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。     

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。     

热带假丝酵母ctpxa1基因缺失菌的构建及对长链二元酸积累的影响

Pxa1p为酿酒酵母Saccharomyces cerevisiae过氧化物酶体上的膜蛋白,与Pxa2p组成二聚体,参与转运长链脂肪酸进入过氧化物酶体过程。热带假丝酵母能够发酵烷烃和脂肪酸生产长链二元酸,而过氧化物酶体中发生的β-氧化会消耗产生的长链二元酸造成产率降低。本研究以热带假丝酵母Candida tropicalis 1798为宿主菌,通过基于PCR片段的同源单交换法,快速构建ctpxa1基因敲除菌株C.tropicalis 1798-pxa1。利用半定量RT-PCR技术,检测ctpxa1基因在C.tropicalis 1798、C.tropicalis 1798-pxa1的表达量,灰度值比值为2.03,表明ctpxa1在C.tropicalis 1798-pxa1中的表达被弱化。经144 h发酵,C.tropicalis 1798-pxa1比C.tropicalis 1798的十二碳二元酸产量明显提升,其产出浓度为10.3 g/L,比野生型菌株C.tropicalis 1798提高了94.3%。     

热带假丝酵母(Candida tropiclis)去除蔗渣木聚糖酶解副产物的研究

该文研究了木糖、木糖醇对木聚糖酶Shearzyme 500L酶解蔗渣木聚糖的影响。通过热带假丝酵母(Candida tropiclis)转化酶解副产物木糖,解除木糖对木聚糖酶的抑制作用,从而获得高木二糖含量的低聚木糖。结果表明:木糖是Shearzyme 500L的酶活性抑制物,其抑制作用与溶液中的木糖量成正比;木糖醇对木聚糖酶无抑制作用;热带假丝酵母可将蔗渣木聚糖酶解液中的木糖转化为木糖醇而不利用低聚木糖,木二糖占总糖比例由53.09%升高到62.92%,经二次酶解后,木二糖比例可达78.90%。     

能源上的应用

900841 木糖的同步发酵和异构化[英] 利用凝结芽孢杆菌(Bacillus coagulans)细胞的市售固定化木糖异构酶,通过将蔗糖转化为木酮糖,从而用木糖制备出乙醇。采用嫌气发酵可同步将木酮糖转化乙醇,所用酵母菌株有热带假丝酵母(Candida tropicalis)ATCC 9968、Y-11860和Y-1552、休哈塔假丝酵母(C.     

代谢改造热带假丝酵母发酵木糖母液生产木糖醇

木糖醇是一种在食品、医药、轻工等领域具有广泛用途的多元醇,目前主要通过酸水解木聚糖获得木糖并进一步化学催化加氢方法制备。提取木糖过程中会产生大量的木糖母液副产物,其中含有一定浓度的葡萄糖、木糖、阿拉伯糖等碳源,以及少量的糠醛、四氢呋喃等物质。研究微生物转化木糖母液生产高附加值化学品不仅能够提高木糖母液的利用价值,而且能够减少环境污染。热带假丝酵母不仅能够利用葡萄糖,也具有高效的木糖代谢途径。首先利用代谢工程技术删除了热带假丝酵母菌株的木糖醇脱氢酶基因,获得能够转化木糖积累木糖醇的突变株。在此基础上,评价了突变株在木糖母液培养基中的发酵性能。通过单因素优化实验确定了突变株发酵生产木糖醇较优的发酵工艺:培养基组成为木糖母液300g/L,玉米浆5g/L;最佳发酵条件为:发酵温度35℃,初始p H为5.0,接种量15%,200r/min摇床培养140h。利用优化后的发酵工艺,木糖醇产量达到83.01g/L。初步建立了转化木糖母液生产木糖醇的工艺,为进一步利用木糖母液奠定了基础。     

高效发酵木糖生产乙醇酵母菌株的构建

获得高效发酵木糖生产乙醇的酵母菌株是木质纤维素生物转化生产燃料乙醇的重要前提。在4%乙醇驯化的基础上,选择了乙醇耐性提高的休哈塔假丝酵母（Candida shehatae）CICC1766菌株进一步进行紫外诱变,得到了木糖发酵性能较强的呼吸缺陷型突变体,并与乙醇发酵性能良好的酿酒酵母（Saccharomyces cerevisiae）ATCC4126进行原生质体融合。采用单亲灭活法对休哈塔假丝酵母原生质体进行紫外灭活,在聚乙二醇（PEG）诱导下融合,对得到的融合子进行木糖发酵能力测定,选择到了一株能够更好地利用木糖产乙醇,并且木糖发酵性能比亲本得到明显提高的融合子F6,此融合子发酵50 g/L木糖,最高乙醇浓度达到18.75g/L,乙醇得率为0.375,达到理论转化值0.511的73.4%。与原始出发菌株CICC1766相比,乙醇产量提高了28%。     

芝麻香型白酒大曲中酵母菌的分离与鉴定

为了开发利用白酒大曲中的酵母菌资源,采用稀释涂布平板法,从芝麻香型白酒大曲中分离得到15株酵母菌株。利用26S rRNA基因序列分析技术对其进行分类鉴定。结果表明,其中6株酵母菌为酿酒酵母（Saccharomyces cerevisiae）,6株为库德里阿兹威氏毕赤酵母（Pichia kudriavzevii）,3株为热带假丝酵母（Candida tropicalis）;并对代表菌株Y1、Y2及Y4进行了形态观察;最后通过随机扩增多态性DNA标记（random amplified polymorphic DNA, RAPD）对分离得到的酵母菌进行分型,表明6株酿酒酵母分属于5个株型,6株库德里阿兹威氏毕赤酵母分属于5个株型,3株热带假丝酵母分属于3个株型。     

麦芽糖假丝酵母菌混合糖代谢的发酵特性

葡萄糖和木糖的混合糖共代谢是木质纤维素资源高效转化利用的关键环节。利用本实验室保藏的天然木糖利用酵母菌,麦芽糖假丝酵母(Candida maltosa)Xu316,本研究对该菌代谢利用不同比例的葡萄糖、木糖发酵特性进行了系统测试,总结了麦芽糖假丝酵母混合糖代谢的一般规律。研究结果表明麦芽糖假丝酵母菌具有较高的葡萄糖利用率和木糖醇积累能力。在糖浓度低于20%时,该菌可以共同利用葡萄糖和木糖,最大乙醇产量和木糖醇产量分别为0.43g·g-1和0.58g·g-1,具有工业应用生产生物基产品的潜力。     

产核酸和乳糖酶的热带假丝酵母QZN0209培养条件研究

经筛选得到一株具有一定核酸含量和乳糖酶活力的热带假丝酵母（Candida tropicalis)QZN0209,以综合利用酵母为目的,通过着重优化该菌株产核酸的培养条件。将其摇瓶产核酸水平从4.16%提高至13.94%;同时改变乳糖诱导方法将其乳糖酶活力提高约4倍,达到10.56ONPG单位/g湿菌体。     

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 .     

Xylitol production from xylose by two yeast strains: Sugar tolerance

The kinetics and enzymology ofd-xylose utilization are studied in micro-, semi-, and aerobic batch cultures during growth ofCandida guilliermondii andCandida parapsilosis in the presence of several initial xylose concentrations. The abilities of xylitol accumulation by these two yeast strains are high and similar, although observed under various growth conditions. WithCandida parapsilosis, optimal xylitol production yield (0.74 g/g) was obtained in microaerobiosis with 100 g/L of xylose, whereas optimal conditions to produce xylitol byCandida guilliermondii (0.69 g/g) arose from aerobiosis with 300 g/L of sugar. The different behavior of these yeasts is most probably explained by differences in the nature of the initial step of xylose metabolism: a NADPH-linked xylose reductase activity is measured with a weaker NADH-linked activity. These activities seem to be dependent on the degree of aerobiosis and on the initial xylose concentration and correlate with xylitol accumulation.     

休哈塔假丝酵母乙醇发酵性能的研究

木糖的高效发酵是制约纤维素燃料乙醇生产的技术瓶颈之一,高性能发酵菌种的开发是本领域研究的重点。以木糖发酵的典型菌株休哈塔假丝酵母为材料,研究氮源配比、葡萄糖和木糖初始浓度、葡萄糖添加及典型抑制物等因素对其木糖利用和乙醇发酵性能的影响规律。结果表明,硫酸铵更适宜于木糖和葡萄糖发酵产乙醇。在摇瓶振荡发酵条件下,该酵母可发酵164.0 g/L葡萄糖生成61.9 g/L乙醇,糖利用率和乙醇得率分别为99.8%和74.0%;受酵母细胞膜上转运体系的限制,对木糖的最高发酵浓度为120.0 g/L,可生成45.7 g/L乙醇,糖利用率和乙醇得率分别达到94.8%和87.0%。休哈塔假丝酵母发酵木糖的主要产物为乙醇,仅生成微量的木糖醇;添加葡萄糖可促进木糖的利用;休哈塔假丝酵母在葡萄糖发酵时的乙酸和甲酸的耐受浓度分别为8.32和2.55 g/L,木糖发酵时的乙酸和甲酸的耐受浓度分别为6.28和1.15 g/L。     

Kinetic behavior of Candida guilliermondii yeast during xylitol production from Brewer's spent grain hemicellulosic hydrolysate

Brewer's spent grain, the main byproduct of breweries, was hydrolyzed with dilute sulfuric acid to produce a hemicellulosic hydrolysate (containing xylose as the main sugar). The obtained hydrolysate was used as cultivation medium by Candidaguilliermondii yeast in the raw form (containing 20 g/L xylose) and after concentration (85 g/L xylose), and the kinetic behavior of the yeast during xylitol production was evaluated in both media. Assays in semisynthetic media were also performed to compare the yeast performance in media without toxic compounds. According to the results, the kinetic behavior of the yeast cultivated in raw hydrolysate was as effective as in semisynthetic medium containing 20 g/L xylose. However, in concentrated hydrolysate medium, the xylitol production efficiency was 30.6% and 42.6% lower than in raw hydrolysate and semisynthetic medium containing 85 g/L xylose, respectively. In other words, the xylose-to-xylitol bioconversion from hydrolysate medium was strongly affected when the initial xylose concentration was increased; however, similar behavior did not occur from semisynthetic media. The lowest efficiency of xylitol production from concentrated hydrolysate can be attributed to the high concentration of toxic compounds present in this medium, resulting from the hydrolysate concentration process.     

Intracellular fluxes in a recombinant xylose-utilizing Saccharomyces cerevisiae cultivated anaerobically at different dilution rates and feed concentrations

A metabolic flux model was constructed for the yeast Saccharomyces cerevisiae comprising the most important reactions during anaerobic metabolism of xylose and glucose. The model was used to calculate the intracellular fluxes in a recombinant, xylose-utilizing strain of S. cerevisiae (TMB 3001) grown anaerobically in a defined medium at dilution rates of 0.03, 0.06, and 0.18 h(-1). The feed concentration was varied from 0 g/L xylose and 20 g/L glucose to a mixture of 15 g/L xylose and 5 g/L glucose, so that the total concentration of carbon source was kept at 20 g/L. The specific uptake of xylose increased with the xylose concentration in the feed and with increasing dilution rate. The excreted xylitol was less than half of the xylose consumed. With increasing xylose concentration in the feed, the fluxes in the pentose phosphate pathway increased, whereas the flux through glycolysis decreased. Under all cultivation conditions, nicotinamide adenine dinucleotide (NADH) was the preferred cofactor for xylose reductase. The model showed that the flux through the reaction from ribulose 5-phosphate to xylulose 5-phosphate was very low under all cultivation conditions.     

Formation of xylitol in Candida guilliermondii 2581 culture

The yeast strain Candida guilliermondii 2581 was chosen for its ability to produce xylitol in media with high concentrations of xylose. The rate of xylitol production at a xylose concentration of 150 g/l is 1.25 g/l per h; the concentration of xylitol after three days of cultivation is 90 g/l; and the relative xylitol yield is 0.6 g per g substrate consumed. The growth conditions were found that resulted in the maximum relative xylitol yield with complete consumption of the sugar: xylose concentration, 150 g/l; pH 6.0; and shaking at 60 rpm. It was shown that the growth under conditions of limited aeration favors the reduction of xylose.     

Xylitol Production by a Culture ofCandida guilliermondii2581

The yeast strain Candida guilliermondii2581 was chosen for its ability to produce xylitol in media with high concentrations of xylose. The rate of xylitol production at a xylose concentration of 150 g/l is 1.25 g/l per h; the concentration of xylitol after three days of cultivation is 90 g/l; and the relative xylitol yield is 0.6 g per g substrate consumed. The growth conditions were found that resulted in the maximum relative xylitol yield with complete consumption of the sugar: xylose concentration, 150 g/l; pH 6.0; and shaking at 60 rpm. It was shown that the growth under conditions of limited aeration favors the reduction of xylose.     

高浓度糖发酵制备乙醇

以树干毕赤酵母为发酵菌株,混合糖（木糖、葡萄糖）为发酵底物,通过培养基和培养条件的改变来确定树干毕赤酵母高糖浓度发酵时所需的条件。研究结果表明：在24h发酵周期内初始木糖质量浓度为63．0g／L较适宜;在36h发酵周期内初始木糖质量浓度为72．0g/L较适宜。24h发酵周期内,在36．0g／L木糖中添加的葡萄糖质量浓度以54．0g/L为最佳,发酵结束乙醇质量浓度达32．9g／L;36h发酵周期内,添加的葡萄糖质量浓度以72．0g／L为最佳,发酵结束乙醇质量浓度为36．9g／L。以（NH4）2SO4为N源时较适合戊糖发酵制备乙醇,（NH2）2SO4的最佳质量浓度为1．1g／L。发酵前8h摇床转速为90r／min,后16h为150r／min,乙醇质量浓度较高,可达17．5g/L。     

Variables that affect xylitol production from sugarcane bagasse hydrolysate in a zeolite fluidized bed reactor

The operational conditions for xylitol production by fermentation of sugarcane bagasse hydrolysate in a fluidized bed reactor with cells immobilized on zeolite were evaluated. Fermentations were carried out under different conditions of air flowrate (0.0125-0.0375 vvm), zeolite mass (100-200 g), initial pH (4-6), and xylose concentration (40-60 g/L), according to a 2(4) full factorial design. The air flowrate increase resulted in a metabolic deviation from product to biomass formation. On the other hand, the pH increase favored both the xylitol yield (Y(P/S)) and volumetric productivity (Q(P)), and the xylose concentration increase positively influenced the xylitol concentration. The best operational conditions evaluated were based on the use of an air flowrate of 0.0125 vvm, 100 g of zeolite, pH 6, and xylose concentration of 60 g/L. Under these conditions, 38.5 g/L of xylitol were obtained, with a Y(P/S) of 0.72 g/g, Q(P) of 0.32 g/L.h, and cell retention of 25.9%.     

Decreased xylitol formation during xylose fermentation in Saccharomyces cerevisiae due to overexpression of water-forming NADH oxidase

The recombinant xylose-fermenting Saccharomyces cerevisiae strain harboring xylose reductase (XR) and xylitol dehydrogenase (XDH) from Scheffersomyces stipitis requires NADPH and NAD(+), creates cofactor imbalance, and causes xylitol accumulation during growth on d-xylose. To solve this problem, noxE, encoding a water-forming NADH oxidase from Lactococcus lactis driven by the PGK1 promoter, was introduced into the xylose-utilizing yeast strain KAM-3X. A cofactor microcycle was set up between the utilization of NAD(+) by XDH and the formation of NAD(+) by water-forming NADH oxidase. Overexpression of noxE significantly decreased xylitol formation and increased final ethanol production during xylose fermentation. Under xylose fermentation conditions with an initial d-xylose concentration of 50 g/liter, the xylitol yields for of KAM-3X(pPGK1-noxE) and control strain KAM-3X were 0.058 g/g xylose and 0.191 g/g, respectively, which showed a 69.63% decrease owing to noxE overexpression; the ethanol yields were 0.294 g/g for KAM-3X(pPGK1-noxE) and 0.211 g/g for the control strain KAM-3X, which indicated a 39.33% increase due to noxE overexpression. At the same time, the glycerol yield also was reduced by 53.85% on account of the decrease in the NADH pool caused by overexpression of noxE.