使用动态分子开关调控大肠杆菌生产莽草酸

莽草酸是大肠杆菌合成芳香族氨基酸的中间代谢物,也是抗流感药物"达菲"的重要合成前体。合成莽草酸需要截断莽草酸途径,导致芳香族氨基酸无法合成,因此面临细胞生长受到抑制的问题。使用动态调控策略通过将细胞生长和莽草酸的合成相互分离,可以提高菌株的生产性能。通过使用生长偶联型启动子和降解决定子(Degrons),组建动态分子开关。利用该动态分子开关实现细胞生长与莽草酸合成分离,在5L发酵罐中经过72h发酵得到了14.33g/L的莽草酸。结果表明,这种动态分子开关可以通过调控靶蛋白丰度来改变碳流量平衡,使菌株获得更优秀的生产性能。     

Efficient Itaconic acid production via protein–protein scaffold introduction between GltA,AcnA, and CadA in recombinant Escherichia coli

Itaconic acid, which is a promising organic acid in synthetic polymers and some base-material production, has been produced by Aspergillus terreus fermentation at a high cost. The recombinant Escherichia coli that contained the cadA gene from A. terreus can produce itaconic acid but with low yield. By introducing the protein–protein scaffold between citrate synthesis, aconitase, and cis-aconitase decarboxylase, 5.7 g/L of itaconic acid was produced, which is 3.8-fold higher than that obtained with the strain without scaffold. The optimum pH and temperature for itaconic acid production were 8.5 and 30°C, respectively. When the competing metabolic network was inactivated by knock-out mutation, the itaconic acid concentration further increased, to 6.57 g/L.     

Metabolic engineering of Escherichia coli for the production of fumaric acid

Fumaric acid is a naturally occurring organic acid that is an intermediate of the tricarboxylic acid cycle. Fungal species belonging to Rhizopus have traditionally been employed for the production of fumaric acid. In this study, Escherichia coli was metabolically engineered for the production of fumaric acid under aerobic condition. For the aerobic production of fumaric acid, the iclR gene was deleted to redirect the carbon flux through the glyoxylate shunt. In addition, the fumA, fumB, and fumC genes were also deleted to enhance fumaric acid formation. The resulting strain was able to produce 1.45 g/L of fumaric acid from 15 g/L of glucose in flask culture. Based on in silico flux response analysis, this base strain was further engineered by plasmid‐based overexpression of the native ppc gene, encoding phosphoenolpyruvate carboxylase (PPC), from the strong tac promoter, which resulted in the production of 4.09 g/L of fumaric acid. Additionally, the arcA and ptsG genes were deleted to reinforce the oxidative TCA cycle flux, and the aspA gene was deleted to block the conversion of fumaric acid into L ‐aspartic acid. Since it is desirable to avoid the use of inducer, the lacI gene was also deleted. To increase glucose uptake rate and fumaric acid productivity, the native promoter of the galP gene was replaced with the strong trc promoter. Fed‐batch culture of the final strain CWF812 allowed production of 28.2 g/L fumaric acid in 63 h with the overall yield and productivity of 0.389 g fumaric acid/g glucose and 0.448 g/L/h, respectively. This study demonstrates the possibility for the efficient production of fumaric acid by metabolically engineered E. coli. Biotechnol. Bioeng. 2013; 110: 2025–2034. © 2013 Wiley Periodicals, Inc.     

进化代谢选育高渗透压耐受型产琥珀酸大肠杆菌

在以碳酸钠为酸中和剂的大肠杆菌两阶段发酵产琥珀酸的过程中,由于Na+的积累造成发酵体系中渗透压的提高,严重抑制了琥珀酸的产物浓度。为了增强大肠杆菌对渗透压的耐受性,考察了利用进化代谢方法筛选高渗透压耐受型高产琥珀酸大肠杆菌菌株的可行性。进化代谢系统作为一种菌株突变装置,可以使菌体在连续培养条件下以最大的生长速率生长。以NaCl为渗透压调节剂,通过在连续培养装置中逐步提高NaCl浓度使菌体在高渗透压条件下快速生长,最终得到了一株高渗透压耐受型琥珀酸生产菌株Escherichia coli XB4。以碳酸钠为酸中和剂,在7 L发酵罐中利用Escherichia coli XB4进行两阶段发酵,厌氧培养60 h后,琥珀酸产量达到了69.5 g/L,琥珀酸生产速率达到了1.81 g/(L.h),分别比出发菌株提高了18.6%和20%。     

Pathway engineering of Escherichia coli for α-ketoglutaric acid production

α-Ketoglutaric acid (α-KG) is a multifunctional dicarboxylic acid in the tricarboxylic acid (TCA) cycle, but microbial engineering for α-KG production is not economically efficient, due to the intrinsic inefficiency of its biosynthetic pathway. In this study, pathway engineering was used to improve pathway efficiency for α-KG production in Escherichia coli. First, the TCA cycle was rewired for α-KG production starting from pyruvate, and the engineered strain E. coli W3110Δ4-PCAI produced 15.66 g/L α-KG. Then, the rewired TCA cycle was optimized by designing various strengths of pyruvate carboxylase and isocitrate dehydrogenase expression cassettes, resulting in a large increase in α-KG production (24.66 g/L). Furthermore, acetyl coenzyme A (acetyl-CoA) availability was improved by overexpressing acetyl-CoA synthetase, leading to α-KG production up to 28.54 g/L. Finally, the engineered strain E. coli W3110Δ4-P_(H)CAI_(H)A was able to produce 32.20 g/L α-KG in a 5-L fed-batch bioreactor. This strategy described here paves the way to the development of an efficient pathway for microbial production of α-KG.     

Production of p-Aminobenzoic acid by metabolically engineered Escherichia coli

The production of chemical compounds from renewable resources is an important issue in building a sustainable society. In this study, Escherichia coli was metabolically engineered by introducing T7lac promoter-controlled aroF^fbr, pabA, pabB, and pabC genes into the chromosome to overproduce para-aminobenzoic acid (PABA) from glucose. Elevating the copy number of chromosomal P_T7lac-pabA-pabB distinctly increased the PABA titer, indicating that elevation of 4-amino-4-deoxychorismic acid synthesis is a significant factor in PABA production. The introduction of a counterpart derived from Corynebacterium efficiens, pabAB (ce), encoding a fused PabA and PabB protein, resulted in a considerable increase in the PABA titer. The introduction of more than two copies of P_T7lac-pabAB (ce-mod), a codon-optimized pabAB (ce), into the chromosome of a strain that simultaneously overexpressed aroF^fbr and pabC resulted in 5.1?mM PABA from 55.6?mM glucose (yield 9.2%). The generated strain produced 35?mM (4.8?g?L^?1) PABA from 167?mM glucose (yield 21.0%) in fed-batch culture.     

Self-cycling operation increases productivity of recombinant protein in Escherichia coli

Self-cycling fermentation (SCF), a cyclical, semi-continuous process that induces cell synchrony, was incorporated into a recombinant protein production scheme. Escherichia coli CY15050, a lac(-) mutant lysogenized with temperature-sensitive phage λ modified to over-express β-galactosidase, was used as a model system. The production scheme was divided into two de-coupled stages. The host cells were cultured under SCF operation in the first stage before being brought to a second stage where protein production was induced. In the first stage, the host strain demonstrated a stable cycling pattern immediately following the first cycle. This reproducible pattern was maintained over the course of the experiments and a significant degree of cell synchrony was obtained. By growing cells using SCF, productivity increased 50% and production time decreased by 40% compared to a batch culture under similar conditions. In addition, synchronized cultures induced from the end of a SCF cycle displayed shorter lysis times and a more complete culture-wide lysis than unsynchronized cultures. Finally, protein synthesis was influenced by the time at which the lytic phase was induced in the cell life cycle. For example, induction of a synchronized culture immediately prior to cell division resulted in the maximum protein productivity, suggesting protein production can be optimized with respect to the cell life cycle using SCF.     

Metabolic flux analysis for succinic acid production by recombinant Escherichia coli with amplified malic enzyme activity

A pfl ldhA double mutant Escherichia coli strain NZN111 was used to produce succinic acid by overexpressing the E. coli malic enzyme. Escherichia coli strain NZN111 harboring pTrcML produced 6 and 8 g/L of succinic acid from 20 g/L of glucose in flask culture at 37 degrees C and 30 degrees C, respectively. When NZN111(pTrcML) was cultured at 30 degrees C with intermittent glucose feeding the final succinic acid concentration obtained was 9.5 g/L and the ratio of succinic acid to acetic acid was 13:1. This system could not be analyzed by conventional metabolic flux analysis techniques, since some pyruvate and succinic acid were accumulated intracellularly. Therefore, a new flux analysis method was proposed by introducing intracellular pyruvate and succinic acid pools. By this new method the concentrations of intracellular metabolites were successfully predicted and the differences between the measured and calculated reaction rates could be considerably reduced.     

Enhancing extracellular protein production in Escherichia coli by deleting the d‐alanyl‐d‐alanine carboxypeptidase gene dacC

d ‐Alanyl‐d ‐alanine carboxypeptidase DacC is important for synthesis and stabilization of the peptidoglycan layer of Escherichia coli. In this work, dacC of E. coli BL21 (DE3) was successfully deleted, and the effects of this deletion on extracellular protein production in E. coli were investigated. The extracellular activities and fluorescence value of recombinant amylase, green fluorescent protein, and α‐galactosidase of the deletion mutants were increased by 82.3, 29.1, and 37.7%, respectively, compared with that of control cells. The outer membrane permeability and intracellular soluble peptidoglycan accumulation of deletion mutant were also enhanced compared with those of control cells, respectively. Based on fluorescence‐assisted cell sorting analyses, we found that the morphology of the E. coli deletion mutant cells was altered compared with that of control cells. Local transparent bulges in the poles of the E. coli mutant with deletion of the dacC gene were found by transmission electron microscopy analysis. These bulges in the poles could explain the improvement in the production of extracellular protein by the E. coli mutant with deletion of the dacC gene. These findings provide important insights into the extracellular production of proteins using E. coli as microbial cell factories.     

Strain engineering for high‐level 5‐aminolevulinic acid production in Escherichia coli

Herein, we report the development of a microbial bioprocess for high‐level production of 5‐aminolevulinic acid (5‐ALA), a valuable non‐proteinogenic amino acid with multiple applications in medical, agricultural, and food industries, using Escherichia coli as a cell factory. We first implemented the Shemin (i.e., C4) pathway for heterologous 5‐ALA biosynthesis in E. coli. To reduce, but not to abolish, the carbon flux toward essential tetrapyrrole/porphyrin biosynthesis, we applied clustered regularly interspersed short palindromic repeats interference (CRISPRi) to repress hemB expression, leading to extracellular 5‐ALA accumulation. We then applied metabolic engineering strategies to direct more dissimilated carbon flux toward the key precursor of succinyl‐CoA for enhanced 5‐ALA biosynthesis. Using these engineered E. coli strains for bioreactor cultivation, we successfully demonstrated high‐level 5‐ALA biosynthesis from glycerol (~30 g L^?1) under both microaerobic and aerobic conditions, achieving up to 5.95 g L^?1 (36.9% of the theoretical maximum yield) and 6.93 g L^?1 (50.9% of the theoretical maximum yield) 5‐ALA, respectively. This study represents one of the most effective bio‐based production of 5‐ALA from a structurally unrelated carbon to date, highlighting the importance of integrated strain engineering and bioprocessing strategies to enhance bio‐based production.     

Metabolic costs of amino acid and protein production in Escherichia coli

Escherichia coli is the most popular microorganism for the production of recombinant proteins and is gaining increasing importance for the production of low-molecular weight compounds such as amino acids. The metabolic cost associated with the production of amino acids and (recombinant) proteins from glucose, glycerol and acetate was determined using three different computational techniques to identify those amino acids that put the highest burden on the biosynthetic machinery of E. coli. Comparing the costs of individual amino acids, we find that methionine is the most expensive amino acid in terms of consumed mol of ATP per molecule produced, while leucine is the most expensive amino acid when taking into account the cellular abundances of amino acids. Moreover, we show that the biosynthesis of a large number of amino acids from glucose and particularly from glycerol provides a surplus of energy, which can be used to balance the high energetic cost of amino acid polymerization.     

Recombinant Escherichia coli engineered for production of L-lactic acid from hexose and pentose sugars

Recombinant Escherichia coli have been constructed for the conversion of glucose as well as pentose sugars into L-lactic acid. The strains carry the lactate dehydrogenase gene from Streptococcus bovis on a low copy number plasmid for production of L-lactate. Three E. coli strains were transformed with the plasmid for producing L-lactic acid. Strains FBR9 and FBR11 were serially transferred 10 times in anaerobic cultures in sugar-limited medium containing glucose or xylose without selective antibiotic. An average of 96% of both FBR9 and FBR11 cells maintained pVALDH1 in anaerobic cultures. The fermentation performances of FBR9, FBR10, and FBR11 were compared in pH-controlled batch fermentations with medium containing 10% w/v glucose. Fermentation results were superior for FBR11, an E. coli B strain, compared to those observed for FBR9 or FBR10. FBR11 exhausted the glucose within 30 h, and the maximum lactic acid concentration (7.32% w/v) was 93% of the theoretical maximum. The other side-products detected were cell mass and succinic acid (0.5 g/l). Journal of Industrial Microbiology & Biotechnology (2001) 27, 259–264. Received 05 November 2000/ Accepted in revised form 03 July 2001     

Kinetic characterization in batch and continuous culture of Escherichia coli mutants affected in phosphoenolpyruvate metabolism: differences in acetic acid production

The growth kinetics of an Escherichia coli wild type strain and two derivative mutants were examined in batch cultures and in glucose-limited chemostats. One mutant (PB12) had an inactive phosphotranferase transport system and the other (PB25) had interrupted pykA and pykF genes that code for the two pyruvate kinase isoenzymes. In both batch and continuous culture, important differences in acetic acid accumulation and other metabolic activities were found. Compared to the wild type strain, we observed a reduction in acetic acid accumulation of 25 and 80% in PB25 and PB12 strains respectively, in batch culture. Continuous culture experiments revealed that compared to the other two strains, PB25 accumulated less acetic acid as a function of dilution rate. In continuous cultures, oxidoreductase metabolic activities were substantially affected in the two mutant strains. These changes in turn were reflected in different levels of biomass and CO₂ production, and in oxygen consumption.     

Metabolic adaptation of Escherichia coli during temperature-induced recombinant protein production: 1. Readjustment of metabolic enzyme synthesis

The metabolic burden and the stress load resulting from temperature-induced production of human basic fibroblast growth factor is connected to an increase in the respiratory activity of recombinant Escherichia coli, thereby reducing the biomass yield. To study the underlying changes in metabolic enzyme synthesis rates, the radiolabeled proteom was subjected to two-dimen- sional gel electrophoresis. After temperature-induction, the cAMP-CRP controlled dehydrogenases of the pyruvate dehydrogenase complex and the tricarboxylic acid cycle (LpdA and SdhA) were induced four times, reaching a maximum 1 h after the temperature upshift. The more abundant tricarboxylic acid cycle dehydrogenases (Icd and Mdh) were initially produced at reduced rates but regained preshift rates within 30 min. The adenylate energy charge dropped immediately after the temperature upshift but recovered within 1 h. Similar profiles in dehydrogenase synthesis rates and adenylate energy charge were found in a control cultivation of a strain carrying the "empty" parental expression vector. Although both strains exhibited significant differences in growth pattern and respiration rates after the temperature upshift, the adaptation of the energetic state of the cells and the synthesis of enzymes from the energy-generating catabolic pathway did not seem to be affected by the strong overproduction of the recombinant growth factor. In contrast, the synthesis rates of enzymes belonging to the biosynthetic machinery, e.g., translational elongation factors, decreased more strongly in the culture synthesizing the recombinant protein. In control and producing culture, synthesis rates of elongation factors paralleled the respective growth rate profiles. Thus, cells seem to readjust their metabolic activities according to their energetic requirements and, if necessary, at the cost of their biosynthetic capabilities.