In silico and in vivo analyses reveal key metabolic pathways enabling the fermentative utilization of glycerol in Escherichia coli

Most microorganisms can metabolize glycerol when external electron acceptors are available (i.e. under respiratory conditions). However, few can do so under fermentative conditions owing to the unique redox constraints imposed by the high degree of reduction of glycerol. Here, we utilize in silico analysis combined with in vivo genetic and biochemical approaches to investigate the fermentative metabolism of glycerol in Escherichia coli. We found that E. coli can achieve redox balance at alkaline pH by reducing protons to H₂, complementing the previously reported role of 1,2-propanediol synthesis under acidic conditions. In this new redox balancing mode, H₂ evolution is coupled to a respiratory glycerol dissimilation pathway composed of glycerol kinase (GK) and glycerol-3-phosphate (G3P) dehydrogenase (G3PDH). GK activates glycerol to G3P, which is further oxidized by G3PDH to generate reduced quinones that drive hydrogenase-dependent H₂ evolution. Despite the importance of the GK-G3PDH route under alkaline conditions, we found that the NADH-generating glycerol dissimilation pathway via glycerol dehydrogenase (GldA) and phosphoenolpyruvate (PEP)-dependent dihydroxyacetone kinase (DHAK) was essential under both alkaline and acidic conditions. We assessed system-wide metabolic impacts of the constraints imposed by the PEP dependency of the GldA-DHAK route. This included the identification of enzymes and pathways that were not previously known to be involved in glycerol metabolisms such as PEP carboxykinase, PEP synthetase, multiple fructose-1,6-bisphosphatases and the fructose phosphate bypass.     

Production of 1,3-propanediol from Glycerol by Recombinant <Emphasis Type="Italic">E. coli</Emphasis> Using Incompatible Plasmids System

1,3-Propanediol (1,3-PD) has numerous applications in polymers, cosmetics, foods, lubricants, and medicines as a bifunctional organic compound. The genes for the production of 1,3-PD in Klebsiella pneumoniae, dhaB, which encodes glycerol dehydratase, and dhaT, which encodes 1,3-PD oxidoreductase, and gdrAB, which encodes glycerol dehydratase reactivating factor, are naturally under the control of different promoters and are transcribed in different directions. These genes were coexpressed in E. coli using two incompatible plasmids (pET28a and pET22b) in the presence of selective pressure. The recombinant E. coli coexpressed the glycerol dehydratase, 1,3-propanediol oxidoreductase and reactivating factor for the glycerol dehydratase at high levels. In a fed-batch fermentation of glycerol and glucose, the recombinant E. coli containing these two incompatible plasmids consumed 14.3 g/l glycerol and produced 8.6 g/l 1,3-propanediol. In the substitution case of yqhD (encoding alcohol dehydrogenase from E. coli) for dhaT, the final 1,3-propanediol concentration of the recombinant E. coli could reach 13.2 g/l.     

A Novel Glycerol Kinase from Flavobacterium meningosepticum: Characterization,Gene Cloning and Primary Structure

A thermostable glycerol kinase (FGK) was purified 34-fold to homogeneity from Flavobacterium meningosepticum. The molecular masses of the enzyme were 200 kDa by gel filtration and 50 kDa by SDS-PAGE. The Km for glycerol and ATP were 0.088 and 0.030 mM, respectively. The enzyme was stable at 65°C for 10 min and at 37°C for two weeks. The enzyme gene was cloned into Escherichia coli and its complete DNA was sequenced. The FGK gene consists of an open reading frame of 1494-bp encoding a protein of 498 amino acids. The deduced amino acid sequence of the gene had 40-60% similarity to those of glycerol kinases from other origins and the amino acid sequence of the putative active site residue reported for E. coli GK is identical to the corresponding sequence of FGK except for one amino acid residue.     

Functional Analysis of the C-Terminal Region of γ-Glutamyl Kinase of Saccharomyces cerevisiae

γ-Glutamyl kinase (GK) is the rate-limiting enzyme in proline synthesis in microorganisms. Most microbial GKs contain an N-terminal kinase domain and a C-terminal pseudouridine synthase and archaeosine transglycosylase (PUA) domain. In contrast, higher eukaryotes possess a bifunctional Δ¹-pyrroline-5-carboxylate synthetase, which consists of a PUA-free GK domain and a γ-glutamyl phosphate reductase (GPR) domain. Here, to examine the role of the C-terminal region, including the PUA domain of Saccharomyces cerevisiae GK, we constructed a variety of truncated yeast GK and GK/GPR fusion proteins from which the C-terminal region was deleted. A complementation test in Escherichia coli and S. cerevisiae and enzymatic analysis of recombinant proteins revealed that a 67-residue linker sequence between a 255-residue kinase domain and a 106-residue PUA domain is essential for GK activity. It also appeared that 67 or more residues of the C-terminal region, not the PUA domain itself, are required for the full display of GK activity. Further, the GK/GPR fusion protein was functional in E. coli, but decreased stability and Mg-binding ability as compared to wild-type GK. These results suggest that the C-terminal region of S. cerevisiae GK is involved in the folding and/or the stability of the kinase domain.     

Glutamate kinase from Thermotoga maritima: characterization of a thermophilic enzyme for proline biosynthesis

Glutamate kinase (GK), an enzyme involved in osmoprotection in plants and microorganisms, catalyses the first and controlling step of proline biosynthesis. The proB gene encoding GK was cloned from the hyperthermophilic bacterium Thermotoga maritima and overexpressed in Escherichia coli, and the resulting protein was purified to homogeneity in three simple steps. T. maritima GK behaved as a tetramer, showing maximal activity at 83°C, and was inhibited by ADP and proline. Although T. maritima GK exhibited high amino acid similarity to the mesophilic E. coli GK, it was less dependent of Mg ions and was not aggregated in the presence of proline. Moreover, it displayed a greater thermostability and higher catalytic efficiency than its mesophilic counterpart at elevated temperatures.     

Characterization of alditol oxidase from Streptomyces coelicolor and its application in the production of rare sugars

A synthetic platform for the cascade synthesis of rare sugars using Escherichia coli whole cells was established. In the cascade, the donor substrate dihydroxyacetone phosphate (DHAP) was generated from glycerol by glycerol kinase (GK) and glycerol phosphate oxidase (GPO). The acceptor d-glyceraldehyde was directly produced from glycerol by an alditol oxidase. Then, the aldol reaction between DHAP and d-glyceraldehyde was performed by l-rhamnulose-1-phosphate aldolase (RhaD) to generate the corresponding sugar-1-phosphate. Finally, the phosphate group was removed by fructose-1-phosphatase (YqaB) to obtain the rare sugars d-sorbose and d-psicose. To accomplish this goal, the alditol oxidase from Streptomyces coelicolor (AldO_S.coe) was expressed in E. coli and the purified AldO_S.coe was characterized. Furthermore, a recombinant E. coli strain overexpressing six enzymes including AldO_S.coe was constructed. Under the optimized conditions, it produced 7.9 g/L of d-sorbose and d-psicose with a total conversion rate of 17.7% from glycerol. This study provides a useful and cost-effective method for the synthesis of rare sugars.     

Identification of the glycerol kinase gene and its role in diapause embryo restart and early embryo development of Artemia sinica

Glycerol kinase (GK) catalyzes the rate-limiting step in glycerol utilization by transferring a phosphate from ATP to glycerol, yielding glycerol 3-phosphate, which is an important intermediate for both energy metabolism and glycerolipid production. Artemia sinica has an unusual diapause process under stress conditions of high salinity, low temperature and lack of food. In the process, diapause embryos of A. sinica (brine shrimp) accumulate high concentrations of glycerol as a cryoprotectant to prevent low temperature damage to embryos. Upon embryo restart, glycerol is converted into glucose and other carbohydrates. Therefore, GK plays an important role in the diapause embryo restart process. However, the role of GK in diapause termination of embryo development in A. sinica remains unknown.     

Escherichia coli genome-scale metabolic gene knockout of lactate dehydrogenase (ldhA), increases succinate production from glycerol

Genome-scale metabolic model (GEM) of Escherichia coli has been published with applications in predicting metabolic engineering capabilities on different carbon sources and directing biological discovery. The use of glycerol as an alternative carbon source is economically viable in biorefinery. The use of GEM for predicting metabolic gene deletion of lactate dehydrogenase (ldhA) for increasing succinate production in Escherichia coli from glycerol carbon source remained largely unexplored. Here, I hypothesized that metabolic gene knockout of ldhA in E. coli from glycerol could increase succinate production. A proof-of-principle strain was constructed and designated as E. coli BMS5 (ΔldhA), by predicting increased succinate production in E. coli GEM and confirmed the predicted outcomes using wet cell experiments. The mutant GEM (ΔldhA) predicted 11% increase in succinate production from glycerol compared to its wild-type model (iAF1260), and the E. coli BMS5 (ΔldhA) showed 1.05 g/l and its corresponding wild-type produced .05 g/l (23-fold increase). The proof-of-principle strain constructed in this study confirmed the aforementioned hypothesis and further elucidated the fact that E. coli GEM can prospectively and effectively predict metabolic engineering interventions using glycerol as substrate and could serve as platform for new strain design strategies and biological discovery.     

In silico deletion of PtsG gene in Escherichia coli genome-scale model predicts increased succinate production from glycerol

Systems metabolic engineering and in silico analyses are necessary to study gene knockout candidate for enhanced succinic acid production by Escherichia coli. Metabolically engineered E. coli has been reported to produce succinate from glucose and glycerol. However, investigation on in silico deletion of ptsG/b1101 gene in E. coli from glycerol using minimization of metabolic adjustment algorithm with the OptFlux software platform has not yet been elucidated. Herein we report what is to our knowledge the first direct predicted increase in succinate production following in silico deletion of the ptsG gene in E. coli GEM from glycerol with the OptFlux software platform. The result indicates that the deletion of this gene in E. coli GEM predicts increased succinate production that is 20% higher than the wild-type control model. Hence, the mutant model maintained a growth rate that is 77% of the wild-type parent model. It was established that knocking out of the ptsG/b1101 gene in E. coli using glucose as substrate enhanced succinate production, but the exact mechanism of this effect is still obscure. This study informs other studies that the deletion of ptsG/b1101 gene in E. coli GEM predicted increased succinate production, enabling a model-driven experimental inquiry and/or novel biological discovery on the underground metabolic role of this gene in E. coli central metabolism in relation to increasing succinate production when glycerol is the substrate.     

Glycerol metabolism in superoxide dismutase-deficient Escherichia coli.

Escherichia coli, which lacks cytoplasmic superoxide dismutases, exhibits various phenotypic deficits if grown aerobically. Here we report that sodAsodB E. coli cannot use glycerol under aerobic conditions. The reason is low activity of glycerol kinase (GK), the rate-limiting enzyme in glycerol metabolism. Superoxide does not inactivate GK, but makes it susceptible to inactivation by a heat-labile factor present in the cell-free extracts. This factor seems to be part of a proteolytic system, which recognizes and degrades oxidatively modified proteins.     

Model-aided atpE gene knockout strategy in Escherichia coli for enhanced succinic acid production from glycerol

Succinic acid is an important platform chemical with a variety of applications. Model-guided metabolic engineering strategies in Escherichia coli for strain improvement to increase succinic acid production using glucose and glycerol remain largely unexplored. Herein, we report what are, to our knowledge, the first metabolic knockout of the atpE gene to have increased succinic acid production using both glucose and alternative glycerol carbon sources in E. coli. Guided by a genome-scale metabolic model, we engineered the E. coli host to enhance anaerobic production of succinic acid by deleting the atpE gene, thereby generating additional reducing equivalents by blocking H⁺ conduction across the mutant cell membrane. This strategy produced 1.58 and .49 g l^?1 of succinic acid from glycerol and glucose substrate, respectively. This work further elucidates a model-guided and/or system-based metabolic engineering, involving only a single-gene deletion strategy for enhanced succinic acid production in E. coli.     

Model-assisted formate dehydrogenase-O (fdoH) gene knockout for enhanced succinate production in Escherichia coli from glucose and glycerol carbon sources

Succinic acid is an important platform chemical that has broad applications and is been listed as one of the top twelve bio-based chemicals produced from biomass by the US Department of Energy. The metabolic role of Escherichia coli formate dehydrogenase-O (fdoH) under anaerobic conditions in relation to succinic acid production remained largely unspecified. Herein we report, what are to our knowledge, the first metabolic fdoH gene knockout that have enhanced succinate production using glucose and glycerol substrates in E. coli. Using the most recent E. coli reconstruction iJO1366, we engineered its host metabolism to enhance the anaerobic succinate production by deleting the fdoH gene, which blocked H⁺ conduction across the mutant cell membrane for the enhanced succinate production. The engineered mutant strain BMS4 showed succinate production of 2.05 g l^?1 (41.2-fold in 7 days) from glycerol and .39 g l^?1 (6.2-fold in 1 day) from glucose. This work revealed that a single deletion of the fdoH gene is sufficient to increase succinate production in E. coli from both glucose and glycerol substrates.     

Metabolic engineering of Escherichia coli for the production of 1,2-propanediol from glycerol

Due to its availability, low‐price, and high degree of reduction, glycerol has become an attractive carbon source for the production of fuels and reduced chemicals. Using the platform we have established from the identification of key pathways mediating fermentative metabolism of glycerol, this work reports the engineering of Escherichia coli for the conversion of glycerol into 1,2‐propanediol (1,2‐PDO). A functional 1,2‐PDO pathway was engineered through a combination of overexpression of genes involved in its synthesis from the key intermediate dihydroxyacetone phosphate (DHAP) and the manipulation of the fermentative glycerol utilization pathway. The former included the overexpression of methylglyoxal synthase (mgsA), glycerol dehydrogenase (gldA), and aldehyde oxidoreductase (yqhD). Manipulation of the glycerol utilization pathway through the replacement of the native E. coli PEP‐dependent dihydroxyacetone kinase (DHAK) with an ATP‐dependent DHAK from C. freundii increased the availability of DHAP allowing for higher 1,2‐PDO production. Analysis of the major fermentative pathways indentified ethanol as a required co‐product while increases in 1,2‐PDO titer and yield were achieved through the disruption of the pathways for acetate and lactate production. Combination of these key metabolic manipulations resulted in an engineered E. coli strain capable of producing 5.6 g/L 1,2‐PDO, at a yield of 21.3% (w/w). This strain also performed well when crude glycerol, a by‐product of biodiesel production, was used as the substrate. The titer and yield achieved in this study were favorable to those obtained with the use of E. coli for the production of 1,2‐PDO from common sugars. Biotechnol. Bioeng. 2011; 108:867–879. © 2010 Wiley Periodicals, Inc.     

Glycerol and dihydroxyacetone metabolizing enzymes in fission yeasts of the genus Schizosaccharomyces

The only species of fission yeasts capable of growing on glycerol or dihydroxyacetone were Schizosaccharomyces pombe and S. malidevorans. When growing on glycerol or grown on glucose until it was exhausted, these species contained glycerol:NAD⁺ 2-oxidoreductase and dihydroxyacetone kinase but no glycerol kinase, consistent with utilization of glycerol via dihydroxyacetone. When grown to exhaustion of glucose, S. octosporus, S. slooffiae and S. japonicus contained dihydroxyacetone kinase but no glycerol:NAD⁺ 2-oxidoreductase or glycerol kinase. Prior to exhaustion of glucose in the medium, all species contained dihydroxyacetone kinase, all species except S. japonicus contained glycerol:NADP⁺ 2-oxidoreductase, and only S. pombe and S. malidevorans contained glycerol:NAD⁺ 2-oxidoreductase. Possible roles for the glycerol:NAD⁺ 2-oxidoreductase, glycerol:NADP⁺ 2-oxidoreductase and dihydroxyacetone kinase in metabolism of glycerol and dihydroxyacetone are discussed.Non-standard abbreviations DHA dihydroxyacetone - DHAK dihydroxyacetone kinase - DHAP dihydroxyacetone phosphate - GK glycerol kinase - G2DH-NAD glycerol - NAD⁺ 2-oxidoreductase - G2DH-NADP glycerol - NADP⁺ 2-oxidoreductase - MEA malt extract agar - YEP yeast extract phosphate medium     

Expression of dha Operon Required for 1,3-PD Formation in Escherichia coli and Saccharomyces cerevisiae

The 1,3-propanediol (1,3-PD) synthesis operon (dha operon) was mainly composed of four genes: dhaB, dhaT, gdrA, and gdrB, which encoded glycerol dehydratase, 1,3-PD oxidoreductase and reactivating factor for glycerol dehydratase, respectively. In the present study, dha operon was cloned from 1,3-PD producing strain Klebsiella pneumoniae. Heterologous expression of cloned dha operon was carried out in Escherichia coli and Saccharomyces cerevisiae W303-1A, respectively. The results indicated that recombinant E. coli harboring the dha operon can produce 8–9 g/l 1,3-PD from glycerol while the 1,3-PD yield of recombinant strain W303-1A-dha could not be detected. In order to complete the 1,3-PD production from glucose, further, we also constructed the recombinant S. cerevisiae W303-1A-BT harboring plasmid pZ-BT. The 1,3-PD production and enzymatic activities of DhaB and DhaT were found in the engineered strain W303-1A-BT. Our results demonstrated that the recombinant S. cerevisiae strain W303-1A-BT that can produce 1,3-PD at low cost was constructed. This study might open a novel way to a safe and cost-efficient method for microbial production of 1,3-PD.     

A systematic analysis of TCA Escherichia coli mutants reveals suitable genetic backgrounds for enhanced hydrogen and ethanol production using glycerol as main carbon source

Biodiesel has emerged as an environmentally friendly alternative to fossil fuels; however, the low price of glycerol feed‐stocks generated from the biodiesel industry has become a burden to this industry. A feasible alternative is the microbial biotransformation of waste glycerol to hydrogen and ethanol. Escherichia coli, a microorganism commonly used for metabolic engineering, is able to biotransform glycerol into these products. Nevertheless, the wild type strain yields can be improved by rewiring the carbon flux to the desired products by genetic engineering. Due to the importance of the central carbon metabolism in hydrogen and ethanol synthesis, E. coli single null mutant strains for enzymes of the TCA cycle and other related reactions were studied in this work. These strains were grown anaerobically in a glycerol‐based medium and the concentrations of ethanol, glycerol, succinate and hydrogen were analysed by HPLC and GC. It was found that the reductive branch is the more relevant pathway for the aim of this work, with malate playing a central role. It was also found that the putative C4‐transporter dcuD mutant improved the target product yields. These results will contribute to reveal novel metabolic engineering strategies for improving hydrogen and ethanol production by 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 B₁₂-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.     

Production of 3‐Fucosyllactose in Engineered Escherichia coli with α‐1,3‐Fucosyltransferase from Helicobacter pylori

3‐Fucosyllactose (3‐FL), one of the major oligosaccharides in human breast milk, is produced in engineered Escherichia coli. In order to search for a good α‐1,3‐fucosyltransferase, three bacterial α‐1,3‐fucosyltransferases are expressed in engineered E. coli deficient in β‐galactosidase activity and expressing the essential enzymes for the production of guanosine 5′‐diphosphate‐l ‐fucose, the donor of fucose for 3‐FL biosynthesis. Among the three enzymes tested, the fucT gene from Helicobacter pylori National Collection of Type Cultures 11637 gives the best 3‐FL production in a simple batch fermentation process using glycerol as a carbon source and lactose as an acceptor. In order to use glucose as a carbon source, the chromosomal ptsG gene, considered the main regulator of the glucose repression mechanism, is disrupted. The resulting E. coli strain of ?LP‐YA+FT shows a much lower performance of 3‐FL production (4.50 g L^?1) than the ?L‐YA+FT strain grown in a glycerol medium (10.7 g L^?1), suggesting that glycerol is a better carbon source than glucose. Finally, the engineered E. coli ?LW‐YA+FT expressing the essential genes for 3‐FL production and blocking the colanic acid biosynthetic pathway (?wcaJ) exhibits the highest concentration (11.5 g L^?1), yield (0.39 mol mol^?1), and productivity (0.22 g L^?1 h) of 3‐FL in glycerol‐limited fed‐batch fermentation.     

A Particulate Phospholipid Synthesizing System from Escherichia coli B

The phosphatidate formed by glycerol 3-phosphate acyltransferase present in a particulate fraction from E. coli remained associated with the particulate material and was converted to phosphatidylethanolamine and phosphatidylglycerol by other enzymes contained in the particulate fraction. Those enzymes required a heat-labile factor for the synthesis of phosphatidylethanolamine and a heat-stable factor for the synthesis of phosphatidylglycerol. Both of these phospholipids like their precursor remained bound to the particulate fraction.     

Periplasmic aggregation limits the proteolytic maturation of the Escherichia coli Penicillin G amidase precursor polypeptide

The Escherichia coli penicillin G amidase (PGA), which is a key enzyme in the production of penicillin G derivatives is generated from a precursor polypeptide by an unusual internal maturation process. We observed the accumulation of the PGA precursor polypeptide in the insoluble material recovered after sonication of recombinant E. coli JM109 cells grown at 26°C. The aggregated nature of the accumulated molecules was demonstrated using detergents and chaotrophic agents in solubilization assays. The periplasmic location of the aggregates was shown by trypsin-accessibility experiments performed on the spheroplast fraction. Finally, we showed that addition of sucrose or glycerol in the medium strongly reduces this periplasmic aggregation and as a consequence PGA production is substantially increased. Thus, periplasmic aggregation of the PGA precursor polypeptide limits PGA production by recombinant E. coli and this limitation can be overcome by addition in the medium of a non-metabolizable sugar, such as sucrose, or of glycerol.