Effects of over-expression of glycerol dehydrogenase and 1,3-propanediol oxidoreductase on bioconversion of glycerol into 1,3-propandediol by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> under micro-aerobic conditions

Glycerol dehydrogenase (GDH) and 1,3-propanediol (1,3-PD) oxidoreductase had been proved two key enzymes for 1,3-PD production by Klebsiella pneumoniae. Fed-batch fermentations of the recombinant K. pneumoniae strains, over-expressing the two enzymes individually, were carried out under micro-aerobic conditions, and the behaviors of the recombinants were investigated. Results showed that over-expression of 1,3-PD oxidoreductase did not affect the concentration of 1,3-PD. However, it enhanced the molar yield from 50.6 to 64.0% and reduced the concentration of by-products. Among them, the concentrations of lactic acid, ethanol and succinic acid were decreased by 51.8, 50.6 and 47.4%, respectively. Moreover, in the recombinant the maximal concentration of 3-hydroxypropionaldehyde decreased by 73.6%. Over-expression of GDH decreased the yield of ethanol and 2,3-butanediol, meanwhile it increased the concentration of acetic acid. No significant changes were observed both in 1,3-PD yield and glycerol flux distributed to oxidative branch.     

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.     

Decrease of 3-hydroxypropionaldehyde accumulation in 1,3-propanediol production by over-expressing <Emphasis Type="Italic">dha</Emphasis>T gene in <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> TUAC01

Glycerol can be biologically converted to 1,3-propanediol, a key raw material required for the synthesis of polytrimethylene terephthalate and other polyester fibers. In 1,3-propanediol synthesis pathway, 3-hydroxypropionaldehyde (3-HPA) was an inhibitory intermediary metabolite. The accumulation of 3-HPA in broth would cause an irreversible cessation of the fermentation process. With the object of reducing 3-HPA level in the fermentation broth, dhaT gene which encodes 1,3-propanediol oxidoreductase (PDOR) was cloned and over expressed in 1,3-propanediol producing bacterium Klebsiella pneumoniae TUAC01. dhaT gene was linked downstream of the ptac promoter in an expressing vector pDK6 to form plasmid pDK-dhaT. The newly formed pDK-dhaT was transformed to K. pneumoniae TUAC01. Under the inducement of IPTG, PDOR was over-expressed when the constructed strain was cultured on an LB medium or a fermentation medium. A 5 L scale-up fermentation experiment was done to test the 3-HPA accumulation in broth, with the initial substrate glycerol 30 g/L; the peak levels of 3-HPA in broth were 7.55 and 1.49 mmol/L for control host strain and the constructed strain, respectively. In 50 g/L initial glycerol experiment, the peak level of 3-HPA in broth was 12.57 and 2.02 mmol/l for the control host strain and the constructed strain, respectively. Thus the fermentation cessation caused by the toxicity of 3-HPA was alleviated in the constructed strain.     

3-Hydroxypropionaldehyde guided glycerol feeding strategy in aerobic 1,3-propanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

3-Hydroxypropionaldehyde (3-HPA) is a toxic intermediary metabolite in the biological route of 1,3-propanediol biosynthesis from glycerol. 3-HPA accumulated in culture medium would arouse an irreversible cessation of the fermentation process. The role of substrate (glycerol) on 3-HPA accumulation in aerobic fermentation was investigated in this paper. 1,3-Propanediol oxidoreductase and glycerol dehydratase, two key enzyme catalyzing reactions of 3-HPA formation and consumption, were sensitive to high concentration of 3-HPA. When the concentration of 3-HPA increased to a higher level in medium (ac 10 mmol/L), the activity of 1,3-propanediol oxidoreductase in cell decreased correspondingly, which led to decrease of the 3-HPA conversion rate, then the 3-HPA concentration increasing was accelerated furthermore. 3-HPA accumulation in culture medium was triggered by this positive feedback mechanism. In the cell exponential growth phase, the reaction catalyzed by 1,3-propanediol oxidoreductase was the rate limiting step in 1,3-propanediol production. The level of 3-HPA in culture medium could be controlled by the substrate (glycerol) concentration, and lower level of glycerol could avoid 3-HPA accumulating to a high, lethal concentration. In fed batch fermentation, under the condition of initial glycerol concentration 30 g/L, and keeping glycerol concentration lower than 7–8 g/L in cell exponential growth phase, 3-HPA accumulation could not be incurred. Based on this result, a glycerol feeding strategy was set up in fed batch fermentation. Under the optimized condition, 50.1 g/L of 1,3-propanediol was produced in 24 h, and 73.1 g/L of final 1,3-propanediol concentration was obtained in 54 h.     

Inactivation of <Emphasis Type="Italic">dhaD</Emphasis> and <Emphasis Type="Italic">dhaK</Emphasis> abolishes by-product accumulation during 1,3-propanediol production in <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

1,3-Propanediol (1,3-PD) can be used for the industrial synthesis of a variety of compounds, including polyesters, polyethers, and polyurethanes. 1,3-PD is generated from petrochemical and microbial sources. 1,3-Propanediol is a typical product of glycerol fermentation, while acetate, lactate, 2,3-butanediol, and ethanol also accumulate during the process. Substrate and product inhibition limit the final concentration of 1,3-propanediol in the fermentation broth. It is impossible to increase the yield of 1,3-propanediol by using the traditional whole-cell fermentation process. In this study, dhaD and dhaK, the genes for glycerol dehydrogenase and dihydroxyacetone kinase, respectively, were inactivated by homologous recombination in Klebsiella pneumoniae. The dhaD/dhaK double mutant (designated TC100), selected from 5,000 single or double cross homologous recombination mutants, was confirmed as a double cross by using polymerase chain reaction. Analysis of the cell-free supernatant with high-performance liquid chromatography revealed elimination of lactate and 2,3-butanediol, as well as ethanol accumulation in TC100, compared with the wild-type strain. Furthermore, 1,3-propanediol productivity was increased in the TC100 strain expressing glycerol dehydratase and 1,3-PDO dehydrogenase regulated by the arabinose P_BAD promoter. The genetic engineering and medium formulation approaches used here should aid in the separation of 1,3-propanediol from lactate, 2,3-butanediol, and ethanol and lead to increased production of 1,3-propanediol in Klebsiella pneumoniae.     

Production of 1,3-propanediol by <Emphasis Type="Italic">Clostridium butyricum</Emphasis> VPI 3266 using a synthetic medium and raw glycerol

Growth inhibition of Clostridium butyricum VPI 3266 by raw glycerol, obtained from the biodiesel production process, was evaluated. C. butyricum presents the same tolerance to raw and to commercial glycerol, when both are of similar grade, i.e. above 87% (w/v). A 39% increase of growth inhibition was observed in the presence of 100 g l^–1 of a lower grade raw glycerol (65% w/v). Furthermore, 1,3-propanediol production from two raw glycerol types (65% w/v and 92% w/v), without any prior purification, was observed in batch and continuous cultures, on a synthetic medium. No significant differences were found in C. butyricum fermentation patterns on raw and commercial glycerol as the sole carbon source. In every case, 1,3-propanediol yield was around 0.60 mol/mol glycerol consumed.     

Expression of 1,3-propanediol oxidoreductase and its isoenzyme in Klebsiella pneumoniae for bioconversion of glycerol into 1,3-propanediol

In the Klebsiella pneumoniae reduction pathway for 1,3-propanediol (1,3-PD) synthesis, glycerol is first dehydrated to 3-hydroxypropionaldehyde (3-HPA) and then reduced to 1,3-PD with NADH consumption. Rapid conversion of 3-HPA to 1,3-PD is one of the ways to improve the yield of 1,3-PD from glycerol and to avoid 3-HPA accumulation, which depends on enzyme activity of the reaction and the amount of reducing equivalents available from the oxidative pathway of glycerol. In the present study, the yqhD gene, encoding 3-propanediol oxidoreductase isoenzyme from Escherichia coli and the dhaT gene, encoding 3-propanediol oxidoreductase from K. pneumoniae were expressed individually and co-expressed in K. pneumoniae using the double tac promoter expression plasmid pEtac-dhaT-tac-yqhD. The three resultant recombinant strains (K. pneumoniae/pEtac-yqhD, K. pneumoniae/pEtac-dhaT, and K. pneumoniae/pEtac-dhaT-tac-yqhD) were used for fermentation studies. Experimental results showed that the peak values for 3-HPA production in broth of the three recombinant strains were less than 25% of that of the parent strain. Expression of dhaT reduced formation of by-products (ethanol and lactic acid) and increased molar yield of 1,3-PD slightly, while expression of yqhD did not enhance molar yield of 1,3-PD, but increased ethanol concentration in broth as NADPH participation in transforming 3-HPA to 1,3-PD allowed more cellular NADH to be used to produce ethanol. Co-expression of both genes therefore decreased by-products and increased the molar yield of 1,3-PD by 11.8%, by catalyzing 3-HPA conversion to 1,3-propanediol using two cofactors (NADH and NADPH). These results have important implications for further studies involving use of YqhD and DhaT for bioconversion of glycerol into 1,3-PD.     

Characterization of 1,3-propanediol oxidoreductase (DhaT) from <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> J2B

1,3-propanediol oxidoreductase (DhaT) of Klebsiella pneumoniae converts 3-hydroxypropionaldehyde (3-HPA) to 1,3-propanediol (1,3-PD) during microbial production of 1,3-PD from glycerol. In this study, DhaT from newly isolated K. pneumoniae J2B was cloned, expressed, purified, and studied for its kinetic properties. It showed, on its physiological substrate 3-HPA, higher activity than similar aldehydes such as acetaldehyde, propionaldehyde and butyraldehyde. The turnover numbers (k _cat , 1/s) were estimated as 59.4 for the forward reaction (3-HPA to 1,3-PD at pH 7.0) and 10.0 for the reverse reaction (1,3-PD to 3-HPA at pH 9.0). The Michaelis constants (K _m , mM) were 0.77 (for 3-HPA) and 0.03 (for NADH) for the forward reaction (at pH 7.0), and 7.44 (for 1,3-PD) and 0.23 (for NAD⁺) for the reverse reaction (at pH 9.0). Between these forward and reverse reactions, the optimum temperature and pH were significantly different (37°C and 7.0 vs. 55°C and 9.0, respectively). These results indicate that, under physiological conditions, DhaT mostly catalyzes the forward reaction. The enzyme was seriously inhibited by heavy metal ions such as Ag⁺ and Hg²⁺. DhaT was highly unstable when incubated with its own substrate 3-HPA, indicating the necessity of enhancing its stability for improved 1,3-PD production from glycerol.     

Enhancement of 1,3-propanediol Production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> with Fumarate Addition

Addition of 5 mm fumarate to cultures of Klebsiella pneumoniae enhanced the rate of glycerol consumption and the production of 1,3-propanediol (PDO). Compared to the control, the activity of glycerol dehydrogenase increased by 35, 33 and 46%, the activity of glycerol dehydratase increased by 160, 210 and 115%, and the activity of 1,3-propanediol oxidoreductase increased by 25, 39 and 85% when, respectively, 5, 15 and 25 mm fumarate were provided. At the same time, the ratio of NAD⁺ to NADH decreased by 20, 23 and 29%. Using a 5 l bioreactor with 5 mM fumarate addition, the specific rate of glycerol consumption and the productivity of PDO was 30 mmol/l h and 17 mmol/l h, respectively, both increased by 35% over the control. Revisions requested 15 July 2005; Revisions received 30 August 2005     

Ammonium and phosphate limitation in 1,3-propanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

Excretion of 1,3-propanediol (1,3-PD) by K. pneumoniae was compared in ammonium- and phosphate-limited chemostat cultures running with an excess of glycerol. 59 and 43% catabolic flux were directed to 1,3-PD in ammonia-limited cultures and phosphate-limited cultures at dilution rate of 0.1 h⁻¹, respectively. Ammonia-limited fed-batch cultures produced 61 g 1,3-PD l⁻¹ and a total of 15 g l⁻¹ organic acid in 36 h. However, phosphate-limited fed-batch cultures excreted 61 g lactate l⁻¹ and 44 g 1,3-PD l⁻¹.     

Dielectric barrier discharge plasma as a novel approach for improving 1,3-propanediol production in <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

Dielectric barrier discharge plasma was used to generate a stable strain of Klebsiella pneumoniae (designated to as Kp-M2) with improved 1,3-propanediol production. The specific activities of glycerol dehydrogenase, glycerol dehydatase and 1,3-propanediol oxidoreductase in the crude cell extract increased from 0.11, 9.2 and 0.15 U mg⁻¹, respectively, for wild type to 0.67, 14.4 and 1.6 U mg⁻¹ for Kp-M2. The glycerol flux of Kp-M2 was redistributed with the flux to the reductive pathway being increased by 20% in batch fermentation. The final 1,3-propanediol concentrations achieved by Kp-M2 in batch and fed-batch fermentations were 19.9 and 76.7 g l⁻¹, respectively, which were higher than those of wild type (16.2 and 49.2 g l⁻¹). The results suggested that dielectric barrier discharge plasma could be used as an effective approach to improve 1,3-propanediol production in K. pneumoniae.     

Multiple growth inhibition of <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> in 1,3-propanediol fermentation

The inhibition of substrate and product on the growth of Klebsiella pneumoniae in anaerobic and aerobic batch fermentation for the production of 1,3-propanediol was studied. The cells under anaerobic conditions had a higher maximum specific growth rate of 0.19 h^–1 and lower tolerance to 110 g glycerol l^–1, compared to the maximum specific growth rate of 0.17 h^–1 and tolerance to 133 g glycerol l^–1 under aerobic conditions. Acetate was the main inhibitory metabolite during the fermentation under anaerobic conditions, with lactate and ethanol the next most inhibitory. The critical concentrations of acetate, lactate and ethanol were assessed to be 15, 19, 26 g l^–1, respectively. However, cells grown under aerobic conditions were more resistant to acetate and lactate but less resistant to ethanol. The critical concentrations of acetate, lactate and ethanol were assessed to be 24, 26, and 17 g l^–1, respectivelyRevisions requested 8 september; Revisions received 2 November 2004     

High-level expression of the 1,3-propanediol oxidoreductase from klebsiella pneumoniae in escherichia coli

As one of four key enzymes in glycerol dismutation process, 1,3-propanediol oxidoreductase (EC.1.1.1.202) is important in converting glycerol to 1,3-propanediol in Klebsiella pneumoniae. The dhaT gene encoding 1,3-propanediol oxidoreductase was amplified by polymerase chain reaction (PCR) using the genome DNA of K. pneumoniae as template, and then cloned into cloning vector pMD18-T. After DNA sequence was determined, the dhaT gene was subcloned into Escherichia coli expression vector pET-22b (+) and pET-28a (+). Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) analysis revealed that both the recombinant E. coli BL21 (DE3) (pET-22b (+)-dhaT) and E. coli BL21(DE3)(pET-28a (+)-dhaT) expressed predicted 42-kDa 1,3-propanediol oxidoreductase after induced by isopropyl-β-d-thiogalactopyranoside (IPTG), and the recombinant enzyme of E. coli BL21 (DE3) (pET-28a (+)-dhaT) was mostly in soluble form, and exhibited high activity (96.8 U/mL culture). The recombinant enzyme was purified and biochemically characterized. The apparent K _m values of the enzyme for 1,3-propanediol and NAD⁺ were 8.5 and 0.21 mM, respectively. The enzyme had maximum activity at pH 9.5 and 30°C.     

Identification and utilization of a 1,3-propanediol oxidoreductase isoenzyme for production of 1,3-propanediol from glycerol in Klebsiella pneumoniae

In a previous study, we showed that 1,3-propanediol (1,3-PD) was still produced from glycerol by the Klebsiella pneumoniae mutant strain defective in 1,3-PD oxidoreductase (DhaT), although the production level was lower compared to the parent strain. As a potential candidate for another putative 1,3-PD oxidoreductase, we identified and characterized a homolog of Escherichia coli yqhD (88% homology in amino acid sequence), which encodes an alcohol dehydrogenase and is well known to replace the function of DhaT in E. coli. Introduction of multiple copies of the yqhD homolog restored 1,3-PD production in the mutant K. pneumoniae strain defective in DhaT. In addition, by-product formation was still eliminated in the recombinant strain due to the elimination of the glycerol oxidative pathway. An increase in NADP-dependent 1,3-PD oxidoreductase activity was observed in the recombinant strain harboring multiple copies of the yqhD homolog. The level of 1,3-PD production during batch fermentation in the recombinant strain was comparable to that of the parent strain; further engineering can generate an industrial strain producing 1,3-propanediol.     

Effect of aeration strategy on the metabolic flux of <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> producing 1,3-propanediol in continuous cultures at different glycerol concentrations

The microbial production of 1,3-propaneidol (1,3-PD) by Klebsiella pneumoniae in continuous fermentation was investigated under low, medium and high glycerol concentrations in the absence and presence of oxygen. The production of 1,3-PD increased with increasing glycerol concentrations, reaching a maximum (266 mmol l⁻¹) under high glycerol concentration (760 mmol l⁻¹) with air sparging at 0.04 vvm. The yield of 1,3-PD, however, decreased gradually with increasing glycerol concentrations, with the highest yield (0.52 mol mol⁻¹) obtained for low glycerol concentration (270 mmol l⁻¹) under anaerobic condition. Enzyme activity assays showed that the specific activity of glycerol dehydratase was highest (0.04 U mg⁻¹) for culture sparged with 0.04 vvm air under high glycerol concentration. The specific activities of glycerol dehydrogenase and 1,3-propanediol oxidoreductase were also improved for all glycerol concentrations and in the presence of oxygen, implying that the dha operon was not repressed under microaerobic conditions. Analysis of metabolic fluxes showed that more carbon flux was shifted to the oxidative pathway with increasing glycerol concentrations, resulting in a reduced flux to 1,3-PD formation. However, the increases in carbon fluxes were not evenly distributed among the oxidative branches of the pathway. Furthermore, ethanol and acetic acid levels were slightly increased whereas 2,3-butanediol and lactic levels were greatly enhanced.     

Optimization of culture conditions for 1,3-propanediol production from crude glycerol by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> using response surface methodology

To produce 1,3-propanediol (1,3-PD) from crude glycerol, cultivation conditions were optimized by response surface methodology (RSM) based on a 2⁵ factorial central composite design (CCD). RSM was adopted to derive a statistical model for the individual and interactive effects of crude glycerol, (NH₄)₂SO₄, pH, cultivation time and temperature on the production of 1,3-PD. Optimal conditions for maximum 1,3-PD production were as follows: crude glycerol, 35 g/L; (NH₄)₂SO₄, 8 g/L; pH, 7.37; cultivation time, 10.8 h; temperature, 36.88°C. Under these optimal conditions, the design expert presented the maximal numerical solution with a predicted 1,3-PD production level of up to 13.74 g/L. The experimental production of 1,3-PD yielded 13.8 g/L, which was in close agreement with the model prediction.     

Stimulation of reductive glycerol metabolism by overexpression of an aldehyde dehydrogenase in a recombinant <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> strain defective in the oxidative pathway

Previously, we constructed a glycerol oxidative pathway-deficient mutant strain of Klebsiella pneumoniae by inactivation of glycerol dehydrogenase (dhaD) to eliminate by-product synthesis during production of 1,3-propanediol (1,3-PD) from glycerol. Although by-product formation was successfully blocked in the resultant strain, the yield of 1,3-PD was not enhanced, probably because dhaD disruption resulted in insufficient regeneration of the cofactor NADH essential for the activity of 1,3-PD oxidoreductase (DhaT). To improve cofactor regeneration, in the present study we overexpressed an NAD⁺-dependent aldehyde dehydrogenase in the recombinant strain. To this end, an aldehyde dehydrogenase AldHk homologous to E. coli AldH but with NAD⁺-dependent propionaldehyde dehydrogenase activity was identified in K. pneumoniae. Functional analysis revealed that the substrate specificity of AldHk embraced various aldehydes including propionaldehyde, and that NAD⁺ was preferred over NADP⁺ as a cofactor. Overexpression of AldHk in the glycerol oxidative pathway-deficient mutant AK/pVOTHk resulted in a 3.6-fold increase (0.57 g l⁻¹ to 2.07 g l⁻¹) in the production of 3-hydroxypropionic acid (3-HP), and a 1.1-fold enhancement (8.43 g l⁻¹ to 9.65 g l⁻¹) of 1,3-PD synthesis, when glycerol was provided as the carbon source, compared to the levels synthesized by the control strain (AK/pVOT). Batch fermentation using AK/pVOTHk showed a significant increase (to 70%, w/w) in conversion of glycerol to the reductive metabolites, 1,3-PD and 3-HP, with no production of by-products except acetate.     

Chemometric modeling and two-dimensional fluorescence analysis of bioprocess with a new strain of <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> to convert residual glycerol into 1,3-propanediol

The goal of this study was to show that the metabolism of Klebsiella pneumoniae under different aeration strategies could be monitored and predicted by the application of chemometric models and fluorescence spectroscopy. Multi-wavelength fluorescence was applied to the on-line monitoring of process parameters for K. pneumoniae cultivations. Differences observed in spectra collected under aerobiosis and anaerobiosis can be explained by the different metabolic states of the cells. To predict process variables such as biomass, glycerol, and 1,3-propanediol (1,3-PD), chemometric models were developed on the basis of the acquired fluorescence spectra, which were measured continuously. Although glycerol and 1,3-PD are not fluorescent compounds, the results showed that this technique could be successfully applied to the on-line monitoring of variables in order to understand the process and thus improve 1,3-PD production. The root mean square errors of predictions were 0.78 units, 10 g/L, and 2.6 g/L for optical density, glycerol, and 1,3-PD, respectively.     

Construction of stress-induced metabolic pathway from glucose to 1,3-propanediol in <Emphasis Type="Italic">Escherichia coli</Emphasis>

1,3-Propanediol is an important chemical widely used in polymer production, but its availability is being restricted owing to its expensive synthesis. The aim of this study was to engineer an Escherichia coli strain that can produce 1,3-propanediol directly from glucose. We successfully constructed a stress-induced metabolic pathway from glucose to 1,3-propanediol in recombinant E. coli by the expression of gpd1 and gpp2 genes from Saccharomyces cerevisiae and dha operon from Klebsiella pneumoniae, respectively. Batch cultivation of the recombinant E. coli showed that 12.1 g/L 1,3-propanediol was accumulated in the culture without using any inducer.