The expression of a Pichia stipitis xylose reductase mutant with higher K(M) for NADPH increases ethanol production from xylose in recombinant Saccharomyces cerevisiae

Xylose fermentation by Saccharomyces cerevisiae requires the introduction of a xylose pathway, either similar to that found in the natural xylose-utilizing yeasts Pichia stipitis and Candida shehatae or similar to the bacterial pathway. The use of NAD(P)H-dependent XR and NAD(+)-dependent XDH from P. stipitis creates a cofactor imbalance resulting in xylitol formation. The effect of replacing the native P. stipitis XR with a mutated XR with increased K(M) for NADPH was investigated for xylose fermentation to ethanol by recombinant S. cerevisiae strains. Enhanced ethanol yields accompanied by decreased xylitol yields were obtained in strains carrying the mutated XR. Flux analysis showed that strains harboring the mutated XR utilized a larger fraction of NADH for xylose reduction. The overproduction of the mutated XR resulted in an ethanol yield of 0.40 g per gram of sugar and a xylose consumption rate of 0.16 g per gram of biomass per hour in chemostat culture (0.06/h) with 10 g/L glucose and 10 g/L xylose as carbon source.     

Batch xylitol production from wheat straw hemicellulosic hydrolysate using Candida guilliermondii in a stirred tank reactor

Batch production of xylitol from the hydrolysate of wheat straw hemicellulose using Candida guilliermondii was carried out in a stirred tank reactor (agitation speed of 300 rpm, aeration rate of 0.6 vvm and initial cell concentration of 0.5 g l^–1). After 54 h, xylitol production from 30.5 g xylose l^–1 reached 27.5 g l^–1, resulting in a xylose-to-xylitol bioconversion yield of 0.9 g g^–1 and a productivity of 0.5 g l^–1 h^–1.     

Optimization of fed-batch fermentation for xylitol production by Candida tropicalis

Xylitol, a functional sweetener, was produced from xylose by biological conversion using Candida tropicalis ATCC 13803. Based on a two-substrate fermentation using glucose for cell growth and xylose for xylitol production, fed-batch fermentations were undertaken to increase the final xylitol concentration. The effects of xylose and xylitol on xylitol production rate were studied to determine the optimum concentrations for fed-batch fermentation. Xylose concentration in the medium (100 g l⁻¹) and less than 200 g l⁻¹ total xylose plus xylitol concentration were determined as optimum for maximum xylitol production rate and xylitol yield. Increasing the concentrations of xylose and xylitol decreased the rate and yield of xylitol production and the specific cell growth rate, probably because of an increase in osmotic stress that would interfere with xylose transport, xylitol flux to secretion to cell metabolism. The feeding rate of xylose solution during the fed-batch mode of operation was determined by using the mass balance equations and kinetic parameters involved in the equations in order to increase final xylitol concentration without affecting xylitol and productivity. The optimized fed-batch fermentation resulted in 187 g l⁻¹ xylitol concentration, 0.75 g xylitol g xylose⁻¹ xylitol yield and 3.9 g xylitol l⁻¹ h⁻¹ volumetric productivity. Journal of Industrial Microbiology & Biotechnology (2002) 29, 16–19 doi:10.1038/sj.jim.7000257 Received 15 October 2001/ Accepted in revised form 30 March 2002     

The production of xylitol by enzymatic hydrolysis of agricultural wastes

Agricultural waste products, beech wood and walnut shells, were hydrolyzed at 40°C using mixed crude enzymes produced byPenicillium sp. AHT-1 andRhizomucor pusillus HHT-1.d-xylose, 4.1 g and 15.1 g was produced from the hydrolysis of 100 g of beech wood and walnut shells, respectively. For xylitol production,Candida tropicalis IFO0618 and the waste product hydrolyzed solutions were used. The effects on xylitol production, of adding glucose as a NADPH source,d-xylose and yeast extract, were examined. Finally, a 50% yield of xylitol was obtained by using the beech wood hydrolyzed solution with the addition of 1% yeast extract and 1% glucose at an initial concentration.     

半纤维素水解物生物转化生产木糖醇

木糖醇在食品、医药及化工行业中有着广泛的用途而深受关注。但是,传统的化学法生产木糖醇需要一系列复杂的分离纯化步骤,过高的生产成本限制了木糖醇的使用范围。发酵工艺生产木糖醇无需木糖的纯化步骤,是取代化学合成法的一条可行工艺路线。本文着重介绍产木糖醇的微生物,酵母对木糖的同化途径,半纤维素水解物的脱毒方法,影响木糖醇发酵的工艺条件等。     

Optimization of D-xylose to xylitol biotransformation by Candida guilliermondii cells permeabilized with Triton X-100

Abstract

The effect of NADP⁺ and glucose-6-phosphate (G6P) on the biotransformation of D-xylose to xylitol by cells of Candida guilliermondii permeabilized with surfactant Triton X-100 was evaluated. The experimental runs were performed with 12 g L^?1 of permeabilized cells and a reaction medium composed of Tris–HCl buffer (0.1 M pH 7), D-xylose (57 g L^?1), and MgCl₂.6H₂O (5 mM). The levels of NADP⁺ (from 0.0 to 1.7 mM) and G6P (from 0.00 to 0.17 M) were varied according a 2²-full factorial composed design. Under optimized conditions (NADP⁺ 0.5 mM and 0.05 M G6P), the xylitol volumetric productivity (Q_P) and yield factor (Y_P/S) predicted were 1.86 ± 0.03 g L^?1 h^{? 1} and 0.64 ± 0.03 g g^?1, respectively. These values were 94% and 19% higher than those obtained with unpermeabilized cells under fermentation conditions (0.97 g L^?1 h^?1 and 0.53 g g^?1, respectively). On the basis of the results, it can be concluded that xylitol production by biotransformation with cells of C. guilliermondii permeabilized with Triton X-100 is a promising alternative to the fermentative process.     

Molecular analysis of NAD+-dependent xylitol dehydrogenase from the zygomycetous fungus Rhizomucor pusillus and reversal of the coenzyme preference

The zygomycetous fungus Rhizomucor pusillus NBRC 4578 is able to ferment not only d-glucose but also d-xylose into ethanol. Xylitol dehydrogenase from R. pusillus NBRC 4578 (RpXDH), which catalyzes the second step of d-xylose metabolism, was purified, and its enzymatic properties were characterized. The purified RpXDH preferred NAD⁺ as its coenzyme and showed substrate specificity for xylitol, d-sorbitol, and ribitol. cDNA cloning of xyl2 gene encoding RpXDH revealed that the gene included a coding sequence of 1,092?bp with a molecular mass of 39,185?kDa. Expression of the xyl2 in R. pusillus NBRC 4578 was induced by d-xylose, and the expression levels were increased with accumulation of xylitol. The xyl2 gene was expressed in Escherichia coli, and coenzyme preference of the recombinant RpXDH was reversed from NAD⁺ to NADP⁺ in the double mutant D205A/I206R by site-directed mutagenesis.     

葡萄糖酸氧化杆菌木糖醇脱氢酶基因的克隆与表达

【目的】获得葡萄糖酸氧化杆菌(Gluconobacter oxydans CGMCC 1.637)的木糖醇脱氢酶基因,研究其酶学性质及碳源特别是D-阿拉伯醇和木糖醇对该酶活性的影响。【方法】通过已报道序列的木糖醇脱氢酶的保守区设计引物,用聚合酶链式反应(polymerase chain reaction,PCR)扩增获得目的基因片段。根据获得的片段序列设计引物克隆目的基因的5’和3’片段,将所获得的片段拼接,获得完整的木糖醇脱氢酶基因。通过构建工程菌获得重组蛋白,并利用氧化还原反应测定重组酶的活性。用含不同碳源的培养基培养G.oxydans CGMCC 1.637,并测定其破胞上清液木糖醇脱氢酶氧化木糖醇的活性;用不同碳源培养的G.oxydans CGMCC 1.637转化木酮糖,用高效液相色谱法测定木糖醇的产量。【结果】获得一个新的798bp的木糖醇脱氢酶基因,所编码的木糖醇脱氢酶含265个氨基酸,属于短链脱氢酶家族。酶学性质研究发现,该木糖醇脱氢酶催化木糖醇氧化的最适合条件为35℃、pH 10.0,最高活性为23.27 U/mg,催化木酮糖还原为木糖醇的最适条件为30℃、pH 6.0。最高活性为255.55 U/mg;该木糖醇脱氢酶的对木糖醇的Km和Vmax分别为78.97 mmol/L和40.17 U/mg。碳源诱导实验表明,d-山梨醇对G.oxydans CGMCC 1.637木糖醇脱氢酶的活性有明显的促进作用,而葡萄糖、果糖、木糖、木糖醇、D-阿拉伯醇对木糖醇脱氢酶活性有明显的抑制作用。而在转化实验中,用d-甘露糖培养的G.oxydans CGMCC 1.637的转化能力明显高于其他碳源培养的G.oxydans CGMCC 1.637的转化能力,其中,用阿拉伯醇培养的G.oxydans CGMCC 1.637的转化能力最低,仅为对照的35%。【结论】克隆自G.oxydans CGMCC 1.637的木糖醇脱氢酶基因是一个新的基因,用阿拉伯醇培养的G.oxydans CGMCC 1.637破胞液木糖醇脱氢酶活性低;且阿拉伯醇对G.oxydans CGMCC 1.637木酮糖的还原能力具有抑制作用。     

Influence of Medium Composition on Xylitol Bioproduction from Wheat Straw Hemicellulosic Hydrolysate

Summary Xylose-to-xylitol batch bioconversions from wheat straw hemicellulosic hydrolysate were carried out in Erlenmeyer flasks in order to assess the influence of medium composition (hydrolysate concentration, supplementation with ammonium sulphate, calcium chloride and rice bran extract, and initial pH) on xylitol production, productivity and yield. By using the screening design and the response surface methodologies, the statistically significant variables influencing the bioconversion were selected and linear models were fitted to the experimental data. According to the results, the best conditions to perform the bioconversion consisted in using a threefold concentrated hydrolysate supplemented with ammonium sulphate (1.0 g/l) and rice bran extract (5.0 g/l), whose pH was adjusted to 6.0 prior to inoculation. Under these conditions, a xylitol production of 24.17 g/l was observed after 72 h of fermentation, resulting in a productivity of 0.34 g/l h and in a bioconversion yield of 0.49 g/g.     

酵母发酵蔗渣半纤维素水解物生产木糖酶

采用二次正交旋转组合设计研究了蔗渣半纤维素水解过程中硫酸浓度与液 固比对木糖收率的影响。回归分析表明 ,这两个因素与木糖的收率之间存在显著的回归关系。通过回归方程优化水解条件 ,当硫酸浓度 2 .4g L ,液 固 =6 .2 ,在蒸汽压力 2 .5× 10 4Pa的条件下水解 2 .5h ,10 0g蔗渣可水解生成木糖约 2 4g。大孔树脂吸附层析处理蔗渣半纤维素水解物 ,能有效地减少其中的酵母生长抑制物含量 ,显著改善水解物的发酵性能。用大孔树脂在pH 2条件下处理过的蔗渣半纤维素水解物作基质 ,含木糖 2 0 0g L ,产木糖醇酵母菌株CandidatropicalisAS2 .1776发酵 110h耗完基质中的木糖 ,生成木糖醇 12 7g L ,产物转化率 0 .6 4(木糖醇g 木糖g) ,产物生成速率 1.15g L·h .