副产物途径的缺失对大肠杆菌合成D-1,2,4-丁三醇的影响

【目的】敲除副产物途径,提高重组大肠杆菌D-1,2,4-丁三醇(D-1,2,4-Butanetriol,BT)产量。【方法】利用Red重组技术敲除木糖途径xyl AB基因及2-酮-3-脱氧木糖酸代谢途径的yag E及yjh H基因,考察其对重组菌生长、BT生产及副产物积累的影响。【结果】敲除xyl AB基因后,重组菌生物量降低57%,BT产量降低20%,单位菌体产量提高84%,木糖酸积累量提高52%。yag E或yjh H基因单独缺失重组菌生物量分别提高10%和5%,BT产量提高36%和14%。基因共同缺失后重组菌生物量降低了21%,BT产量提高184%,达到2.44 g/L,单位菌体产量提高258%。而共同敲除两途径,生物量降低了72%,虽然单位菌体产量提高了约4倍,但BT产量仅提高43%。p H调控下,重组菌木糖酸积累量下降,BT产量进一步提高,最高达3.11 g/L。【结论】xyl AB基因缺失后,虽有利于提高BT途径的效率,但由于木糖无法进入PPP途径及木糖酸积累,造成生物量降低,不利于BT合成。单独敲除yag E或yjh H后BT产量略有提高,而共同敲除这两基因更为有效地调整碳流向BT合成偏转。两途径共同敲除利于BT的合成,但由于菌体量的减少,无法大量获得BT。     

产D-乳酸重组大肠杆菌ptsG基因的敲除及其混合糖同步发酵

为构建能够同时高效利用五碳糖和六碳糖发酵产D-乳酸的重组大肠杆菌工程菌,以能高效利用五碳糖发酵产D-乳酸的大肠杆菌工程菌E.coli JH13为出发菌株,通过Red同源重组技术敲除葡萄糖跨膜转运基因pts G。实验结果表明,pts G缺陷菌株E.coli JH15在10%混合糖(5%葡萄糖和5%木糖)培养基中发酵,可同时利用五碳糖和六碳糖以完成发酵;而对照菌葡萄糖消耗完才利用木糖,发酵结束还有18 g/L木糖残留;JH15乳酸产量为83.04 g/L,相比于对照菌株提高了25.86%;在稻草秸秆水解液中发酵,JH15同时利用葡萄糖、木糖和L-阿拉伯糖,乳酸产量为25.15 g/L,转化率为86.42%。JH15作为能利用混合糖同步发酵产D-乳酸的大肠杆菌工程菌,它的成功构建为利用廉价的木质纤维素水解物为原料发酵生产D-乳酸提供参考依据。     

代谢工程改造大肠杆菌合成D-1,2,4-丁三醇

【目的】D-1,2,4-丁三醇是一种四碳的多元醇,在军事和医药领域具有广泛的应用。为实现生物法一步转化生产D-1,2,4-丁三醇,对Escherichia coli W3100的木糖代谢途径进行改造。【方法】将来源于柄杆菌的D-木糖脱氢酶基因xylB和恶臭假单胞菌的苯甲酰甲酸脱羧酶基因mdlC克隆至E.coli W3100,得到重组菌E.coli(pEtac-mdlC-tac-xylB)。在此基础上对重组菌代谢木糖合成D-1,2,4-丁三醇的能力进行考察。【结果】在30°C下,以30 g/L D-木糖为底物,重组菌E.coli(pEtac-mdlC-tac-xylB)的D-1,2,4-丁三醇产量达到了0.9 g/L,摩尔转化率为4%。【结论】实现了D-1,2,4-丁三醇的一步法发酵生产,为国内开展相关研究奠定了坚实的基础。     

异源表达木糖异构酶基因对克雷伯氏菌合成1,3-丙二醇的影响

【目的】提高克雷伯氏菌胞内还原力以强化1,3-丙二醇合成。【方法】将来源于大肠杆菌的木糖异构酶基因在克雷伯氏菌中异源表达,构建重组菌。研究重组菌添加不同浓度木糖为辅底物与甘油共发酵过程中代谢产物和NADH的变化规律。【结果】与对照菌相比,重组菌细胞内还原力NADH提高了0.1?0.3倍,1,3-丙二醇产量达到23.31 g/L,提高20%,1,3-丙二醇转化率从0.60 mol/mol提高到0.73 mol/mol。【结论】木糖异构酶基因的表达强化了木糖代谢途径,经磷酸戊糖途径积累大量还原力,促进了1,3-丙二醇的生成。     

代谢工程改造热带假丝酵母生产1,2,4-丁三醇

【背景】 1,2,4-丁三醇属于手性多羟基醇,是一种重要的有机合成的化学中间体,以木糖为原料经四步酶反应是目前研究最多的生物合成路线。然而大肠杆菌的鲁棒性较弱,对发酵液中一些抑制剂的耐受性不是很好,同时存在严重的碳代谢抑制。近年来,鲁棒性较好的酵母菌成为更有吸引力的宿主,其中热带假丝酵母具有天然的木糖代谢途径,可以更好地利用木糖。【目的】在热带假丝酵母中构建从木糖到1,2,4-丁三醇的代谢途径。【方法】在热带假丝酵母中敲除木糖还原酶基因GRE3,从而阻断自身的木糖代谢途径。将来源于Caulobacter crescentus的木糖脱氢酶基因(xylB)和木糖酸脱水酶基因(xylD)及来源于Lactococcus lactis的酮酸脱羧酶基因(kdcA)克隆至C. tropicalis 207中,得到重组菌C. tropicalis BT,在此基础上考察重组菌代谢木糖合成1,2,4-丁三醇的能力,确定限速步骤,并通过增加关键基因xylD与kdcA的拷贝数提高1,2,4-丁三醇产量。【结果】在30℃、200 r/min、接种量1%、以30 g/L木糖为底物的情况下,重组菌的1,2,4-丁三醇的产量达到了1.2 g/L,在5 L发酵罐中的产量达到了3.7 g/L。【结论】在热带假丝酵母中实现以木糖为底物的1,2,4-丁三醇代谢途径,并通过在基因组上增加关键基因xylD与kdcA的拷贝数,获得了一株高产1,2,4-丁三醇的重组酵母菌株,这为后续在热带假丝酵母中进一步提高1,2,4-丁三醇产量奠定了基础。     

混合糖发酵重组酿酒酵母的菌株构建和菊芋秸秆同步糖化发酵研究

【目的】构建可用于纤维素乙醇高效生产的混合糖发酵重组酿酒酵母菌株,并利用菊芋秸秆为原料进行乙醇发酵。【方法】筛选在木糖中生长较好的酿酒酵母YB-2625作为宿主菌,构建木糖共代谢菌株YB-2625 CCX。进一步通过r DNA位点多拷贝整合的方式,以YB-2625 CCX为出发菌株构建木糖脱氢酶过表达菌株,并筛选得到优势菌株YB-73。采用同步糖化发酵策略研究YB-73的菊芋秸秆发酵性能。【结果】YB-73菌株以90 g/L葡萄糖和30 g/L木糖为碳源进行混合糖发酵,乙醇产量比出发菌株YB-2625 CCX提高了13.9%,副产物木糖醇产率由0.89 g/g降低至0.31 g/g,下降了64.6%。利用重组菌YB-73对菊芋秸秆进行同步糖化发酵,48 h最高乙醇浓度达到6.10%(体积比)。【结论】通过转入木糖代谢途径以及r DNA位点多拷贝整合过表达木糖脱氢酶基因可有效提高菌株木糖发酵性能,并用于菊芋秸秆的纤维素乙醇生产。这是首次报道利用重组酿酒酵母进行菊芋秸秆原料的纤维素乙醇发酵。     

罗氏真养菌W50的D-木糖代谢途径工程改造

【目的】拓宽高产聚-β-羟基丁酸酯(poly-β-hydroxybutyrate,PHB)罗氏真养菌(Ralstonia eutropha)W50的碳源使用范围,使其获得D-木糖代谢能力。【方法】运用PCR技术扩增大肠杆菌(Escherichia coli)K-12W3110来源的D-木糖转运蛋白基因xylE,利用同源重组技术将xylE基因整合到R.eutropha W50的染色体上构建菌株W50-E。运用PCR技术扩增E.coli K-12 W3110来源的D-木糖代谢基因xylAB和R.eutropha H16来源的PHA合酶基因phaC1的启动子片段P pha C1,同表达载体连接后构建重组质粒p1-AB。将重组质粒分别转入菌株R.eutropha W50和W50-E中构建工程菌株W50-AB和W50-EAB。通过摇瓶发酵研究W50-AB和W50-EAB的D-木糖代谢特性。【结果】酶活分析结果表明,xylA和xylB基因在菌株R.eutropha W50中得到表达。摇瓶发酵结果表明,W50-AB在含0.1 mol/L D-木糖的基础发酵培养基中的最大比生长速率为0.025 h-1,在含0.01 mol/L D-木糖的基础发酵培养基中没有生长;W50-EAB在含0.01 mol/L D-木糖的基础发酵培养基中表现出一定生长,在含0.1 mol/L D-木糖的基础发酵培养基中最大比生长速率为0.035 h-1。PHB含量分析结果表明,摇瓶发酵终点时,W50-AB和W50-EAB菌株内的PHB含量分别为细胞干重的15.07±1.01%和15.07±1.64%,其相应的D-木糖-PHB转化率分别为0.0920 g·g-1和0.0838 g·g-1,低于两重组菌株利用葡萄糖发酵的糖-PHB转化率(0.22 g·g-1)。另外,重组菌株W50-AB和W50-EAB在含葡萄糖(0.01 mol/L)和D-木糖(0.09 mol/L)的混合糖培养基中的发酵结果表明,两重组菌株均表现出更高的生长速率和D-木糖消耗速率以及胞内PHB积累量。【结论】来源于E.coli K-12W3110菌株的xylAB基因的表达使R.eutropha W50获得了一定的D-木糖代谢能力,通过D-木糖转运蛋白基因xylE的表达能提高菌株的D-木糖代谢能力,同时重组菌株利用D-木糖能积累一定量PHB。     

大肠杆菌乙醇工程菌mglB基因的敲除对混合糖发酵木糖利用效率的影响

为明晰葡萄糖非PTS转运系统相关基因对木糖利用效率的影响,探讨葡萄糖PTS和非PTS转运系统是否对木糖利用存在协同影响,以大肠杆菌工程菌SZ470和SZ470P为出发菌株,通过RED同源重组技术敲除葡萄糖转运基因mglB,构建mglB单缺陷菌SZ470M和ptsG/mglB双缺陷菌SZ470PM。比较四株菌的混合糖(3%葡萄糖+2%木糖)发酵情况以及木糖转运代谢相关基因的转录水平。实验结果表明,SZ470M相较于出发菌株SZ470,其发酵性能无明显变化;SZ470PM的木糖消耗速度为0.37 g/L,乙醇产量为23.25 g/L,转化率为82.6%,相比于出发菌株SZ470P分别提高了32%,9.8%和5.8%。基因转录水平的分析也表明菌株SZ470P和SZ470PM的木糖转运与代谢基因的转录水平上调。综上,ptsG和mglB基因的双敲除对木糖利用效率的提高有协同影响,为促进木质纤维素作为发酵原料时木糖的高效利用提供理论依据。     

大肠杆菌合成1,2,4-丁三醇的途径优化

1,2,4-丁三醇(BT)是一种在工业中有多种用途的重要的非天然化合物。文中通过将外源基因xdh和mdlC导入大肠杆菌BW25113表达,并敲除了xylA、xylB、yagE、yjhH、yiaE和ycdW等木糖和中间产物代谢旁路基因,构建了能够将D-木糖转化为BT的重组菌株。为优化BT合成途径,针对BT合成途径中的限速步骤——3-脱氧-D-甘油-戊酮糖酸的脱羧反应,进行了新酶的筛选和评价,获得了可显著提高反应效率的新的2-酮酸脱羧酶——KivD,并构建了表达该酶的重组菌株BW-025。在此基础上,通过初步条件优化,将BT产量提高至2.38g/L;进一步调节途径中各个酶的表达量,探究了它们对BW-025合成BT的影响,最终获得了BT产量较BW-025提高了48.62%的重组菌株BW-074。     

重组菌Ralstonia eutropha W50-EAB D-木糖代谢相关的限速靶点

【目的】通过代谢工程改造真养罗氏菌(Ralstonia eutropha)W50-EAB木糖代谢的相关限速靶点,进一步提高R.eutropha W50-EAB的D-木糖利用效率,为获得高效利用纤维素水解液的菌株奠定基础。【方法】利用PCR技术扩增R.eutropha转酮酶基因tkt A,cbb T2和转醛酶基因tal,将扩增的tkt A,cbb T2和tal基因分别构建到表达载体p BBR1MCS-3上,获得重组质粒p WL1-TKT,p WL1-CBBT2,p WL1-TAL。通过电转的方式将质粒分别转化W50-EAB获得重组菌W50-KAB,W50-CAB和W50-TAB。利用基因敲除的方法,获得醛还原酶基因h16_A3186敲除株W50’-EAB。通过电转的方式将重组质粒p WL1-TAL导入敲除株W50’-EAB获得重组菌株W50’-TAB。通过摇瓶发酵研究重组菌株W50-KAB,W50-CAB,W50-TAB,W50’-EAB以及W50’-TAB的发酵特性。【结果】酶活分析结果表明,转酮酶和转醛酶基因实现表达。摇瓶发酵结果表明,转酮酶基因过表达菌株W50-KAB和W50-CAB相比于对照菌株W50-EAB/p3,表现出降低的木糖利用能力;而转醛酶基因过表达重组菌株W50-TAB以及敲除菌株W50’-EAB对木糖的利用得到一定的提高。在0.1 mol/L木糖的发酵培养基中,W50-EAB的最大比生长速率为0.035 h-1,PHB干重比为16.2±1.01%;而W50-TAB的最大比生长速率提高到0.039 h-1,PHB干重比达到20.5±0.76%;醛还原酶基因敲除菌株W50’-EAB最大比生长速率提高到0.040 h-1,PHB含量提高到19.8±1.05%。结果显示转醛酶基因的过表达与醛还原酶基因的敲除对木糖利用均表现出一定的优势,将这两种优势组合获得菌株W50’-TAB,摇瓶发酵分析结果为最大比生长速率达到0.042 h-1,PHB积累达到27.9±0.47%,相比于对照菌株提高了72.2%。另外,在含有葡萄糖(0.01 mol/L)和木糖(0.09 mol/L)的混合糖培养下,重组菌株W50-TAB,W50’-EAB和W50’-TAB相比于在纯木糖培养下都表现出更高的生物量和胞内PHB积累量。【结论】磷酸戊糖途径关键酶转醛酶基因的过表达加速了木糖代谢流,从而可以高效利用木糖积累一定量的PHB。醛还原酶对木糖代谢有阻碍作用,敲除该酶基因后木糖代谢能力有了一定的提高,而两者协同作用可以进一步提高重组菌株的木糖利用效率和PHB积累能力。     

一株中型假丝酵母发酵木糖产乙醇的特性研究

本研究对自然界中筛选得到的1株可以发酵木糖产乙醇的中型假丝酵母(Candida intermedia)的特性进行了研究.该菌株在28℃、120 r/min、72 h条件下,发酵3%木糖的乙醇产率最高,达到理论值的43.70%,发酵7%木糖得到的乙醇产量最高,为6.480 g/L.发酵时间延长到156 h,可以利用8%木糖产乙醇21.225 g/L,产率为理论值的72.87%.该菌株还可以在同样条件下,发酵13%葡萄糖得到乙醇50.965 g/L,达到理论值的76.90%.以3% 2% 3%分批补加糖,比一次性发酵8%木糖的乙醇产量提高9.91%.在葡萄糖和木糖的混合培养基中,优先利用葡萄糖,同时还表现出葡萄糖对木糖发酵的促进作用,当2%的木糖与6%葡萄糖混合时,乙醇产量比两者单独发酵的加和提高了25%.     

Homo-d-lactic acid production from mixed sugars using xylose-assimilating operon-integrated Lactobacillus plantarum

In order to achieve efficient D-lactic acid fermentation from a mixture of xylose and glucose, the xylose-assimilating xylAB operon from Lactobacillus pentosus (PXylAB) was introduced into an L-lactate dehydrogenase gene (ldhL1)-deficient Lactobacillus plantarum (ΔldhL1-xpk1::tkt-Δxpk2) strain in which the phosphoketolase 1 gene (xpk1) was replaced with the transketolase gene (tkt) from Lactococcus lactis, and the phosphoketolase 2 (xpk2) gene was deleted. Two copies of xylAB introduced into the genome significantly improved the xylose fermentation ability, raising it to the same level as that of ΔldhL1-xpk1::tkt-Δxpk2 harboring a xylAB operon-expressing plasmid. Using the two-copy xylAB integrated strain, successful homo-D-lactic acid production was achieved from a mixture of 25 g/l xylose and 75 g/l glucose without carbon catabolite repression. After 36-h cultivation, 74.2 g/l of lactic acid was produced with a high yield (0.78 g per gram of consumed sugar) and an optical purity of D-lactic acid of 99.5%. Finally, we successfully demonstrated homo-D-lactic acid fermentation from a mixture of three kinds of sugar: glucose, xylose, and arabinose. This is the first report that describes homo-D-lactic acid fermentation from mixed sugars without carbon catabolite repression using the xylose-assimilating pathway integrated into lactic acid bacteria.     

树干毕赤酵母NLP31发酵产乙醇的研究

研究了树干毕赤酵母NLP31在木糖质量浓度为45 g/L的3种发酵培养基Ⅰ、Ⅱ和Ⅲ上发酵3轮的发酵性能以及在45 g/L木糖或混合糖(葡萄糖30 g/L,木糖15 g/L)的发酵培养基Ⅲ上的代谢历程。结果表明:树干毕赤酵母NLP31在发酵培养基Ⅲ上,乙醇浓度和乙醇得率均达到最高,分别为(17.29±0.15)g/L和(84.65±0.58)%。在45 g/L木糖或混合糖(葡萄糖30 g/L,木糖15 g/L)的发酵培养基Ⅲ上的代谢历程表明:混合糖发酵达到最大乙醇得率的时间仅为12 h,要比单一木糖发酵缩短了8 h。树干毕赤酵母NLP31在以廉价的无机N源为发酵培养基上的乙醇发酵性能高,能够降低燃料乙醇的生产成本。     

利用木糖-葡萄糖为原料产乙醇酵母的筛选、鉴定及发酵试验

建立筛选利用木糖为碳源产乙醇酵母模型,获得一株适合利用木质纤维素为原料产乙醇的酵母菌株。样品经麦芽汁培养基培养后,以木糖为唯一碳源的筛选培养基初筛,再以重铬酸钾显色法复筛。通过生理生化和26D1/D2区对筛选得到的菌株进行分析和鉴定,该菌初步鉴定为Pichia caribbica。经过筛选得到的菌株Y2-3以木糖（40g/L）为唯一碳源发酵时：生物量为23.5g/L,木糖利用率为94.7 %,乙醇终产量为4.57 g/L;以混合糖（葡萄糖40 g/L,木糖20 g/L）发酵时：生物量为28.6 g/L,木糖利用率为94.2 %,葡萄糖利用率为95.6%,乙醇终产量为20.6 g/L。Pichia caribbica是可以转化木糖及木糖-葡萄糖混合糖为乙醇的酵母菌株,为利用木质纤维素发酵乙醇的进一步研究奠定了基础。     

Improvement of kojic acid production in Aspergillus oryzae B008 mutant strain and its uses in fermentation of concentrated corn stalk hydrolysate

A strain designated M866, producing kojic acid with a high yield, was obtained by combining induced mutation using ion beam implantation and ethyl methane sulfonate treatment of a wild type strain of Aspergillus oryzae B008. The amount of kojic acid produced by the strain M866 in a shaking flask was 40.2 g/L from 100 g/L of glucose, which was 1.7 times higher than that produced by wild strain (23.58 g/L). When the mixture of glucose and xylose was used as carbon source, the resulting kojic acid production was raised with the increasing of glucose ratios in the mixture. With concentrations of glucose at 75 g/L and xylose at 25 g/L mixed in the medium, the production of kojic acid reached 90.8 %, which was slightly lower than with glucose as the sole source of carbon. In addition, the kojic acid fermentation of the concentrated hydrolysate from corn stalk was also investigated in this study, the maximum concentration of kojic acid accumulated at the end of the fermentation was 33.1 g/L and this represents the yield based on reducing sugar consumed and the overall productivity of 0.36 g/g and 0.17 g/L/h, respectively.     

Ethanol production from wood hydrolysate using genetically engineered Zymomonas mobilis

An ethanologenic microorganism capable of fermenting all of the sugars released from lignocellulosic biomass through a saccharification process is essential for secondary bioethanol production. We therefore genetically engineered the ethanologenic bacterium Zymomonas mobilis such that it efficiently produced bioethanol from the hydrolysate of wood biomass containing glucose, mannose, and xylose as major sugar components. This was accomplished by introducing genes encoding mannose and xylose catabolic enzymes from Escherichia coli. Integration of E. coli manA into Z. mobilis chromosomal DNA conferred the ability to co-ferment mannose and glucose, producing 91 % of the theoretical yield of ethanol within 36 h. Then, by introducing a recombinant plasmid harboring the genes encoding E. coli xylA, xylB, tal, and tktA, we broadened the range of fermentable sugar substrates for Z. mobilis to include mannose and xylose as well as glucose. The resultant strain was able to ferment a mixture of 20 g/l glucose, 20 g/l mannose, and 20 g/l xylose as major sugar components of wood hydrolysate within 72 h, producing 89.8 % of the theoretical yield. The recombinant Z. mobilis also efficiently fermented actual acid hydrolysate prepared from cellulosic feedstock containing glucose, mannose, and xylose. Moreover, a reactor packed with the strain continuously produced ethanol from acid hydrolysate of wood biomass from coniferous trees for 10 days without accumulation of residual sugars. Ethanol productivity was at 10.27 g/l h at a dilution rate of 0.25 h(-1).     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from a mixture of xylose and glucose by co-cultivation of lactic acid bacteria

The production of optically pure lactic acid in a high yield from xylose or a mixture of xylose and glucose, which is a model hydrolysate of lignocellulose, is described. In a single cultivation, Enterococcus casseliflavus produced 38 g/l of lactic acid with an optical purity of 96% enantiomeric excess (ee) and 6.4 g/l of acetic acid from 50 g/l of xylose when MRS medium was used. When a mixture of 50 g/l of xylose and 100 g/l of glucose was used as the carbon source in a cultivation of E. casseliflavus alone, glucose was converted to lactic acid in the early phase of the cultivation but xylose was hardly consumed. In a co-cultivation where E. casseliflavus and Lactobacillus casei specific for glucose were simultaneously inoculated, little or no lactic acid was produced after the glucose was almost consumed. A co-cultivation with two-stage inoculation (in which E. casseliflavus was added at a cultivation time of 40 h after L. casei cells were inoculated) resulted in complete consumption of 50 g/l of xylose and 100 g/l of glucose. In the co-cultivation, 95 g/l of lactic acid with a high optical purity of 96% ee was obtained at 192 h. Such a co-cultivation using two microorganisms specific for each sugar is considered to be one promising cultivation technique for the efficient production of lactic acid from a sugar mixture derived from lignocellulose.     

重组大肠杆菌利用木糖发酵产高纯度L-乳酸

对重组大肠杆菌JH16利用木糖产高纯度的三一乳酸进行研究。通过无氧管驯化EscherwhiacdiJH12菌株得到E．coliJH16,驯化后的菌株茵体浓度提高了31％,乙酸积累减少了43％;在摇瓶中考察不同Mg2＋浓度对EcoliJHl6产三一乳酸的影响,确定最适Mg2＋质量浓度为0．25g/L;EcoEJH16以60g/L木糖为C源,在7L全自动发酵罐中添加0．25g／LMg2＋,乳酸积累量提高了18％,达38．18g/L,乳酸纯度高达95％;E．coliJH16在30g／L木糖和30g／L葡萄糖混合C源中,优先利用葡萄糖,当葡萄糖质量浓度低于1．56g/L后,菌体开始利用木糖进行乳酸发酵,最终得到39g／L乳酸。     

Characterization of sugar mixtures utilization by an Escherichia coli mutant devoid of the phosphotransferase system

Due to catabolite repression in microorganisms, sugar mixtures cannot be metabolized in a rapid and efficient manner. Therefore, the development of mutant strains that avoid this regulatory system is of special interest to fermentation processes. In the present study, the utilization of sugar mixtures by an Escherichia coli mutant strain devoid of the phosphotransferase system (PTS) was characterized. This mutant can transport glucose (PTS- Glucose+ phenotype) by a non-PTS mechanism as rapidly as its wild-type parental strain. In cultures grown in minimal medium supplemented with glucose-xylose or glucose-arabinose mixtures, glucose repressed arabinose- or xylose-utilization in the wild-type strain. However, under the same culture conditions with the PTS- Glucose+ mutant, glucose and arabinose were co-metabolized, but glucose still exerted a partial repressive effect on xylose consumption. In cultures growing with a triple mixture of glucose-arabinose-xylose, the wild-type strain sequentially utilized glucose, arabinose and finally, xylose. In contrast, the PTS- Glucose+ strain co-metabolized glucose and arabinose, whereas xylose was utilized after glucose-arabinose depletion. As a result of glucose-arabinose co-metabolism, the PTS- Glucose+ strain consumed the total amount of sugars contained in the culture medium 16% faster than the wild-type strain. [14C]-Xylose uptake experiments showed that in the PTS- Glucose+ strain, galactose permease increases xylose transport capacity and the observed partial repression of xylose utilization depends on the presence of intracellular glucose.