm.nih.gov/pubmed/18947407",
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            "creatorSummary": "Lu et al.",
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            "title": "Cellulase adsorption and an evaluation of enzyme recycle during hydrolysis of steam-exploded softwood residues",
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                    "firstName": "Yanpin",
                    "lastName": "Lu"
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                {
                    "creatorType": "author",
                    "firstName": "Bin",
                    "lastName": "Yang"
                },
                {
                    "creatorType": "author",
                    "firstName": "David",
                    "lastName": "Gregg"
                },
                {
                    "creatorType": "author",
                    "firstName": "John",
                    "lastName": "Saddler"
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                    "creatorType": "author",
                    "firstName": "Shawn",
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            ],
            "abstractNote": "The sugar yield and enzyme adsorption profile obtained during the hydrolysis of SO2-catalyzed steam-exploded Douglas-fir and posttreated steamexploded Douglas-fir substrates were determined. After hot alkali\nperoxide posttreatment, the rates and yield of hydrolysis attained from the posttreated Douglas-fir were significantly higher,\neven at lower enzyme loadings, than those obtained with the corresponding steam-exploded Douglas-fir. The enzymatic adsorption\nprofiles observed during hydrolysis of the two substrates were significantly different. Ultrafiltration was employed to recover\nenzyme in solution (supernatant) and reused in subsequent hydrolysis reactions with added, fresh substrate. These recycle\nfindings suggested that the enzyme remained relatively active for three rounds of recycle. It is likely that enzyme recovery\nand reuse during the hydrolysis of posttreated softwood substrates could lead to reductions in the need for the addition of\nfresh enzyme during softwood-based bioconversion processes.",
            "publicationTitle": "Applied Biochemistry and Biotechnology",
            "publisher": "",
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            "date": "March 09, 2002",
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            "title": "Butanol production from agricultural residues: Impact of degradation products on Clostridium beijerinckii growth and butanol fermentation.",
            "creators": [
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                    "creatorType": "author",
                    "firstName": "T.",
                    "lastName": "Ezeji"
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                    "firstName": "N.",
                    "lastName": "Qureshi"
                },
                {
                    "creatorType": "author",
                    "firstName": "H. P.",
                    "lastName": "Blaschek"
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            "abstractNote": "During pretreatment and hydrolysis of fiberrich\nagricultural biomass, compounds such as salts, furfural,\nhydroxymethyl furfural (HMF), acetic, ferulic, glucuronic,\nr-coumaric acids, and phenolic compounds are produced.\nClostridium beijerinckii BA101 can utilize the individual\nsugars present in lignocellulosic [e.g., corn fiber, distillers\ndry grain solubles (DDGS), etc] hydrolysates such as cellobiose,\nglucose, mannose, arabinose, and xylose. In these\nstudies we investigated the effect of some of the lignocellulosic\nhydrolysate inhibitors associated with C. beijerinckii\nBA101 growth and acetone–butanol–ethanol (ABE) production.\nWhen 0.3 g/L r-coumaric and ferulic acids were\nintroduced into the fermentation medium, growth and\nABE production by C. beijerinckii BA101 decreased significantly.\nFurfural and HMF are not inhibitory to C. beijerinckii\nBA101; rather they have stimulatory effect on the growth of\nthe microorganism and ABE production.",
            "publicationTitle": "Biotechnology and Bioengineering",
            "publisher": "",
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            "date": "2007",
            "volume": "97",
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            "title": "Bioproduction of butanol from biomass: From genes to bioreactors",
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                    "firstName": "T. C.",
                    "lastName": "Ezeji"
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                {
                    "creatorType": "author",
                    "firstName": "H. P.",
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            ],
            "abstractNote": "Butanol is produced chemically using either the oxo process\nstarting from propylene (with H2 and CO over a rhodium\ncatalyst) or the aldol process starting from acetaldehyde. The\nkey problems associated with the bioproduction of butanol are\nthe cost of substrate and butanol toxicity/inhibition of the\nfermenting microorganisms, resulting in a low butanol titer in\nthe fermentation broth. Recent interest in the production of\nbiobutanol from biomass has led to the re-examination of\nacetone-butanol-ethanol (ABE) fermentation, including\nstrategies for reducing or eliminating butanol toxicity to the\nculture and for manipulating the culture to achieve better\nproduct specificity and yield. Advances in integrated\nfermentation and in situ product removal processes have\nresulted in a dramatic reduction of process streams, reduced\nbutanol toxicity to the fermenting microorganisms, improved\nsubstrate utilization, and overall improved bioreactor\nperformance.",
            "publicationTitle": "Current opinion in biotechnology",
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                    "lastName": "Dien"
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                {
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                    "lastName": "Cotta"
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                    "firstName": "T.W.",
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            ],
            "abstractNote": "The lack of industrially suitable microorganisms for converting biomass into fuel ethanol has traditionally been cited as a major technical roadblock to developing a bioethanol industry. In the last two decades, numerous microorganisms have been engineered to selectively produce ethanol. Lignocellulosic biomass contains complex carbohydrates that necessitate utilizing microorganisms capable of fermenting sugars not fermentable by brewers' yeast. The most significant of these is xylose. The greatest successes have been in the engineering of Gram-negative bacteria: Escherichia coli, Klebsiella oxytoca, and Zymomonas mobilis. E. coli and K. oxytoca are naturally able to use a wide spectrum of sugars, and work has concentrated on engineering these strains to selectively produce ethanol. Z. mobilis produces ethanol at high yields, but ferments only glucose and fructose. Work on this organism has concentrated on introducing pathways for the fermentation of arabinose and xylose. The history of constructing these strains and current progress in refining them are detailed in this review.",
            "publicationTitle": "Applied Microbiology and Biotechnology",
            "publisher": "",
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            ],
            "abstractNote": "The fermentability of a corn cob, acid-hydrolysed hemicellulose by Pichia stipitis was considerably improved by pre-treatment with Ca(OH)2. The total sugars utilized and ethanol yield for the untreated hydrolysate were 18% and 0.21 g/g, respectively, compared with 82% and 0.32 g/g respectively for the treated material. Adaptation of the yeast to the hydrolysate resulted in a significantly higher fermentation rate with over 90% of the initial total sugars being utilized and an ethanol yield and maximum ethanol concentration of 0.41 g/g and 13.3 g/l, respectively.",
            "publicationTitle": "World Journal of Microbiology and Biotechnology",
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            "title": "What is (and is not) vital to advancing cellulosic ethanol",
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                    "creatorType": "author",
                    "firstName": "Charles E.",
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            "abstractNote": "Ethanol made biologically from cellulosic biomass, including agricultural and forestry residues, portions of municipal waste, and herbaceous and woody crops, is finally being widely recognized as a unique transportation fuel with powerful economic, environmental and strategic attributes. Although underfunded, it has been advanced to be competitive with corn ethanol; however, government policies are needed to overcome the perceived risk of first applications if we are to realize its societal benefits soon. Costs below those for fossil sources are foreseeable, with advances in pretreatment, enzyme production, and enzymatic hydrolysis - the steps that overcome the natural resistance of plants to biological breakdown - offering, by far, the greatest economic leverage. We must also build on the wisdom gained from past experience to avoid directing limited funds to projects that offer little new insight, could have marginal impact on commercial outcomes, or could be better improved through the power and wisdom of the learning curve.",
            "publicationTitle": "Trends in Biotechnology",
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            "date": "April 2007",
            "volume": "25",
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            "DOI": "10.1016/j.tibtech.2007.02.009",
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            "creatorSummary": "Hahn-Hägerdal et al.",
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            "itemType": "journalArticle",
            "title": "Towards industrial pentose-fermenting yeast strains",
            "creators": [
                {
                    "creatorType": "author",
                    "firstName": "Bärbel",
                    "lastName": "Hahn-Hägerdal"
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                {
                    "creatorType": "author",
                    "firstName": "Kaisa",
                    "lastName": "Karhumaa"
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                    "firstName": "César",
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                    "firstName": "Isabel",
                    "lastName": "Spencer-Martins"
                },
                {
                    "creatorType": "author",
                    "firstName": "Marie",
                    "lastName": "Gorwa-Grauslund"
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            ],
            "abstractNote": "Production of bioethanol from forest and agricultural products requires a fermenting organism that converts all types of sugars in the raw material to ethanol in high yield and with a high rate. This review summarizes recent research aiming at developing industrial strains of Saccharomyces cerevisiae with the ability to ferment all lignocellulose-derived sugars. The properties required from the industrial yeast strains are discussed in relation to four benchmarks: (1) process water economy, (2) inhibitor tolerance, (3) ethanol yield, and (4) specific ethanol productivity. Of particular importance is the tolerance of the fermenting organism to fermentation inhibitors formed during fractionation/pretreatment and hydrolysis of the raw material, which necessitates the use of robust industrial strain background. While numerous metabolic engineering strategies have been developed in laboratory yeast strains, only a few approaches have been realized in industrial strains. The fermentation performance of the existing industrial pentose-fermenting S. cerevisiae strains in lignocellulose hydrolysate is reviewed. Ethanol yields of more than 0.4 g ethanol/g sugar have been achieved with several xylose-fermenting industrial strains such as TMB 3400, TMB 3006, and 424A(LNF-ST), carrying the heterologous xylose utilization pathway consisting of xylose reductase and xylitol dehydrogenase, which demonstrates the potential of pentose fermentation in improving lignocellulosic ethanol production.",
            "publicationTitle": "Applied Microbiology and Biotechnology",
            "publisher": "",
            "place": "",
            "date": "April 01, 2007",
            "volume": "74",
            "issue": "5",
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            "pages": "937-953",
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            "DOI": "10.1007/s00253-006-0827-2",
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            "dateAdded": "2009-06-24T12:28:27Z",
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    {
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            },
            "creatorSummary": "Monavari et al.",
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            "version": 1,
            "itemType": "journalArticle",
            "title": "The influence of solid/liquid separation techniques on the sugar yield in two-step dilute acid hydrolysis of softwood followed by enzymatic hydrolysis",
            "creators": [
                {
                    "creatorType": "author",
                    "firstName": "Sanam",
                    "lastName": "Monavari"
                },
                {
                    "creatorType": "author",
                    "firstName": "Mats",
                    "lastName": "Galbe"
                },
                {
                    "creatorType": "author",
                    "firstName": "Guido",
                    "lastName": "Zacchi"
                }
            ],
            "abstractNote": "ABSTRACT: BACKGROUND: Two-step dilute acid hydrolysis of softwood, either as a stand-alone process or as pretreatment before enzymatic hydrolysis, is considered to result in higher sugar yields than one-step acid hydrolysis. However, this requires removal of the liquid between the two steps. In an industrial process, filtration and washing of the material between the two steps is difficult, as it should be performed at high pressure to reduce energy demand. Moreover, the application of pressure leads to more compact solids, which may affect subsequent processing steps. This study was carried out to investigate the influence of pressing the biomass, in combination with the effects of not washing the material, on the sugar yield obtained from two-step dilute acid hydrolysis, with and without subsequent enzymatic digestion of the solids. RESULTS: Washing the material between the two acid hydrolysis steps, followed by enzymatic digestion, resulted in recovery of 96% of the mannose and 81% of the glucose (% of the theoretical) in the liquid fraction, regardless of the choice of dewatering method (pressing or vacuum filtration). Not washing the solids between the two acid hydrolysis steps led to elevated acidity of the remaining solids during the second hydrolysis step, which resulted in lower yields of mannose, 85% and 74% of the theoretical, for the pressed and vacuum-filtered slurry, respectively, due to sugar degradation. However, this increase in acidity resulted in a higher glucose yield (94.2%) from pressed slurry than from filtered slurry (77.6%). CONCLUSION: Pressing the washed material between the two acid hydrolysis steps had no significant negative effect on the sugar yields of the second acid hydrolysis step or on enzymatic hydrolysis. Not washing the material resulted in a harsher second acid hydrolysis step, which caused greater degradation of the sugars during subsequent acid hydrolysis of the solids, particularly in case of the vacuum-filtered solids. However, pressing in combination with not washing the material between the two steps enhanced the sugar yield of the enzymatic digestion step. Hence, it is suggested that the unwashed slurry be pressed to as high a dry matter content as possible between the two acid hydrolysis stages in order to achieve high final sugar yields.",
            "publicationTitle": "Biotechnology for Biofuels",
            "publisher": "",
            "place": "",
            "date": "2009",
            "volume": "2",
            "issue": "1",
            "section": "",
            "partNumber": "",
            "partTitle": "",
            "pages": "6",
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            "seriesTitle": "",
            "seriesText": "",
            "journalAbbreviation": "Biotechnol Biofuels",
            "DOI": "10.1186/1754-6834-2-6",
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            "url": "http://www.ncbi.nlm.nih.gov/pubmed/19291286",
            "accessDate": "2009-06-12T15:08:39Z",
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            "extra": "PMID: 19291286",
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