2002
DOI: 10.1385/abab:98-100:1-9:341
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Characterization of Heterologous and Native Enzyme Activity Profiles in Metabolically Engineered Zymomonas mobilis Strains During Batch Fermentation of Glucose and Xylose Mixtures

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Cited by 28 publications
(8 citation statements)
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“…Xylose isomerase (XI) activity was assayed in a reaction mixture containing 1 mM triethanolamine (TEA) (pH 7.5), 0.3 mM NADH, 100 mM xylose, 10 mM MgSO 4 , 4 U/mL SDH (Roche Diagnostics, Indianapolis, IN) and 10 µL of crude cell extract (Gao et al, 2002; Schellenberg et al, 1984). Xylulokinase was assayed by a method a described in Akinterinwa and Cirino (2009).…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…Xylose isomerase (XI) activity was assayed in a reaction mixture containing 1 mM triethanolamine (TEA) (pH 7.5), 0.3 mM NADH, 100 mM xylose, 10 mM MgSO 4 , 4 U/mL SDH (Roche Diagnostics, Indianapolis, IN) and 10 µL of crude cell extract (Gao et al, 2002; Schellenberg et al, 1984). Xylulokinase was assayed by a method a described in Akinterinwa and Cirino (2009).…”
Section: Methodsmentioning
confidence: 99%
“…An important breakthrough came when Zhang et al (1995) successfully applied metabolic engineering to expand its substrate range to xylose. In the ensuing decade, however, xylose metabolism continued to be a focal point of research as it was found that the ability of engineered strains to metabolize xylose was considerably lower than that of glucose and improvement was needed (De Graaf et al, 1999; Gao et al, 2002; Jeon et al, 2005; Kim et al, 2000).…”
Section: Introductionmentioning
confidence: 99%
“…A number of different conversion technologies exist (Farrell et al 2006;Rammamorth et al 2000;Huber et al 2006) for the conversion of cellulosic biomass to biofuels. The predominant differentiation between the conversion options is the primary catalysis system (Foust et al 2008). Biochemical conversion routes rely on biocatalysts, such as enzymes and microbial cells, in addition to heat and chemicals to convert biomass first to an intermediate mixed sugar stream and then to ethanol or other fermentation produced biofuel.…”
Section: Introductionmentioning
confidence: 99%
“…The process and metabolic ethanol yields (Yp and Ym g/g) were calculated as the maximum amounts of ethanol formed per gram of initial fermentable sugars and of total sugar consumed, respectively. The ethanol volumetric productivity and sugar consumption rates (g/l h) were calculated as the amounts of ethanol produced and of sugar consumed per liter of medium per hour, respectively (Gao et al 2002). Lane M, protein molecular weight standard; lanes 1-3, the total proteins in transformants CP4-P1-1, CP4-P2-1, and CP4-P3-1 grown on xylose alone, respectively; lane 4, total protein in CP4 grown on glucose; lanes 5-6, total proteins in CP4 and CP4-P2-1 precultured on glucose alone, respectively; and lane 7, total protein from xylose-grown precultured cells of CP4-P2-1.…”
Section: Analytical Methods and Yield Calculationsmentioning
confidence: 99%
“…Foreign XI and XK enzymes are considered potential rate-limiting enzymes during xylose metabolism (Rogers et al 2007;Gao et al 2002); nevertheless, XK overexpression does not enhance xylose metabolism (Jeon et al 2005). TKT and TAL convert the intermediates of the pentose metabolism pathway into glyceraldehyde 3-phosphate and fructose 6-phosphate, key intermediates Electronic supplementary material The online version of this article (doi:10.1007/s10529-012-0897-4) contains supplementary material, which is available to authorized users.…”
Section: Introductionmentioning
confidence: 99%