NADPH依赖的甘露醇脱氢酶的重组表达及甘露醇的转化条件

对NADPH依赖的甘露醇脱氢酶的异源表达和对果糖的转化情况进行分析,为在细胞内构建甘露醇的合成途径奠定基础。构建重组菌株BL21(DE3)/p ET28a-mdh,对其进行诱导发酵后,通过His标签对目的蛋白进行纯化,并利用HPLC分析纯化后的甘露醇脱氢酶转化果糖生成甘露醇的情况。成功构建了NADPH依赖的甘露醇脱氢酶重组表达菌株BL21(DE3)/p ET28amdh,并对表达后的甘露醇脱氢酶进行了纯化,测得纯化后的甘露醇脱氢酶酶活力为270 U/m L。对酶法转化果糖得到甘露醇的转化条件进行优化,确定最佳的转化条件为:当底物浓度为300 g/L,反应初始p H5.8,温度40℃,NADPH终浓度为9 mmol/L时,甘露醇转化率可以达到97.4%。实现了NADPH依赖的甘露醇脱氢酶在大肠杆菌中的活性表达,为进一步研究大肠杆菌合成甘露醇的代谢调控提供了依据。     

以蔗糖为底物利用重组大肠杆菌合成甘露醇

【目的】异型发酵乳酸菌可利用胞内产生的甘露醇脱氢酶将果糖高效转化为甘露醇,但果糖作为底物相对昂贵,不利于工业化生产。为了降低生产成本,必须选择廉价的底物。蔗糖相对便宜,并且大量存在于自然界中,能够被重组大肠杆菌利用产生甘露醇。蔗糖水解酶(Sucrose hydrolase)和甘露醇脱氢酶(Mannitol dehydrogenase)是发酵生产甘露醇中催化蔗糖转化成甘露醇的关键酶,构建蔗糖水解酶和甘露醇脱氢酶共表达菌株并进行相关研究是本文的主旨。【方法】利用PCR方法分别从植物乳杆菌(Lactobacillus plantarum)和布氏乳杆菌(Lactobacillus buchneri)基因组DNA中获得sac A和mdh基因,得到大小分别为1 502 bp和1 032 bp的目的基因,经序列分析后将其连接到表达载体p ET-28a(+)上,得到重组表达载体p ET28a-sac A-mdh。将重组质粒转化到大肠杆菌BL21(DE3)中,并用SDS-PAGE分析目的蛋白的表达情况并测定其酶活。【结果】SDS-PAGE显示表达蛋白的大小亚基分子量分别为55.1 k D和37.8 k D,与预期分子量一致,实现sac A和mdh基因的表达。蔗糖水解酶和甘露醇脱氢酶酶活分别为25.78 U/m L和14.56 U/m L。对重组菌株BL21(DE3)/p ET28a-sac A-mdh进行发酵条件优化,甘露醇质量浓度达到45.19 g/L,总糖转化率为37.66%。【结论】与乳酸菌利用蔗糖发酵生产甘露醇相比,产量提高了6倍,且具有发酵周期短、稳定性高等优点,菌株的成功构建为甘露醇工业化生产奠定了基础。     

信息库

1　乳酸乳球菌基因工程菌产生甘露醇　　甘露醇对健康有利 ,发酵时增加食品中甘露醇的含量可以提高发酵食品的营养价值。甘露醇是一种低热量甜味剂 ,在小肠中吸收很慢 ,它还是氢氧根的清除剂。在人的肠道中 ,甘露醇可以转化成短链脂肪酸 (如丁酸 ) ,可以预防结肠癌发生。　　异型发酵乳酸菌在果糖发酵时通过甘露醇脱氢酶产生甘露醇。而在同型发酵乳酸菌中 ,只有失去NAD+ 再生能力的菌株才能形成甘露醇。本研究组曾报道 ,乳酸乳球菌的乳酸脱氢酶缺失株可以合成甘露醇和甘露醇 1 磷酸。但是 ,在葡萄糖耗尽后甘露醇很快被吸收和代谢。本研究…     

基于双酶级联协调表达策略高效催化合成D-甘露醇北大核心CSCD

D-甘露醇(D-mannitol)作为合成抗肿瘤药和免疫刺激剂的重要前体被广泛应用于制药和医疗等行业,酶法合成D-甘露醇反应成本昂贵无法满足工业化生产。本研究首先筛选关键酶获得较优性能的甘露醇脱氢酶Lp MDH和用于辅因子NADH再生的葡萄糖脱氢酶Ba GDH,在大肠杆菌(Escherichia coli)BL21(DE3)中共表达,实现了基于双酶级联反应催化底物D-果糖合成D-甘露醇,D-甘露醇的初步摩尔转化率为59.7%。针对双酶级联催化反应中辅酶再生用酶与催化用酶表达量不协调的问题,通过增加Bagdh拷贝量来提高辅因子循环能力,获得了双酶催化速率平衡的重组大肠杆菌E.coli BL21/pETDuet-Lpmdh-Bagdh-Bagdh。进一步对重组菌的全细胞转化条件进行优化,确定了最适转化条件为反应温度30℃,初始pH值6.5,菌体量OD600=30,底物D-果糖100.0 g/L,辅底物葡萄糖与底物1︰1摩尔当量。于最优转化条件下5 L发酵罐转化24 h,D-甘露醇的最高产量为81.9g/L,摩尔转化率为81.9%。本研究提供了一种绿色、高效生物催化生产D-甘露醇的方法,为实现其规模化生产奠定了基础,同时也对其他相关稀有糖醇的研究具有指导意义。     

产丁二酸谷氨酸棒状杆菌基因缺失代谢工程菌株的构建

【目的】提高谷氨酸棒状杆菌(Corynebacterium glutamicum)ATCC13032厌氧条件下的丁二酸产量,并降低发酵产物中副产物的含量。【方法】以谷氨酸棒状杆菌(Corynebacterium glutamicum)ATCC13032为出发菌,首先敲除乳酸形成的关键酶乳酸脱氢酶基因(ldh),构建ldh缺失株谷氨酸棒状杆菌ATCC13032Δldh;然后以缺失株谷氨酸棒状杆菌ATCC13032Δldh为出发菌,敲除该菌的丙酮酸脱氢酶系的E1p酶基因(aceE),构建一株双缺失突变菌株谷氨酸棒状杆菌ATCC13032ΔldhΔaceE。【结果】与供试菌比较,谷氨酸棒状杆菌ATCC13032Δldh的丁二酸产量和转化率分别提高了94.9%和32%,并且主要的副产物乳酸产量由出发菌产量的63.5 g/L降低到很微量的程度。丙酮酸脱氢酶的失活并不能完全消除副产物乙酸的形成,但乙酸的产量较ATCC13032Δldh降低了37.9%,丁二酸的产量略有提高。【结论】该重组菌具有较强的丁二酸生产工业化潜力,并且该研究方法为微生物代谢育种提供参考。     

乳糖诱导丙酮酸羧化酶基因在大肠杆菌中的表达及对丁二酸产量的影响

大肠杆菌DC1515是敲除葡萄糖磷酸转移酶(ptsG)、乳酸脱氢酶(ldhA)、丙酮酸甲酸裂解酶(pflA)基因的菌株,具有发酵生产丁二酸的潜力。为进一步提高菌株DC1515的丁二酸生产能力,将枯草芽孢杆菌丙酮酸羧化酶(pyc)基因转入其中。用乳糖代替IPTG诱导pyc表达,确定了最佳乳糖加入时间、乳糖浓度及诱导温度。在此基础上,考察了补加乳糖对丁二酸产量的影响。结果表明:由于ptsG基因缺失,当培养基中葡萄糖浓度达到15g/L时,乳糖诱导作用并不受葡萄糖抑制。优化诱导条件后,pyc过表达菌株的丁二酸产量达15.17g/L,为对照菌株的1.78倍。间歇补加乳糖2次至浓度为1g/L,丁二酸产量可进一步增至17.54g/L。研究结果为以葡萄糖为底物生产丁二酸的过程中乳糖诱导外源基因在大肠杆菌中的表达奠定了基础。乳糖诱导降低了成本,有利于实现丁二酸发酵生产的工业化。     

丁醇合成途径关键酶基因在大肠杆菌中的克隆和表达

【目的】克隆丙酮丁醇梭状芽胞杆菌(Clostridium acetobutylicum)ATCC824丁醇合成途径关键酶基因,构建产丁醇的工程大肠杆菌。【方法】以C.acetobutylicum ATCC824基因组为模板,分别扩增丁醇合成途径关键酶基因thil,adhE2和BCS operon(crt-bcd-etfB-etfA-hbd)基因序列,构建BCS operon-adhE2-thil/pTrc99a/MG1655(pBAT)。重组菌E.coli pBAT采用0.1 mmol异丙基-β-硫代半乳糖苷(IPTG)诱导5 h,测定乙酰基转移酶(THL)、3-羟基丁酰辅酶A脱氢酶(HBD)、3-羟基丁酰辅酶A脱水酶(CRT)、丁酰辅酶A脱氢酶(BCD)、醛醇脱氢酶(BYDH/BDH)的酶活。并以该基因工程菌作为发酵菌种,采用好氧、厌氧和微好氧三种培养方式,检测丁醇产量。【结果】酶活测定结果显示:THL酶活达到0.160 U/mg protein,酶活力提高了近30倍;HBD酶活力提高了近5倍;CRT酶活达到1.53 U/mg protein,野生菌株无此酶活;BCD酶活力提高了32倍;BYDH/BDH酶活力无显著提高。3种发酵培养结果显示在微好氧和厌氧条件下,均有丁醇产生,且丁醇的最大产量约为84 mg/L。【结论】本实验通过构建产丁醇基因工程大肠杆菌,实现了丁醇关键酶基因在大肠杆菌中的活性表达以及发酵产丁醇,为发酵法生产丁醇开辟了一条新的途径。     

来自詹氏乳杆菌的耐热D-乳酸脱氢酶的酶学性质研究

【目的】D-乳酸脱氢酶是催化丙酮酸合成D-乳酸的关键酶。由于其不耐热,从而限制了D-乳酸高温发酵菌株的构建。本文从詹氏乳杆菌中克隆新型D-乳酸脱氢酶研究其酶学性质,为构建D-乳酸高温发酵菌株,进一步降低D-乳酸生产成本奠定基础。【方法】通过克隆詹氏乳杆菌的D-乳酸脱氢酶,将其进行体外表达,并与来自植物乳杆菌中的D-乳酸脱氢酶的最适温度、最适pH、动力学参数及热稳定性和热失活性相比较,研究詹氏乳杆菌D-乳酸脱氢酶的耐热性。【结果】詹氏乳杆菌的D-乳酸脱氢酶最适温度(45 °C)比植物乳杆菌中的D-乳酸脱氢酶的最适温度(30 °C)高很多,热失活的时间和温度均要比植物乳杆菌中D-乳酸脱氢酶高很多。同时其催化效率(kcat/Km)是植物乳杆菌D-乳酸脱氢酶的3倍左右。【结论】詹氏乳杆菌的D-乳酸脱氢酶具有更好的耐热性和更高的催化活力。     

过量表达苹果酸脱氢酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111是敲除了乳酸脱氢酶的编码基因 (ldhA) 和丙酮酸-甲酸裂解酶的编码基因 (pflB) 的工程菌,厌氧条件下由于辅酶NAD(H) 的不平衡导致其丧失了代谢葡萄糖的能力。构建了苹果酸脱氢酶的重组菌大肠杆菌NZN111/pTrc99a-mdh,在厌氧摇瓶发酵过程中通过0.3 mmol/L的IPTG诱导后重组菌的苹果酸脱氢酶 (Malate dehydrogenase,MDH) 酶活较出发菌株提高了14.8倍,NADH/NAD+的比例从0.64下降到0.26,同时NAD+和NADH浓度分别     

不同碳源对大肠杆菌lpdA突变菌累积丙酮酸的影响

为了利用大肠杆菌构建模式"细胞工厂",必须了解在构建过程中各种因素的影响。本研究选用敲除了lpdA基因的大肠杆菌作为模型细胞,考察了该突变菌在合成培养基中利用葡萄糖、果糖、木糖和甘露糖累积丙酮酸的能力。结果显示,在初始糖浓度为10g/L的情况下,lpdA突变菌可以很好地利用葡萄糖、果糖、木糖和甘露糖转化丙酮酸,其得率分别达到了0.884g/g、0.802g/g、0.817g/g和0.808g/g,且在以葡萄糖、果糖和木糖发酵时,丙酮酸的积累过程与细胞生长偶联。甘露糖发酵的情况则不同:菌浓度很快达到平台期,随后丙酮酸积累和甘露糖消耗都表现为线性变化。当在考察了不同的接种量对lpdA突变菌发酵葡萄糖的影响时发现,大接种量能加快葡萄糖消耗速率、丙酮酸的积累速率和细胞生长速率,但丙酮酸得率却明显下降。这些结果对构建以大肠杆菌为母体的模式"细胞工厂"有参考价值。     

Engineering a homobutanol fermentation pathway in Escherichia coli EG03

A homobutanol fermentation pathway was engineered in a derivative of Escherichia coli B (glucose [glycolysis] => 2 pyruvate + 2 NADH; pyruvate [pyruvate dehydrogenase] => acetyl-CoA + NADH; 2 acetyl-CoA [butanol pathway enzymes] + 4 NADH => butanol; summary stoichiometry: glucose => butanol). Initially, the native fermentation pathways were eliminated from E. coli B by deleting the genes encoding for lactate dehydrogenase (ldhA), acetate kinase (ackA), fumarate reductase (frdABCD), pyruvate formate lyase (pflB), and alcohol dehydrogenase (adhE), and the pyruvate dehydrogenase complex (aceEF-lpd) was anaerobically expressed through promoter replacement. The resulting strain, E. coli EG03 (ΔfrdABCD ΔldhA ΔackA ΔpflB Δ adhE ΔpdhR ::pflBp6-aceEF-lpd ΔmgsA), could generate 4 NADH for every glucose oxidized to two acetyl-CoA through glycolysis and the pyruvate dehydrogenase complex. However, EG03 lost its ability for anaerobic growth due to the lack of NADH oxidation pathways. When the butanol pathway genes that encode for acetyl-CoA acetyltransferase (thiL), 3-hydroxybutyryl-CoA dehydrogenase (hbd), crotonase (crt), butyryl-CoA dehydrogenase (bcd, etfA, etfB), and butyraldehyde dehydrogenase (adheII) were cloned from Clostridium acetobutylicum ATCC 824, and expressed in E. coli EG03, a balanced NADH oxidation pathway was established for homobutanol fermentation (glucose => 4 NADH + 2 acetyl-CoA => butanol). This strain was able to convert glucose to butanol (1,254 mg l(-1)) under anaerobic condition.     

Evaluation of Genetic Manipulation Strategies on d-Lactate Production by Escherichia coli

In order to rationally manipulate the cellular metabolism of Escherichia coli for D: -lactate production, single-gene and multiple-gene deletions with mutations in acetate kinase (ackA), phosphotransacetylase (pta), phosphoenolpyruvate synthase (pps), pyruvate formate lyase (pflB), FAD-binding D-lactate dehydrogenase (dld), pyruvate oxidase (poxB), alcohol dehydrogenase (adhE), and fumarate reductase (frdA) were tested for their effects in two-phase fermentations (aerobic growth and oxygen-limited production). Lactate yield and productivity could be improved by single-gene deletions of ackA, pta, pflB, dld, poxB, and frdA in the wild type E. coli strain but were unfavorably affected by deletions of pps and adhE. However, fermentation experiments with multiple-gene mutant strains showed that deletion of pps in addition to ackA-pta deletions had no effect on lactate production, whereas the additional deletion of adhE in E. coli B0013-050 (ackA-pta pps pflB dld poxB) increased lactate yield. Deletion of all eight genes in E. coli B0013 to produce B0013-070 (ackA-pta pps pflB dld poxB adhE frdA) increased lactate yield and productivity by twofold and reduced yields of acetate, succinate, formate, and ethanol by 95, 89, 100, and 93%, respectively. When tested in a bioreactor, E. coli B0013-070 produced 125 g/l D-lactate with an increased oxygen-limited lactate productivity of 0.61 g/g h (2.1-fold greater than E. coli B0013). These kinetic properties of D-lactate production are among the highest reported and the results have revealed which genetic manipulations improved D-lactate production by E. coli.     

过量表达烟酸转磷酸核糖激酶对大肠杆菌NZN111产丁二酸的影响

大肠杆菌NZN111厌氧发酵的主要产物为丁二酸,是发酵生产丁二酸的潜力菌株。但是由于敲除了乳酸脱氢酶的编码基因 (ldhA) 和丙酮酸甲酸裂解酶的编码基因 (pflB),导致辅酶NADH/NAD+不平衡,厌氧条件下不能利用葡萄糖生长代谢。构建烟酸转磷酸核糖激酶的重组菌Escherichia coli NZN111/pTrc99a-pncB,在厌氧摇瓶发酵过程中通过添加0.5 mmol/L的烟酸、0.3 mmol/L的IPTG诱导后重组菌的烟酸转磷酸核糖激酶 (Nicotinic acid phosphor     

D-mannitol production by resting state whole cell biotrans-formation of D-fructose by heterologous mannitol and formate dehydrogenase gene expression in Bacillus megaterium

An in vivo system was developed for the biotransformation of D-fructose into D-mannitol by the expression of the gene mdh encoding mannitol dehydrogenase (MDH) from Leuconostoc pseudomesenteroides ATCC12291 in Bacillus megaterium. The NADH reduction equivalents necessary for MDH activity were regenerated via the oxidation of formate to carbon dioxide by coexpression of the gene fdh encoding Mycobacterium vaccae N10 formate dehydrogenase (FDH). High-level protein production of MDH in B. megaterium required the adaptation of the corresponding ribosome binding site. The fdh gene was adapted to B. megaterium codon usage via complete chemical gene synthesis. Recombinant B. megaterium produced up to 10.60 g/L D-mannitol at the shaking flask scale. Whole cell biotransformation in a fed-batch bioreactor increased D-mannitol concentration to 22.00 g/L at a specific productivity of 0.32 g D-mannitol (gram cell dry weight)(-1) h(-1) and a D-mannitol yield of 0.91 mol/mol. The nicotinamide adenine dinucleotide (NAD(H)) pool of the B. megaterium producing D-mannitol remained stable during biotransformation. Intra- and extracellular pH adjusted itself to a value of 6.5 and remained constant during the process. Data integration revealed that substrate uptake was the limiting factor of the overall biotransformation. The information obtained identified B. megaterium as a useful production host for D-mannitol using a resting cell biotransformation approach.     

Biotechnological production of mannitol and its applications

Mannitol, a naturally occurring polyol (sugar alcohol), is widely used in the food, pharmaceutical, medical, and chemical industries. The production of mannitol by fermentation has become attractive because of the problems associated with its production chemically. A number of homo- and heterofermentative lactic acid bacteria (LAB), yeasts, and filamentous fungi are known to produce mannitol. In particular, several heterofermentative LAB are excellent producers of mannitol from fructose. These bacteria convert fructose to mannitol with 100% yields from a mixture of glucose and fructose (1:2). Glucose is converted to lactic acid and acetic acid, and fructose is converted to mannitol. The enzyme responsible for conversion of fructose to mannitol is NADPH- or NADH-dependent mannitol dehydrogenase (MDH). Fructose can also be converted to mannitol by using MDH in the presence of the cofactor NADPH or NADH. A two enzyme system can be used for cofactor regeneration with simultaneous conversion of two substrates into two products. Mannitol at 180 g l⁻¹ can be crystallized out from the fermentation broth by cooling crystallization. This paper reviews progress to date in the production of mannitol by fermentation and using enzyme technology, downstream processing, and applications of mannitol.     

产顺,顺-粘康酸细胞工厂的构建与优化

顺,顺-粘康酸是重要的平台化学品。目前,生物合成顺,顺-粘康酸还缺乏高性能菌株,已报道的主要工程菌株不仅需要诱导表达,遗传不稳定,而且发酵培养基组分复杂,不利于大规模工业化生产。构建能利用简单无机盐培养基、遗传稳定且不需要诱导表达的新型工程菌受到人们的关注。本研究在实验室前期构建的产三脱氢莽草酸工程菌株WJ060中,整合合成顺,顺-粘康酸的3个外源基因(aro Z、aro Y、cat A),并且利用3个不同强度的组成型启动子进行组合调控,成功构建了27株顺,顺-粘康酸工程菌,得到的最优工程菌MA30的产量达到1.7 g/L。为了进一步提高顺,顺-粘康酸工程菌的生产能力,利用基因组复制工程构建突变体库,结合高通量筛选方法,经过两轮筛选,成功筛选到了顺,顺-粘康酸产量提高超过8%的大肠杆菌MA30-G2。利用5 L发酵罐进行分批补料发酵,MA30-G2的顺,顺-粘康酸产量达到了11.5 g/L。本研究采用组合调控和高通量筛选相结合的策略不仅促进了顺,顺-粘康酸的生物合成,同时也为其他生物基化学品的生物制造提供了重要参考。     

Purification and properties of Klebsiella aerogenes D-arabitol dehydrogenase.

An Escherichia coli K12 strain was constructed that synthesized elevated quantities of Klebsiella aerogenes D-arabitol dehydrogenase; the enzyme accounted for about 5% of the soluble protein in this strain. Some 280 mg of enzyme was purified from 180 g of cell paste. The purified enzyme was active as a monomer of 46,000 mol.wt. The amino acid composition and kinetic constants of the enzyme for D-arabitol and D-mannitol are reported. The apparent Km for D-mannitol was more than 3-fold that for D-arabitol, whereas the maximum velocities with both substrates were indistinguishable. The enzyme purified from the E. coli K12 construct was indistinguishable by the criteria of molecular weight, electrophoretic mobility in native polyacrylamide gel and D-mannitol/D-arabitol activity ratio from D-arabitol dehydrogenase synthesized in wild-type K. aerogenes. Purified D-arabitol dehydrogenase showed no immunological cross-reaction with K. aerogenes ribitol dehydrogenase. During electrophoresis in native polyacrylamide gels, oxidation by persulphate catalysed the formation of inactive polymeric forms of the enzyme. Dithiothreitol and pre-electrophoresis protected against this polymerization.     

敲除aceE基因对大肠杆菌生长和丙酮酸代谢的影响

大肠杆菌aceE基因是编码丙酮酸脱氢酶多酶复合体PdhR的关键酶之一。利用Red重组系统敲除大肠杆菌MG1655的aceE基因后,阻断了丙酮酸流向TCA循环,导致丙酮酸的累积,也使菌体生长受到影响,在培养基中补加5 g/L KAc后可以在一定程度上弥补菌株在生长上的缺陷。摇瓶发酵36 h,MG1655没有积累丙酮酸,MG1655ΔaceE∷cat菌株可以积累26.77 g/L丙酮酸,为利用大肠杆菌发酵生产丙酮酸奠定了基础。