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。     

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。     

寄生曲霉CICC40365利用木糖产L-苹果酸的发酵条件优化

【目的】为提高L-苹果酸产量及木糖利用率,以寄生曲霉(Aspergillus parasiticus CICC40365)为菌种,木糖为碳源,对其发酵工艺及木糖代谢途径进行初步研究。【方法】采用单因素试验和响应曲面法(Box-Behnken设计)对培养基和发酵条件进行优化。【结果】获得最佳培养基配方为:木糖100.0 g/L、硫酸铵2.0 g/L、酵母浸粉3.0 g/L、硫酸镁0.20 g/L、硫酸锰0.15 g/L、硫酸亚铁0.08 g/L、碳酸钙80.00 g/L,L-苹果酸的产量为53.58 g/L,较优化前提高40.5%。发酵条件较好组合为:接种量为8%(体积比)、摇瓶装液量60 mL/250 mL、发酵温度32°C、摇床转速170 r/min、发酵周期8 d,L-苹果酸的产量为55.47 g/L。Mg2+、Mn2+对木糖代谢中相关酶的影响研究结果表明,木酮糖激酶在该菌株代谢木糖过程中起着重要作用。【结论】寄生曲霉CICC40365能够较好地利用木糖发酵产L-苹果酸,其产量及木糖的利用效率均得到提高。     

枯草芽孢杆菌核黄素操纵子与ribC基因的修饰与遗传效应

[目的]研究核黄素操纵子(rib)组成型高表达,以及ribC基因低水平表达对枯草芽孢杆菌过量合成核黄素的影响.[方法]在染色体原位修饰启动子,用mRNA稳定子替换mRNA前导区,使rib操纵子组成型高表达;修饰ribC基因的启动子,降低ribC基因的表达水平.采用qRT-PCR方法,表征基因的相对表达水平;通过摇瓶发酵,测定重组菌的生物量和核黄素产量,表征相关基因修饰所表现的遗传效应.[结果]用gsiB mRNA稳定子替换核黄素操纵子的mRNA前导区,使其相对表达水平提高了约1 500倍.ribC基因启动子-35区的首个碱基由“T”突变为“C”,使ribC基因的表达水平下降了97％以上.得到的重组菌株LX34在补加蔗糖20 g/L的LB培养基上摇瓶发酵36 h,可积累核黄素2.1 g/L,同时生物量没有明显下降.[结论]使用gsiB mRNA稳定子,能够有效地提高目标基因或操纵子的表达水平;启动子-35区首个碱基的点突变,能够有效降低ribC基因的表达水平;rib操纵子过量表达和ribC基因低水平表达,使细胞能够过量合成并积累核黄素.     

系列过表达非氧化磷酸戊糖途径基因对重组酿酒酵母菌株木糖代谢的影响

【目的】通过系统研究一个、两个及多个非氧化磷酸戊糖(PP)途径基因组合过表达对酿酒酵母木糖代谢的影响,以优化重组菌株的构建过程,构建高效的木糖代谢酿酒酵母菌株。【方法】在酿酒酵母中双拷贝过表达上游代谢途径的关键酶(木糖还原酶XR,木糖醇脱氢酶XDH,木酮糖激酶XKS),在此基础上构建了一系列PP途径基因过表达菌株,并对其木糖发酵性能进行比较研究。【结果】木糖发酵结果显示,不同组合过表达PP途径基因能不同程度改善重组菌株的木糖发酵性能。其中,过表达PP途径全部基因(RKI1,RPE1,TAL1和TKL1)使菌株的发酵性能最优,其乙醇产率和产量较对照菌株分别提高了39.25%和12.57%,同时较其他基因组合过表达菌株也有不同程度的改善。【结论】通过构建PP途径基因不同组合过表达酿酒酵母菌株,首次对PP途径基因对酿酒酵母木糖代谢的影响进行了系统研究,结果表明,不同组合强化PP途径基因对重组菌株木糖代谢的影响存在差异,相对于其他基因过表达组合,同步过表达PP途径全部基因最有利于碳通量流向乙醇。     

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。     

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。     

米根霉在氮源限制下的木糖代谢和关键酶特性北大核心CSCD

【目的】解析氮源浓度对米根霉木糖代谢途径及产物的影响,提高木糖利用率。【方法】以木糖为碳源,考察不同氮源浓度下米根霉的生物量、有机酸积累量、木糖代谢关键酶(木糖还原酶、葡萄糖-6-磷酸脱氢酶)活力以及胞内还原力(NADH/NAD+、NADPH/NADP+)的差异。【结果】富氮条件下(2.4 g/L尿素),木糖代谢速率达2.03 g/(L·h),木糖还原酶、葡萄糖-6-磷酸脱氢酶的活力以及胞内还原力较高,生物量达18.01g/L,几乎不积累有机酸;限氮条件下(0.15 g/L尿素),木糖还原酶、葡萄糖-6-磷酸脱氢酶的活力以及胞内还原力水平降低,生物量仅4.02 g/L,富马酸积累量为6.55 g/L,残余木糖量较高;氮源浓度为0.6 g/L时,木糖还原酶和葡萄糖-6-磷酸脱氢酶的活力以及NADPH/NADP+处于前二者之间,此时生物量9.11 g/L,有机酸积累量较大,其中富马酸为12.28 g/L。【结论】充足的氮源可使米根霉通过木糖代谢关键酶与胞内还原力的协同效应强化木糖代谢活力,通过优化氮源浓度后,米根霉可积累更多有机酸。     

解淀粉芽胞杆菌关键酶基因过表达对鸟苷积累的影响

【目的】研究鸟苷生物合成途径中的3个关键酶编码基因(prs,purF,guaB)过表达对解淀粉芽胞杆菌(Bacillus amyloliquefaciens)发酵生产鸟苷的影响。【方法】利用穿梭表达载体PBE43,构建含有prs、purF和guaB基因的单独表达载体和prs、purF基因的串联表达载体,将它们分别转入鸟苷生产菌B.amyloliquefaciens TA208后,通过实时定量PCR测定各工程菌株内相关基因的转录水平;通过酶活检测分析关键酶基因扩增对肌苷酸脱氢酶活性的影响;通过摇瓶发酵实验考察工程菌株与对照菌株的生长、耗糖和鸟苷积累情况。【结果】转录分析结果表明prs、purF和guaB基因过表达的同时都伴随着自身转录水平的显著上调。与此同时,prs和purF基因单独表达均轻微下调了嘌呤操纵子的转录水平,但是guaB基因的过表达并不影响嘌呤操纵子和prs基因的转录。酶活分析结果表明prs和purF基因扩增并不影响肌苷酸脱氢酶的活性,guaB基因的扩增使其活性提高了126%。摇瓶发酵实验发现prs和purF基因的单独过表达均未促进宿主菌合成鸟苷,而含guaB基因过表达载体的工程菌鸟苷产量较出发菌株提高20.7%。将prs和purF基因串联表达后,鸟苷产量提高14.4%,糖苷转化率增加6.8%。【结论】过表达guaB基因能够大幅提高鸟苷产量,而prs和purF基因只有实现协同表达才能对宿主菌积累鸟苷产生积极影响,为通过代谢工程技术提高鸟苷产量奠定了研究基础。     

嗜热棉毛菌木糖苷酶Xyl43基因优化及其在毕赤酵母中高效表达

【目的】通过外源表达手段构建重组毕赤酵母实现木糖苷酶的高效表达。【方法】基于毕赤酵母密码子偏好性优化嗜热棉毛菌β-木糖苷酶(Xyl43)基因密码子,将其导入毕赤酵母GS115中实现分泌表达,并对重组木糖苷酶酶学性质进行分析。通过单因素实验优化高产菌株的摇瓶发酵条件,并在5 L发酵罐中进行扩大培养。【结果】Xyl43基因优化后的序列中222个碱基发生改变,G+C含量由52.8%降低到44.6%,序列一致性为78.17%;将构建的表达载体p PIC9K-Opt Xyl43电击转入毕赤酵母中,利用平板初筛和摇瓶复筛获得一株高效表达重组菌(命名为P.pastoris GS115-Xyl43);其所产重组木糖苷酶大小为51.5 k D,动力学参数Km为2.93 mmol/L、Vmax为157.9μmol/(min·mg),最适反应温度55°C,最适p H 7.0,在p H 6.0-9.5条件下具有良好的稳定性;摇瓶优化结果表明:培养基初始p H 6.0、甲醇补加浓度1.0%、培养温度28°C、摇床转速250 r/min为最佳产酶条件,在此条件下发酵144 h胞外酶活达到42 U/m L(蛋白含量0.54 g/L);5 L发酵罐放大培养,发酵156 h(甲醇诱导96 h),木糖苷酶酶活为222.2 U/m L,蛋白含量2.36 g/L,较摇瓶提高了4.3倍。【结论】木糖苷酶在毕赤酵母中实现了高效表达,具有较好的工业化应用前景。     

Riboflavin synthesis genes are linked with the lux operon of Photobacterium phosphoreum.

Four genes immediately downstream of luxG in the Photobacterium phosphoreum lux operon (ribEBHA) have been sequenced and shown to be involved in riboflavin synthesis. Sequence analyses and complementation of Escherichia coli riboflavin auxotrophs showed that the gene products of ribB and ribA are 3,4-dihydroxy-2-butanone 4-phosphate (DHBP) synthetase and GTP cyclohydrolase II, respectively. By expression of P. phosphoreum ribE in E. coli using the bacteriophage T7 promoter-RNA polymerase system, ribE was shown to code for riboflavin synthetase, which catalyzes the conversion of lumazine to riboflavin. Increased thermal stability of RibE on expression with RibH indicated that ribH coded for lumazine synthetase. The organization of the rib genes in P. phosphoreum is quite distinct, with ribB and ribA being linked but separated by ribH, whereas in E. coli, they are unlinked and in Bacillus subtilis, RibB and RibA functions are coded by a single gene.     

枯草芽孢杆菌ccpA基因敲除及对其核黄素产量的影响

CcpA蛋白是介导枯草芽孢杆菌碳分解代谢物阻遏(CCR)的全局调控因子,由ccpA基因编码。CCR效应的存在影响B.subtilis对葡萄糖的利用,降低B.subtilis生产发酵产品的效率。采用基因重组技术敲除了核黄素发酵菌株B.subtilis24/pMX45的ccpA基因,构建了CcpA缺陷株B.subtilis24A1/pMX45。发酵结果显示:B.subtilis24A1/pMX45能够在70h内基本耗尽10%的葡萄糖,生物量达到1.5×109个细胞/mL,溢流代谢产物积累量减少,在8%和10%葡萄糖浓度下,B.subtilis24A1/pMX45核黄素产量分别比B.subtilis24/pMX45提高了62%和95%。CcpA的缺陷,可以缓解葡萄糖引起的CCR效应,显著提高菌株的核黄素产量。     

Redirection electron flow to high coupling efficiency of terminal oxidase to enhance riboflavin biosynthesis

The metabolic impact of redirection electron flow to high coupling efficiency of terminal oxidases on riboflavin biosynthetic ability was quantitatively assessed during batch culture in this paper. While disruption of the low coupling bd oxidase of the riboflavin overproducing B. subtilis PK, the apparent phenotype with more rapid specific growth rate and higher biomass yield was achieved. Compared to by-products formation, a discernible shift to less acetate and more acetoin in cyd mutant was observed. As the overflow metabolism was decreased in B. subtilis PK cyd, more carbon source was directed to biomass and riboflavin biosynthetic pathway, which resulted in higher biomass and about 30% improvement of riboflavin biosynthetic ability. The higher product-corrected biomass yield in mutant showed that the efficient energy generation is an important factor for exponential growth of riboflavin overproducing B. subtilis strain in batch culture.     

Biomass recycling from a riboflavin cultivation with B. subtilis: lysis, extract production and testing as substrate in riboflavin cultivation

Autolysis of riboflavin-producing B. subtilis can be induced by pH, lack of carbon source, and the buffer system. Stress factors like temperature shift or oxygen dearth enhance the autolysis process. After cultivation of a riboflavin-producing strain, the pH of the whole culture broth was adjusted to 6.5-7.5. At a temperature of 40 degrees C, autolysis started after 1 h. Adding a defined amount of commercially available endo- and exo-proteases enhanced both auto- and proteo-lysis. Optimization of endo- and exo-protease concentrations and of the time increased the degree of proteolysis. Additionally, the amount of DNA and Protein trapped in the riboflavin crystals could be significantly reduced by autolysis. After autolysis, the cultivation broth was centrifuged and the supernatant was cross-flow filtrated with a cut off of 10 kDa. Using this autolysate instead of yeast extract as a medium component for riboflavin production with B. subtilis, a riboflavin yield of 77% was obtained in comparison with the standard cultivation on yeast extract.     

Characterization of D-ribose biosynthesis in Bacillus subtilis JY200 deficient in transketolase gene

D-Ribose is a functional five-carbon sugar, which has been used for the commercial production of riboflavin. Mechanisms of d-ribose biosynthesis from xylose were investigated in the genetically engineered Bacillus subtilis JY200 with a deficiency in transketolase. A transketolase gene (tkt) disruption cassette in plasmid pUNKC was introduced into the chromosomal tkt gene in the wild type B. subtilis 168. Analysis of culture broth by thin layer chromatography confirmed that the disruption of tkt allowed B. subtilis JY200 to produce d-ribose. In a batch culture of B. subtilis JY200, a loss of cell viability was observed after glucose depletion. Fed-batch cultivation by feeding 400 gl(-1) glucose solution as a co-substrate was carried out to supply energy to xylose metabolism and to maintain cell viability throughout cultivation. Fed-batch cultivation of B. subtilis JY200 in a complex medium containing 11 gl(-1) xylose and 5 gl(-1) glucose initially gave the best result of 10.1 gl(-1)D-ribose concentration, 0.24 gg(-1)D-ribose yield and 0.29 gl(-1)h(-1) productivity, corresponding to 40-, 5- and 12-fold increases compared with those in the batch culture. A kinetic study of D-ribose production in fed-batch cultivations of B. subtilis JY200 suggested that xylose uptake might be critical to maximize D-ribose biosynthesis from xylose.     

Multi-level metabolic engineering of Pseudomonas mutabilis ATCC31014 for efficient production of biotin

Biotin (Vitamin H or B₇) is one of the most important cofactors involved in central metabolism of pro- and eukaryotic cells. Currently, chemical synthesis is the only route for commercial production. This study reports efficient microbial production of biotin in Pseudomonas mutabilis via multi-level metabolic engineering strategies: Level 1, overexpressing rate-limiting enzyme encoding genes involved in biotin synthesis (i.e. promoter and ribosome binding site engineering); Level 2, deregulating biotin biosynthesis (i.e. deletion of the negative regulator and the biotin importer genes); Level 3, enhancing the supply of co-factors (i.e. S-adenosyl-L-methionine and [Fe-S] cluster) for biotin biosynthesis; Level 4, increasing the availability of the precursor pimelate thioester (i.e. introduction of the BioW-BioI pathway from Bacillus subtilis). The combination of these interventions resulted in the establishment of a biotin overproducing strain, with the secretion of biotin increased for more than 460-fold. In combination with bioprocess engineering efforts, biotin was produced at a final titer of 87.17 mg/L in a shake flask and 271.88 mg/L in a fed-batch fermenter with glycerol as the carbon source. This is the highest biotin titer ever reported so far using rationally engineered microbial cell factories.