Modulation of phosphoenolpyruvate synthase expression increases shikimate pathway product yields in E. coli

Product yields in microbial synthesis are ultimately limited by the mechanism utilized for glucose transport. Altered expression of phosphoenolpyruvate synthase was examined as a method for circumventing these limits. Escherichia coli KL3/pJY1.216A was cultured under fed-batch fermentor conditions where glucose was the only source of carbon for the formation of microbial biomass and the synthesis of product 3-dehydroshikimic acid. Shikimate pathway byproducts 3-deoxy-D-arabino-heptulosonic acid, 3-dehydroquinic acid, and gallic acid were also generated. An optimal expression level of phosphoenolpyruvate synthase was identified, which did not correspond to the highest expression levels of this enzyme, where the total yield of 3-dehydroshikimic acid and shikimate pathway byproducts synthesized from glucose was 51% (mol/mol). For comparison, the theoretical maximum yield is 43% (mol/mol) for synthesis of 3-dehydroshikimic acid and shikimate pathway byproducts from glucose in lieu of amplified expression of phosphoenolpyruvate synthase.     

Phosphoenolpyruvate availability and the biosynthesis of shikimic acid

The impact of increased availability of phosphoenolpyruvate during shikimic acid biosynthesis has been examined in Escherichia coli K-12 constructs carrying plasmid-localized aroF(FBR) and tktA inserts encoding, respectively, feedback-insensitive 3-deoxy-d-arabino-heptulosonic acid 7-phosphate synthase and transketolase. Strategies for increasing the availability of phosphoenolpyruvate were based on amplified expression of E. coli ppsA-encoded phosphoenolpyruvate synthase or heterologous expression of the Zymomonas mobilis glf-encoded glucose facilitator. The highest titers and yields of shikimic acid biosynthesized from glucose in 1 L fermentor runs were achieved using E. coli SP1.lpts/pSC6.090B, which expressed both Z. mobilis glf-encoded glucose facilitator protein and Z. mobilis glk-encoded glucose kinase in a host deficient in the phosphoenolpyruvate:carbohydrate phosphotransferase system. At 10 L scale with yeast extract supplementation, E. coli SP1.lpts/pSC6.090B synthesized 87 g/L of shikimic acid in 36% (mol/mol) yield with a maximum productivity of 5.2 g/L/h for shikimic acid synthesized during the exponential phase of growth.     

Fed-batch fermentor synthesis of 3-dehydroshikimic acid using recombinant Escherichia coli.

3-Dehydroshikimic acid (DHS), in addition to being a potent antioxidant, is the key hydroaromatic intermediate in the biocatalytic conversion of glucose into aromatic bioproducts and a variety of industrial chemicals. Microbial synthesis of DHS, like other intermediates in the common pathway of aromatic amino acid biosynthesis, has previously been examined only under shake flask conditions. In this account, synthesis of DHS using recombinant Escherichia coli constructs is examined in a fed-batch fermentor where glucose availability, oxygenation levels, and solution pH are controlled. DHS yields and titers are also determined by the activity of 3-deoxy-D-arabino-heptulosonic acid 7-phosphate (DAHP) synthase. This enzyme's expression levels, sensitivity to feedback inhibition, and the availability of its substrates, phosphoenolpyruvate (PEP) and D-erythrose 4-phosphate (E4P), dictate its in vivo activity. By combining fed-batch fermentor control with amplified expression of a feedback-insensitive isozyme of DAHP synthase and amplified expression of transketolase, DHS titers of 69 g/L were synthesized in 30% yield (mol/mol) from D-glucose. Significant concentrations of 3-dehydroquinic acid (6.8 g/L) and gallic acid (6.6 g/L) were synthesized in addition to DHS. The pronounced impact of transketolase overexpression, which increases E4P availability, on DHS titers and yields indicates that PEP availability is not a limiting factor under the fed-batch fermentor conditions employed.     

Metabolic engineering of Corynebacterium glutamicum for shikimate overproduction by growth-arrested cell reaction

Corynebacterium glutamicum with the ability to simultaneously utilize glucose/pentose mixed sugars was metabolically engineered to overproduce shikimate, a valuable hydroaromatic compound used as a starting material for the synthesis of the anti-influenza drug oseltamivir. To achieve this, the shikimate kinase and other potential metabolic activities for the consumption of shikimate and its precursor dehydroshikimate were inactivated. Carbon flux toward shikimate synthesis was enhanced by overexpression of genes for the shikimate pathway and the non-oxidative pentose phosphate pathway. Subsequently, to improve the availability of the key aromatics precursor phosphoenolpyruvate (PEP) toward shikimate synthesis, the PEP: sugar phosphotransferase system (PTS) was inactivated and an endogenous myo-inositol transporter IolT1 and glucokinases were overexpressed. Unexpectedly, the resultant non-PTS strain accumulated 1,3-dihydroxyacetone (DHA) and glycerol as major byproducts. This observation and metabolome analysis identified glyceraldehyde-3-phosphate dehydrogenase (GAPDH)-catalyzed reaction as a limiting step in glycolysis. Consistently, overexpression of GAPDH significantly stimulated both glucose consumption and shikimate production. Blockage of the DHA synthesis further improved shikimate yield. We applied an aerobic, growth-arrested and high-density cell reaction to the shikimate production by the resulting strain and notably achieved the highest shikimate titer (141 g/l) and a yield (51% (mol/mol)) from glucose reported to date after 48 h in minimal medium lacking nutrients required for cell growth. Moreover, comparable shikimate productivity could be attained through simultaneous utilization of glucose, xylose, and arabinose, enabling efficient shikimate production from lignocellulosic feedstocks. These findings demonstrate that C. glutamicum has significant potential for the production of shikimate and derived aromatic compounds.     

Microbial synthesis of p-hydroxybenzoic acid from glucose.

A series of recombinant Escherichia coli strains have been constructed and evaluated for their ability to synthesize p-hydroxybenzoic acid from glucose under fed-batch fermentor conditions. The maximum concentration of p-hydroxybenzoic acid synthesized was 12 g/L and corresponded to a yield of 13% (mol/mol). Synthesis of p-hydroxybenzoic acid began with direction of increased carbon flow into the common pathway of aromatic amino acid biosynthesis. This was accomplished in all constructs with overexpression of a feedback-insensitive isozyme of 3-deoxy-D-arabino-heptulosonic acid 7-phosphate synthase. Expression levels of enzymes in the common pathway of aromatic amino acid biosynthesis were also increased in all constructs to deliver increased carbon flow from the beginning to the end of the common pathway. A previously unreported inhibition of 3-dehydroquinate synthase by L-tyrosine was discovered to be a significant impediment to the flow of carbon through the common pathway. Chorismic acid, the last metabolite of the common pathway, was converted into p-hydroxybenzoic acid by ubiC-encoded chorismate lyase. Constructs differed in the strategy used for overexpression of chorismate lyase and also differed as to whether mutations were present in the host E. coli to inactivate other chorismate-utilizing enzymes. Use of overexpressed chorismate lyase to increase the rate of chorismic acid aromatization was mitigated by attendant decreases in the specific activity of DAHP synthase and feedback inhibition caused by p-hydroxybenzoic acid. The toxicity of p-hydroxybenzoic acid towards E. coli metabolism and growth was also evaluated.     

Microbial synthesis of 3-dehydroshikimic acid: a comparative analysis of D-xylose, L-arabinose, and D-glucose carbon sources.

3-Dehydroshikimic acid is a hydroaromatic precursor to chemicals ranging from L-phenylalanine to adipic acid. The concentration and yield of 3-dehydroshikimic acid microbially synthesized from various carbon sources has been examined under fed-batch fermentor conditions. Examined carbon sources included D-xylose, L-arabinose, and D-glucose. A mixture consisting of a 3:3:2 molar ratio of glucose/xylose/arabinose was also evaluated as a carbon source to model the composition of pentose streams potentially resulting from the hydrolysis of corn fiber. Escherichia coli KL3/pKL4.79B, which overexpresses feedback-insensitive DAHP synthase, synthesizes higher concentrations and yields of 3-dehydroshikimic acid when either xylose, arabinose, or the glucose/xylose/arabinose mixture is used as a carbon source relative to when glucose alone is used as a carbon source. E. coli KL3/pKL4.124A, which overexpresses transketolase and feedback-insensitive DAHP synthase, synthesizes higher concentrations and yields of 3-dehydroshikimic acid when the glucose/xylose/arabinose mixture is used as the carbon source relative to when either xylose or glucose is used as a carbon source. Observed high-titer, high-yielding synthesis of 3-dehydroshikimic acid from the glucose/xylose/arabinose mixture carries significant ramifications relevant to the employment of corn fiber in the microbial synthesis of value-added chemicals.     

Protocatechuate overproduction by Corynebacterium glutamicum via simultaneous engineering of native and heterologous biosynthetic pathways

Protocatechuic acid (3, 4-dihydroxybenzoic acid, PCA) is a natural bioactive phenolic acid potentially valuable as a pharmaceutical raw material owing to its diverse pharmacological activities. Corynebacterium glutamicum forms PCA as a key intermediate in a native pathway to assimilate shikimate/quinate through direct conversion of the shikimate pathway intermediate 3-dehydroshikimate (DHS), which is catalyzed by qsuB-encoded DHS dehydratase (the DHS pathway). PCA can also be formed via an alternate pathway extending from chorismate by introducing heterologous chorismate pyruvate lyase that converts chorismate into 4-hydroxybenzoate (4-HBA), which is then converted into PCA catalyzed by endogenous 4-HBA 3-hydroxylase (the 4-HBA pathway). In this study, we generated three plasmid-free C. glutamicum strains overproducing PCA based on the markerless chromosomal recombination by engineering each or both of the above mentioned two PCA-biosynthetic pathways combined with engineering of the host metabolism to enhance the shikimate pathway flux and to block PCA consumption. Aerobic growth-arrested cell reactions were performed using the resulting engineered strains, which revealed that strains dependent on either the DHS or 4-HBA pathway as the sole PCA-biosynthetic route produced 43.8 and 26.2 g/L of PCA from glucose with a yield of 35.3% and 10.0% (mol/mol), respectively, indicating that PCA production through the DHS pathway is significantly efficient compared to that produced through the 4-HBA pathway. Remarkably, a strain simultaneously using both DHS and 4-HBA pathways achieved the highest reported PCA productivity of 82.7 g/L with a yield of 32.8% (mol/mol) from glucose in growth-arrested cell reaction. These results indicated that simultaneous engineering of both DHS and 4-HBA pathways is an efficient method for PCA production. The generated PCA-overproducing strain is plasmid-free and does not require supplementation of aromatic amino acids and vitamins due to the intact shikimate pathway, thereby representing a promising platform for the industrial bioproduction of PCA and derived chemicals from renewable sugars.     

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%。     

Modular engineering of L-tyrosine production in Escherichia coli

Efficient biosynthesis of L-tyrosine from glucose is necessary to make biological production economically viable. To this end, we designed and constructed a modular biosynthetic pathway for L-tyrosine production in E. coli MG1655 by encoding the enzymes for converting erythrose-4-phosphate (E4P) and phosphoenolpyruvate (PEP) to L-tyrosine on two plasmids. Rational engineering to improve L-tyrosine production and to identify pathway bottlenecks was directed by targeted proteomics and metabolite profiling. The bottlenecks in the pathway were relieved by modifications in plasmid copy numbers, promoter strength, gene codon usage, and the placement of genes in operons. One major bottleneck was due to the bifunctional activities of quinate/shikimate dehydrogenase (YdiB), which caused accumulation of the intermediates dehydroquinate (DHQ) and dehydroshikimate (DHS) and the side product quinate; this bottleneck was relieved by replacing YdiB with its paralog AroE, resulting in the production of over 700 mg/liter of shikimate. Another bottleneck in shikimate production, due to low expression of the dehydroquinate synthase (AroB), was alleviated by optimizing the first 15 codons of the gene. Shikimate conversion to L-tyrosine was improved by replacing the shikimate kinase AroK with its isozyme, AroL, which effectively consumed all intermediates formed in the first half of the pathway. Guided by the protein and metabolite measurements, the best producer, consisting of two medium-copy-number, dual-operon plasmids, was optimized to produce >2 g/liter L-tyrosine at 80% of the theoretical yield. This work demonstrates the utility of targeted proteomics and metabolite profiling in pathway construction and optimization, which should be applicable to other metabolic pathways.     

Transport and utilization of the biosynthetic intermediate shikimic acid in Escherichia coli.

Auxotrophic mutants of Escherichia coli W or K12 blocked before shikimic acid in the aromatic biosynthetic pathway grew poorly on shikimic acid as sole aromatic supplement. This poor growth response was correlated with a relatively poor ability to transport shikimic acid. If citrate was present in the growth medium (as it is in some commonly used basal media) the growth of some of the E. coli K12 mutants on shikimate was further reduced. Mutants were derived from pre-shikimate auxotrophs which grew rapidly on media containing shikimic acid. These derivatives all had an increased ability to transport shikimic acid. Thus, it is proposed that the growth on shikimate observed in the parent cells is restricted by their relatively poor uptake of shikimate from the medium and that this restriction may be removed by a mutation which enhances shikimate transport. Transduction analysis of the mutations which enhanced utilization and transport of shikimic acid by E. coli K12 strains indicated at least two classes. Class 1 was about 20% cotransduced with the histidine region of the E. coli K12 chromosome and appeared to be coincident with a known shikimate transport locus, shiA. Class 2 was not cotransduced with his. The locus (or loci) of this class is unknown. Kinetic measurements suggested that both classes had shikimate uptake systems derived from the wild-type system. Two class 1 mutants had increased levels of otherwise unaltered wild-type transport while one class 2 mutant had an altered Michaelis constant (Km) for shikimate transport.     

大肠杆菌PTS系统改造及重组菌生长性能测定

利用Red重组系统对野生大肠杆菌Escherichia coli磷酸烯醇式丙酮酸-糖磷酸转移酶系统(Phosphoenolpyruvate:carbohydrate phosphotransferase system,PTS)进行修饰改造,敲除PTS系统中关键组分EⅡCBGlc的编码基因(ptsG),磷酸组氨酸搬运蛋白HPr的编码基因(ptsI),同时敲入来源于运动发酵单胞菌Zymomonas mobilis的葡萄糖易化体(Glucose facilitator)编码基因(glf),构建重组大肠杆菌,比较测定并系统评价了基因敲除和敲入对细胞的生长、葡萄糖代谢和乙酸积累的影响。敲除基因ptsG和ptsI造成大肠杆菌PTS系统部分功能缺失,细胞生长受到一定限制,敲入glf基因后,重组大肠杆菌能够利用Glf-Glk(葡萄糖易化体-葡萄糖激酶)途径,消耗ATP将葡萄糖进行磷酸化并转运进入细胞。通过该途径转运葡萄糖能够提高葡萄糖利用效率,降低副产物乙酸生成,同时能够使更多的碳代谢流进入后续相关合成途径,预期能够提高相关产物产量。     

产琥珀酸重组大肠杆菌的发酵性能研究

研究了重组大肠杆菌JM001(△ppc)/pTrc99a-pck发酵产琥珀酸的性能,结果表明厌氧条件下其耗糖能力和产酸能力分别为对照菌株JM001的4.2倍和15.3倍。进一步优化发酵条件表明：采用接入菌泥的发酵方式比按照10%接种量转接厌氧发酵的效果要好,琥珀酸的对葡萄糖的质量收率提高了约10%,且副产物乙酸的量进一步降低。初始葡萄糖浓度高于60g/L时会对菌株的生长和产酸产生抑制,且浓度越高,抑制作用越明显。7L发酵罐放大实验中,整个厌氧发酵阶段葡萄糖的消耗速率为0.42g/(L.h),琥珀酸对葡萄糖的质量收率为67.75%,琥珀酸的生产强度为0.28g/(L.h)。     

Benzene-free synthesis of adipic acid

Strains of Escherichia coli were constructed and evaluated that synthesized cis,cis-muconic acid from D-glucose under fed-batch fermentor conditions. Chemical hydrogenation of the cis,cis-muconic acid in the resulting fermentation broth has also been examined. Biocatalytic synthesis of adipic acid from glucose eliminates two environmental concerns characteristic of industrial adipic acid manufacture: use of carcinogenic benzene and benzene-derived chemicals as feedstocks and generation of nitrous oxide as a byproduct of a nitric acid catalyzed oxidation. While alternative catalytic syntheses that eliminate the use of nitric acid have been developed, most continue to rely on petroleum-derived benzene as the ultimate feedstock. In this study, E. coli WN1/pWN2.248 was developed that synthesized 36.8 g/L of cis,cis-muconic acid in 22% (mol/mol) yield from glucose after 48 h of culturing under fed-batch fermentor conditions. Optimization of microbial cis,cis-muconic acid synthesis required expression of three enzymes not typically found in E. coli. Two copies of the Klebsiella pneumoniae aroZ gene encoding DHS dehydratase were inserted into the E. coli chromosome, while the K. pneumoniae aroY gene encoding PCA decarboxylase and the Acinetobacter calcoaceticus catA gene encoding catechol 1,2-dioxygenase were expressed from an extrachromosomal plasmid. After fed-batch culturing of WN1/pWN2.248 was complete, the cells were removed from the broth, which was treated with activated charcoal and subsequently filtered to remove soluble protein. Hydrogenation of the resulting solution with 10% Pt on carbon (5% mol/mol) at 3400 kPa of H2 pressure for 2.5 h at ambient temperature afforded a 97% (mol/mol) conversion of cis,cis-muconic acid into adipic acid.     

Proposed mechanism of acetate accumulation in two recombinant Escherichia coli strains during high density fermentation

The productivity of Escherichia coli as a producer of recombinant proteins is affected by its metabolic properties, especially by acetate production. Two commercially used E. coli strains, BL21 (lambdaDE3) and JM109, differ significantly in their acetate production during batch fermentation at high initial glucose concentrations. E. coli BL21 grows to an optical density (OD, 600 nm) of 100 and produces no more than 2 g/L acetate, while E. coli JM109 grows to an OD (600 nm) of 80 and produces up to 14 g/L acetate. Even in fed-batch fermentation, when glucose concentration is maintained between 0.5 and 1.0 g/L, JM109 accumulates 4 times more acetate than BL21. To investigate the difference between the two strains, metabolites and enzymes involved in carbon utilization and acetate production were analyzed (isocitrate, ATP, phosphoenolpyruvate, pyruvate, isocitrate lyase, and isocitrate dehydrogenase). The results showed that during batch fermentation isocitrate lyase activity and isocitrate concentration were higher in BL21 than in JM109, while pyruvate concentration was higher in JM109. The activation of the glyoxylate shunt pathway at high glucose concentrations is suggested as a possible explanation for the lower acetate accumulation in E. coli BL21. Metabolic flux analysis of the batch cultures supports the activity of the glyoxylate shunt in E. coli BL21.     

Unique biosynthesis of dehydroquinic acid?

A search of the genomic sequences of the thermophilic microorganisms Aquifex aeolicus, Archaeoglobus fulgidus, Methanobacterium thermoautotrophicum, and Methanococcus jannaschii for the first seven enzymes (aroG, B, D, E, K, A, and C ) involved in the shikimic acid biosynthetic pathway reveal two key enzymes are missing. The first enzyme in the pathway, 3-deoxy-d-arabino-heptulosonic acid 7-phosphate synthase (aroG) and the second enzyme in the pathway, 5-dehydroquinic acid synthase (aroB) are "missing." The remaining five genes for the shikimate pathway in these organism are present and are similar to the corresponding Escherichia coli genes. The genomic sequences of the thermophiles Pyrococcus abyssi and Thermotoga maritima contain the aroG and aroB genes. Several fungi such as Aspergillus fumigatus, Aspergillus nidulans, Saccharomyces cerevisiae, Schizosaccharomyces pombe, Pneumocystis carinii f. sp. carinii, and Neurospora crassa contain the gene aroM, a pentafunctional enzyme whose overall activity is equivalent to the combined catalytic activities of proteins expressed by aroB, D, E, K, and A genes. Two of these fungi also lack an aroG gene. A discussion of potential reasons for these missing enzymes is presented.     

氨基酸对禾粟链霉菌生物合成ε-聚赖氨酸的影响

为了探索氨基酸对Streptomyces graminearus LS-B1以葡萄糖发酵生产ε-聚赖氨酸(ε-PL)的影响,分别在发酵过程中添加了16种常见氨基酸.研究结果表明,苯丙氨酸(Phe)、精氨酸(Arg)、酪氨酸(Tyr)、甘氨酸(Gly)、天冬酰胺(Asn)、色氨酸(Try)6种氨基酸对ε-PL合成有一定的...     

Shikimic acid production by a modified strain of E. coli (W3110.shik1) under phosphate-limited and carbon-limited conditions

Shikimic acid is one of several industrially interesting chiral starting materials formed in the aromatic amino acid pathway of plants and microorganisms. In this study, the physiology of a shikimic acid producing strain of Escherichia coli (derived from W3110) deleted in aroL (shikimic acid kinase II gene), was compared to that of a corresponding control strain (W3110) under carbon- and phosphate-limited conditions. For the shikimic acid producing strain (referred to as W3110.shik1), phosphate limitation resulted in a higher yield of shikimic acid (0.059 +/- 0.012 vs. 0.024 +/- 0.005 c-mol/c-mol) and a lower yield of by-products from the shikimate pathway, when compared to carbon-limited condition. The yield of the by-product 3-dehydroshikimic acid (DHS) decreased from 0.076 +/- 0.028 to 0.022 +/- 0.001 c-mol/c-mol. Several other by-products were only detected under carbon-limited conditions. The latter group included 3-dehydroquinic acid (0.021 +/- 0.021 c-mol/c-mol), quinic acid (0.012 +/- 0.005 c-mol/c-mol), and gallic acid (0.002 +/- 0.001 c-mol/c-mol). For both strains, more acetate was produced under phosphate than the carbon-limited case. Considerable cell lysis was found for both strains but was higher for W3110.shik1, and increased for both strains under phosphate limitation. The advantages of the latter condition in terms of an increased shikimic acid yield was thus counteracted by an increased cell lysis, which may make downstream processing more difficult.     

Non-light-dependent Shikimate Pathway in Plastids from Pea Roots

Non-green plastids (leucoplasts) isolated from pea roots are shown to be considerably active in forming aromatic amino acids by the shikimate pathway which, in contrast to the chloroplast pathway, is independent of light. Supply of phosphoenolpyruvate and 3-dehydroquinate, 3-dehydroshikimate, shikimate and quinate effectively enhances the formation of aromatic amino acids suggesting an intra- or/and intercellular intermediate transport.     

MFA for overdetermined systems reviewed and compared with rna expression data to elucidate the difference in shikimate yield between carbon- and phosphate-limited continuous cultures of E. coli W3110.shik1

The present contribution focuses on the mathematical techniques used to solve steady state metabolic models for the case of an overdetermined system. Even when parts of the system are underdetermined it is possible to solve the model partially and obtain statistically meaningful results. This is illustrated with data gathered from a set of E. coli W3110.shik1 phosphate- or carbon-limited continuous cultures. It is shown that the low yield in shikimate for C-limited cultures is not due to a lower flux going to the shikimate pathway but is caused by a high secretion of byproducts. Carbon-limited cultures could be better for shikimate production than carbon-abundant cultures provided the byproduct secretion is reduced. Finally, flux calculations are compared with RNA expression data.