高产谷胱甘肽的酵母菌选育及其培养条件研究

筛选到一株具有较高GSH产量的酵母菌株S.cerevisiae2165,然后以该菌株为出发菌,采用紫外照射,紫外照射 LiCl联合处理,亚硝基胍（MNNG）等诱变处理,获得一株高产GSH的酿酒酵母优良菌株S.cerevisiaeJN-5-8。该菌株具有稳定的遗传性能,在经过优化的培养条件下培养24h,其GSH产量达到339.1mg/L。比出发菌株提高2.2倍。     

高生物量富铁酵母菌的选育及其发酵条件的研究

对402株不同种属的酵母菌株进行初筛、复筛,筛选到一株生物量较高的二倍体菌株ZY-46(Saccharomyces cerevisiae)和一株铁富集量较高的二倍体菌株ZY-173(Saccharomyces kluyveri)。然后以它们为出发菌,分别进行单倍体分离、硫酸二乙酯(DES)诱变,并通过原生质体融合,得到一株高生物量富铁酵母融合菌株ZYF-15。在优化的发酵条件下,该融合菌株生物量可达11．2g／L,细胞铁含量达24．5mg／g干细胞,细胞总铁含量分别比原始亲株ZY-46和ZY-173提高了2．6倍和1．9倍。     

复合诱变选育高产GSH的菌株

目的:选育出GSH的高产菌株.方法:以产GSH的产朊假丝酵母(Candida utilis)为出发菌株,利用紫外-超声波复合诱变.结果:筛选得到ZnCl2抗性突变株UU3,GSH菌体含量为53.50mg·g-1,比出发菌株提高137.03%.结论:突变株UU3遗传性能稳定,可做进一步研究.     

等离子体-紫外线复合诱变选育高产谷胱甘肽酵母菌

以产还原型谷胱甘肽（glutathione,GSH）的啤酒酵母（Sacchromyces cerevisiae）SC-20为出发菌株,采用氩气等离子体射线、紫外照射及两者的复合诱变处理,获得一株高产GSH的酿酒酵母优良菌株（S．cerevisiae）DU-20．结果表明该菌株具有稳定的遗传性能,GSH含量与产量分别比出发菌株提高了78.33％和118．4％．     

专一性脱硫菌的鉴定及高DBT降解力菌株的选育

从大庆油田土壤中分离得到1株可降解二苯并噻吩(DBT)的脱硫微生物HDBS-1,对该微生物的种属地位进行了鉴定并通过诱变手段提高了该菌株的脱硫能力。经过形态观察、生理生化特征分析及16S rDNA序列测定发现该微生物为坂崎肠杆菌(Enterobacter sakazakii),该菌种可以按特异性脱硫途径(简称4S途径)将DBT转化为2-羟基联苯(2-HBP)。利用紫外线(UV)、硫酸二乙酯(DES)和UV+DES对该菌株复合诱变后,得到菌株HDBS-4,其降解DBT生成2-HBP的能力得到了极大的提高,发酵液中2-HBP生成含量(2.574 mg/L)较原始菌株(0.434 mg/L)提高了5.93倍。     

高通量筛选高产酪氨酸的酿酒酵母菌株

酪氨酸是重要的芳香族氨基酸,自身不仅具有重要的营养价值,也是合成香豆素类化合物和黄酮类化合物的重要前体。文中以实验室前期构建的一株解除了酪氨酸反馈抑制的酿酒酵母Saccharomyces cerevisiae LTH0 (ARO4K229L,ARO7G141S,Δaro10,Δzwf1,Δura3) 为出发菌株,异源表达甜菜黄素合成基因DOD和CYP76AD1,使酿酒酵母产生黄色荧光。然后利用紫外诱变和常压室温等离子体 (Atmospheric and room temperature plasma,ARTP) 诱变相结合的方法对上述菌株进行随机诱变,并通过流式细胞仪筛选荧光强度显著提高的突变株。其中突变株LTH2-5-DOD-CYP76AD1在激发波长485 nm、发射波长505 nm处荧光强度为 (5 941±435) AU/OD,比诱变前提高了8.37倍。对诱变后荧光强度提高较多的14株突变株进行发酵生产酪氨酸,胞外酪氨酸产量最高为26.8 mg/L,比出发菌株提高了3.96倍。进一步异源表达约翰逊黄杆菌Flavobacterium johnsoniae来源的酪氨酸解氨酶FjTAL,对香豆酸产量达到119.8 mg/L,比出发菌株LTH0-FjTAL提高了1.02倍。     

Kluyveromyces marxianus发酵己糖和戊糖生产乙醇

对利用底物广泛的乙醇发酵菌株马克斯克鲁维(Kluyveromyces marxianus)DL1菌株与工业用乙醇发酵菌株酿酒酵母(Saccharomyces cerevisiae)6525利用己糖(葡萄糖、甘露糖、半乳糖)和戊糖(木糖、阿拉伯糖)的情况进行对比研究。结果发现:以己糖为底物时,K.marxianus DL1均表现出细胞生长快、乙醇得率高的特点;在不通气、糖20 g/L条件下,K.marxianus DL1的最大乙醇质量浓度均比S.cerevisiae 6525高出10%左右,细胞量及乙醇生产强度分别是S.cerevisiae 6525的近2和1.7倍。当以戊糖为底物时,K.marxianus DL1可以利用木糖和阿拉伯糖;在不通气、糖20g/L条件下,K.marxianus DL1利用木糖产木糖醇和乙醇,乙醇终质量浓度可达7.68 g/L,木糖醇质量浓度为9.12 g/L;以阿拉伯糖为发酵底物时,阿拉伯糖醇的产量可达6 g/L左右;而S.cerevisiae 6525不能利用戊糖。马克斯克鲁维酵母比酿酒酵母更适合纤维乙醇生产。     

L-精氨酸高产菌的选育及基于代谢流量分布的育种机制

从分析钝齿棒杆菌(Corynebacterium crenatum)的精氨酸合成途径入手,提出了一种通过选育脯氨酸结构类似物抗性突变株以提高其精氨酸合成能力的育种思路。采用亚硝基胍(NTG)诱变处理出发菌株YD8(His-,SGr1.2 mg/mL,D-Argr15 mg/mL),经含15 mg/mL的脯氨酸结构类似物S-甲基半胱氨酸(S-MC)的抗性筛选获得精氨酸高产突变株YDM403(His-,SGr1.2 mg/mL,D-Argr15 mg/mL,S-MCr15 mg/mL),产酸水平可达29.4 g/L,较出发菌株YD8的产酸高出55.0%。通过代谢流量分布分析了菌株YD8和YDM403代谢网络的变化,结果表明,菌株YD8可能存在顺序反馈抑制作用,出发株YD8解除了Arg对Glu到Arg的反馈抑制,而YDM403又解除了Pro对Glu到Pro的反馈抑制,从而使中间物Glu累积量下降而对-αKG到Glu不再有反馈抑制,其通量提高,与此同时从Glu向Arg的代谢通量也相应增加。     

原生质体诱变选育ε-聚赖氨酸高产菌株

以白色链霉菌UN2-71为出发菌株,对其原生质体进行硫酸二乙酯(DES)诱变,选育ε-聚赖氨酸高产菌株。经过试管初筛和摇瓶复筛,得到1株稳定性好的菌株D3-32,摇瓶产量达到1.56g/L,比出发菌株提高49.43%。采用2.3L发酵罐进行发酵试验,控制pH分两阶段培养后,ε-聚赖氨酸最高产量达到4.59g/L,比出发菌株提高了2.65倍。     

乙酰辅酶A合成代谢对酿酒酵母生理功能的影响

【目的】研究酿酒酵母(Saccharomycesc erevisiae)中乙酰辅酶A合成酶基因ACS1和ACS2的生理作用。【方法】将来源于S.cerevisiae的ACS1和ACS2分别进行过量表达,研究过量表达ACS1和ACS2后S.cerevisiae胞内乙酰辅酶A含量、ATP水平、甲羟戊酸途径转录和乙醇耐受性等生理学特性变化。【结果】与出发菌株相比,过量表达ACS1和ACS2使得:(1)胞内乙酰辅酶A含量提高了2.19倍(ACS1)和5.02倍(ACS2);(2)胞内ATP含量提高了3.93倍(ACS1)和2.05倍(ACS2);(3)甲羟戊酸途径8个关键基因表达量显著上调;(4)S.cerevisiae对乙醇胁迫抵御能力显著增强。过量表达ACS1对乙醇胁迫的耐受能力强于过量表达ACS2。【结论】增加胞内乙酰辅酶A的含量可以显著增加甲羟戊酸途径碳代谢流量,并增强S.cerevisiae对发酵过程主要副产物乙醇的耐受能力。     

基于代谢通量分析的琥珀酸放线杆菌高产选育研究

在对产琥珀酸放线杆菌代谢分析的基础上选育出高产突变株对琥珀酸的工业生物转化有重要意义.在矩阵分析代谢通量基础上,围绕柔性节点下的副产物乙酸及乙醇的降低分别实施软X诱变及定点突变选育,并对比分析了突变株与出发株相关酶活及基因序列变化.针对出发株的流量分析显示产物琥珀酸的代谢通量为1.78(mmol/g/h),主要副产物乙酸与乙醇的代谢通量分别为(0.60mmol/g/h)和(1.04 mmol/g/h),并发现乙醇代谢加剧了琥珀酸合成中的H电子供体的不足;筛选出的氟乙酸抗性突变株S.JST1的乙酸代谢通量降低了96%,为0.024(mmol/g/h),酶活检测表明磷酸乙酰转移酶(Pta)的酶比活力从602降低到74,进一步的序列对比分析发现pta突变基因中产生了一个突变位点:adh定点复合突变株S.JST2的乙醇代谢通量降低了98%,为0.020(mmol/g/h),酶活检测表明Adh的酶比活力从585降低到62.最终突变株S.JST2琥珀酸累积产量达65.7 g/L.围绕产琥珀酸放线杆菌Pta及Adh酶活的降低实施定向选育,在降低副产物流量的同时,有助于改善细胞H供体代谢平衡进而提高琥珀酸的流量.所获突变株具有工业应用潜力.     

调控酿酒酵母类异戊二烯合成途径强化芳樟醇合成

芳樟醇是一种重要单萜,广泛应用于食品、医药、日化等工业领域.然而芳樟醇在植物中含量低且难提取,限制了其大规模生产.目前通常以酿酒酵母Saccharomyces cerevisiae作为单萜生物合成宿主,其内源类异戊二烯合成途径提供合成单萜物质的前体——香叶基二磷酸(GPP).由于该途径代谢通量较低,导致GPP供应不足,极大地降低了异源单萜的合成效率.为了调节该途径的代谢通量,构建酿酒酵母整合表达载体pRS305-tHMG1和游离表达载体pYLIS-IDI1,并分别转入酿酒酵母CEN.PK2-lC中,获得酿酒酵母工程菌LS01和LS02.同时将载体pYLIS-IDIl转入酿酒酵母工程菌LS01中,构建酿酒酵母工程菌LS03.GC-MS检测结果显示,通过提高异戊二烯二磷酸异构酶(IDIl)和羟甲基戊二酸单酰辅酶A(HMG-CoA)还原酶活性区域(tHMGl)的表达水平,最终使芳樟醇产量提高1.3倍至(127.71±7.68) tg/L.结果表明,通过调控类异戊二烯合成途径,强化GPP合成前体供给,可以显著提高酿酒酵母中芳樟醇的产量.     

产瓦伦西亚烯酿酒酵母的表达载体适配及发酵碳氮源优化

瓦伦西亚烯是一种倍半萜类化合物,广泛应用于香水、香皂、食品和饮料等工业制造上。但由于其自然含量极低,且目前获取瓦伦西亚烯的方法较为麻烦且花费高,因而构建细胞工厂进行瓦伦西亚烯的生物合成是更为高效和环保的方法。选取酿酒酵母(Saccharomyces cerevisiae)作为宿主构建细胞工厂,先在酿酒酵母基因组上引入黄扁柏的瓦伦西亚烯合成酶(Valencene synthase from Callitropsis nootkatensis,CnVS),实现瓦伦西亚烯的初步合成,初始产量为4.16 mg/L。随后利用CRISPR/Cas9系统对酿酒酵母中Mevalonate(MVA)途径的erg9和rox1基因进行敲除,提高通往瓦伦西亚烯合成的碳流量。不同碳氮源浓度发酵的结果表明,细胞生长积累过高可能不利于瓦伦西亚烯的积累。最后探究了不同CnVS表达载体对瓦伦西亚烯产量的影响,并获得17.54 mg/L的最高产量,是出发菌株的4.2倍。     

Strain improvement and metabolic flux modeling of wild-type and mutant <Emphasis Type="Italic">Alcaligenes</Emphasis> sp. NX-3 for synthesis of exopolysaccharide welan gum

Low-energy nitrogen ion beam implantation technique was used for the strain improvement of Alcaligenes sp. NX-3 for the production of exopolysaccharide welan gum. A high welan gum producing mutant, Alcaligenes sp. NX-3-1, was obtained through 20 keV N⁺ ion beam irradiation. Starting at a concentration of 50 g/L of glucose, mutant NX-3-1 produced 25.0 g/L of welan gum after 66 h of cultivation in a 7.5 L bioreactor, which was 34.4% higher than that produced by the wild-type strain. The results of metabolic flux analysis showed that the glucose-6-phosphate and acetyl coenzyme A nodes were the principle and flexible nodes, respectively. At the glucose-6-phosphate node, the fraction of carbon measured from glucose-6-phosphate to glucose-1-phosphate was enhanced after mutagenesis, which indicated that more flux was used to synthesize welan gum in the mutant. By analyzing the activities of related enzymes in the biosynthetic pathway of sugar nucleotides essential for welan gum production, we found that the specific activities of phosphoglucomutase, UDP-glucose pyrophosphorylase, UDP-glucose dehydrogenase, and dTDP-glucose pyrophosphorylase in the mutant strain were higher than those in the wild-type strain. These improvements in enzyme activities could be due to the affected of ion beam implantation.     

Engineering of Corynebacterium glutamicum for high-level γ-aminobutyric acid production from glycerol by dynamic metabolic control

Synthetic biology seeks to reprogram microbial cells for efficient production of value-added compounds from low-cost renewable substrates. A great challenge of chemicals biosynthesis is the competition between cell metabolism and target product synthesis for limited cellular resource. Dynamic regulation provides an effective strategy for fine-tuning metabolic flux to maximize chemicals production. In this work, we created a tunable growth phase-dependent autonomous bifunctional genetic switch (GABS) by coupling growth phase responsive promoters and degrons to dynamically redirect the carbon flux for metabolic state switching from cell growth mode to production mode, and achieved high-level GABA production from low-value glycerol in Corynebacterium glutamicum. A ribosome binding sites (RBS)-library-based pathway optimization strategy was firstly developed to reconstruct and optimize the glycerol utilization pathway in C. glutamicum, and the resulting strain CgGly2 displayed excellent glycerol utilization ability. Then, the initial GABA-producing strain was constructed by deleting the GABA degradation pathway and introducing an exogenous GABA synthetic pathway, which led to 5.26 g/L of GABA production from glycerol. In order to resolve the conflicts of carbon flux between cell growth and GABA production, we used the GABS to reconstruct the GABA synthetic metabolic network, in which the competitive modules of GABA biosynthesis, including the tricarboxylic acid (TCA) cycle module and the arginine biosynthesis module, were dynamically down-regulated while the synthetic modules were dynamically up-regulated after sufficient biomass accumulation. Finally, the resulting strain G7-1 accumulated 45.6 g/L of GABA with a yield of 0.4 g/g glycerol, which was the highest titer of GABA ever reported from low-value glycerol. Therefore, these results provide a promising technology to dynamically balance the metabolic flux for the efficient production of other high value-added chemicals from a low-value substrate in C. glutamicum.     

具有高谷胱甘肽合成活性重组大肠杆菌的构建及合成反应过程

以野生型大肠杆菌E.coliⅡ为宿主细胞,转化带有编码谷胱甘肽合成酶系的基因gshⅠ和gshⅡ的质粒pGH501,获得了一株谷胱甘肽合成活性、质粒稳定性和传代稳定性俱佳,并且能够重复使用的重组大肠杆菌E.coliⅡ\|1。该菌株经过甲苯处理后,能够在胞外积累4g/L左右的谷胱甘肽(GSH)。在合成反应体系中,提高L谷氨酸浓度可促进GSH合成,但L半胱氨酸浓度增大到20mmol/L后会抑制GSH的合成。根据GSH合成反应中能量辅因子的变化情况,提出E.coliⅡ\|1细胞控制的GSH合成反应机理：由谷胱甘肽合成酶(GSHⅡ)控制的第二步反应的能量供体是ADP而非ATP,该反应是整个GSH合成反应的限速步骤,高浓度ADP可能会抑制GSHⅡ的活性。在GSH合成反应体系中添加100mmol/L的L丝氨酸-硼酸钾混合物,可以有效地防止GSH的进一步降解,反应3 h后,GSH产量达到230mmol/L(约71g/L)。     

Strain improvement and metabolic flux analysis in the wild-type and a mutant Lactobacillus lactis strain for L(+)-lactic acid production

The effects of initial glucose concentration and calcium lactate concentration on the lactic acid production by the parent strain, Lactobacillus lactis BME5-18, were studied. The results of the experiments indicated that glucose and lactate repressed the cell growth and the lactic acid production by Lactobacillus lactis BME5-18. A L(+)-lactic acid overproducing strain, Lactobacillus lactis BME5-18M, was screened by mutagenizing the parent strain with ultraviolet (UV) light irradiation and selecting the high glucose and lactate calcium concentration repression resistant mutant. Starting with a concentration of 100g L(-1) glucose, the mutant produced 98.6 g L(-1) lactic acid after 60 h in flasks, 73.9% higher than that of the parent strain. The L(+)-lactic acid purity was 98.1% by weight based on the amount of total lactic acid. The culture of the parent strain could not be analyzed well by conventional metabolic flux analysis techniques, since some pyruvate were accumulated intracellularly. Therefore, a revised flux analysis method was proposed by introducing intracellular pyruvate pool. Further studies demonstrate that there is a high level of NADH oxidase activity (12.11 mmol mg(-1) min(-1)) in the parent strain. The molecular mechanisms of the strain improvement were proposed, i.e., the high level of NADH oxidase activity was eliminated and the uptake rate of glucose was increased from 82.1 C-mmol (g DW h)(-1) to 98.9 C-mmol (g DW h)(-1) by mutagenizing the parent strain with UV, and therefore the mutant strain converts mostly pyruvate to lactic acid with a higher productivity (1.76 g L(-1) h(-1)) than the parent strain (0.95 g L(-1) h(-1)).     

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.     

Carbon-Flux Distribution within Streptomyces coelicolor Metabolism: A Comparison between the Actinorhodin-Producing Strain M145 and Its Non-Producing Derivative M1146

Metabolic Flux Analysis is now viewed as essential to elucidate the metabolic pattern of cells and to design appropriate genetic engineering strategies to improve strain performance and production processes. Here, we investigated carbon flux distribution in two Streptomyces coelicolor A3 (2) strains: the wild type M145 and its derivative mutant M1146, in which gene clusters encoding the four main antibiotic biosynthetic pathways were deleted. Metabolic Flux Analysis and ¹³C-labeling allowed us to reconstruct a flux map under steady-state conditions for both strains. The mutant strain M1146 showed a higher growth rate, a higher flux through the pentose phosphate pathway and a higher flux through the anaplerotic phosphoenolpyruvate carboxylase. In that strain, glucose uptake and the flux through the Krebs cycle were lower than in M145. The enhanced flux through the pentose phosphate pathway in M1146 is thought to generate NADPH enough to face higher needs for biomass biosynthesis and other processes. In both strains, the production of NADPH was higher than NADPH needs, suggesting a key role for nicotinamide nucleotide transhydrogenase for redox homeostasis. ATP production is also likely to exceed metabolic ATP needs, indicating that ATP consumption for maintenance is substantial.Our results further suggest a possible competition between actinorhodin and triacylglycerol biosynthetic pathways for their common precursor, acetyl-CoA. These findings may be instrumental in developing new strategies exploiting S. coelicolor as a platform for the production of bio-based products of industrial interest.     

代谢工程改造酿酒酵母合成葡萄糖二酸

葡萄糖二酸是一种高附加值的有机酸,广泛用于食品、医药和化工领域。为获得生产葡萄糖二酸的微生物细胞工厂,通过共表达小鼠来源的肌醇加氧酶(MIOX)及恶臭假单胞菌来源的醛酸脱氢酶(Udh),在酿酒酵母Saccharomyces cerevisiae CEN.PK2-1C中构建了葡萄糖二酸合成途径,产量为(28.28±3.15)mg/L。在此基础上,通过调控前体肌醇的合成途径,发现肌醇-1-磷酸合成酶(INO1)是葡萄糖二酸合成途径的限速酶,过量表达INO1,葡萄糖二酸产量达到(107.51±10.87)mg/L,提高了2.8倍。进一步弱化竞争支路中磷酸果糖激酶(PFK1)的表达,最终葡萄糖二酸的产量达到(230.22±10.75)mg/L,为进一步获得高产葡萄糖二酸细胞工厂提供基础。