谷氨酸棒杆菌代谢工程高效生产L-缬氨酸北大核心CSCD

L-缬氨酸作为一种支链氨基酸,广泛应用于医药和饲料等领域。本研究借助多种代谢工程策略相结合的方法,构建了生产L-缬氨酸的微生物细胞工厂,实现了L-缬氨酸的高效生产。首先,通过增强糖酵解途径、减弱副产物代谢途径相结合的方式,强化了L-缬氨酸合成前体丙酮酸的供给;其次,针对L-缬氨酸合成路径关键酶—乙酰羟酸合酶进行定点突变,提高了菌株的抗反馈抑制能力,并利用启动子工程策略,优化了路径关键酶的基因表达水平;最后,利用辅因子工程策略,改变了乙酰羟酸还原异构酶和支链氨基酸转氨酶的辅因子偏好性,由偏好NADPH转变为偏好NADH,从而提高了L-缬氨酸的合成能力。在5L发酵罐中,最优谷氨酸棒杆菌工程菌株Corynebacterium glutamicum K020的L-缬氨酸产量、得率和生产强度分别达到了110g/L、0.51g/g和2.29 g/(L·h)。     

Pgk和ilvN基因对谷氨酸棒杆菌产L-丝氨酸的影响

为增加谷氨酸棒杆菌A36的L-丝氨酸合成途径的碳流,首先过表达磷酸甘油酸激酶(pgk),以增加前体物质3-磷酸甘油酸的积累,但经发酵分析发现其对菌株A36的L-丝氨酸产量无显著影响。进一步敲除副产物L-缬氨酸合成途径的乙酰羟酸合酶(AHAS)基因ilvN,敲除该基因后L-缬氨酸只有微量积累,但重组菌并未形成营养缺陷型菌株,L-丝氨酸的产量反而下降,分析发现L-缬氨酸的存在在一定程度上有助于L-丝氨酸的生成。在培养基中分别添加不同质量浓度的L-缬氨酸,在L-缬氨酸添加量为750 mg/L时,重组菌L-丝氨酸产量达到34.19 g/L,糖酸转化率为0.34 g/g,生产强度为0.28 g/(L·h),相比出发菌株A36分别提高了11.8%、13.3%和12.0%。     

谷氨酸棒杆菌metX、dapA基因敲除对苏氨酸合成的影响

谷氨酸棒杆菌中metX基因编码蛋氨酸合成途径关键酶高丝氨酸乙酰转移酶,dapA基因编码赖氨酸合成途径关键酶二氢吡啶二羧酸合成酶。为研究这两个基因缺失对苏氨酸积累的影响,以谷氨酸棒杆菌R102(AHVr)为出发菌株,通过重叠延伸PCR及同源重组技术分别构建了metX、dapA单基因缺失突变株R102ΔmetX、R102ΔdapA以及双基因缺失的突变株R102ΔmetXΔdapA。对出发菌以及上述3株重组菌进行初步摇瓶发酵试验,用HPLC法测定发酵液中苏氨酸含量。结果表明,发酵72 h后,3株重组菌的苏氨酸产量分别为2.58、2.38和3.01 g/L,比原始菌株分别提高了42.5%、31.5%和66.3%。     

lysC定点突变及lysC、asdA串联表达对谷氨酸棒杆菌L-苏氨酸积累的影响

lysC、asdA基因分别编码的天冬氨酸激酶(Aspartate kinase,AK)和天冬氨酸半醛脱氢酶(Aspartate semi-aldehyde dehydrogenase,ASD)是L-苏氨酸合成途径中两个关键限速酶基因,其中AK受到代谢产物赖氨酸与苏氨酸的协同抑制。以选育获得的一株谷氨酸棒状杆菌T11(Corynebacterium glutamicum T11)为出发菌株,通过构建lysC-asdA串联表达盒,并对其关键限速酶基因lysC进行定点突变,突变位点为Ala279Thr,获得抗反馈抑制突变型编码基因lysCr-asdA,将其插入含强启动子tac的穿梭表达载体pZ8-1中成功构建串联表达质粒pZ8-1-lysCr-asdA转化出发菌株,筛选获得工程菌株T11/pZ8-1-lysCr-asdA。摇瓶发酵其L-苏氨酸产量达到7.18 g/L,较出发菌株提高27.8%。进一步的30 L发酵罐补料分批发酵结果显示,发酵60 h L-苏氨酸产量达65.5 g/L,糖酸转化率达到39.5%,较出发菌株分别提高29.5%和33.9%,为后续的进一步构建高产L-苏氨酸的谷氨酸棒杆菌工程菌株提供强有力的基础。     

L-缬氨酸高产菌株的选育研究

以产L-缬氨酸的谷氨酸棒状杆菌(Corynebacterium glutamicum)为原始菌株,利用注入低能氮离子束进行一系列诱变,获得一株稳定的高产L-缬氨酸突变菌株。摇瓶培养96h后发酵能力可达38.0g·L-1,较出发菌株提高18.01%。通过对摇瓶中葡萄糖、玉米浆浓度及培养条件进行优化,发酵能力达到40.6g·L-1,50L发酵罐的发酵能力可达70g·L-1左右。     

双功能尿苷酰转移/去除酶GlnD在谷氨酸棒杆菌JNR中的功能

【目的】通过改造谷氨酸棒杆菌JNR中双功能尿苷酰转移/去除酶GlnD,减弱尿苷酰去除酶的活性,增强NH_4~+的转运和利用,提高L-精氨酸的合成。【方法】本文对来源于谷氨酸棒杆菌的突变菌株JNR中的双功能尿苷酰转移/去除酶GlnD进行整合突变,采用同源重组的方法将H_(414)和D_(415)位点突变为两个丙氨酸AA,在此菌株的基础上过量表达PII蛋白GlnK,并对其进行尿苷酰化研究,离子色谱检测摇瓶发酵过程中NH4+的浓度,并对最终的改造菌株进行连续流加发酵分析。【结果】该双功能尿苷酰转移/去除酶在谷氨酸棒杆菌中成功进行整合突变,有效减弱了尿苷酰去除酶的活性;同时过表达PII蛋白GlnK,其酰基化程度明显增强。摇瓶发酵结果表明菌株L4消耗NH_4~+增加,L-精氨酸产量为36.2±1.2 g/L,比对照菌株L3高出22.7%。5-L发酵罐实验结果显示改造菌株L4的L-精氨酸的产量为52.2 g/L,较野生型菌株L0提高了25.3%。【结论】谷氨酸棒杆菌合成L-精氨酸的过程中氮源是必不可少的。减弱GlnD尿苷酰去除酶的活性后,胞内尿苷酰化的GlnK-UMP增加,GlnK-UMP与氮转录调控因子AmtR结合,转运至胞内的NH_4~+浓度提高,促使L-精氨酸产量显著提高。     

谷氨酸棒杆菌ilvE基因的敲除对相关氨基酸合成的影响

L-缬氨酸是谷氨酸棒杆菌SYPS-062发酵生产L-丝氨酸的主要副产物.为减少L-缬氨酸的积累,利用基因重组技术敲除SYPS-062转氨酶B编码基因ilvE内部的987 bp核苷酸序列,构建了ilvE基因缺失突变株SYPS-062△ilvE.研究表明,重组菌ilvE基因的缺失直接导致了分支氨基酸(Val、Ile、Leu)的合成能力的降低,影响了菌体的生长,其中Ile成为生长限制性因子,在培养基中添加分支氨基酸能明显促进其生长.重组菌培养96 h,发酵液中L-缬氨酸含量低于0.5 g/L,与出发菌株相比,其生成率降低90％.     

钝齿棒杆菌中异源表达N-乙酰鸟氨酸脱乙酰基酶合成L-鸟氨酸的研究

目的:对一株产鸟氨酸的钝齿棒杆菌Corynebacterium crenatum SYPA5-5/△proB/△argF(SYPO-1)进行代谢工程改造,筛选不同细菌来源的N-乙酰鸟氨酸脱乙酰基酶在大肠杆菌中克隆与表达,纯化后对其进行酶学性质的比较;将黏质沙雷氏菌Serratia marcescens Y213来源的Smarg E基因编码的N-乙酰鸟氨酸脱乙酰基酶在L-鸟氨酸生产菌株C.crenatum SYPO-1中过量表达,进一步提高L-鸟氨酸的产量。方法:通过利用pDXW10穿梭质粒对不同来源的N-乙酰鸟氨酸脱乙酰化酶进行克隆表达和酶学性质比较,选择性质最优来源的N-乙酰鸟氨酸脱乙酰基酶编码基因Smarg E在产L-鸟氨酸重组钝齿棒杆菌中表达,考察重组菌株发酵过程中参数的变化。结果:来源于S.marcescens Y213的N-乙酰鸟氨酸脱乙酰基酶比酶活最高为798.98U/mg,最适pH为7,最适温度为37℃,0.1mmol/L的Mg~(2+)、Li~+、Mn~(2+)促进酶的比酶活提高了50%;在钝齿棒杆菌中表达N-乙酰鸟氨酸脱乙酰基酶酶活达到128.4U/ml,显著提高了钝齿棒杆菌中胞内乙酰基循环水平;5L发酵罐发酵重组菌株96h,L-鸟氨酸的产量达到38.5g/L,比出发菌株,L-鸟氨酸的产量提高了33.2%,产率达0.401g/(L·h)。结论:筛选出最佳来源的N-乙酰鸟氨酸脱乙酰基酶,在鸟氨酸生产菌株C.crenatum(SYPO-1)中过量表达,可以促进鸟氨酸的前体物质N-乙酰鸟氨酸的快速消耗,实现鸟氨酸的积累。     

磷酸烯醇式丙酮酸羧化酶基因的敲除对于谷氨酸棒杆菌V1生理代谢的影响

【目的】L-缬氨酸生物合成的前体物质是丙酮酸。为了增加磷酸烯醇式丙酮酸向丙酮酸的代谢流向,优化L-缬氨酸前体物质的供应,以一株积累L-缬氨酸的谷氨酸棒杆菌V1(Corynebacterium glutamicum V1)为对象,构建磷酸烯醇式丙酮酸羧化酶(PEPC)基因敲除的重组菌株C.glutamicum V1-Δpepc,并研究pepc敲除后菌株生理特性的改变。【方法】运用交叉PCR方法得到pepc基因内部缺失的同源片段Δpepc,并构建敲除质粒pK18mobsacB-Δpepc。利用同源重组技术获得pepc基因缺陷突变株C.glutamicum V1-Δpepc。采用摇瓶发酵对C.glutamicum V1-Δpepc进行发酵特性的研究。对谷氨酸棒杆菌模式菌株C.glutamicum ATCC 13032、出发菌株C.glutamicum V1和敲除菌株C.glu-tamicum V1-Δpepc的丙酮酸激酶(Pyruvate kinase,PK)、丙酮酸脱氢酶(Pyruvate dehydro-genase,PDH)、丙酮酸羧化酶(Pyruvate carboxylase,PC)分别进行测定和分析。【结果】PCR验证以及PEPC酶活测定都表明筛选到pepc缺陷的突变菌株C.glutamicum V1-Δpepc,摇瓶发酵结果表明,突变菌株C.glutamicum V1-Δpepc不再积累L-缬氨酸而是积累L-精氨酸达到7.48 g/L。酶活测定结果表明出发菌株的PDH和PC酶活均低于模式菌株C.glu-tamicum ATCC13032和重组菌株C.glutamicum V1-Δpepc,出发菌株的PK与PEPC酶活与模式菌株没有较大的差异。【结论】研究表明,通过切断PEPC参与的三羧酸循环的回补途径,增加磷酸烯醇式丙酮酸向丙酮酸的流向使丙酮酸向TCA循环的流量增加,精氨酸的累积量提高。同时,以丙酮酸为前体的L-缬氨酸和丙氨酸的积累量降低。     

不同来源的谷氨酸棒杆菌氨基脱氧分支酸合成酶的活性分析

分别以高产L-丝氨酸的谷氨酸棒杆菌(Corynebacterium glutamicum)SYPS-062与模式菌株谷氨酸棒杆菌(Corynebacterium glutamicum) ATCC 13032的基因组DNA为模板,运用PCR技术扩增出氨基脱氧分支酸合成酶(ADC synthase)的编码基因pabAB。实验结果表明：来源于SYPS-062和ATCC 13032的pabAB片段全长均为1863bp,编码620个氨基酸。两片段存在16个碱基的差异,引起了7个氨基酸的突变。将pabAB连接表达载体pET-28a(+),构建表达质粒pET-28a-pabAB,并转化E.coli BL21(DE3),在IPTG诱导下,E.coli BL21(DE3)(pET-28a-pabAB)高效表达分子量约为67kDa的可溶性蛋白。表达产物带有His-tag标记,选用Ni柱对表达产物进行纯化,纯化后酶活测定结果表明,来源于SYPS-062氨基脱氧分支酸合成酶的比酶活低于ATCC 13032达46.6%。     

High-yield production of L-valine in engineered Escherichia coli by a novel two-stage fermentation

L-valine is an essential amino acid and an important amino acid in the food and feed industry. The relatively low titer and low fermentation yield currently limit the large-scale application of L-valine. Here, we constructed a chromosomally engineered Escherichia coli to efficiently produce L-valine. First, the synthetic pathway of L-valine was enhanced by heterologous introduction of a feedback-resistant acetolactate acid synthase from Bacillus subtilis and overexpression of other two enzymes in the L-valine synthetic pathway. For efficient efflux of L-valine, an exporter from Corynebacterium glutamicum was subsequently introduced. Next, the precursor pyruvate pool was increased by knockout of GTP pyrophosphokinase and introduction of a ppGpp 3′-pyrophosphohydrolase mutant to facilitate the glucose uptake process. Finally, in order to improve the redox cofactor balance, acetohydroxy acid isomeroreductase was replaced by a NADH-preferring mutant, and branched-chain amino acid aminotransferase was replaced by leucine dehydrogenase from Bacillus subtilis. Redox cofactor balance enabled the strain to synthesize L-valine under oxygen-limiting condition, significantly increasing the yield in the presence of glucose. Two-stage fed-batch fermentation of the final strain in a 5 L bioreactor produced 84 g/L L-valine with a yield and productivity of 0.41 g/g glucose and 2.33 g/L/h, respectively. To the best of our knowledge, this is the highest L-valine titer and yield ever reported in E. coli. The systems metabolic engineering strategy described here will be useful for future engineering of E. coli strains for the industrial production of L-valine and related products.     

Linking central metabolism with increased pathway flux: L-valine accumulation by Corynebacterium glutamicum

Mutants of Corynebacterium glutamicum were made and enzymatically characterized to clone ilvD and ilvE, which encode dihydroxy acid dehydratase and transaminase B, respectively. These genes of the branched-chain amino acid synthesis were overexpressed together with ilvBN (which encodes acetohydroxy acid synthase) and ilvC (which encodes isomeroreductase) in the wild type, which does not excrete L-valine, to result in an accumulation of this amino acid to a concentration of 42 mM. Since L-valine originates from two pyruvate molecules, this illustrates the comparatively easy accessibility of the central metabolite pyruvate. The same genes, ilvBNCD, overexpressed in an ilvA deletion mutant which is unable to synthesize L-isoleucine increased the concentration of this amino acid to 58 mM. A further dramatic increase was obtained when panBC was deleted, making the resulting mutant auxotrophic for D-pantothenate. When the resulting strain, C. glutamicum 13032DeltailvADeltapanBC with ilvBNCD overexpressed, was grown under limiting conditions it accumulated 91 mM L-valine. This is attributed to a reduced coenzyme A availability and therefore reduced flux of pyruvate via pyruvate dehydrogenase enabling its increased drain-off via the L-valine biosynthesis pathway.     

Metabolic engineering of Corynebacterium glutamicum for L-serine production

Although L-serine proceeds in just three steps from the glycolytic intermediate 3-phosphoglycerate, and as much as 8% of the carbon assimilated from glucose is directed via L-serine formation, previous attempts to obtain a strain producing L-serine from glucose have not been successful. We functionally identified the genes serC and serB from Corynebacterium glutamicum, coding for phosphoserine aminotransferase and phosphoserine phosphatase, respectively. The overexpression of these genes, together with the third biosynthetic serA gene, serA(delta197), encoding an L-serine-insensitive 3-phosphoglycerate dehydrogenase, yielded only traces of L-serine, as did the overexpression of these genes in a strain with the L-serine dehydratase gene sdaA deleted. However, reduced expression of the serine hydroxymethyltransferase gene glyA, in combination with the overexpression of serA(delta197), serC, and serB, resulted in a transient accumulation of up to 16 mM L-serine in the culture medium. When sdaA was also deleted, the resulting strain, C. glutamicum delta sdaA::pK18mobglyA'(pEC-T18mob2serA(delta197)CB), accumulated up to 86 mM L-serine with a maximal specific productivity of 1.2 mmol h(-1) g (dry weight)(-1). This illustrates a high rate of L-serine formation and also utilization in the C. glutamicum wild type. Therefore, metabolic engineering of L-serine production from glucose can be achieved only by addressing the apparent key position of this amino acid in the central metabolism.     

Feedback-resistant acetohydroxy acid synthase increases valine production in Corynebacterium glutamicum

Acetohydroxy acid synthase (AHAS), which catalyzes the key reactions in the biosynthesis pathways of branched-chain amino acids (valine, isoleucine, and leucine), is regulated by the end products of these pathways. The whole Corynebacterium glutamicum ilvBNC operon, coding for acetohydroxy acid synthase (ilvBN) and aceto hydroxy acid isomeroreductase (ilvC), was cloned in the newly constructed Escherichia coli-C. glutamicum shuttle vector pECKA (5.4 kb, Km(r)). By using site-directed mutagenesis, one to three amino acid alterations (mutations M8, M11, and M13) were introduced into the small (regulatory) AHAS subunit encoded by ilvN. The activity of AHAS and its inhibition by valine, isoleucine, and leucine were measured in strains carrying the ilvBNC operon with mutations on the plasmid or the ilvNM13 mutation within the chromosome. The enzyme containing the M13 mutation was feedback resistant to all three amino acids. Different combinations of branched-chain amino acids did not inhibit wild-type AHAS to a greater extent than was measured in the presence of 5 mM valine alone (about 57%). We infer from these results that there is a single binding (allosteric) site for all three amino acids in the enzyme molecule. The strains carrying the ilvNM13 mutation in the chromosome produced more valine than their wild-type counterparts. The plasmid-free C. glutamicum DeltailvA DeltapanB ilvNM13 strain formed 90 mM valine within 48 h of cultivation in minimal medium. The same strain harboring the plasmid pECKAilvBNC produced as much as 130 mM valine under the same conditions.     

Improvement of the redox balance increases L-valine production by Corynebacterium glutamicum under oxygen deprivation conditions

Production of L-valine under oxygen deprivation conditions by Corynebacterium glutamicum lacking the lactate dehydrogenase gene ldhA and overexpressing the L-valine biosynthesis genes ilvBNCDE was repressed. This was attributed to imbalanced cofactor production and consumption in the overall L-valine synthesis pathway: two moles of NADH was generated and two moles of NADPH was consumed per mole of L-valine produced from one mole of glucose. In order to solve this cofactor imbalance, the coenzyme requirement for L-valine synthesis was converted from NADPH to NADH via modification of acetohydroxy acid isomeroreductase encoded by ilvC and introduction of Lysinibacillus sphaericus leucine dehydrogenase in place of endogenous transaminase B, encoded by ilvE. The intracellular NADH/NAD(+) ratio significantly decreased, and glucose consumption and L-valine production drastically improved. Moreover, L-valine yield increased and succinate formation decreased concomitantly with the decreased intracellular redox state. These observations suggest that the intracellular NADH/NAD(+) ratio, i.e., reoxidation of NADH, is the primary rate-limiting factor for L-valine production under oxygen deprivation conditions. The L-valine productivity and yield were even better and by-products derived from pyruvate further decreased as a result of a feedback resistance-inducing mutation in the acetohydroxy acid synthase encoded by ilvBN. The resultant strain produced 1,470 mM L-valine after 24 h with a yield of 0.63 mol mol of glucose(-1), and the L-valine productivity reached 1,940 mM after 48 h.     

L-valine production with pyruvate dehydrogenase complex-deficient Corynebacterium glutamicum

Corynebacterium glutamicum was engineered for the production of L-valine from glucose by deletion of the aceE gene encoding the E1p enzyme of the pyruvate dehydrogenase complex and additional overexpression of the ilvBNCE genes encoding the L-valine biosynthetic enzymes acetohydroxyacid synthase, isomeroreductase, and transaminase B. In the absence of cellular growth, C. glutamicum DeltaaceE showed a relatively high intracellular concentration of pyruvate (25.9 mM) and produced significant amounts of pyruvate, L-alanine, and L-valine from glucose as the sole carbon source. Lactate or acetate was not formed. Plasmid-bound overexpression of ilvBNCE in C. glutamicum DeltaaceE resulted in an approximately 10-fold-lower intracellular pyruvate concentration (2.3 mM) and a shift of the extracellular product pattern from pyruvate and L-alanine towards L-valine. In fed-batch fermentations at high cell densities and an excess of glucose, C. glutamicum DeltaaceE(pJC4ilvBNCE) produced up to 210 mM L-valine with a volumetric productivity of 10.0 mM h(-1) (1.17 g l(-1) h(-1)) and a maximum yield of about 0.6 mol per mol (0.4 g per g) of glucose.     

<Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> tailored for high-yield L-valine production

We recently engineered the wild type of Corynebacterium glutamicum for the growth-decoupled production of L: -valine from glucose by inactivation of the pyruvate dehydrogenase complex and additional overexpression of the ilvBNCE genes, encoding the L-valine biosynthetic enzymes acetohydroxyacid synthase, isomeroreductase, and transaminase B. Based on the first generation of pyruvate-dehydrogenase-complex-deficient C. glutamicum strains, a second generation of high-yield L-valine producers was constructed by successive deletion of the genes encoding pyruvate:quinone oxidoreductase, phosphoglucose isomerase, and pyruvate carboxylase and overexpression of ilvBNCE. In fed-batch fermentations at high cell densities, the newly constructed strains produced up to 410 mM (48 g/l) L-valine, showed a maximum yield of 0.75 to 0.86 mol/mol (0.49 to 0.56 g/g) of glucose in the production phase and, in contrast to the first generation strains, excreted neither pyruvate nor any other by-product tested.     

产L-苏氨酸重组大肠杆菌的构建和发酵性能

【背景】大肠杆菌由于生长性能优良、遗传背景清晰,常被用作苏氨酸生产菌。【目的】敲除大肠杆菌Escherichia coli THR苏氨酸合成途径的非必需基因,并异源表达苏氨酸合成必需的关键酶,构建一株苏氨酸高产菌株。【方法】利用FLP/FRT重组酶系统,敲除E. coli THR中lysC、pfkB和sstT,同时进行谷氨酸棒杆菌中lysC~(fbr)、thrE和丙酮丁醇梭菌中gapC的重组质粒构建并转化到宿主菌中。【结果】以E. coli THR为出发菌株,敲除其苏氨酸合成途径中表达天冬氨酸激酶Ⅲ (AKⅢ)的基因lysC、磷酸果糖激酶Ⅱ基因pfkB及苏氨酸吸收蛋白表达基因sstT,使菌株积累苏氨酸的产量达到75.64±0.35g/L,比出发菌株增加9.9%。随后异源表达谷氨酸棒杆菌中解除了反馈抑制的天冬氨酸激酶(lysC~(fbr))、苏氨酸分泌转运蛋白(thrE)及丙酮丁醇梭菌中由gapC编码的NADP+依赖型甘油醛-3-磷酸脱氢酶,获得重组菌株E. coli THR6菌株。该菌株积累苏氨酸的产量提高到105.3±0.5 g/L,糖酸转化率提高了43.20%,单位产酸能力提高到5.76 g/g DCW,最大生物量为18.26 g DCW/L。【结论】单独敲除某个基因或改造某个途径不能使苏氨酸大量合成和积累,对多个代谢途径共同改造是构建苏氨酸工程菌的最有效方法。