Eucalyptus hydrolysate detoxification with activated charcoal adsorption or ion-exchange resins for xylitol production

Eucalyptus hemicellulosic hydrolysate used for xylitol production by Candida guilliermondii FTI20037 was previously treated either with ion-exchange resins or with activated charcoal adsorption combined with pH adjustment, in order that acetic acid, furfural and hydroxymethylfurfural could be removed. The best results for xylitol yield factor (0.76 g/g) and volumetric productivity (0.68 g/(l h) were attained when a three-fold concentrated hydrolysate was treated with ion-exchange resins. Using activated charcoal combined with pH adjustment for treating a three-fold concentrated hydrolysate resulted in a xylitol yield factor of 0.40 g/g and a volumetric productivity of 0.30 g/(l h). This same treatment applied to a six-fold concentrated hydrolysate resulted in a xylitol yield factor of 0.66 g/g and a volumetric productivity of 0.50 g/(l h).     

Adaptation yields a highly efficient xylose-fermenting Zymomonas mobilis strain

Zymomonas mobilis is a superb ethanol producer with productivity exceeding yeast strains by several fold. Although metabolic engineering was successfully applied to expand its substrate range to include xylose, xylose fermentation lagged far behind glucose. In addition, xylose fermentation was often incomplete when its initial concentration was higher than 5%. Improvement of xylose fermentation is therefore necessary. In this work, we applied adaptation to improve xylose fermentation in metabolically engineered strains. As a result of adaptation over 80 days and 30 serial transfers in a medium containing high concentration of xylose, a strain, referred as A3, with markedly improved xylose metabolism was obtained. The strain was able to grow on 10% (w/v) xylose and rapidly ferment xylose to ethanol within 2 days and retained high ethanol yield. Similarly, in mixed glucose-xylose fermentation, a total of 9% (w/v) ethanol was obtained from two doses of 5% glucose and 5% xylose (or a total of 10% glucose and 10% xylose). Further investigation reveals evidence for an altered xylitol metabolism in A3 with reduced xylitol formation. Additionally xylitol tolerance in A3 was increased. Furthermore, xylose isomerase activity was increased by several times in A3, allowing cells to channel more xylose to ethanol than to xylitol. Taken together, these results strongly suggest that altered xylitol metabolism is key to improved xylose metabolism in adapted A3 strain. This work further demonstrates that adaptation and metabolic engineering can be used synergistically for strain improvement.     

Influence of magnesium concentration on growth,ethanol and xylitol production by Pichia stipitis NRRL Y-7124

Summary The effect of Mg⁺² on Pichia stipitis growth and ethanol production was studied under condition of constant oxygen uptake rate (OUR) . Biomass/xylose and biomass/Mg⁺² yields increased with Mg⁺² concentration with a maximum value at Mg⁺² 4mM, ethanol being the main product obtained. At low Mg⁺² levels (ImM) 49 % of carbon flux to ethanol was redirected to xylitol production, accomplished through NADH intracellular accumulation.     

Microaerophilic metabolism of Pachysolen tannophilus at different pH values

Microaerophilic production of xylitol by Pachysolen tannophilus from detoxified hemicellulose hydrolyzate was optimal between pH values 6.0 to 7.5 when about 90% of xylose was utilized for xylitol production, the rest being fermented to ethanol. At pH values of 3.0 and 12.0, respiration became important, consuming up to 30% of available xylose. A graphic procedure suggests that histamine and cysteine are at the active site of xylose reductase in this yeast.     

Structure and Engineering of l-Arabinitol 4-Dehydrogenase from Neurospora crassa

l-Arabinitol 4-dehydrogenase (LAD) catalyzes the conversion of l-arabinitol into l-xylulose with concomitant NAD⁺ reduction. It is an essential enzyme in the development of recombinant organisms that convert l-arabinose into fuels and chemicals using the fungal l-arabinose catabolic pathway. Here we report the crystal structure of LAD from the filamentous fungus Neurospora crassa at 2.6 Å resolution. In addition, we created a number of site-directed variants of N. crassa LAD that are capable of utilizing NADP⁺ as cofactor, yielding the first example of LAD with an almost completely switched cofactor specificity. This work represents the first structural data on any LAD and provides a molecular basis for understanding the existing literature on the substrate specificity and cofactor specificity of this enzyme. The engineered LAD mutants with altered cofactor specificity should be useful for applications in industrial biotechnology.     

假丝酵母发酵玉米芯半纤维素水解液生产木糖醇

采用一株驯化过的假丝酵母(Candida sp.)直接发酵经过简单脱毒处理的玉米芯半纤维素水解液生产木糖醇。确定了水解液的最适浓缩倍数在3.0～3.72的范围内。利用正交实验,确定了摇瓶分批发酵工艺条件的最适组合为：摇床转速180r/min,起始C/N为50,起始pH 5.5,接种量5% (体积比)。在此基础上,重点研究了在发酵罐中通气量对酵母发酵玉米芯水解液生产木糖醇的影响。结果表明采用先高后低的分段通气发酵在木糖醇得率方面明显优于恒定通气发酵;其中,在0～24h,3.75 L/min;24～108h,1.25 L/min的分段通气条件下(装液量为2.5L),木糖醇得率(木糖醇/木糖,g/g) 达到0.75 g/g。该结果将有助于建立一种高效的、大规模的利用玉米芯半纤维素水解液发酵生产木糖醇的工艺。     

代谢工程改善野生酵母利用木糖产乙醇的性能

从256个自然样品中筛选得到1株可高效转化D-木糖的酵母。通过生理生化和分子生物学方法鉴定, 证实该菌株是属于Candida tropicalis。以该酵母为研究对象, 增加木糖醇脱氢酶表达量, 通过改变代谢流以达到提高酒精产率的目的。以pXY212-XYL2质粒为基础载体, 构建了含有潮霉素抗性的pYX212-XYL2-Hygro, 电击转化进入野生型C. tropicalis, 潮霉素抗性筛选, 得到含高拷贝木糖醇脱氢酶基因的重组菌株C. tropicalis XYL2-7。重组菌的比酶活达到0.5 u/mg protein, 比原始菌株提高了3倍。实验表明, 重组菌木糖醇得率比原始菌株降低了3倍, 酒精得率提高了5倍。首次通过实验验证了热带假丝酵母利用木糖产乙醇的可行性, 这对研究酵母利用秸秆、麦糠、谷壳等纤维质农业废弃物生产燃料乙醇具有重要启示。     

紫茎泽兰微生物发酵生产木糖醇的工艺

木糖醇（ｘｙｌｉｔｏｌ）是一种天然五碳多元醇,存在于许多水果、蔬菜及蘑菇中,但含量均很低,其中以蘑菇（ＡｇａｒｉｃｕｓｃａｍｐｅｓｔｒｉｓＬ．ｅｘＦｒ．）含量较高,约为１００ｍｇ／ｋｇ（干重）;木糖醇也是一种常见的代谢中间体,存在于哺乳动物的碳水化合...     

Novel amphiphilic fluoroalkylated derivatives of xylitol,D-glucose and D-galactose for medical applications: hemocompatibility and co-emulsifying properties

1-O-(4,4,5,5,6,6,7,7,8,8,9,9,9-Tridecafluorononyl)xylitol 6 was synthesized as a novel standard compound for the assessment of hemocompatibility and co-emulsifying properties in microemulsions for biomedical uses. 3-O-(1,1,2,4,4,5,7,7,8,8,9,9,9-Tridecafluoro-5-trifluoro-methyl-3,6-dioxanonyl)-D-glucose 9 and 6-O-(1,1,2,4,4,5,7,7,8,8,9,9,9-tridecafluoro-5-trifluoromethyl-3,6-dioxanonyl)-D-galactose 12 were synthesized by nucleophilic addition of protected carbohydrates to perfluorinated vinyl oligoether. Biological tests revealed very good hemocompatibility and co-emulsifying properties for the amphiphiles 6, 9 and 12.