产1,3-丙二醇新型重组大肠杆菌的构建

利用PCR技术从大肠杆菌(Escherichia coli )中扩增出1.16 kb的编码1,3-丙二醇氧化还原酶同工酶的基因yqhD,将其连接到表达载体pEtac,得到重组载体pEtac-yqhD,重组载体在大肠杆菌JM109中得到高效表达。SDS_PAGE分析显示融合表达产物的分子量均为43 kD,同核酸序列测定所推导的值相符。对含有yqh-D的基因工程菌进行表达研究表明：37 ℃,以1.0 mmol /L IPTG诱导4 h,1,3-丙二醇氧化还原酶同工酶的酶活力达到120 u/mg蛋白,而对照菌株的酶活力为0.5 u/mg蛋白。再将含甘油脱水酶基因dhaB和含1,3-丙二醇氧化还原酶同工酶基因yqhD的重组质粒共转化大肠杆菌JM109得到重组大肠杆菌JM109（pUCtac-dhaB, pEtac-yqhD）,该菌株在好氧条件下,以1.0mmol/L IPTG诱导可将50 g/L甘油转化为38.0 g/L 1,3-丙二醇。首次发现1,3-丙二醇氧化还原酶同工酶在好氧条件下表现出较高的活性。     

含甘油脱水酶激活因子编码基因的产1,3-丙二醇新型重组菌的构建

利用PCR技术扩增来源于弗氏柠檬杆菌(Citrobacter freundii)的甘油脱水酶编码基因dhaB以及甘油脱水酶激活因子编码基因dhaGdhaF,将其与1,3-丙二醇氧化还原酶同工酶的编码基因yqhD串联在温控表达载体pHsh上,构建重组菌E.coliJM109(pHsh-dhaB-dhaG-dhaF-yqhD)。SDS-PAGE分析显示,融合表达产物的分子量同核酸序列测定的推导值相符。与未串联甘油脱水酶激活因子编码基因的重组菌E.coliJM109(pHsh-dhaB-yqhD)相比,1,3-丙二醇的产量提高了28%。     

生物法生产1，3-丙二醇

生物炼制技术（biorefmery technology）或白色生物技术（white biotechnology）近几年受石油价格不断攀升的影响而越发受到人们的关注,尤其是生物质能源和生物基大宗化学品,如燃料乙醇、生物柴油、沼气、生物氢气以及1,3-丙二醇、2,3-丁二醇、乳酸、琥珀酸、丁醇／丙酮等。2006年原油价格由40美元／桶上升至70余美元／桶．最高达到75美元／桶：     

生物法生产1，3-丙二醇

生物炼制技术（biorefmery technology）或白色生物技术（white biotechnology）近几年受石油价格不断攀升的影响而越发受到人们的关注,尤其是生物质能源和生物基大宗化学品,如燃料乙醇、生物柴油、沼气、生物氢气以及1,3-丙二醇、2,3-丁二醇、乳酸、琥珀酸、丁醇／丙酮等。2006年原油价格由40美元／桶上升至70余美元／桶．最高达到75美元／桶：     

利用甘油发酵耦联生产3-羟基丙酸及1,3-丙二醇重组菌的构建及筛选

在肺炎克雷伯杆菌(Klebsiella pneumoniae)代谢甘油生产1,3-丙二醇(1,3-PD)的过程中,为了减少有毒中间产物3-羟基丙醛(3-HPA)的积累,可将其转化为3-羟基丙酸(3-HP),从而实现1,3-丙二醇和3-羟基丙酸的联产。克隆来自于酿酒酵母的NAD+依赖型的乙醛脱氢酶(ALDH)的基因aldh4,构建了表达载体pKP-aldh,转化K.pneumoniae,得到了有效表达乙醛脱氢酶的重组肺炎克雷伯杆菌(K.pneumoniae A+)。在此基础上,使用紫外诱变联合菌种驯化的方法对K.pneumoniae A+进行筛选,获得了可耐受较高3-HP浓度(≥35 g/L)的重组肺炎克雷伯杆菌K.pneumoniae A+5-3。发酵实验结果表明,K.pneumoniae A+5-3可将3-HPA转化为3-HP,能够同时利用甘油耦联生产3-HP和1,3-PD,产量分别达到5.0 g/L和74.5 g/L。     

一步法产1,3-丙二醇酿酒酵母基因工程菌的构建

1,3-丙二醇(1,3-PD)是一种重要的化工原料,发酵法生产1,3-PD是一条新颖且具有潜在竞争力的生产途径。本研究在前期工作的基础上,将分别来源于大肠杆菌和肺炎克雷伯氏菌的基因片段yqhD和dhaB串联表达,构建重组表达载体pYX212-zeocin-pGAP-yqhD-pGAP-dhaB;并得到重组酿酒酵母(Saccharomyces cerevisiae)W303-1A/pYX212-zeocin-pGAP-yqhD-pGAP-dhaB。该重组菌和对照S.cerevisiae分别以葡萄糖为底物摇瓶发酵72h后,重组酿酒酵母发酵液中1,3-PD含量约为1.5g/L;而对照菌株不产1,3-PD。以上结果表明本研究在国内首次成功构建了直接以葡萄糖为底物发酵生产1,3-PD的酿酒酵母基因工程菌。为进一步将dhaB、yqhD基因导入其他以葡萄糖为底物高产甘油的酵母宿主中表达,获得以葡萄糖为底物一步法发酵高产1,3-丙二醇工程菌打下了坚实的基础。     

两步发酵过程中有机酸对产1，3-丙二醇的影响

考察了基因工程菌发酵生产1.3 丙二醇过程中,有机酸对发酵过程的影响,并选用了不同的离子交换树脂对甘油发酵液进行处理。发现有机酸、特别是乳酸对1.3丙二醇生产的抑制作用最明显。在使用离子交换树脂处理有机酸的过程中,确定了使用005号离子交换树脂处理效果最好,005号离子交换树脂可除去大部分的有机酸,处理后的发酵液发酵产1.3丙二醇产量比未处理的发酵液产量提高166%,转化率提高34%。     

产3-羟基丙酸重组菌的构建及其转化甘油的研究

将连接编码甘油脱水酶的基因重组质粒pEtac-dhaB和连接编码乙醛脱氢酶编码基因aldh的重组质粒pUCtac共转化大肠杆菌,得到产3-羟基丙酸重组大肠杆菌JM109(pUCtac-aldh,pEtac-dhaB),并对影响该重组菌发酵的营养因子进行研究.试验结果表明:该重组菌转化甘油合成3-羟基丙酸的适宜培养基组成为甘油40 g/L、酵母膏6 g/L、维生素B12 0.02 g/L以及KH2PO4 7.5 g/L; 3-羟基丙酸产量和转化率分别达到4.92 g/L和12.3 %.     

克雷伯氏菌产1,3-丙二醇ldhA基因缺失菌株的构建

克雷伯氏菌(Klebsiella pneumonia)甘油歧化发酵生产1,3-丙二醇(1,3-PD)的过程中,乳酸是氧化途径最主要的副产物,乳酸的产生和积累,不仅限制了菌体本身的生长,而且严重影响了1,3-丙二醇的转化率。利用λRed重组技术对Klebsiella pneumonia中的酶乳酸脱氢酶基因(ldhA)进行改造。在λRed重组系统作用下,将带有300 bp的线性同源片段ldhA1-Cm-ldh A2与基因组DNA的同源重组,经过抗性筛选和PCR鉴定最终获得了ldhA基因缺失菌株K.pneumonia2-1ΔldhA。经过24 h发酵可知,乳酸最大产出浓度由原来的10.16 g/L降为0.49 g/L,1,3-PD由原来的78.83 g/L增长为85.76 g/L,甘油转化率由60.64%增长到65.97%,提高了5.33%。     

利用PDOR同工酶基因yqhD对产1,3-丙二醇克雷伯氏杆菌进行基因工程改造

由于Klebsiella pneumoniae 1,3-丙二醇合成途径中,加强甘油脱水酶基因表达,导致因NADH供应不足使3-羟基丙醛累积,并对菌体生长及1,3-丙二醇合成造成负面影响。为改善Klebsiella pneumoniae 1,3-丙二醇合成途径,本文利用PCR技术从大肠杆菌(Escherichia coli)中扩增出以NADPH 为辅酶的1,3-丙二醇氧化还原酶同工酶编码基因yqhD,从克雷伯氏杆菌中扩增出2.66kb的甘油脱水酶基因（dhaB）,构建了产1,3-丙二醇关键酶基因的串联载体pEtac-dhaB-tac-yqhD,并将其转入到野生克雷伯氏杆菌(Klebsiella pneumoniae)中,重组载体得到了表达。通过初步发酵,重组后的克雷伯氏杆菌产量比原始菌高20%左右,副产物中乙酸和丁二醇分别下降30%左右。     

Disruption of glpF gene encoding the glycerol facilitator improves 1,3-propanediol production from glucose via glycerol in Escherichia coli

Engineered Escherichia coli has recently been applied to produce 1,3-propanediol (1,3-PDO) from glucose. A metabolic intermediate in the production pathway, glycerol, is partially secreted into the extracellular of E. coli through a glycerol facilitator encoded by glpF, and this secretion consequently decreases 1,3-PDO production. Therefore, we aimed to determine whether disrupting the glpF gene would improve 1,3-PDO production in E. coli. The intracellular glycerol concentration in a glpF-disruptant was 7·5 times higher than in a non-disruptant. The glpF-disrupted and non-disrupted E. coli strains produced 0·26 and 0·09 g l⁻¹ of 1,3-PDO, respectively, from 1% glucose after 72 h of cultivation. The specific growth rate (μ) and the 1,3-PDO yield from glucose (Y_P/S) in the disruptant were higher than those in the non-disruptant (ΔglpF, μ = 0·08 ± 0·00 h⁻¹, Y_P/S = 0·06 mol mol-glucose⁻¹; BW25113, μ = 0·06 ± 0·00 h⁻¹, Y_P/S = 0·02 mol mol-glucose⁻¹). Disruption of the glpF gene decreased the production of the by-product, acetic acid. These results indicated that disruption of glpF increased the intracellular concentration of glycerol and consequently increased 1,3-PDO production in E. coli.     

High-level production of 3-hydroxypropionic acid from glycerol as a sole carbon source using metabolically engineered Escherichia coli

As climate change is an important environmental issue, the conventional petrochemical-based processes to produce valuable chemicals are being shifted toward eco-friendly biological-based processes. In this study, 3-hydroxypropionic acid (3-HP), an industrially important three carbon (C3) chemical, was overproduced by metabolically engineered Escherichia coli using glycerol as a sole carbon source. As the first step to construct a glycerol-dependent 3-HP biosynthetic pathway, the dhaB1234 and gdrAB genes from Klebsiella pneumoniae encoding glycerol dehydratase and glycerol reactivase, respectively, were introduced into E. coli to convert glycerol into 3-hydroxypropionaldehyde (3-HPA). In addition, the ydcW gene from K. pneumoniae encoding γ-aminobutyraldehyde dehydrogenase, among five aldehyde dehydrogenases examined, was selected to further convert 3-HPA to 3-HP. Increasing the expression level of the ydcW gene enhanced 3-HP production titer and reduced 1,3-propanediol production. To enhance 3-HP production, fed-batch fermentation conditions were optimized by controlling dissolved oxygen (DO) level and employing different feeding strategies including intermittent feeding, pH-stat feeding, and continuous feeding strategies. Fed-batch culture of the final engineered E. coli strain with DO control and continuous feeding strategy produced 76.2 g/L of 3-HP with the yield and productivity of 0.457 g/g glycerol and 1.89 g·L⁻¹·h⁻¹, respectively. To the best of our knowledge, this is the highest 3-HP productivity achieved by any microorganism reported to date.     

重组大肠杆菌的高密度发酵和甘油生产条件的初步研究

在摇瓶中进行重组大肠杆菌菌株BL21高密度发酵条件的研究,考察了葡萄糖浓度、盐离子浓度、温度、接种量、发酵时间等对该菌株生产甘油的影响。初步确定底物浓度为2.5%,盐离子浓度0.2%,温度为37℃,接种量为2%,经24h的摇瓶发酵,甘油产量最高达6.8g/L。在30L发酵罐实验中、按初步确定的优化条件发酵26h,甘油产量可达46.67g/L,是LB/葡萄糖培养基中甘油产量的2.06倍。     

重组大肠杆菌右旋糖酐蔗糖酶的纯化及其性质

[目的]研究工程菌E.coli BL21(DE3)/pET28-dexYG产右旋糖酐蔗糖酶的纯化和酶学性质.[方法]工程菌经过IPTG诱导后生产含His-tag融合蛋白的右旋糖酐蔗糖酶,通过硫酸铵沉淀、Ni-NTA亲和层析纯化,得到纯度较高的酶蛋白,并对纯酶进行了酶学性质及动力学研究.[结果]经过SDS-PAGE测得该酶的分子量约为170 kDa,与理论推测值基本相同.以蔗糖为底物,酶促反应的最适温度为25～30℃,最适pH值为5.4,动力学常数Km值为10.43 mmol/L;酶活在pH 5.0～8.0较为稳定,在室温(25 ℃)保藏4天仍有59%的酶活力,4℃保存7周酶活力仅下降一半,但在35℃以上失活很快;Ca2 对催化作用有较大的促进,Mg2 有微弱的促进作用,K 对催化反应无影响,Cu2 的抑制作用最强.其他试剂对重组酶的活性有不同程度的影响,其中SDS抑制作用很强.[结论]研究为重组右旋糖酐蔗糖酶纯酶的获取、得到稳定性好、活性高的酶反应体系及利用该酶进行催化反应和工业化应用提供了重要参数.     

产1,3-丙二醇基因工程菌发酵条件的研究

利用途径工程的方法,将来源于克雷伯氏菌(Klebsiella pneumoniae)的甘油脱水酶基因dhaB和1,3-丙二醇氧化还原酶基因dhaT构建成多顺反子重组质粒pSE-dhaB-dhaT并在大肠杆菌JM 109中进行表达,在大肠杆菌中构建一条新的产1,3-丙二醇代谢途径。研究表明,重组菌株JM 109/pSE-dhaB-dhaT在微好氧条件下,尝试用廉价的乳糖为诱导物、维生素B12为辅酶,可以将甘油转化为1,3-丙二醇,产量达15.34 g/L,甘油转化率为35.7%,对低成本生产1,3-丙二醇作了有益的探索。     

克雷伯杆菌产1,3-丙二醇关键酶甘油脱水酶的酶活分析方法研究

有氧条件下,建立了克雷伯杆菌破碎方法及其生产1,3-丙二醇代谢途径中关键酶甘油脱水酶的酶活测定方法。甘油脱水酶酶活测定时在超声时间25min,功率为300w的条件下最适破碎频率为破碎时间1s,停息时间4s;甘油脱水酶酶活测定所用磷酸盐缓冲液的最适浓度为0.045mol/L,最适pH值7.2。甘油脱水酶酶活测定反应的最佳温度为37℃,甘油脱水酶酶活测定反应液的最佳吸收波长为290nm。     

碳源对重组大肠杆菌发酵生产GLP-1融合蛋白的影响

以一株表达人胰高血糖素样肽-1融合蛋白的重组大肠杆菌为研究对象,首先通过摇瓶实验对碳源种类进行了初步选择,发现葡萄糖和甘油对菌体生长以及GLP-1融合蛋白表达较为适宜。进一步在5 L反应器上对初始葡萄糖及甘油浓度进行了考察,发现高浓度碳源有利于菌体生长却抑制GLP-1融合蛋白表达,但能提高GLP-1融合蛋白的体积得率。在0.25%初始葡萄糖或甘油存在的条件下,在培养过程中流加葡萄糖或甘油维持其在发酵液中的浓度,比较了两者对菌体生长以及GLP-1融合蛋白表达的影响,结果发现,以甘油为碳源时,菌体生长以及GLP-1融合蛋白的表达量均高于以葡萄糖为碳源的结果,最终发酵液的菌浓(OD_(600))可达到25.4,较葡萄糖为碳源时19.1提高了33.0%,GLP-1融合蛋白表达水平和体积得率分别可达到22.4%和1.051 g/L,较葡萄糖为碳源的15.8%和0.504 g/L分别提高41.8%和108.5%。该结果对GLP-1融合蛋白表达菌株发酵条件的进一步优化提供了依据。     

Characterization of up-regulated proteases in an industrial recombinant Escherichia coli fermentation

Proteolytic degradation of recombinant proteins is an industry-wide challenge in host organisms such as Escherichia coli. These proteases have been linked to stresses, such as the stringent and heat-shock responses. This study reports the dramatic up-regulation of protease activity in an industrial recombinant E. coli fermentation upon induction. The objective of this project was to detect and characterize up-regulated proteases due to recombinant AXOKINE overexpression upon IPTG induction. AXOKINE is a 22-kDa protein currently in clinical trials as a therapeutic for obesity associated with diabetes. AXOKINE was expressed in both the soluble and inclusion body fractions in E. coli. Sodium dodecyl sulfate gelatin-polyacrylamide gel electrophoresis (SDS-GPAGE) was used to analyze the up-regulated protease activity. Western blot analysis showed degraded AXOKINE in both the soluble and insoluble fractions. Protease inhibitors were used to characterize the proteases. The proteases were ethylenediaminetetraacetic acid (EDTA) sensitive. The protease activity increased in the presence of phenyl-methyl sulfonyl-fluoride (PMSF), a serine protease inhibitor. The incubation buffer composition was varied with respect to Mg2+ and ATP, and the protease activity was ATP independent and Mg2+ dependent. A two-dimensional electrophoresis technique was used to estimate the pI of the proteases to be between 2.9 and 4.0.     

High-level expression of the 1,3-propanediol oxidoreductase from klebsiella pneumoniae in escherichia coli

As one of four key enzymes in glycerol dismutation process, 1,3-propanediol oxidoreductase (EC.1.1.1.202) is important in converting glycerol to 1,3-propanediol in Klebsiella pneumoniae. The dhaT gene encoding 1,3-propanediol oxidoreductase was amplified by polymerase chain reaction (PCR) using the genome DNA of K. pneumoniae as template, and then cloned into cloning vector pMD18-T. After DNA sequence was determined, the dhaT gene was subcloned into Escherichia coli expression vector pET-22b (+) and pET-28a (+). Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) analysis revealed that both the recombinant E. coli BL21 (DE3) (pET-22b (+)-dhaT) and E. coli BL21(DE3)(pET-28a (+)-dhaT) expressed predicted 42-kDa 1,3-propanediol oxidoreductase after induced by isopropyl-β-d-thiogalactopyranoside (IPTG), and the recombinant enzyme of E. coli BL21 (DE3) (pET-28a (+)-dhaT) was mostly in soluble form, and exhibited high activity (96.8 U/mL culture). The recombinant enzyme was purified and biochemically characterized. The apparent K _m values of the enzyme for 1,3-propanediol and NAD⁺ were 8.5 and 0.21 mM, respectively. The enzyme had maximum activity at pH 9.5 and 30°C.