Biotransformation of cinnamyl alcohol to rosavins by non-transformed wild type and hairy root cultures of Rhodiola kirilowii

Non-transformed wild type (NTWT) and hairy root cultures of Rhodiola kirilowii were grown in medium supplemented with 2.5 mM cinnamyl alcohol as a precursor and/or sucrose (1 %) on the day of inoculation or on the 14th day of culture. Rosarin, rosavin, and rosin were produced by NTWT root culture but only rosarin and rosavin by hairy roots. Approximately 80 and 95 % of the glycosides were released into the medium for NTWT and hairy root cultures, respectively. The highest rosavin yield, 505 ± 106 mg/l, was in hairy root culture when cinnamyl alcohol was applied on the day of inoculation with the addition of sucrose on the 14th day of culture. For rosin production, supplementation with cinnamyl alcohol alone on day 14 was more favourable with the highest amount 74 ± 10 mg/l in NTWT root culture. Only traces of rosarin were detected.     

Synthesis of Flavonoid O-Pentosides by Escherichia coli through Engineering of Nucleotide Sugar Pathways and Glycosyltransferase

Plants produce two flavonoid O-pentoses, flavonoid O-xyloside and flavonoid O-arabinoside. However, analyzing their biological properties is difficult because flavonoids are not naturally produced in sufficient quantities. In this study, Escherichia coli was used to synthesize the plant-specific flavonoid O-pentosides quercetin 3-O-xyloside and quercetin 3-O-arabinoside. Two strategies were used. First, E. coli was engineered to express components of the biosynthetic pathways for UDP-xylose and UDP-arabinose. For UDP-xylose biosynthesis, two genes, UXS (UDP-xylose synthase) from Arabidopsis thaliana and ugd (UDP-glucose dehydrogenase) from E. coli, were overexpressed. In addition, the gene encoding ArnA (UDP-l-Ara4N formyltransferase/UDP-GlcA C-4″-decarboxylase), which competes with UXS for UDP-glucuronic acid, was deleted. For UDP-arabinose biosynthesis, UXE (UDP-xylose epimerase) was overexpressed. Next, we engineered UDP-dependent glycosyltransferases (UGTs) to ensure specificity for UDP-xylose and UDP-arabinose. The E. coli strains thus obtained synthesized approximately 160 mg/liter of quercetin 3-O-xyloside and quercetin 3-O-arabinoside.     

Production of 3-O-xylosyl quercetin in Escherichia coli

Quercetin, a flavonol aglycone, is one of the most abundant flavonoids with high medicinal value. The bioavailability and pharmacokinetic properties of quercetin are influenced by the type of sugars attached to the molecule. To efficiently diversify the therapeutic uses of quercetin, Escherichia coli was harnessed as a production factory by the installation of various plant and bacterial UDP-xylose sugar biosynthetic genes. The genes encoding for the UDP-xylose pathway enzymes phosphoglucomutase (nfa44530), glucose-1-phosphate uridylyltransferase (galU), UDP-glucose dehydrogenase (calS8), and UDP-glucuronic acid decarboxylase (calS9) were overexpressed in E. coli BL21 (DE3) along with a glycosyltransferase (arGt-3) from Arabidopsis thaliana. Furthermore, E. coli BL21(DE3)/?pgi, E. coli BL21(DE3)/?zwf, E. coli BL21(DE3)/?pgi?zwf, and E. coli BL21(DE3)/?pgi?zwf?ushA mutants carrying the aforementioned UDP-xylose sugar biosynthetic genes and glycosyltransferase and the galU-integrated E. coli BL21(DE3)/?pgi host harboring only calS8, calS9, and arGt-3 were constructed to enhance whole-cell bioconversion of exogeneously supplied quercetin into 3-O-xylosyl quercetin. Here, we report the highest production of 3-O-xylosyl quercetin with E. coli BL21 (DE3)/?pgi?zwf?ushA carrying UDP-xylose sugar biosynthetic genes and glycosyltransferase. The maximum concentration of 3-O-xylosyl quercetin achieved was 23.78 mg/L (54.75 μM), representing 54.75 % bioconversion, which was an ~4.8-fold higher bioconversion than that shown by E. coli BL21 (DE3) with the same set of genes when the reaction was carried out in 5-mL culture tubes with 100 μM quercetin under optimized conditions. Bioconversion was further improved by 98 % when the reaction was scaled up in a 3-L fermentor at 36 h.     

3个植物源苯甲醇酰基转移酶合成乙酸肉桂酯的研究

[背景]乙酸肉桂酯是一种重要的香料化合物,在化妆品和食品工业上具有广泛的应用,传统的生产方法主要依靠植物提取和化学合成。[目的]通过筛选不同植物源的酰基转移酶,利用大肠杆菌从头合成乙酸肉桂酯。[方法]首先,通过在苯丙氨酸高产菌BPHE中表达异源基因苯丙氨酸解氨酶(Phenylalanine Ammonia-Lyase from Arabidopsis thaliana,AtPAL)、对羟基肉桂酰辅酶A连接酶(Hydroxycinnamate:CoA Ligase from Petroselinum crispum,Pc4CL)和肉桂酰辅酶 A 还原酶(Cinnamyl-CoA Reductase from Arabidopsis thaliana,AtCCR),并结合大肠杆菌自身的内源性醇脱氢酶(Alcohol Dehydrogenases,ADHs)或醛酮还原酶(Aldo-Keto Reductases,AKRs)的催化作用构建了从苯丙氨酸到肉桂醇的生物合成途径。然后,苯甲醇苯甲酰转移酶(Benzyl Alcohol O-Benzoyltransferase from Nicotiana tabacum,ANN09798;Benzyl Alcohol O-Benzoyltransferase from Clarkia breweri,ANN09796)或苯甲醇乙酰转移酶(Benzyl Alcohol Acetyltransferase from Clarkia breweri,BEAT)被引入到上述重组大肠杆菌中发酵培养生产乙酸肉桂酯。最后,在大肠杆菌中过表达乙酰辅酶A合成酶(Acetyl Coenzyme A Synthetase,ACS)来提高底物乙酰辅酶A的量。[结果]探讨了 3个植物源苯甲醇酰基转移酶生物合成乙酸肉桂酯的能力,并应用于合成乙酸肉桂酯的细胞工厂,最终使乙酸肉桂酯最高产量达到166.9±6.6mg/L。[结论]植物源苯甲醇酰基转移酶具有一定的底物宽泛性,能以肉桂醇为底物催化合成乙酸肉桂酯。首次利用植物源的苯甲醇酰基转移酶合成乙酸肉桂酯,为微生物细胞工厂以葡萄糖作为碳源生产乙酸肉桂酯提供参考。     

Biosynthesis of (R)‐(+)‐perillyl alcohol by Escherichia coli expressing neryl pyrophosphate synthase

(R)‐(+)‐perillyl alcohol is widely used in agricultural and anticarcinogenic fields. Microbial production of (R)‐(+)‐perillyl alcohol was investigated in this study. We optimized biosynthesis of (R)‐(+)‐perillyl alcohol in Escherichia coli by using neryl pyrophosphate synthase and NADPH regeneration. Engineering neryl pyrophosphate (NPP)‐supplied pathway resulted in a 4‐fold improvement of (R)‐(+)‐perillyl alcohol titer. Subsequently, combined engineering of p‐cymene monooxygenase (CymA) expression and module for NADPH regeneration exhibited a 15.4‐fold increase of titer over the initial strain S02. Finally, 453 mg/L (R)‐(+)‐perillyl alcohol was achieved in fed‐batch fermentation, which is the highest (R)‐(+)‐perillyl alcohol titer in E. coli.     

Engineered heterologous FPP synthases-mediated Z,E-FPP synthesis in E. coli

Production of Z-type farnesyl diphosphate (FPP) has not been reported in Escherichia coli. Here we present the fusion enzyme (ILRv) of E. coli E,E-FPP synthase (IspA) and Mycobacterium tuberculosis Z,E-FPP synthase (Rv1086), which can produce primarily Z,E-FPP rather than E,E-FPP, the predominant stereoisomer found in most organisms. Z,E-farnesol (FOH) was produced from E. coli harboring the bottom portion of the MVA pathway and the fusion FPP synthase (ILRv) at a titer of 115.6 mg/L in 2 YT medium containing 1% (v/v) glycerol as a carbon source and 5 mM mevalonate. The Z,E-FOH production was improved by 15-fold, compared with 7.7 mg/L obtained from the co-overexpression of separate IspA and Rv1086. The Z,E-FPP was not metabolized in native metabolic pathways of E. coli. It would be of interest to produce Z,E-FPP derived sesquiterpenes from recombinant E. coli due to no loss of Z,E-FPP substrate in endogenous metabolism of the host strain.     

Identification of a Bifunctional UDP-4-keto-pentose/UDP-xylose Synthase in the Plant Pathogenic Bacterium Ralstonia solanacearum Strain GMI1000, a Distinct Member of the 4,6-Dehydratase and Decarboxylase Family

The UDP-sugar interconverting enzymes involved in UDP-GlcA metabolism are well described in eukaryotes but less is known in prokaryotes. Here we identify and characterize a gene (RsU4kpxs) from Ralstonia solanacearum str. GMI1000, which encodes a dual function enzyme not previously described. One activity is to decarboxylate UDP-glucuronic acid to UDP-β-l-threo-pentopyranosyl-4″-ulose in the presence of NAD⁺. The second activity converts UDP-β-l-threo-pentopyranosyl-4″-ulose and NADH to UDP-xylose and NAD⁺, albeit at a lower rate. Our data also suggest that following decarboxylation, there is stereospecific protonation at the C5 pro-R position. The identification of the R. solanacearum enzyme enables us to propose that the ancestral enzyme of UDP-xylose synthase and UDP-apiose/UDP-xylose synthase was diverged to two distinct enzymatic activities in early bacteria. This separation gave rise to the current UDP-xylose synthase in animal, fungus, and plant as well as to the plant Uaxs and bacterial ArnA and U4kpxs homologs.     

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.     

Engineering cofactor and transport mechanisms in Saccharomyces cerevisiae for enhanced acetyl-CoA and polyketide biosynthesis

Synthesis of polyketides at high titer and yield is important for producing pharmaceuticals and biorenewable chemical precursors. In this work, we engineered cofactor and transport pathways in Saccharomyces cerevisiae to increase acetyl-CoA, an important polyketide building block. The highly regulated yeast pyruvate dehydrogenase bypass pathway was supplemented by overexpressing a modified Escherichia coli pyruvate dehydrogenase complex (PDHm) that accepts NADP⁺ for acetyl-CoA production. After 24 h of cultivation, a 3.7-fold increase in NADPH/NADP⁺ ratio was observed relative to the base strain, and a 2.2-fold increase relative to introduction of the native E. coli PDH. Both E. coli pathways increased acetyl-CoA levels approximately 2-fold relative to the yeast base strain. Combining PDHm with a ZWF1 deletion to block the major yeast NADPH biosynthesis pathway resulted in a 12-fold NADPH boost and a 2.2-fold increase in acetyl-CoA. At 48 h, only this coupled approach showed increased acetyl-CoA levels, 3.0-fold higher than that of the base strain. The impact on polyketide synthesis was evaluated in a S. cerevisiae strain expressing the Gerbera hybrida 2-pyrone synthase (2-PS) for the production of the polyketide triacetic acid lactone (TAL). Titers of TAL relative to the base strain improved only 30% with the native E. coli PDH, but 3.0-fold with PDHm and 4.4-fold with PDHm in the Δzwf1 strain. Carbon was further routed toward TAL production by reducing mitochondrial transport of pyruvate and acetyl-CoA; deletions in genes POR2, MPC2, PDA1, or YAT2 each increased titer 2–3-fold over the base strain (up to 0.8 g/L), and in combination to 1.4 g/L. Combining the two approaches (NADPH-generating acetyl-CoA pathway plus reduced metabolite flux into the mitochondria) resulted in a final TAL titer of 1.6 g/L, a 6.4-fold increase over the non-engineered yeast strain, and 35% of theoretical yield (0.16 g/g glucose), the highest reported to date. These biological driving forces present new avenues for improving high-yield production of acetyl-CoA derived compounds.     

Metabolic engineering of Escherichia coli for limonene and perillyl alcohol production

Limonene is a valuable monoterpene used in the production of several commodity chemicals and medicinal compounds. Among them, perillyl alcohol (POH) is a promising anti-cancer agent that can be produced by hydroxylation of limonene. We engineered E. coli with a heterologous mevalonate pathway and limonene synthase for production of limonene followed by coupling with a cytochrome P450, which specifically hydroxylates limonene to produce POH. A strain containing all mevalonate pathway genes in a single plasmid produced limonene at titers over 400 mg/L from glucose, substantially higher than has been achieved in the past. Incorporation of a cytochrome P450 to hydroxylate limonene yielded approximately 100 mg/L of POH. Further metabolic engineering of the pathway and in situ product recovery using anion exchange resins would make this engineered E. coli a potential production platform for any valuable limonene derivative.     

Adaptive evolution of nontransgenic <Emphasis Type="Italic">Escherichia coli</Emphasis> KC01 for improved ethanol tolerance and homoethanol fermentation from xylose

Due to its excellent capability to ferment five-carbon sugars, Escherichia coli has been considered one of the platform organisms to be engineered for production of cellulosic ethanol. Nevertheless, genetically engineered ethanologenic E. coli lacks the essential trait of alcohol tolerance. Development of ethanol tolerance is required for cost-effective ethanol fermentation. In this study, we improved alcohol tolerance of a nontransgenic E. coli KC01 (ldhA pflB ackA frdBC pdhR::pflBp6-aceEF-lpd) through adaptive evolution. During ~350 generations of adaptive evolution, a gradually increased concentration of ethanol was used as a selection pressure to enrich ethanol-tolerant mutants. The evolved mutant, E. coli SZ470, was able to grow anaerobically at 40 g l⁻¹ ethanol, a twofold improvement over parent KC01. When compared with KC01 for small-scale (500 ml) xylose (50 g l⁻¹) fermentation, SZ470 achieved 67% higher cell mass, 48% faster volumetric ethanol productivity, and 50% shorter time to complete fermentation with ethanol titer of 23.5 g l⁻¹ and yield of 94%. These results demonstrate that an industry-oriented nontransgenic E. coli strain could be developed through incremental improvements of desired traits by a combination of molecular biology and traditional microbiology techniques.     

Metabolomics-driven approach to solving a CoA imbalance for improved 1-butanol production in Escherichia coli

High titer 1-butanol production in Escherichia coli has previously been achieved by overexpression of a modified clostridial 1-butanol production pathway and subsequent deletion of native fermentation pathways. This strategy couples growth with production as 1-butanol pathway offers the only available terminal electron acceptors required for growth in anaerobic conditions. With further inclusion of other well-established metabolic engineering principles, a titer of 15 g/L has been obtained. In achieving this titer, many currently existing strategies have been exhausted, and 1-butanol toxicity level has been surpassed. Therefore, continued engineering of the host strain for increased production requires implementation of alternative strategies that seek to identify non-obvious targets for improvement. In this study, a metabolomics-driven approach was used to reveal a CoA imbalance resulting from a pta deletion that caused undesirable accumulation of pyruvate, butanoate, and other CoA-derived compounds. Using metabolomics, the reduction of butanoyl-CoA to butanal catalyzed by alcohol dehydrogenase AdhE2 was determined as a rate-limiting step. Fine-tuning of this activity and subsequent release of free CoA restored the CoA balance that resulted in a titer of 18.3 g/L upon improvement of total free CoA levels using cysteine supplementation. By enhancing AdhE2 activity, carbon flux was directed towards 1-butanol production and undesirable accumulation of pyruvate and butanoate was diminished. This study represents the initial report describing the improvement of 1-butanol production in E. coli by resolving CoA imbalance, which was based on metabolome analysis and rational metabolic engineering strategies.     

Engineering Saccharomyces cerevisiae for isoprenol production

Isoprenol (3-methyl-3-butene-1-ol) is a valuable drop-in biofuel and an important precursor of several commodity chemicals. Synthetic microbial systems using the heterologous mevalonate pathway have recently been developed for the production of isoprenol in Escherichia coli, and a significant yield and titer improvement has been achieved through a decade of research. Saccharomyces cerevisiae has been widely used in the biotechnology industry for isoprenoid production, but there has been no good example of isoprenol production reported in this host. In this study, we engineered the budding yeast S. cerevisiae for improved biosynthesis of isoprenol. The strain engineered with the mevalonate pathway achieved isoprenol production at the titer of 36.02 ± 0.92 mg/L in the flask. The IPP (isopentenyl diphosphate)-bypass pathway, which has shown more efficient isoprenol production by avoiding the accumulation of the toxic intermediate in E. coli, was also constructed in S. cerevisiae and improved the isoprenol titer by 2-fold. We further engineered the strains by deleting a promiscuous endogenous kinase that could divert the pathway flux away from the isoprenol production and improved the titer to 130.52 ± 8.01 mg/L. Finally, we identified a pathway bottleneck using metabolomics analysis and overexpressed a promiscuous alkaline phosphatase to relieve this bottleneck. The combined efforts resulted in the titer improvement to 383.1 ± 31.62 mg/L in the flask. This is the highest isoprenol titer up to date in S. cerevisiae and this work provides the key strategies to engineer yeast as an industrial platform for isoprenol production.     

Engineering Escherichia coli for the synthesis of short- and medium-chain α,β-unsaturated carboxylic acids

Concerns over sustained availability of fossil resources along with environmental impact of their use have stimulated the development of alternative methods for fuel and chemical production from renewable resources. In this work, we present a new approach to produce α,β-unsaturated carboxylic acids (α,β-UCAs) using an engineered reversal of the β-oxidation (r-BOX) cycle. To increase the availability of both acyl-CoAs and enoyl-CoAs for α,β-UCA production, we use an engineered Escherichia coli strain devoid of mixed-acid fermentation pathways and known thioesterases. Core genes for r-BOX such as thiolase, hydroxyacyl-CoA dehydrogenase, enoyl-CoA hydratase, and enoyl-CoA reductase were chromosomally overexpressed under the control of a cumate inducible phage promoter. Native E. coli thioesterase YdiI was used as the cycle-terminating enzyme, as it was found to have not only the ability to convert trans-enoyl-CoAs to the corresponding α,β-UCAs, but also a very low catalytic efficiency on acetyl-CoA, the primer and extender unit for the r-BOX pathway. Coupling of r-BOX with YdiI led to crotonic acid production at titers reaching 1.5 g/L in flask cultures and 3.2 g/L in a controlled bioreactor. The engineered r-BOX pathway was also used to achieve for the first time the production of 2-hexenoic acid, 2-octenoic acid, and 2-decenoic acid at a final titer of 0.2 g/L. The superior nature of the engineered pathway was further validated through the use of in silico metabolic flux analysis, which showed the ability of r-BOX to support growth-coupled production of α,β-UCAs with a higher ATP efficiency than the widely used fatty acid biosynthesis pathway. Taken together, our findings suggest that r-BOX could be an ideal platform to implement the biological production of α,β-UCAs.     

Constructing an ethanol utilization pathway in Escherichia coli to produce acetyl-CoA derived compounds

Engineering microbes to utilize non-conventional substrates could create short and efficient pathways to convert substrate into product. In this study, we designed and constructed a two-step heterologous ethanol utilization pathway (EUP) in Escherichia coli by using acetaldehyde dehydrogenase (encoded by ada) from Dickeya zeae and alcohol dehydrogenase (encoded by adh2) from Saccharomyces cerevisiae. This EUP can convert ethanol into acetyl-CoA without ATP consumption, and generate two molecules of NADH per molecule of ethanol. We optimized the expression of these two genes and found that ethanol consumption could be improved by expressing them in a specific order (ada-adh2) with a constitutive promoter (PgyrA). The engineered E. coli strain with EUP consumed approximately 8 g/L of ethanol in 96 h when it was used as sole carbon source. Subsequently, we combined EUP with the biosynthesis of polyhydroxybutyrate (PHB), a biodegradable polymer derived from acetyl-CoA. The engineered E. coli strain carrying EUP and PHB biosynthetic pathway produced 1.1 g/L of PHB from 10 g/L of ethanol and 1 g/L of aspartate family amino acids in 96 h. We also engineered a E. coli strain to produce 24 mg/L of prenol in an ethanol-containing medium, supporting the feasibility of converting ethanol into different classes of acetyl-CoA derived compounds.     

Cinnamyl alcohol: An attractant of the flower thrips Frankliniella intonsa

Flower-inhabiting thrips find hosts using olfactory and visual cues. In this study, we report the identification of a plant-produced attractant of the flower thrips Frankliniella intonsa (Trybom), an important agricultural pest worldwide. GC–MS analysis of solid-phase microextraction samples from blueberry flowers, Vaccinium corymbosum L., that mediate the attraction of adult F. intonsa revealed that the major component was cinnamyl alcohol, followed by cinnamyl acetate, cinnamaldehyde, germacrene D, β-bourbonene, β-caryophyllene, and benzyl benzoate. The biological activity of the floral compounds was investigated using commercial cinnamaldehyde, cinnamyl alcohol, β-caryophyllene, cinnamyl acetate, and benzyl benzoate in hot pepper (Capsicum annuum L.) fields. Significantly more F. intonsa males and females were caught in red delta traps with cinnamyl alcohol than in all other traps. Cinnamaldehyde and cinnamyl acetate attracted adult F. intonsa but were not as attractive as cinnamyl alcohol. β-Caryophyllene and benzyl benzoate were not attractive. Furthermore, the addition of four minor components to cinnamyl alcohol did not result in increased trap catches relative to cinnamyl alcohol alone, indicating that cinnamyl alcohol is responsible for attracting adult F. intonsa toward blueberry flowers. Therefore, this phenylpropanoid could be used as an effective lure for monitoring and controlling F. intonsa.     

Biosynthesis of two quercetin <Emphasis Type="Italic">O</Emphasis>-diglycosides in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Various flavonoid glycosides are found in nature, and their biological activities are as variable as their number. In some cases, the sugar moiety attached to the flavonoid modulates its biological activities. Flavonoid glycones are not easily synthesized chemically. Therefore, in this study, we attempted to synthesize quercetin 3-O-glucosyl (1→2) xyloside and quercetin 3-O-glucosyl (1→6) rhamnoside (also called rutin) using two uridine diphosphate-dependent glycosyltransferases (UGTs) in Escherichia coli. To synthesize quercetin 3-O-glucosyl (1→2) xyloside, sequential glycosylation was carried out by regulating the expression time of the two UGTs. AtUGT78D2 was subcloned into a vector controlled by a Tac promoter without a lacI operator, while AtUGT79B1 was subcloned into a vector controlled by a T7 promoter. UDP-xyloside was supplied by concomitantly expressing UDP-glucose dehydrogenase (ugd) and UDP-xyloside synthase (UXS) in the E. coli. Using these strategies, 65.0 mg/L of quercetin 3-O-glucosyl (1→2) xyloside was produced. For the synthesis of rutin, one UGT (BcGT1) was integrated into the E. coli chromosome and the other UGT (Fg2) was expressed in a plasmid along with RHM2 (rhamnose synthase gene 2). After optimization of the initial cell concentration and incubation temperature, 119.8 mg/L of rutin was produced. The strategies used in this study thus show promise for the synthesis of flavonoid diglucosides in E. coli.     

Production of mesaconate in Escherichia coli by engineered glutamate mutase pathway

Mesaconate is an intermediate in the glutamate degradation pathway of microorganisms such as Clostridium tetanomorphum. However, metabolic engineering to produce mesaconate has not been reported previously. In this work, two enzymes involved in mesaconate production, glutamate mutase and 3-methylaspartate ammonia lyase from C. tetanomorphum, were recombinantly expressed in Escherichia coli. To improve mesaconate production, reactivatase of glutamate mutase was discovered and adenosylcobalamin availability was increased. In addition, glutamate mutase was engineered to improve the in vivo activity. These efforts led to efficient mesaconate production at a titer of 7.81 g/L in shake flask with glutamate feeding. Then a full biosynthetic pathway was constructed to produce mesaconate at a titer of 6.96 g/L directly from glucose. In summary, we have engineered an efficient system in E. coli for the biosynthesis of mesaconate.     

Structure-guided reshaping of the acyl binding pocket of ‘TesA thioesterase enhances octanoic acid production in E. coli

Medium-chain fatty acids (C6–C10) have attracted much attention recently for their unique properties compared to their long-chain counterparts, including low melting points and relatively higher carbon conversion yield. Thioesterase enzymes, which can catalyze the hydrolysis of acyl-ACP (acyl carrier protein) to release free fatty acids (FAs), regulate both overall FA yields and acyl chain length distributions in bacterial and yeast fermentation cultures. These enzymes typically prefer longer chain substrates. Herein, seeking to increase bacterial production of MCFAs, we conducted structure-guided mutational screening of multiple residues in the substrate-binding pocket of the E. coli thioesterase enzyme ‘TesA. Confirming our hypothesis that enhancing substrate selectivity for medium-chain acyl substrates would promote overall MCFA production, we found that replacement of residues lining the bottom of the pocket with more hydrophobic residues strongly promoted the C8 substrate selectivity of ‘TesA. Specifically, two rounds of saturation mutagenesis led to the identification of the ‘TesA^RD−2 variant that exhibited a 133-fold increase in selectivity for the C8-ACP substrate as compared to C16-ACP substrate. Moreover, the recombinant expression of this variant in an E. coli strain with a blocked β-oxidation pathway led to a 1030% increase in the in vivo octanoic acid (C8) production titer. When this strain was fermented in a 5-L fed-batch bioreactor, it produced 2.7 g/L of free C8 (45%, molar fraction) and 7.9 g/L of total free FAs, which is the highest-to-date free C8 titer to date reported using the E. coli type II fatty acid synthetic pathway. Thus, reshaping the substrate binding pocket of a bacterial thioesterase enzyme by manipulating the hydrophobicity of multiple residues altered the substrate selectivity and therefore fatty acid product distributions in cells. Our study demonstrates the relevance of this strategy for increasing titers of industrially attractive MCFAs as fermentation products.