Efficient production of L-ribose with a recombinant Escherichia coli biocatalyst

A new synthetic platform with potential for the production of several rare sugars, with l-ribose as the model target, is described. The gene encoding the unique NAD-dependent mannitol-1-dehydrogenase (MDH) from Apium graveolens (garden celery) was synthetically constructed for optimal expression in Escherichia coli. This MDH enzyme catalyzes the interconversion of several polyols and their l-sugar counterparts, including the conversion of ribitol to l-ribose. Expression of recombinant MDH in the active form was successfully achieved, and one-step purification was demonstrated. Using the created recombinant E. coli strain as a whole-cell catalyst, the synthetic utility was demonstrated for production of l-ribose, and the system was improved using shaken flask experiments. It was determined that addition of 50 to 500 microM ZnCl(2) and addition of 5 g/liter glycerol both improved production. The final levels of conversion achieved were >70% at a concentration of 40 g/liter and >50% at a concentration of 100 g/liter. The best conditions determined were then scaled up to a 1-liter fermentation that resulted in 55% conversion of 100 g/liter ribitol in 72 h, for a volumetric productivity of 17.4 g liter(-1) day(-1). This system represents a significantly improved method for the large-scale production of l-ribose.     

Design of a recombinant Escherichia coli for producing l-phenylalanine from glycerol

A recombinant Escherichia coli was engineered to produce the commercially important amino acid L: -phenylalanine (L: -Phe) using glycerol as the carbon source. Compared to the conventionally used glucose and sucrose, glycerol is a less expensive carbon source. As phenylalanine dehydrogenase (PheDH) activity is involved in the last step of L: -Phe synthesis in E. coli, a phenylalanine dehydrogenase gene (phedh) from the thermotolerant Bacillus lentus was cloned into pRSFDuet-1 (pPheDH) and expressed in E. coli BL21(DE3). The resulting clone had a limited ability to produce L: -Phe from glycerol, possibly because of a poor glycerol uptake by the cell, or an inability to excrete L: -Phe, or both. Therefore, yddG gene encoding an aromatic amino acid exporter and glpF gene encoding a glycerol transport facilitator were coexpressed with the phedh in a reengineered E. coli. In a glycerol medium, the maximum L: -Phe production rates of the clones pPY (phedh and yddG genes) and pPYF (phedh, yddG and glpF genes) were 1.4- and 1.8-fold higher than the maximum production rate of the pPheDH clone. The better producing pPYF clone was further evaluated in a 5?l stirred-tank fermenter (37?°C, an aeration rate of 1 vvm, an agitation speed of 400?rpm). In the fermenter, the maximum concentration of L: -Phe (366?mg/l) was achieved in a much shorter period compared to in the shake flasks. In the latter, the highest titer of L: -Phe was only 76?% of the maximum value attained in the fermenter.     

一步法产1,3-丙二醇酿酒酵母基因工程菌的构建

1,3-丙二醇(1,3-PD)是一种重要的化工原料,发酵法生产1,3-PD是一条新颖且具有潜在竞争力的生产途径。本研究在前期工作的基础上,将分别来源于大肠杆菌和肺炎克雷伯氏菌的基因片段yqhD和dhaB串联表达,构建重组表达载体pYX212-zeocin-pGAP-yqhD-pGAP-dhaB;并得到重组酿酒酵母(Saccharomyces cerevisiae)W303-1A/pYX212-zeocin-pGAP-yqhD-pGAP-dhaB。该重组菌和对照S.cerevisiae分别以葡萄糖为底物摇瓶发酵72h后,重组酿酒酵母发酵液中1,3-PD含量约为1.5g/L;而对照菌株不产1,3-PD。以上结果表明本研究在国内首次成功构建了直接以葡萄糖为底物发酵生产1,3-PD的酿酒酵母基因工程菌。为进一步将dhaB、yqhD基因导入其他以葡萄糖为底物高产甘油的酵母宿主中表达,获得以葡萄糖为底物一步法发酵高产1,3-丙二醇工程菌打下了坚实的基础。     

Highly efficient biotransformation of eugenol to ferulic acid and further conversion to vanillin in recombinant strains of Escherichia coli

The vaoA gene from Penicillium simplicissimum CBS 170.90, encoding vanillyl alcohol oxidase, which also catalyzes the conversion of eugenol to coniferyl alcohol, was expressed in Escherichia coli XL1-Blue under the control of the lac promoter, together with the genes calA and calB, encoding coniferyl alcohol dehydrogenase and coniferyl aldehyde dehydrogenase of Pseudomonas sp. strain HR199, respectively. Resting cells of the corresponding recombinant strain E. coli XL1-Blue(pSKvaomPcalAmcalB) converted eugenol to ferulic acid with a molar yield of 91% within 15 h on a 50-ml scale, reaching a ferulic acid concentration of 8.6 g liter(-1). This biotransformation was scaled up to a 30-liter fermentation volume. The maximum production rate for ferulic acid at that scale was 14.4 mmol per h per liter of culture. The maximum concentration of ferulic acid obtained was 14.7 g liter(-1) after a total fermentation time of 30 h, which corresponded to a molar yield of 93.3% with respect to the added amount of eugenol. In a two-step biotransformation, E. coli XL1-Blue(pSKvaomPcalAmcalB) was used to produce ferulic acid from eugenol and, subsequently, E. coli(pSKechE/Hfcs) was used to convert ferulic acid to vanillin (J. Overhage, H. Priefert, and A. Steinbüchel, Appl. Environ. Microbiol. 65:4837-4847, 1999). This process led to 0.3 g of vanillin liter(-1), besides 0.1 g of vanillyl alcohol and 4.6 g of ferulic acid liter(-1). The genes ehyAB, encoding eugenol hydroxylase of Pseudomonas sp. strain HR199, and azu, encoding the potential physiological electron acceptor of this enzyme, were shown to be unsuitable for establishing eugenol bioconversion in E. coli XL1-Blue.     

Production of recombinant bacteriocin divercin V41 by high cell density <Emphasis Type="Italic">Escherichia coli</Emphasis> batch and fed-batch cultures

To increase the yield of heterologous production of the class II bacteriocin DvnRV41 with Escherichia coli Origami (DE3) (pLysS/pCR03), induction of bacteriocin gene expression was optimized by varying the inducer isopropyl beta-D-thiogalactopyranoside (IPTG) concentration (0-2 mM), and controlled batch and fed-batch cultures were tested on a 2-L scale. A concentration of 0.5 mM IPTG was found to be optimal for cell growth and bacteriocin production. Shake flask cultivation of E. coli Origami (DE3) (pLysS/pCR03) gave biomass and bacteriocin yields of 1.54 +/- 0.06 g cdw/l and 18 +/- 1 mg DvnRV41/l, respectively. Biomass (2.70 +/- 0.06 and 6.8 +/- 0.6 g cdw/l, respectively) and bacteriocin yields (30 and 74 mg DvnRV41 per liter, respectively) were both increased with batch and fed-batch compared to shake flask cultures. Bacteriocin yields reported in this study are among the highest published for other heterologous expression systems in shake flasks.     

Metabolic engineering of a 1,2-propanediol pathway in Escherichia coli

1,2-Propanediol (1,2-PD) is a major commodity chemical that is currently derived from propylene, a nonrenewable resource. A goal of our research is to develop fermentation routes to 1,2-PD from renewable resources. Here we report the production of enantiomerically pure R-1,2-PD from glucose in Escherichia coli expressing NADH-linked glycerol dehydrogenase genes (E. coli gldA or Klebsiella pneumoniae dhaD). We also show that E. coli overexpressing the E. coli methylglyoxal synthase gene (mgs) produced 1,2-PD. The expression of either glycerol dehydrogenase or methylglyoxal synthase resulted in the anaerobic production of approximately 0.25 g of 1,2-PD per liter. R-1,2-PD production was further improved to 0.7 g of 1,2-PD per liter when methylglyoxal synthase and glycerol dehydrogenase (gldA) were coexpressed. In vitro studies indicated that the route to R-1,2-PD involved the reduction of methylglyoxal to R-lactaldehyde by the recombinant glycerol dehydrogenase and the reduction of R-lactaldehyde to R-1, 2-PD by a native E. coli activity. We expect that R-1,2-PD production can be significantly improved through further metabolic and bioprocess engineering.     

酿酒酵母gpd1和hor2基因在大肠杆菌中的共表达

利用途径工程的方法,在大肠杆菌中构建一条新的产甘油的代谢途径。从酿酒酵母(Saccharomyces cerevisiae)克隆3-磷酸甘油脱氢酶基因(gpd1)和3-磷酸甘油酯酶基因(hor2),并将两个基因串连到启动子trc的下游,构建由trc启动子控制的能高效表达的多顺反子重组质粒pSE-gpd1-hor2,将重组质粒导入大肠杆菌BL21菌株中,构建得到的重组菌株GxB-gh能将葡萄糖转化为甘油。结果表明重组菌株GxB-gh以葡萄糖为底物进行发酵,甘油产量为46．67g／L,葡萄糖的转化率为42.87％。这为利用工程菌绿色生产甘油进行了前期的探索,也为进一步构建能生产1,3-丙二醇的工程菌打下了良好的基础。     

Production of Pseudomonas aeruginosa Rhamnolipid Biosurfactants in Heterologous Hosts

The high-level production of rhamnolipid biosurfactants is a unique feature of Pseudomonas aeruginosa and is strictly regulated in response to environmental conditions. The final step in rhamnolipid biosynthesis is catalyzed by the rhlAB genes encoding a rhamnosyltransferase. The expression of the cloned rhlAB genes was studied in heterologous hosts, either under the control of the rhlR and rhlI rhamnolipid regulatory elements or under the control of the tac promoter. A recombinant P. fluorescens strain harboring multiple plasmid-encoded copies of the rhamnolipid gene cluster produced rhamnolipids (0.25 g liter(sup-1)) when grown under nitrogen-limiting conditions. The highest yields (0.6 g liter(sup-1)) and productivities (24 mg liter(sup-1) h(sup-1)) were obtained in a recombinant Pseudomonas putida strain, KT2442, harboring promoterless rhlAB genes fused to the tac promoter on a plasmid. Active rhamnosyltransferase was synthesized, but no rhamnolipids were produced, by recombinant Escherichia coli upon induction of rhlAB gene expression.     

Effects of deregulation of methionine biosynthesis on methionine excretion in Escherichia coli

Several regulators of methionine biosynthesis have been reported in Escherichia coli, which might represent barriers to the production of excess l-methionine (Met). In order to examine the effects of these factors on Met biosynthesis and metabolism, deletion mutations of the methionine repressor (metJ) and threonine biosynthetic (thrBC) genes were introduced into the W3110 wild-type strain of E. coli. Mutations of the metK gene encoding S-adenosylmethionine synthetase, which is involved in Met metabolism, were detected in 12 norleucine-resistant mutants. Three of the mutations in the metK structural gene were then introduced into metJ and thrBC double-mutant strains; one of the resultant strains was found to accumulate 0.13 g/liter Met. Mutations of the metA gene encoding homoserine succinyltransferase were detected in alpha-methylmethionine-resistant mutants, and these mutations were found to encode feedback-resistant enzymes in a 14C-labeled homoserine assay. Three metA mutations were introduced, using expression plasmids, into an E. coli strain that was shown to accumulate 0.24 g/liter Met. Combining mutations that affect the deregulation of Met biosynthesis and metabolism is therefore an effective approach for the production of Met-excreting strains.     

产甘油假丝酵母产甘油关键酶基因在酿酒酵母中的表达

甘油是一种极其理想的耐高渗透压介质。利用PCR方法,从产甘油假丝酵母WL2002-5中扩增出了2个产甘油的关键酶基因GPD和GPP,分别编码3-磷酸甘油脱氢酶（glycerol 3-phosphate dehydrogenase, GPD）和3-磷酸甘油磷酸酶（glycerol 3-phosphate phosphatase, GPP）。利用T-Vector在Escherichia coli JM109中克隆得到大量的GPD和GPP基因,并成功构建了重组质粒pYX212-GPD和pYX212-GPP;通过LiAc转化法将重组质粒导入酿酒酵母Saccharomyces cerevisiae W303-1A。初步实验结果表明：发酵过程中pYX212-GPD/S. cerevisiae W303-1A的生物量高于pYX212-GPP/S. cerevisiae W303-1A和野生型S. cerevisiae W303-1A;发酵72h后,pYX212 GPD/S. cerevisiae W303-1A发酵液中甘油含量大约为12mmol/L,明显高于野生型S. cerevisiae W303-1A的甘油含量,而pYX212-GPP/S. cerevisiae W303-1A与野生型S. cerevisiae W303-1A在甘油含量上相差不大,均只有4mmol/L 左右。     

Improving the ethanol yield by reducing glycerol formation using cofactor regulation in Saccharomyces cerevisiae

To increase ethanol yield and decrease glycerol production in Saccharomyces cerevisiae, the strategies of direct cofactor-regulation were explored. During anaerobic batch fermentations, the yeast expressing Bacillus cereus gapN gene, encoding non-phosphorylating NADP(+)-dependent glyceraldehyde-3-phosphate dehydrognease, produced 73.8?g ethanol?l(-1), corresponding to 96% of theoretical maximum yield compared to 92% for the wild type. The yeast expressing Escherichia coli frdA gene encoding the NAD(+)-dependent fumarate reductase, exhibited a 22% (relative to the amount of substrate consumed) increase in glycerol yield in medium containing 2?g fumarate?l(-1). The yeast expressing mhpF gene, encoding acetylating NAD(+)-dependent acetaldehyde dehydrogenase, produced 74.5?g ethanol?l(-1), corresponding to 97.4% of theoretical maximum yield while glycerol decreased by 40% when acetic acid was added before inoculation. This strain represents a promising alternative for ethanol production with lignocellulosic hydrolysates where acetate is available at significant amounts.     

重组大肠杆菌生物转化甘油生产3-羟基丙酸

目的:以甘油为底物构建高效的3-羟基丙酸生产菌株。方法:以自身携带乙醛脱氢酶的E.coli BL21(DE3)plysS作为宿主,异源表达源自Klebsiella pneumoniae的甘油脱水酶基因dhaB。结果:重组菌E.coli HP获得的甘油脱水酶比活力在1.0mmol/L IPTG的诱导下达到了77.2 U/mg,摇瓶条件下,3-HP的最大产量为5.44 g/L,摩尔转化率为53%,该产量比目前报道的最高水平(4.4 g/L)提高了23.6%。结论:重组菌株E.coli HP实现了甘油向3-羟基丙酸(3-HP)的高效生物转化。     

Production of poly(3-hydroxybutyrate) by fed-batch culture of filamentation-suppressed recombinant Escherichia coli.

Recombinant Escherichia coli XL1-Blue harboring a high-copy-number plasmid containing the Alcaligenes eutrophus polyhydroxyalkanoate synthesis genes could efficiently synthesize poly(3-hydroxybutyrate) (PHB) in a complex medium containing yeast extract and tryptone but not in a defined medium. One of the reasons for the reduced PHB production in a defined medium was thought to be severe filamentation of cells in this medium. By overexpressing an essential cell division protein, FtsZ, in recombinant E. coli producing PHB, filamentation could be suppressed and PHB could be efficiently produced in a defined medium. A high PHB concentration of 149 g/liter, with high productivity of 3.4 g of PHB/liter/h, could be obtained by the pH-stat fed-batch culture of the filamentation-suppressed recombinant E. coli in a defined medium. It was also found that insufficient oxygen supply at a dissolved oxygen concentration (DOC) of 1 to 3% of air saturation during active PHB synthesis phase did not negatively affect PHB production. By growing cells to the concentration of 110 g/liter and then controlling the DOC in the range of 1 to 3% of air saturation, a PHB concentration of 157 g/liter and PHB productivity of 3.2 g of PHB/liter/h were obtained. For the scale-up studies, fed-batch culture was carried out in a 50-liter stirred tank fermentor, in which the DOC decreased to zero when cell concentration reached 50 g/liter. However, a relatively high PHB concentration of 101 g/liter and PHB productivity of 2.8 g of PHB/liter/h could still be obtained, which demonstrated the possibility of industrial production of PHB in a defined medium by employing the filamentation-suppressed recombinant E. coli.     

Identification and characterization of coenzyme B12-dependent glycerol dehydratase- and diol dehydratase-encoding genes from metagenomic DNA libraries derived from enrichment cultures

To isolate genes encoding coenzyme B(12)-dependent glycerol and diol dehydratases, metagenomic libraries from three different environmental samples were constructed after allowing growth of the dehydratase-containing microorganisms present for 48 h with glycerol under anaerobic conditions. The libraries were searched for the targeted genes by an activity screen, which was based on complementation of a constructed dehydratase-negative Escherichia coli strain. In this way, two positive E. coli clones out of 560,000 tested clones were obtained. In addition, screening was performed by colony hybridization with dehydratase-specific DNA fragments as probes. The screening of 158,000 E. coli clones by this method yielded five positive clones. Two of the plasmids (pAK6 and pAK8) recovered from the seven positive clones contained genes identical to those encoding the glycerol dehydratase of Citrobacter freundii and were not studied further. The remaining five plasmids (pAK2 to -5 and pAK7) contained two complete and three incomplete dehydratase-encoding gene regions, which were similar to the corresponding regions of enteric bacteria. Three (pAK2, -3, and -7) coded for glycerol dehydratases and two (pAK4 and -5) coded for diol dehydratases. We were able to perform high-level production and purification of three of these dehydratases. The glycerol dehydratases purified from E. coli Bl21/pAK2.1 and E. coli Bl21/pAK7.1 and the complemented hybrid diol dehydratase purified from E. coli Bl21/pAK5.1 were subject to suicide inactivation by glycerol and were cross-reactivated by the reactivation factor (DhaFG) for the glycerol dehydratase of C. freundii. The activities of the three environmentally derived dehydratases and that of glycerol dehydratase of C. freundii with glycerol or 1,2-propanediol as the substrate were inhibited in the presence of the glycerol fermentation product 1,3-propanediol. Taking the catalytic efficiency, stability against inactivation by glycerol, and inhibition by 1,3-propanediol into account, the hybrid diol dehydratase produced by E. coli Bl21/pAK5.1 exhibited the best properties of all tested enzymes for application in the biotechnological production of 1,3-propanediol.     

High-level production of tetraacetyl phytosphingosine (TAPS) by combined genetic engineering of sphingoid base biosynthesis and L-serine availability in the non-conventional yeast Pichia ciferrii

The non-conventional yeast Pichia ciferrii is known to secrete the sphingoid long-chain base phytosphingosine in a tetraacetylated form (TAPS). Sphingolipids are important ingredients in cosmetic applications as they play important roles in human skin. Our work aimed to improve TAPS production by genetic engineering of P. ciferrii. In the first step we improved precursor availability by blocking degradation of L-serine, which is condensed with palmitoyl-CoA by serine palmitoyltransferase in the first committed step of sphingolipid biosynthesis. Successive deletion of two genes, SHM1 and SHM2, encoding L-serine hydroxymethyltransferases, and of CHA1 encoding L-serine deaminase, resulted in a strain producing 65 mg((TAPS))g(-1)((cdw)), which is a threefold increase in comparison with the parental strain. Attempts to increase the metabolic flux into and through the L-serine biosynthesis pathway did not improve TAPS production. However, genetic engineering of the sphingolipid pathway further increased secretion of TAPS. Blocking of sphingoid long-chain base phosphorylation by deletion of the LCB kinase gene PcLCB4 resulted in a further increase in TAPS production by 78% and significant secretion of the direct precursor of phytosphingosine, sphinganin, in a triacetylated form (TriASa). Overproduction of two serine palmitoyltransferase subunits, Lcb1 and Lcb2, together with a deletion of the gene ORM12 encoding a putative negative regulator of sphingolipid synthesis resulted in a strain producing 178 mg((TAPS))g(-1)((cdw)). Additional overproduction of the C4-hydroxylase Syr2 converting sphinganine to phytosphingosine reduced TriASa production and further improved TAPS production. The final recombinant P. ciferrii strain produced up to 199 mg((TAPS))g(-1)((cdw)) with a maximal production rate of 8.42 mg×OD(600nm)(-1)h(-1) and a titer of about 2 g L(-1), and should be applicable for industrial TAPS production.     

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。     

Enhanced production of (R)-1,2-propanediol by metabolically engineered Escherichia coli

1,2-Propanediol (1,2-PD) is a major commodity chemical currently derived from propylene. Previously, we have demonstrated the production of enantiomerically pure (R)-1,2-propanediol from glucose by an engineered E. coli expressing genes for NADH-linked glycerol dehydrogenase and methylglyoxal synthase. In this work, we investigate three methods to improve 1,2-PD in E. coli. First, we investigated improving the host by eliminating production of a byproduct, lactate. To do this, we constructed strains with mutations in two enzymes involved in lactate production, lactate dehydrogenase and glyoxalase I. (Surprisingly, when mutations were made in its ability to produce lactate, one strain of E. coli [MM294], produced a small amount of 1,2-PD without any added genes.) Second, we constructed a complete pathway to 1,2-PD from the glycolytic intermediate, dihydroxyacetone phosphate. Our previous 1, 2-PD producing strains relied on at least one endogenous E. coli activity and only produced 0.7 g/L of 1,2-PD. The complete pathway involved the coexpression of methylglyoxal synthase (mgs), glycerol dehydrogenase (gldA), and either yeast alcohol dehydrogenase (adhI) or E. coli 1,2-propanediol oxidoreductase (fucO). Third, we investigated bioprocessing improvements by carrying out a fed-batch fermentation with the best engineered strain (expressing mgs, gldA, and fucO). A final titer of 4.5 g/L of (R)-1,2-PD was produced, with a final yield of 0.19 g of 1,2-PD per gram of glucose consumed. This work provides a basis for further strain and process improvement.     

产1,3-丙二醇基因工程菌发酵条件的研究

利用途径工程的方法,将来源于克雷伯氏菌(Klebsiella pneumoniae)的甘油脱水酶基因dhaB和1,3-丙二醇氧化还原酶基因dhaT构建成多顺反子重组质粒pSE-dhaB-dhaT并在大肠杆菌JM 109中进行表达,在大肠杆菌中构建一条新的产1,3-丙二醇代谢途径。研究表明,重组菌株JM 109/pSE-dhaB-dhaT在微好氧条件下,尝试用廉价的乳糖为诱导物、维生素B12为辅酶,可以将甘油转化为1,3-丙二醇,产量达15.34 g/L,甘油转化率为35.7%,对低成本生产1,3-丙二醇作了有益的探索。