Butanol production from glycerol by recombinant Escherichia coli

Escherichia coli MG1655 (DE3) with the ability to synthesize butanol from glycerol was constructed by metabolic engineering. The genes thil, adhe2, bcs operon (crt, bcd, etfB, etfA, and hbd) were cloned into the plasmid vectors, pETDuet-1 and pACYCDuet-1, then the two resulting plasmids, pACYC-thl-bcs and pET-adhe2, were transferred to E. coli, and the recombinant strain was able to synthesize up to 18.5 mg/L butanol on a glycerol-containing medium. After the glycerol transport protein gene GlpF was expressed, the butanol production was improved to 22.7 mg/L. The competing pathway of byproducts, such as ethanol, succinate, and lactate, was subsequently deleted to improve the 1-butanol production to 97.9 mg/L. Moreover, a NADH regeneration system was introduced into the E. coli, and finally a 154.0 mg/L butanol titer was achieved in a laboratory-scale shake-flask experiment.     

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。     

Engineering the productivity of recombinant Escherichia coli for limonene formation from glycerol in minimal media

The efficiency and productivity of cellular biocatalysts play a key role in the industrial synthesis of fine and bulk chemicals. This study focuses on optimizing the synthesis of (S)‐limonene from glycerol and glucose as carbon sources using recombinant Escherichia coli. The cyclic monoterpene limonene is extensively used in the fragrance, food, and cosmetic industries. Recently, limonene also gained interest as alternative jet fuel of biological origin. Key parameters that limit the (S)‐limonene yield, related to genetics, physiology, and reaction engineering, were identified. The growth‐dependent production of (S)‐limonene was shown for the first time in minimal media. E. coli BL21 (DE3) was chosen as the preferred host strain, as it showed low acetate formation, fast growth, and high productivity. A two‐liquid phase fed‐batch fermentation with glucose as the sole carbon and energy source resulted in the formation of 700 mg L_org^–1 (S)‐limonene. Specific activities of 75 mU g_cdw^–1 were reached, but decreased relatively quickly. The use of glycerol as a carbon source resulted in a prolonged growth and production phase (specific activities of ≥50 mU g_cdw^–1) leading to a final (S)‐limonene concentration of 2,700 mg L_org^–1. Although geranyl diphosphate (GPP) synthase had a low solubility, its availability appeared not to limit (S)‐limonene formation in vivo under the conditions investigated. GPP rerouting towards endogenous farnesyl diphosphate (FPP) formation also did not limit (S)‐limonene production. The two‐liquid phase fed‐batch setup led to the highest monoterpene concentration obtained with a recombinant microbial biocatalyst to date.     

产1，3-丙二醇重组大肠杆菌JM109（pEtac—dhaB—tac—yqhD）的构建

在生物柴油的生产过程中,最高可得到约10％的副产物甘油,副产物甘油的去向将成为生物柴油大规模产业化发展所面临的严峻问题。以生物柴油副产物甘油为原料耦合生产1,3-丙二醇,不仅解决了生物柴油副产物甘油的出路问题,同时降低了1,3-丙二醇的生产成本。本研究在前期工作的基础上,分别获得了来源于肺炎克雷伯氏茵的甘油脱水酶编码基因dhaB和来源于大肠杆菌的1,3-PD氧化还原酶同工酶编码基因yqhD,利用表达载体pEtac串联构建了重组质粒pEtac—dhaB—tac—yqhD,将其转化大肠杆菌得到产1,3-丙二醇重组大肠杆菌JM109（pEtac—dhaB-tac—yqhD）,降低了代谢中间产物3-羟基丙醛的积累,提高了1,3-丙二醇的产量。     

Heterologous expression and characterization of recombinant glycerol dehydratase from Klebsiella pneumoniae in Escherichia coli

Glycerol dehydratase (EC 4.2.1.30), as one of the key enzymes in converting glycerol to the valuable intermediate 1,3-propanediol, is important for biochemical industry. The dhaB genes encoding coenzyme B(12)-dependent glycerol dehydratase in Klebsiella pneumoniae were cloned and expressed in Escherichia coli. An effective co-expression system of multiple subunits protein was constructed. Heterologous expression vectors were constructed using the splicing by overlap extension-PCR technique to co-express the three subunits of the glycerol dehydratase. After induction by isopropyl-beta-D-thiogalactopyranoside, SDS-PAGE analysis revealed that: (i) only the alpha subunit of glycerol dehydratase was expressed in direct expression system, (ii) the three subunits of glycerol dehydratase with predicted molecular massess of 64 (agr;), 22 (beta), and 16 kDa (gamma) were expressed simultaneously in co-expression system, and (iii) the fusion expression system expressed the fusion protein of 99 kDa. Enzyme assay showed that the activities of three heterologous expression products were 27.4, 2.3, and 0.2 U/mg. The highest enzyme activity was almost 17 times of that in K. pneumoniae. The recombinant enzyme was purified and biochemically characterized. The apparent Km values of the enzyme for coenzyme B(12) and 1, 2-propanediol were 8.5 nM and 1.2 mM, respectively. The enzyme showed maximum activity at pH 8.5 and 37 degrees C.     

以甘油为底物利用重组大肠杆菌生产聚3-羟基丙酸

【目的】解决前期研究中所构建的以甘油为底物合成聚3-羟基丙酸(P3HP)的代谢途径中存在两个主要的问题——细胞内还原力不平衡和质粒丢失,以提高P3HP的产量。【方法】克隆来源于肺炎克雷伯氏菌的1,3-丙二醇(1,3-PDO)氧化还原酶基因,构建P3HP和1,3-PDO联产的菌株,解决细胞内还原力不平衡的问题。利用自杀性载体系统介导的同源重组技术,将甘油脱水酶及其激活因子的基因整合到大肠杆菌基因组中,提高质粒的稳定性。同时,对发酵条件进行优化。【结果】菌种改造和发酵条件优化显著提高了P3HP产量,在摇瓶条件下到达2.7 g/L,比以前的报道提高2倍,并可同时得到2.4 g/L 1,3-PDO。【结论】该重组大肠杆菌合成P3HP的产量得到提高,具有较好的工业化生产前景。     

产普鲁兰酶重组大肠杆菌质粒稳定性的研究

通过对产普鲁兰酶的重组大肠杆菌E.coli BL21(DE3)/p ET28a-s-pul菌株在发酵过程中质粒稳定性和普鲁兰酶生成量的考察,发现不同宿主对质粒稳定性及酶活性有重要影响。本文利用E.coli BL21(DE3)p Lys S菌株为宿主,构建重组菌E.coli BL21(DE3)p Lys S/p ET28a-s-pul,通过控制外源蛋白的本底表达,提高了重组菌株的质粒稳定性。优化发酵培养基和发酵条件以后,重组菌产普鲁兰酶能力由480 U/m L提高至627 U/m L,增幅为30.6%。研究结果认为,严格控制外源蛋白的本底表达,是改善重组菌稳定性的重要方法之一。     

Activity of recombinant GST in Escherichia coli grown on glucose and glycerol

We have investigated production, solubility and activity of recombinant glutathione-S-transferase (GST) expressed in Escherichia coli BL21 grown in defined media with glucose or glycerol as carbon source. GST was predominantly expressed as a soluble protein on both carbon sources, and 83–84% was found in the supernatant after cell lysis. In cultures grown on glucose, only 32 ± 9% of the GST was active, while 76 ± 13% of the GST was active in cultures grown on glycerol. This shows that glycerol has the potential to increase the activity of soluble GST in E. coli cultures in vivo.     

Proteome analysis of recombinant Escherichia coli producing human glucagon-like peptide-1

The proteomic response of recombinant Escherichia coli producing human glucagon-like peptide-1 was analyzed by two-dimensional gel electrophoresis. Protein spots in two-dimensional gel could be identified by using matrix-assisted laser desorption/ionization time-of-flight mass spectrometry and their expression profiles were compared with those of nonproducing cells. Thirty-five intracellular proteins exhibited differential expression levels between the production and control strains. These changes reflected physiological responses to heterologous peptide production in recombinant E. coli. Specifically, physiological changes included the down-regulation of proteins involved in the central carbon metabolism, biosynthesis of cellular building blocks and peptides, and up-regulation of cell protection proteins and some sugar transport proteins. This comprehensive analysis would provide useful information for understanding physiological alterations to heterologous peptide production and for designing efficient metabolic engineering strategies for the production of recombinant peptides in E. coli.     

Overproduction of alkaline polygalacturonate lyase in recombinant Escherichia coli by a two-stage glycerol feeding approach

This work aims to achieve the overproduction of alkaline polygalacturonate lyase (PGL) with recombinant Escherichia coli by a two-stage glycerol feeding approach. First, the PGL coding gene from Bacillus subtilis WSHB04-02 was expressed in E. coli BL21 (DE3) under the strong inducible T7 promoter of the pET20b (+) vector. And then the influence of media composition, induction temperature, and inducer isopropyl β-D-1-thiogalactopyranoside (IPTG) concentration on cell growth and PGL production was investigated. Finally, a two-stage glycerol feeding strategy was proposed and applied in a 3-L fermenter, where cultivation was conducted at a controlled specific growth rate (μset=0.2) during pre-induction phase, followed by a constant glycerol feeding rate of 12 ml h(-1) at post-induction phase. The total PGL yield reached 371.86 U mL(-1), which is the highest PGL production by recombinant E. coli expression system.     

Purification of streptomycin adenylyltransferase from a recombinant Escherichia coli

Bacterial resistance to aminoglycosides continues to escalate and is widely recognized as a serious health threat, contributing to interest in understanding the mechanisms of resistance. One important mechanism of streptomycin modification is through ATP dependent O-adenylation, catalyzed by streptomycin adenylyltransferase (SMATase). The aim of this study was to purify the recombinant SMATase by Ni(2+)-IDA-His bind resin column chromatography. Thioredoxin-His6-tagged SMATase fusion protein was produced in a bacterial intracellular expression system mainly in a soluble form. The purified fusion protein showed a single band on SDS-PAGE corresponding to 49 kDa. The recovery of fusion protein was 47% with ninefold purification. The fusion system provided a single step, easy and very rapid purification of SMATase and is suitable for obtaining a highly purified functional protein of interest. The fusion does not affect the functionality of the protein.     

Overexpression of a recombinant gamma-glutamyltranspeptidase from Escherichia coli Novablue

A truncated Escherichia coli Novablue gamma-glutamyltranspeptidase (EcGGT) gene, lacking the first 48-bp coding sequence for part of the signal sequence, was amplified by polymerase chain reaction (PCR) and cloned into expression vector pQE-30 to generate pQE-EcGGT. The maximum production of His6-tagged enzyme by E. coli M15 (pQE-EcGGT) was achieved with 0.1 mM IPTG induction for 12 h at 20 degrees C. The overexpressed enzyme was purified to homogeneity by nickel-chelate chromatography to a specific transpeptidase activity of 4.25 U/mg protein and a final yield of 83%. The molecular masses of the subunits of the purified enzyme were determined to be 41 and 21 kDa respectively by SDS-PAGE, indicating the precursor EcGGT still undergoes the post-translational processing even in the truncation of signal sequence. His6-tagged EcGGT migrated relative to the molecular mass of approximately 120 kDa and its heterodimeric structure was confirmed by a native-PAGE gel.     

Production and characterization of Escherichia coli glycerol dehydrogenase as a tool for glycerol recycling

NAD⁺-dependent glycerol (Gro) dehydrogenase (GroDHase) catalyzes the conversion of Gro into dihydroxyacetone (DHA), the first step for fermentative Gro metabolism in Escherichia coli. In this work, we cloned the gldA gene that codes for the E. coli GroDHase and homologously expressed, purified, and kinetically characterized the recombinant protein. To achieve this, the enzyme was over-produced using Gro supplemented growth medium and lactose as the inducer. The enzyme was highly purified using either pseudo-affinity chromatography or a simple heat-shock treatment, which is potentially valuable for industrial production of GroDHase. We detected efficient oxidation of Gro derived from biodiesel production to DHA by gas chromatography. The results presented in this work support recombinant GroDHase production in a biorefinery setting as a relevant tool for converting Gro into DHA for future biotechnological applications.     

Measurement of crude-cell-extract glycerol dehydratase activity in recombinant Escherichia coli using coupled-enzyme reactions

Journal of Industrial Microbiology & Biotechnology - Glycerol dehydratase (GDHt), which converts glycerol to 3-hydroxypropionaldehyde, is essential to the production of 1,3-propanediol...