高糖和氮源对鼠李糖乳杆菌(Lactobacillus rhamnosus)L-乳酸发酵的影响

鼠李糖乳杆菌经实验室耐高糖高酸选育,能够在高糖浓度下高效高产L-乳酸。以酵母粉为氮源和生长因子,葡萄糖初始浓度分别为120 g/L和146 g/L,摇瓶培养120h,L-乳酸产量分别为104g/L和117.5g/L,L-乳酸得率分别为86.7%和80.5%。高葡萄糖浓度对菌的生长和乳酸发酵有一定的抑制。增加接种量,在高糖浓度发酵条件下,可以缩短发酵时间,但对增加乳酸产量效果不明显。乳酸浓度对鼠李糖乳杆菌生长和产酸有显著的影响。初始乳酸浓度到达70g/L以上时,鼠李糖乳杆菌基本不生长和产酸,葡萄糖消耗也被抑制。酵母粉是鼠李糖乳杆菌的优良氮源,使用其它被测试的氮源菌体生长和产酸都有一定程度的下降。用廉价的黄豆粉并补充微量维生素液,替代培养基中的酵母粉,可以使产酸浓度和碳源得率得以基本维持。     

高产二羟基丙酮重组菌株的构建

旨在构建一株过量表达编码膜系甘油脱氢酶的sld AB基因的重组菌株,以提高二羟基丙酮产量。以氧化葡萄糖酸杆菌ATCC621H的基因组DNA为模板,运用PCR方法扩增得到基因sld AB,并连接到p BBR1MCS-2质粒上,构建表达载体p BBR1MCS-2-sld AB。通过电转化将载体p BBR1MCS-2-sld AB转化进入氧化葡萄糖酸杆菌ATCC621H内,得到重组菌株GOX205。结果显示,重组菌株构建成功,其甘油脱氢酶的酶活力较之于出发菌株提高了26%。在甘油初始浓度100 g/L的甘油发酵培养基中,较之于出发菌株,GOX205的生长状况良好,发酵52 h时DHA浓度达到94.1 g/L,较之于出发菌株提高了19.7%,甘油残量降低了15.1 g/L。     

一株具有噬菌体抗性的芽孢杆菌BS-2的鉴定及葡萄糖流加工艺优化

筛选噬菌体抗性菌株以解决枯草芽孢杆菌(Bacillus subtilis)生产过程中噬菌体污染问题并提高抗性菌株的发酵水平。采用双层平板法从异常发酵液中分离并纯化以枯草芽孢杆菌为宿主的噬菌体,利用纯化得到的噬菌体筛选实验室芽孢杆菌库以得到抗性菌株,结合16S rDNA和gyrA基因序列进行系统发育分析确定其分类地位,以分批发酵的生长曲线及葡萄糖含量曲线作为基础,对发酵培养基的初糖浓度及葡萄糖的流加方式进行优化提高筛选到的噬菌体抗性菌株的发酵水平。从异常发酵液中分离到噬菌体S01及S02并在实验室芽孢杆菌库中筛选到一株噬菌体无法侵染的芽孢杆菌BS-2,结合16S rDNA及gyrA基因序列的系统发育分析将BS-2鉴定为枯草芽孢杆菌,按照葡萄糖初始浓度15 g/L,葡萄糖浓度低于5 g/L时以2 g/L·h的速度流加葡萄糖,补加量10 g/L的流加补料方法,可以将发酵水平提高至2.43×1010 CFU/mL。枯草芽孢杆菌BS-2具有较好的噬菌体抗性且经过工艺优化可以达到较高发酵水平,有较强工业化应用潜力。     

Ketogulonigenium vulgare四环素诱导表达穿梭质粒的构建

采用重叠延伸PCR方法合成阻遏蛋白的编码基因tetr和插入操纵基因teto的Ketogulonigenium vulgare山梨糖脱氢酶启动子psndhteto的基因序列,借助宽宿主质粒p BBR1MCS-5,构建四环素诱导表达的穿梭质粒,转化Ketogulonigenium vulgare,获得阳性重组菌株,实现卡那霉素抗性的调控表达,结果表明:培养重组菌株2小时后,添加0.4μg/ml的四环素诱导剂后,能够在含有卡那霉素的培养基中生长,不添加四环素诱导剂的重组菌株不能在含卡那霉素的培养基中生长,确定了最适四环素的诱导浓度为0.6μg/ml。     

戊糖乳杆菌发酵产乳酸及高产菌株诱变选育

戊糖乳杆菌(Lactobacillus pentosus)是能利用木质纤维素水解液发酵产乳酸的潜力菌株,发酵条件优化与高产菌株的选育是提高乳酸产量的重要手段。通过单因素试验、Plackett-Burman设计与响应面试验,对戊糖乳杆菌ATCC 8041产乳酸的发酵培养基及发酵条件进行了优化。结果表明,该菌株发酵培养基的最佳组合为葡萄糖93.11 g/L、酵母浸粉5.19 g/L、碳酸钙29.43 g/L、蛋白胨10.00 g/L、Na2HPO4·12H2O 5.00 g/L、Mg SO4 0.20 g/L、Mn SO4 50 mg/L;最佳发酵条件为37℃、p H6.5、接种量6%、装液量80%。在此优化条件下,该菌株发酵产乳酸为54.12 g/L。进一步以戊糖乳杆菌ATCC 8041为出发菌株,通过原生质体进行紫外诱变,经多重筛选,最终获得一株遗传稳定性好的高产乳酸突变株,命名为戊糖乳杆菌Lactic UVC-02,由中国典型培养物保藏中心保存,注册号为CCTCC M 2013209。该突变株Lactic UVC-02经葡萄糖发酵,乳酸产量达64.17 g/L,比出发菌株ATCC 8041(54.12g/L)提高18.6%。     

过表达长链鞘氨醇激酶基因LCB4提高酿酒酵母抑制物耐受性

木质纤维素预处理过程中产生的有毒副产物严重影响了纤维素乙醇发酵,提高酿酒酵母抑制物耐受性是提高纤维素乙醇发酵效率的有效方法。文中通过过表达LCB4基因,研究了重组菌株S288C-LCB4在乙酸、糠醛和香草醛胁迫下的细胞生长和乙醇发酵性能。结果表明,LCB4过表达菌株在分别含有10 g/L乙酸、1.5 g/L糠醛和1 g/L香草醛的平板中生长均优于对照菌株;在分别含有10 g/L乙酸、3 g/L糠醛和2 g/L香草醛的液体乙醇发酵过程中,重组菌株S288C-LCB4乙醇发酵产率分别为0.85 g/(L·h)、0.76 g/(L·h)和1.12 g/(L·h),比对照菌株提高了34.9%、85.4%和330.8%;且糠醛和香草醛胁迫下发酵时间分别缩短了30 h和44 h。根据发酵终点发酵液代谢物分析发现重组菌株比对照菌株产生了更多甘油、海藻糖和琥珀酸,这些物质有利于增强菌株的抑制物耐受性。综上所述,LCB4基因过表达可显著提高酿酒酵母S288C在乙酸、糠醛和香草醛胁迫下的乙醇发酵性能。     

一株高产脯氨酸的嗜醋酸棒杆菌的选育及发酵条件优化

以嗜醋酸棒杆菌为出发菌株,经过片段化全基因组体外诱变、重组和连续的磺胺胍抗性筛选,获得一株L-脯氨酸的高产菌株。摇瓶发酵优化结果表明,葡萄糖、生物素和硫胺素的最适用量分别为16%、300μg/L、400μg/L,最适pH为6.8~7.0,装液量为25ml/500ml摇瓶,发酵培养72h后L-脯氨酸产率高达到75.6g/L,与对照相比提高了5%。考察了50L发酵罐中细胞生长对L-脯氨酸产量的影响,补料分批发酵结果表明(比生长速率分别为0.06/h、0.08/h和0.1/h),比生长速率在0.08/h左右时L-脯氨酸的产率最高,L-脯氨酸的比生产速率Q_P达到0.091 g/(g.h),产率高达82.1 g/L,比优化前提高了14%。     

大肠杆菌甘油激酶基因(glpK)和甘油脱氢酶基因(gldA)的敲除及其对甘油产量的影响

利用Red重组系统构建了大肠杆菌JM109甘油激酶基因(glpK)和甘油脱氢酶基因(gldA)缺失的双突变菌株JM109B,然后将表达酿酒酵母3-磷酸甘油脱氢酶基因(GPD1)和3-磷酸甘油酯酶基因(HOR2)的质粒pSE-gpd1-hor2转化到JM109B突变菌株中,在含1%葡萄糖的摇瓶发酵培养基中37℃发酵24 h,甘油的最高产量为5.61 g/L,是原始菌株JM109/pSE-gpd1-hor2甘油产量的1.59倍;在30 L发酵罐中发酵28 h,甘油的最高产量为103.12 g/L,是原始菌株JM109/pSE-gpd1-hor2甘油产量的1.59倍,是原始菌株BL21/pSE-gpd1-hor2甘油产量的1.41倍,葡萄糖转化率为50.39%。     

谷氨酸棒杆菌高丝氨酸脱氢酶编码基因hom的敲除

本研究以谷氨酸棒杆菌（Corynebacterium glutamicum）标准菌株ATCC 13032染色体为模板,设计引物PCR扩增高丝氨酸脱氢酶编码基因（hom）,在hom基因内部插入一段来源于质粒pET28a的卡那霉素抗性基因（Km）,得到基因元件hom::Km;通过电击转化法将hom::Km转入出发菌株替换原菌株的hom,在含卡那霉素的平板上挑取阳性转化子,通过PCR验证得到高丝氨酸脱氢酶缺陷的重组菌。发酵结果表明重组菌C.g- hom::Km -8发酵60小时赖氨酸产量达到4.7 g／L,是出发菌株谷氨酸棒杆菌ATCC 13032（0.7 g／L）的6.7倍。     

代谢工程改造谷氨酸棒杆菌生成丙酮酸

旨在增加谷氨酸棒杆菌代谢过程中丙酮酸的积累、减少副产物的生成,利用同源重组的方法,敲除了丙酮酸代谢过程中支流代谢途径的关键基因:丙酮酸醌氧化还原酶pqo基因、丙酮酸脱氢酶pdh基因和乳酸脱氢酶lldh基因,获得了基因缺失工程菌株。利用4.5%的葡萄糖复合培养基,工程菌经摇瓶发酵48 h,丙酮酸的浓度达到14.6 g/L,而野生菌株仅为0.45 g/L;工程菌的糖酸转化率为33.18%,比野生菌提高了32.5倍。     

Improved gellan gum production by a newly-isolated Sphingomonas azotifigens GL-1 in a cheese whey and molasses based medium

Gellan gum is a water-soluble exopolysaccharide, it has applications in the food, pharmaceutical and chemical industries. In this study, a gellan gum producing strain was isolated from rice root, and this strain was identified be the species of Sphingomonas azotifigens. The Plackett-Burman design was applied to investigate the main factors affecting gellan gum production by S. azotifigens GL-1 in a molasses and cheese whey based medium; the medium compositions were optimized by response surface methodology. The optimum cheese whey based medium consisted of cheese whey 68.34 g/L, Na₂HPO₄ 14.58 g/L and KH₂PO₄ 7.66 g/L, and the maximum gellan gum production that using this medium was 33.75 ± 1.55 g/L. 14.75 ± 0.65 g/L gellan gum was obtained with an optimized molasses medium, which consisted of molasses 50 g/L, Na₂HPO₄ 9.71 g/L and KH₂PO₄ 5.92 g/L. The molecular weight of gellan gum obtained from two medias were 1.06 × 10⁶ and 0.89 × 10⁶ Da, respectively. The cheese whey-derived gellan gum showed a higher rhamnose, lower glucuronic acid and higher glycerate content compared to the molasses-derived gellan gum. S. azotifigens GL-1 has a high gellan gum production capacity in a cheap medium suggesting it has great potential as an industrial gellan gum producer.     

Lactic acid production from corn stover using mixed cultures of Lactobacillus rhamnosus and Lactobacillus brevis

Mixed cultures of Lactobacillus rhamnosus and Lactobacillus brevis was studied for improving utilization of both cellulose- and hemicellulose-derived sugars from corn stover for lactic acid production. During simultaneous saccharification and fermentation (SSF) of NaOH-treated corn stover by the mixed cultures, a lactic acid yield of 0.70 g/g was obtained, which was about 18.6% and 29.6% higher than that by single cultures of L. rhamnosus and L. brevis, respectively. Our results indicated that lactic acid yield from NaOH-pretreated corn stover by mixed cultures of L. rhamnosus and L. brevis was comparable to that from pure sugar mixtures (0.73 g/g of glucose/xylose mixture at 3:1 w/w).     

Production of mycelial biomass and exo-polymer by <Emphasis Type="Italic">Hericium erinaceus</Emphasis> CZ-2: Optimization of nutrients levels using response surface methodology

The Doehlert experimental design was used to optimize the production of mycelial biomass and exopolymer from Hericium erinaceus CZ-2 in this study. Statistical analysis showed that the linear and quadric terms of 3 variables: corn flour, yeast extract, and corn steep liquor had significant effects. The optimized combination of these 3 variables was confirmed through validation experiments. The optimal conditions for higher production of mycelial biomass (19.92 g/L) were estimated when the media composition concentrations were set as: 30.85 g/L, corn flour; 2.81 g/L, yeast extract; 16.9 mL/L, corn steep liquor; 10 g/L, glucose; 1 g/L, KH₂PO₄; and 0.5 g/L, MgSO₄·7H₂O; while a maximal exo-polymer yield (1.653 g/L) could be achieved when setting concentrations of: 32.71 g/L, corn flour; 2.35 g/L, Yeast extract; 14.42 mL/L, Corn steep liquor; 10 g/L, glucose; 1 g/L, KH₂PO₄; and 0.5 g/L, MgSO₄·7H₂O. The upscale production was also investigated using a 15 L fermentor using the optimized medium.     

产GL-7-ACA酰化酶重组菌的构建及高表达研究

戊二酰基-7-氨基头孢烷酸(GL-7-ACA)酰化酶是7-氨基头孢烷酸(7-ACA)两步酶法生产中的关键酶。成功构建组成型表达的产GL-7-ACA酰化酶重组大肠杆菌JM105/pMKC-ACY,并对其高表达条件进行了研究,得到了组成简单、廉价的国产培养基配方及操作简便、易于实现工业化的发酵工艺。在优化条件下,上罐补料高密度发酵的酶活高达6668.9U/L,是优化前的12.4倍,产率最高可达275.5U/(L.h),达到了工业生产的要求。     

Control of glucose feeding using exit gas data and its application to the production of PHB from tapioca hydrolysate byAlcaligenes eutrophus

Summary A method to estimate the glucose concentration in the culture broth using CO₂ evolution rate (CER) data from a mass spectrometer was developed.Alcaligenes eutrophus was cultivated to produce poly(3-hydroxybutyric acid) (PHB) from tapioca hydrolysate using this method. Thek value (g glucose/mol CO₂), defined as the glucose consumption per CO₂ evolution, decreased with culture time and was automatically changed using CER data. The glucose concentration in the culture broth could be controlled at 10 to 20 g/L. A final cell concentration of 106 g/L, PHB concentration of 61 g/L. and PHB content of 58 % of dry cell weight were obtained after 59 h of cultivation.     

耐盐性毒死蜱降解菌HY-1 的产酶培养基及发酵条件优化

为了明确生化处理和微生物降解的关系,通过增加耐盐菌的比例可以提高农药废水生化处理效果。从农药厂废水中分离到1株耐盐性毒死蜱降解菌——蜡状芽孢杆菌(Bacillus cereus HY-1),以从该菌中提取到的降解酶比活力为指标,进行产酶培养基和发酵条件的优化研究。通过单一因素试验和正交试验,对细菌HY-1的产酸培养基和发酵条件进行了优化。运用SPSS软件进行结果分析,所获优化培养基配方为:葡萄糖6.0 g/L,胰蛋白胨2.2 g/L,K2HPO4 2.0 g/L,KH2PO4 0.2 g/L,MgSO4.7H2O 0.1 g/L,NaCl 0.1 g/L和微量元素溶液2 mL/L。得到菌株发酵培养的最佳优化条件为:种子液培养时间为16 h,发酵培养时间为18 h,接种量为1%(V/V),发酵培养基初始pH值为7.0。氯化钠浓度为0?30 g/L时降解酶比活力不受影响,这是已报道的耐盐性最强的一株毒死蜱降解菌。     

Butyric acid production from brown algae using <Emphasis Type="Italic">Clostridium tyrobutyricum</Emphasis> ATCC 25755

Butyric acid fermentation by Clostridium tyrobutyricum ATCC 25755 using glucose or brown algae as a carbon source was carried out. Initially, different fermentation modes (batch, fed-batch, and semi-continuous) at pH 6 and 37°C were compared using a model medium containing glucose as a carbon source. By feeding the whole medium containing 40 ∼ 50 and 30 g/L of glucose into the fed-batch and semi-continuous fermentations, very similar butyrate yields (0.274 and 0.252 g butyrate/g glucose, respectively) and productivities (0.362 and 0.355 g/L/h, respectively) were achieved. The highest butyrate concentration was about 50 g/L, which was observed in the fed-batch fermentation with whole medium feeding. However, semi-continuous fermentation sustained a longer fermentation cycle than the fed-batch fermentation due to end-product and metabolic waste inhibition. The established conditions were then applied to the fermentation using brown algae, Laminaria japonica and Undaria pinnatifida, as substrates for butyric acid fermentation. To hydrolyze brown algae, 7.5 ∼ 10% (w/v) dried brown algae powder was suspended in 1% (w/v) NaOH or 0.5 ∼ 2.5% (w/v) H₂SO₄ and then autoclaved at 121°C for 30 ∼ 90 min. The resulting butyrate concentration was about 11 g/L, which was produced from 100 g/L of L. japonica autoclaved for 60 min in 1.5% H₂SO₄ acid solution.     

Improving the production of S-adenosyl-L-methionine in Escherichia coli by overexpressing metk

S-adenosyl-L-methionine (SAM) has important applications in many fields including chemical therapy and pharmaceutical industry. In this study, the recombinant Escherichia coli strain was constructed for effective production of SAM by introducing the SAM synthase gene (metK). This strain produced 34.5?mg/L of SAM in basic medium in shake flask. Yeast extract, pH, and loaded volume had a significant positive effect on the yield of SAM. Their optimal values were 35?g/L, 7.5, and 30?mL, respectively. The final conditions optimized were as follows: glucose 20, g/L; peptone, 40?g/L; yeast extract, 35?g/L; NaCl, 10?g/L; MgSO₄, 1.2?g/L; L-methionine, 1?g/L; rotate speed, 220?rpm; loaded volume, 30?mL; inoculation, 1%; temperature, 37°C; and initial medium, pH 7.5. The recombinant strain produced 128.2?mg/L of SAM under the above conditions in shake flask. The production of SAM in a 5?L fermentor was also investigated. The maximal biomass of the recombinant strain was 60.4?g/L after the cells were cultured for 20?hr, and the highest yield of SAM was 300.9?mg/L after induction for 8?hr in a 5?L fermentor. This study provides a good foundation for the future production and use of SAM.     

Synthesis of nylon 4 from gamma-aminobutyrate (GABA) produced by recombinant Escherichia coli

In this study, we developed recombinant Escherichia coli strains expressing Lactococcus lactis subsp. lactis Il1403 glutamate decarboxylase (GadB) for the production of GABA from glutamate monosodium salt (MSG). Syntheses of GABA from MSG were examined by employing recombinant E. coli XL1-Blue as a whole cell biocatalyst in buffer solution. By increasing the concentration of E. coli XL1-Blue expressing GadB from the OD₆₀₀ of 2–10, the concentration and conversion yield of GABA produced from 10 g/L of MSG could be increased from 4.3 to 4.8 g/L and from 70 to 78 %, respectively. Furthermore, E. coli XL1-Blue expressing GadB highly concentrated to the OD₆₀₀ of 100 produced 76.2 g/L of GABA from 200 g/L of MSG with 62.4 % of GABA yield. Finally, nylon 4 could be synthesized by the bulk polymerization using 2-pyrrolidone that was prepared from microbially synthesized GABA by the reaction with Al₂O₃ as catalyst in toluene with the yield of 96 %.     

人干扰素INF-ω在植物乳杆菌中的表达与鉴定

目的以植物乳杆菌为载体,将干扰素IFN-ω基因导入植物乳杆菌内,作为先期探索和尝试,构建重组阴道微生态菌株。方法采用抗菌肽诱导双组分调节表达系统,以细菌素SakacinA为诱导物、sapK和sapR为双组分调节基因的穿梭质粒pSIP300,将干扰素ω基因置于pstP300上,构成重组质粒psIP300-ω,在大肠埃希菌DI-ISet中进行扩增,分别电转化3株植物乳杆菌。Lacbacillus plantarum1．3,Lacbacillus plantarum 1．11,Lacbacillus plantarum 14917。结果与结论经SDS-PAGE与ELISA检测证实,成功构建了能够表达IFN-ω重组植物乳杆菌Lacbacillus plantarum 1．11／pSIIB00-ω。