大肠杆菌木糖生物合成琥珀酸的代谢工程研究

目的:对大肠杆菌进行代谢网络改造,考察木糖好氧发酵生产琥珀酸的可行性。方法:以有氧条件下大肠杆菌木糖生物合成琥珀酸的代谢途径分析为基础,以大肠杆菌BL21为出发菌株,通过P1噬菌体一步敲除法敲除琥珀酸脱氢酶基因(sdhA)、磷酸转乙酰基酶基因(pta)、丙酮酸脱氢酶基因(poxB)及异柠檬酸裂解酶阻遏物基因(iclR),构建木糖好氧发酵生产琥珀酸的大肠杆菌工程菌JLS400(△poxB△pta△iclR△sdhA)。将携带磷酸烯醇式丙酮酸羧化酶基因的质粒pJW225转化到JLS400中。结果:摇瓶发酵结果表明,构建的工程菌能以木糖为碳源,在好氧发酵条件下琥珀酸产率较高,副产物仅有少量乙酸和丙酮酸。结论:基因工程大肠杆菌JLS400pJW225的构建,为有氧条件下以木糖为原料生产琥珀酸的进一步研究奠定了基础。     

异源表达多巴脱羧酶促进大肠杆菌从头合成多巴胺

多巴胺是多种天然抗氧化药物生物合成的前体物质,在人体内作为神经递质调控中枢神经系统的多种生理功能,常用于多种类型休克的临床治疗。目前,通过微生物合成技术已经实现了多巴胺的从头合成,但是合成效率很低。针对该问题,在左旋多巴 (l-DOPA) 大肠杆菌工程菌基础上,利用不同拷贝数质粒表达野猪Sus scrofa来源的多巴脱羧酶基因Ssddc,实现了葡萄糖到多巴胺的生产。为了进一步提高多巴胺合成效率,从100个候选基因中筛选出5个多巴脱羧酶基因进行测试,其中来源于人Homo sapiens多巴脱羧酶基因Hsddc的工程菌摇瓶发酵的多巴胺产量最高,达到3.33 g/L;而来源于果蝇Drosophila melanogaster多巴脱羧酶基因Dmddc的工程菌摇瓶发酵的左旋多巴残余量最低,仅有0.02 g/L;这两株工程菌分批补料发酵表明,多巴胺的产量可以分别达到13.3 g/L和16.2 g/L,左旋多巴残余量分别是0.45 g/L和0.23 g/L。将多巴脱羧酶基因Dmddc和Ssddc分别整合到基因组上,获得遗传稳定的工程菌,在分批补料发酵条件下,多巴胺产量最高达到17.7 g/L,是目前国内外报道的最高产量。     

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。     

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%。     

好氧发酵生产琥珀酸工程菌株的构建

通过分析大肠杆菌的碳源代谢途径, 利用基因敲除手段, 以Escherichia coli MG1655为出发菌株, 成功构建了琥珀酸好氧发酵生产工程菌E. coli QZ1111 (MG1655?ptsG?poxB?pta?iclR?sdhA)。检测结果表明该菌株能以葡萄糖为碳源, 在好氧发酵且不表达任何异源基因的条件下大量积累琥珀酸。摇瓶试验证明, 琥珀酸发酵产量达到26.4 g/L, 乙酸盐作为唯一检测到的副产物产量为2.3 g/L。二者浓度比达到11.5:1。     

过表达羧化途径及失活苹果酸酶基因对大肠杆菌好氧发酵产苹果酸的影响

苹果酸是一种重要的C4二羧酸,在食品、医药、化工等领域有广泛的应用。本文主要研究羧化途径强化及苹果酸酶失活对大肠杆菌好氧发酵生产苹果酸的影响。首先在大肠杆菌E2中过表达了磷酸烯醇式丙酮酸羧化酶基因ppc,得到菌株E21,苹果酸积累量从0.57 g/L提高到3.83 g/L。随后,分别过表达来自谷氨酸棒杆菌的丙酮酸羧化酶基因pyc和来自琥珀酸放线杆菌的磷酸烯醇式丙酮酸激酶pck基因,相应的工程菌株E21(pTrcpyc)和E21(pTrc-A-pck)分别产6.04和5.01 g/L苹果酸,得率分别达到0.79和0.65 mol/mol葡萄糖。敲除E21中的苹果酸酶基因mae A和mae B,苹果酸产量也显著提高了36%,达到5.21 g/L,得率为0.62 mol/mol。然而,在过表达pyc的基础上敲除苹果酸酶基因并不能进一步提高苹果酸的产量。经过摇瓶发酵条件的初步优化,菌株E21(pTrcpyc)生产12.45 g/L苹果酸,得率为0.84 mol/mol,达到理论得率的63.2%。     

基因重组大肠杆菌表达HrpNEcc蛋白的发酵条件及诱导条件优化

对已构建好的表达HrpNEcc蛋白的工程菌BL21(DE3)/pET30a(+)hrpN Ecc的摇瓶发酵条件及乳糖诱导进行优化, 通过在7L发酵罐中放大发酵实验,以期提高蛋白产量并降低生产成本。在摇瓶中优化的发酵及诱导条件是：5% 的接种量,TB培养基,菌体培养至对数生长前期,添加3g/L外源诱导剂乳糖时,HrpNEcc蛋白产量可达417.60mg/L,比不添加乳糖时提高了36.73%,比用IPTG诱导时提高了16.85%。7L发酵罐中发酵,获得菌体湿重达到57.24g/L（WCW）,可溶性HrpNEcc蛋白产量占细胞总蛋白的50.2%,为3.29 g/L。     

重组大肠杆菌多基因串联表达合成反式-4-羟基-L-脯氨酸

[目的]得到表达多个基因的重组大肠杆菌,以期实现葡萄糖为碳源生产反式-4-羟基-L-脯氨酸。[方法]以菌液为模板,PCR得到不同来源的proB、proA、proC、p4h基因,重叠PCR串联相邻基因,所得片段通过无缝组装与p ET-28a载体连接,并在大肠杆菌BL21中表达,筛选阳性表达菌株,电泳及测序验证,重组菌在30 ml MCG培养基摇瓶中发酵,分光光度法和HPLC检测产量。[结果]0.5 mmol/L IPTG诱导24 h,5组串联基因成功在大肠杆菌中表达,并以葡萄糖为碳源,获得产物反式-4-羟基-L-脯氨酸,培养基不添加L-脯氨酸时E.coli BL21/p ET-28a-BAHHbs、E.coli BL21/p ET-28a-HBACkp和E.coli BL21/p ET-28a-HBAmg产量达到0.28 g/L、0.16 g/L和0.29 g/L,添加4 mmol/L的L-脯氨酸时,分别为0.64 g/L、0.55 g/L和0.74 g/L。[结论]proB、proA、proC及p4h基因成功在大肠杆菌中表达,5株重组菌在30℃摇瓶中诱导表达24 h得到产物反式-4-羟基-L-脯氨酸,其中E.coli BL21/p ET-28a-HBAmg产量达到0.74 g/L,为今后在发酵罐中生产奠定基础。     

重组大肠杆菌产Streptomyces sp. FA1来源木聚糖酶的摇瓶发酵优化

为了实现来源于Streptomyces sp. FA1的木聚糖酶的高效胞外分泌表达,对E.coli BL21(DE3)/pET20b(+)/coe/xynA基因工程菌的发酵产酶诱导条件进行优化,获得最优的诱导条件为25 ℃发酵6 h后添加终浓度为0.4 mmol/L的IPTG。在此基础上对发酵培养基进一步优化,得到最优培养基成分为:甘油11 g/L,酵母粉24 g/L,蛋白胨8 g/L,磷酸盐浓度89 mmol/L,镁离子4 mmol/L。最终酶活达到780.2 U/ml,为未优化前的2.2倍,是目前大肠杆菌摇瓶发酵产木聚糖酶的最高表达水平,为实现该酶的工业化生产奠定基础。     

组合代谢调控提高大肠杆菌对氨基苯甲酸产量

对氨基苯甲酸是一种重要的有机合成中间体,广泛应用于医药、染料等行业。近年来对氨基苯甲酸作为一种潜在的高强度共聚物单体越来越受到重视。对氨基苯甲酸作为叶酸合成的前体之一,其合成在大肠杆菌体内由叶酸合成途径的pabA、pabB和pabC三个基因负责,催化分支酸合成对氨基苯甲酸。本研究以实验室构建的酪氨酸高产工程菌TYR002作为出发菌株,首先弱化双功能分支酸突变酶/预苯酸脱氢酶TyrA的表达,以减少酪氨酸积累,然后利用3种不同强度的组成型启动子分别调控pabA、pabB和pabC的表达。摇瓶发酵表明不同的组合调控模式下大肠杆菌发酵培养基中的对氨基苯甲酸积累量存在显著差异,最高可获得0.67 g/L的摇瓶发酵产量。进一步通过发酵条件优化和分批补料发酵,在5L发酵罐中获得了6.4g/L的对氨基苯甲酸产量。本研究为改善对氨基苯甲酸生物合成效率提供了重要理论参考。     

Kojic acid production byAspergillus flavus using gelatinized and hydrolyzed sago starch as carbon sources

Direct conversion of gelatinized sago starch into kojic acid byAspergillus flavus strain having amylolytic enzymes was carried out at two different scales of submerged batch fermentation in a 250-mL shake flask and in a 50-L stirred-tank fermentor. For comparison, fermentations were also carried out using glucose and glucose hydrolyzate from enzymic hydrolysis of sago starch as carbon sources. During kojic acid fermentation of starch, starch was first hydrolyzed to glucose by the action of α-amylase and glucoamylase during active growth phase. The glucose remaining during the production phase (non-growing phase) was then converted to kojic acid. Kojic acid production (23.5g/L) using 100 g/L sago starch in a shake flask was comparable to fermentation of glucose (31.5 g/L) and glucose hydrolyzate (27.9 g/L) but in the 50-L fermentor was greatly reduced due to non-optimal aeration conditions. Kojic acid production using glucose was higher in the 50-L fermentor than in the shake flask.     

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.     

高效合成葡萄糖二酸酿酒酵母工程菌的构建

葡萄糖二酸是天然存在的一种重要二元酸,其在医疗保健和化工工业等领域具有很高的实际应用价值,因此被称为“最具价值的生物炼制产品之一”。以酿酒酵母(Saccharomyces cerevisiae)为底盘微生物,文中考察了过量表达肌醇转运蛋白Itr1、融合表达肌醇加氧酶和葡萄糖醛酸脱氢酶以及弱化表达葡萄糖6-磷酸脱氢酶基因ZWF1三种策略对葡萄糖二酸产量的影响。研究结果显示,过量表达肌醇转运蛋白Itr1使葡萄糖二酸产量在摇瓶发酵条件下较出发菌株Bga-3提高了26%;MIOX4-Udh融合蛋白的表达使葡萄糖二酸的产量较Bga-3菌株提高了40%;在此基础上,弱化表达葡萄糖6-磷酸脱氢酶基因ZWF1后,葡萄糖二酸的产量达5.5 g/L,较相同发酵条件下Bga-3菌株提高了60%。在5 L发酵罐中,该菌株葡萄糖二酸的最高产量达10.85 g/L,较Bga-3菌株提高了80%。由此可见,上述代谢改造策略的应用在很大程度上提高了葡萄糖二酸的途径效率和产量,为通过代谢工程方法在酿酒酵母中合成其他化合物的研究提供了参考。     

代谢工程改造大肠杆菌合成己二酸

己二酸是一种具有重要应用价值的二元羧酸,是合成尼龙-66的关键前体。目前,生物法生产己二酸存在生产周期长、生产效率低的问题。本研究选择一株野生型高产琥珀酸菌株大肠杆菌(Escherichia coli) FMME N-2为底盘细胞,首先通过引入逆己二酸降解途径的关键酶,成功构建了可合成0.34 g/L己二酸的E. coli JL00菌株;接着,对合成路径限速酶进行表达优化,使E. coli JL01菌株在摇瓶发酵条件下产量达到0.87 g/L;随后,通过敲除sucD基因、过表达acs基因和突变lpd基因的组合策略平衡己二酸合成前体的供应,优化菌株E. coli JL12己二酸产量进一步提升至1.51 g/L;最后,在5 L发酵罐上对己二酸发酵工艺进行优化。工程菌株经72 h分批补料发酵,己二酸的产量达到22.3 g/L,转化率为0.25 g/g,生产强度为0.31 g/(L·h),具备了一定的应用潜力。本研究可为包括己二酸在内的多种二元羧酸细胞工厂的构建提供理论依据和技术基础。     

Production of γ-aminobutyric acid in Escherichia coli by engineering MSG pathway

Abstract

The compound γ-aminobutyric acid (GABA) has many important physiological functions. The effect of glutamate decarboxylases and the glutamate/GABA antiporter on GABA production was investigated in Escherichia coli. Three genes, gadA, gadB, and gadC were cloned and ligated alone or in combination into the plasmid pET32a. The constructed plasmids were transformed into Escherichia coli BL21(DE3). Three strains, E. coli BL21(DE3)/pET32a-gadA, E. coli BL21(DE3)/pET32a-gadAB and E. coli BL21(DE3)/pET32a-gadABC were selected and identified. The respective titers of GABA from the three strains grown in shake flasks were 1.25, 2.31, and 3.98?g/L. The optimal titer of the substrate and the optimal pH for GABA production were 40?g/L and 4.2, respectively. The highest titer of GABA was 23.6?g/L at 36?h in batch fermentation and was 31.3?g/L at 57?h in fed-batch fermentation. This study lays a foundation for the development and use of GABA.     

Production of chum salmon cystatin from the recombinant <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> optimized using response surface methodology

Chum salmon cystatin was overexpressed on Saccharomyces cerevisiae YPH 499. At first, the culture condition for the production of recombinant chum salmon cystatin (RC) by S. cerevisiae YPH 499 was optimized in a shake flask using response surface methodology. Three independent variables; medium pH, inducing time, and the amount of inducing assistant, were analyzed to get the optimal condition for the production of RC. The results were fitted to a second-order polynomial equation, in which the determination coefficient (R ²) was 0.904. The highest RC production in a shake flask, 0.57 U/mL was obtained at 5.7 of medium pH, 6.7 h of inducing time, and 5.6 g/L of inducing assistant. Based on the results of shake flask, the effects of agitation and aeration rates on the production of RC by S. cerevisiae YPH 499 were determined for scaleup in a fermentor. The highest production of RC in a fermentor, 0.56 U/mL was obtained at 350 rpm of agitation rate and 1.0 vvm of aeration rate. RC at 100 μg/g showed the highest inhibitory activity against the autolysis of Alaska pollock surimi based on the analysis of TCA-soluble peptides.     

保加利亚乳杆菌ATCC11842 L-乳酸脱氢酶同工酶基因的克隆与表达分析

通过对保加利亚乳杆菌（Lactobacillus delbrueckii subsp.bulgaricus）L-乳酸脱氢酶（L-lactate dehydrogenase,L-LDH）同工酶基因的异源表达、酶活测定和摇瓶发酵研究L-LDH在乳酸合成中的作用。将保加利亚乳杆菌ATCC11842中L-乳酸脱氢酶基因ldb0120和ldb0094分别克隆至载体pET28a(+)中,构建重组表达载体pET28aldb0120和pET28aldb0094,并转化到大肠埃希菌（Escherichia coli） BL21(DE3)中进行表达。进一步对重组蛋白进行Ni-NTA柱亲和层析和酶学活性测定,结果显示,LDB0120和LDB0094的比活力分别为0 和25 U/mg,表明LDB0094是具有低活性的L-乳酸脱氢酶,而LDB0120不具有活性。对两株重组菌分别进行好氧和微好氧发酵,重组菌E.coli BL21/pET28aldb0094在好氧和微好氧条件可以合成L-乳酸,浓度分别为41.9和227.9 mg/L,而菌株E.coli BL21/pET28aldb0120在两种培养条件下均基本不合成L-乳酸,推测保加利亚乳杆菌中L-乳酸脱氢酶LDB0094为催化L-乳酸合成的关键酶。首次对保加利亚乳杆菌的L-乳酸脱氢酶同工酶基因进行研究,通过基因异源表达、蛋白纯化、酶活测定和摇瓶发酵,揭示Ldb0094酶为保加利亚乳杆菌ATCC11842中催化L-乳酸合成的关键酶。     

Production of succinate by a <Emphasis Type="Italic">pfl</Emphasis>B <Emphasis Type="Italic">ldh</Emphasis>A double mutant of <Emphasis Type="Italic">Escherichia coli</Emphasis> overexpressing malate dehydrogenase

The gene encoding malate dehydrogenase (MDH) was overexpressed in a pflB ldhA double mutant of Escherichia coli, NZN111, for succinic acid production. With MDH overexpression, NZN111/pTrc99A-mdh restored the ability to metabolize glucose anaerobically and 0.55 g/L of succinic acid was produced from 3 g/L of glucose in shake flask culture. When supplied with 10 g/L of sodium bicarbonate (NaHCO₃), the succinic acid yield of NZN111/pTrc99A-mdh reached 1.14 mol/mol glucose. Supply of NaHCO₃ also improved succinic acid production by the control strain, NZN111/pTrc99A. Measurement of key enzymes activities revealed that phosphoenolpyruvate (PEP) carboxykinase and PEP carboxylase in addition to MDH played important roles. Two-stage culture of NZN111/pTrc99A-mdh was carried out in a 5-L bioreactor and 12.2 g/L of succinic acid were produced from 15.6 g/L of glucose. Fed-batch culture was also performed, and the succinic acid concentration reached 31.9 g/L with a yield of 1.19 mol/mol glucose.     

Optimization of cellulase production in batch fermentation byTrichoderma reesei

Maximum cellulase production was sought by comparing the activities of the cellulases produced by differentTrichoderma reesei strains andAspergillus niger. Trichoderma reesei Rut-C30 showed higher cellulase activity than otherTrichoderma reesei strains andAspergillus niger that was isolated from soil. By optimizing the cultivation condition during shake flask culture, higher cellulase production could be achieved. The FP (filter paper) activity of 3.7 U/ml and CMCase (Carboxymethylcellulase) activity of 60 U/ml were obtained from shake flask culture. When it was grown in 2.5L fermentor, where pH and DO levels are controlled, the Enzyme activities were 133.35 U/ml (CMCase) and 11.67 U./ml (FP), respectively. Ammonium sulfate precipitation method was used to recover enzymes from fermentation broth. The dried cellulase powder showed 3074.9 U/g of CMCase activity and 166.7 U/g of FP activity with 83.5% CMCase recovery.     

CRISPR/Cas9编辑大肠杆菌工程菌生产氨基葡萄糖

【背景】氨基葡萄糖(glucosamine, GlcN)及其衍生物N-乙酰氨基葡萄糖(N-acetylglucosamine,GlcNAc)是合成糖胺聚糖的重要前体物质,在医药、化妆品和保健品领域具有广泛的应用价值。传统的生产方式存在诸多弊端,如环境污染、原料限制、不适于海鲜易过敏人群等问题,因此利用微生物发酵法生产GlcN和GlcNAc越来越受到青睐。【目的】利用微生物发酵生产并提高N-乙酰氨基葡萄糖的产量,探索分子改造及发酵条件优化策略。【方法】以大肠杆菌MG1655为出发菌株,首先利用表达载体共表达大肠杆菌来源的glmS和酿酒酵母来源的gna1,构建GlcNAc的生物合成路径,然后利用CRISPR/Cas9技术敲除GlcNAc的分解代谢与转运途径,以提高GlcNAc的产量,最后结合发酵条件优化使GlcNAc的产量得到进一步提升。【结果】通过分子改造得到一株产GlcNAc菌株RY-5,发酵20 h后GlcNAc的产量达到了2.36 g/L,相较于初始构建的菌株RY-1提高了29倍,进一步对装液量和诱导剂IPTG的添加时间等条件进行发酵优化,GlcNAc产量达到了7.74g/L,与优...