Enhanced 2,3-butanediol production by Klebsiella oxytoca using a two-stage agitation speed control strategy

Batch fermentative production of 2,3-butanediol by Klebsiella oxytoca was investigated using various oxygen supply methods though varying agitation speed. Based on the analysis of three kinetic parameters including specific cell growth rate (μ), specific glucose consumption rate (q_s) and specific 2,3-butanediol formation rate (q_p), a two-stage agitation speed control strategy, aimed at achieving high concentration, high yield and high productivity of 2,3-butanediol, was proposed. At the first 15 h, agitation speed was controlled at 300 rpm to obtain high μ for cell growth, subsequently agitation speed was controlled at 200 rpm to maintain high q_p for high 2,3-butanediol accumulation. Finally, the maximum concentration of 2,3-butanediol reached 95.5 g l⁻¹ with the yield of 0.478 g g⁻¹ and the productivity of 1.71 g l⁻¹ h⁻¹, which were 6.23%, 6.22% and 22.14% over the best results controlled by constant agitation speeds.     

Characterization and fouling properties of exopolysaccharide produced by Klebsiella oxytoca

Klebsiella oxytoca produced a type of exopolysaccharide (EPS) with the average molecular weight (Mw) of 116,018 Da and the average size of 260 nm. The EPS monosaccharide components contained rhamnose, fucose, arabinose, xylose, mannose, galactose and glucose and the molar ratio among them was 0.033:0.0411:0.0147:0.0051:0.2393:0.0986:0.1304. Typical EPS absorption peaks in FT-IR spectrum and pseudoplastic properties were also revealed. The polyvinylidenefluoride (PVDF) membrane showed a relatively larger flux decline resulted from the EPS fouling. The EPS filtration was dominated by more than one mechanism at the beginning phase and mainly by the cake formation at the later phase for both membranes. The pore blocking resistance had a predominant contribution to the filtration resistance and the cake resistance played a secondary role for both the membranes. The EPS adsorption resulted in a weak membrane fouling. The PVDF membrane exhibited a larger adsorption resistance than the polypropylene (PP) membrane.     

Influence of sugar source (lactose,glucose, galactose) on 2,3-butanediol production by Klebsiella oxytoca NRRL-B199

The ability of Klebsiella oxytoca NRRL-B199 to use either lactose or the mixture of glucose and galactose as substrate for the production of 2,3-butanediol was studied in batch fermentations with different conditions of aeration and pH. 2,3-butanediol was undetected, or present in minute concentration in the fermentation broths with lactose, while it was the main product from glucose+galactose with final concentrations of up to 18.8 g/l in media at pH 6.0. Under conditions optimal for 2,3-butanediol synthesis, when aeration limited growth, the rate of biomass growth was more tightly related to the aeration rate in lactose medium than in glucose+galactose medium. These relations suggest that the growth rate is very low on lactose but still considerable on glucose+galactose when aeration rate tends toward zero. Correspondingly, the metabolism is more oxidative in the former medium, yielding mainly acetate as product.Abbreviations CDW cell dry weight     

Enhanced 2,3-butanediol production by altering the mixed acid fermentation pathway in <Emphasis Type="Italic">Klebsiella oxytoca</Emphasis>

Klebsiella oxytoca mutants were isolated from the wild type strain ME-303 after mutagenesis with UV coupled with diethyl sulfate and the following modified proton suicide method. By analyzing the activities of lactate dehydrogenase and phosphotransacetylase involved in lactic and acetic acid formation pathways and batch fermentation, one mutant, ME-UD-3, was isolated that produced 7.8% more 2,3-butanediol than ME-303 with the corresponding byproducts of lactic and acetic acid decreased by 88% and 92%, respectively.     

Engineering Bacillus subtilis for acetoin production from glucose and xylose mixtures

As a vital flavor compound, acetoin is extensively used in dairy products and drinks industry. In this study, Bacillus subtilis was engineered to metabolize glucose and xylose as substrates for acetoin production. Initially, gene araE from B. subtilis, encoding the xylose transport protein AraE, was placed under the control of the constitutive promoter P₄₃ for over-expression. Batch cultures showed that 10 g/L xylose was depleted completely in 32 h. Subsequently, genes xylA and xylB from Escherichia coli, encoding xylose isomerase and xylulokinase respectively, were introduced into B. subtilis, and the recombinant turned out to assimilate glucose and xylose without preference. In shake-flask fermentations, 5.5 g/L acetoin with a yield of 0.70 mol (mol sugar)⁻¹ was obtained by the optimum strain BSUL13 under microaerobic conditions, which offered a metabolic engineering strategy on engineering microbe as cell factory for the production of high-valued chemicals from renewable resource.     

Improved 1,3-propanediol production by engineering the 2,3-butanediol and formic acid pathways in integrative recombinant Klebsiella pneumoniae

In the biotechnological process, insufficient cofactor NADH and multiple by-products restrain the final titer of 1,3-propanediol (1,3-PD). In this study, 1,3-PD production was improved by engineering the 2,3-butanediol (2,3-BD) and formic acid pathways in integrative recombinant Klebsiella pneumoniae. The formation of 2,3-BD is catalysed by acetoin reductase (AR). An inactivation mutation of the AR in K. pneumoniae CF was generated by insertion of a formate dehydrogenase gene. Inactivation of AR and expression of formate dehydrogenase reduced 2,3-BD formation and improved 1,3-PD production. Fermentation results revealed that intracellular metabolic flux was redistributed pronouncedly. The yield of 1,3-PD reached 0.74 mol/mol glycerol in flask fermentation, which is higher than the theoretical yield. In 5 L fed-batch fermentation, the final titer and 1,3-PD yield of the K. pneumoniae CF strain reached 72.2 g/L and 0.569 mol/mol, respectively, which were 15.9% and 21.7% higher than those of the wild-type strain. The titers of 2,3-BD and formic acid decreased by 52.2% and 73.4%, respectively. By decreasing the concentration of all nonvolatile by-products and by increasing the availability of NADH, this study demonstrates an important strategy in the metabolic engineering of 1,3-PD production by integrative recombinant hosts.     

Effect of lactic acid on growth and butanediol production byKlebsiella oxytoca

Summary Production of 2,3-butanediol byKlebsiella oxytoca was enhanced in the presence of low levels (<8 g/l) of added sodium lactate. Cell growth was inhibited, however, and essentially stopped above 15 g/l added lactate. Levels of by-products (acetic acid and ethanol) were also higher. With 3 g/l lactate and an initial glucose level of 98 g/l, butanediol concentration and productivity increased 164% with 98% utilization of glucose. With high glucose concentration (219 g/l), addition of 2.64 g/l lactate after the growth phase resulted in 81 g/l butanediol, with a productivity of 0.65 g/l/h and 71% glucose utilization.     

Enhanced 2,3-butanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> SDM

Enhanced 2,3-butanediol (BD) production was carried out by Klebsiella pneumoniae SDM. The nutritional requirements for BD production by K. pneumoniae SDM were optimized statistically in shake flask fermentations. Corn steep liquor powder and (NH₄)₂HPO₄ were identified as the most significant factors by the two-level Plackett–Burman design. Steepest ascent experiments were applied to approach the optimal region of the two factors and a central composite design was employed to determine their optimal levels. The optimal medium was used to perform fed-batch fermentations with K. pneumoniae SDM. BD production was then studied in a 5-l bioreactor applying different fed-batch strategies, including pulse fed batch, constant feed rate fed batch, constant residual glucose concentration fed batch, and exponential fed batch. The maximum BD concentration of 150 g/l at 38 h with a diol productivity of 4.21 g/l h was obtained by the constant residual glucose concentration feeding strategy. To the best of our knowledge, these results were new records on BD fermentation. Cuiqing Ma and Ailong Wang contributed equally to this work.     

Enhancement of ethanol production from glycerol in a Klebsiella pneumoniae mutant strain by the inactivation of lactate dehydrogenase

Previously, using γ-irradiation treatment, we isolated a mutant strain of Klebsiella pneumoniae (named GEM167) that showed high-level ethanol production from glycerol. In the present study, in an effort to enhance ethanol production, we used a deletion of the lactate dehydrogenase gene to engineer a mutant strain incapable of lactate synthesis. In the ΔldhA mutant of GEM167, the production of ethanol was significantly increased from 21.5 g/l to 28.9 g/l and from 0.93 g/(l h) to 1.2 g/(l h). Introduction of the Zymomonas mobilis pdc and adhII genes encoding pyruvate decarboxylase and aldehyde dehydrogenase, respectively, further improved the ethanol production level from glycerol to 31.0 g/l; this is the highest level reported to date.     

Production of (2S,3S)-2,3-butanediol and (3S)-acetoin from glucose using resting cells of Klebsiella pneumonia and Bacillus subtilis

Production of highly pure (2S,3S)-2,3-butanediol ((2S,3S)-2,3-BD) and (3S)-acetoin ((3S)-AC) in high concentrations is desirable but difficult to achieve. In the present study, glucose was first transformed to a mixture of (2S,3S)-2,3-BD and meso-2,3-BD by resting cells of Klebsiella pneumoniae CICC 10011, followed by biocatalytic resolution of the mixture by resting cells of Bacillus subtilis 168. meso-2,3-BD was transformed to (3S)-AC, leaving (2S,3S)-2,3-BD in the reaction medium. Using this approach, 12.5 g l(-1) (2S,3S)-2,3-BD and 56.7 g l(-1) (3S)-AC were produced. Stereoisomeric purity of (2S,3S)-2,3-BD and enantiomeric excess of (3S)-AC was 96.9 and 96.2%, respectively.     

Strain engineering of Saccharomyces cerevisiae for enhanced xylose metabolism

Efficient and rapid fermentation of all sugars present in cellulosic hydrolysates is essential for economic conversion of renewable biomass into fuels and chemicals. Xylose is one of the most abundant sugars in cellulosic biomass but it cannot be utilized by wild type Saccharomyces cerevisiae, which has been used for industrial ethanol production. Therefore, numerous technologies for strain development have been employed to engineer S. cerevisiae capable of fermenting xylose rapidly and efficiently. These include i) optimization of xylose-assimilating pathways, ii) perturbation of gene targets for reconfiguring yeast metabolism, and iii) simultaneous co-fermentation of xylose and cellobiose. In addition, the genetic and physiological background of host strains is an important determinant to construct efficient and rapid xylose-fermenting S. cerevisiae. Vibrant and persistent researches in this field for the last two decades not only led to the development of engineered S. cerevisiae strains ready for industrial fermentation of cellulosic hydrolysates, but also deepened our understanding of operational principles underlying yeast metabolism.     

Co-fermentation of a mixture of glucose and xylose to ethanol by Zymomonas mobilis and Pachysolen tannophilus

This research was designed to maximize ethanol production from a glucose-xylose sugar mixture (simulating a sugar cane bagasse hydrolysate) by co-fermentation with Zymomonas mobilis and Pachysolen tannophilus. The volumetric ethanol productivity of Z. mobilis with 50 g glucose/l was 2.87 g/l/h, giving an ethanol yield of 0.50 g/g glucose, which is 98% of the theoretical. P. tannophilus when cultured on 50 g xylose/l gave a volumetric ethanol productivity of 0.10 g/l/h with an ethanol yield of 0.15 g/g xylose, which is 29% of the theoretical. On optimization of the co-fermentation with the sugar mixture (60 g glucose/l and 40 g xylose/l) a total ethanol yield of 0.33 g/g sugar mixture, which is 65% of the theoretical yield, was obtained. The co-fermentation increased the ethanol yield from xylose to 0.17 g/g. Glucose and xylose were completely utilized and no residual sugar was detected in the medium at the end of the fermentation. The pH of the medium was found to be a good indicator of the fermentation status. The optimum conditions were a temperature of 30°C, initial inoculation with Z. mobilis and incubation with no aeration, inactivation of bacterium after the utilization of glucose, followed by inoculation with P. tannophilus and incubation with limited aeration.     

Effects of corn steep liquor on production of 2,3-butanediol and acetoin by Bacillus subtilis

The initial concentration of corn steep liquor (CSL) have remarkable effects on not only 2,3-butanediol (2,3-BD) and acetoin (metabolic precursor) production, but also on the ratio of 2,3-BD to acetoin. When a high concentration of CSL was supplemented, cell growth was improved, acetoin reductase (ACR) was stimulated, the concentration of 2,3-BD increased by 78.6%, acetoin decreased by 61.9%, and the ratio of 2,3-BD to acetoin increased by 3.69-fold. The acr gene, encoding ACR, was over-expressed in Bacillus subtilis. Compared to the control (parent strain), low levels of CSL in the engineered strain increased 2,3-BD concentration and the ratio 2,3-BD to acetoin by 13.9% and 39.5%, respectively, and decreased acetoin titer by 18.3%. Acetoin became a major product under low levels of CSL. Also, a knockout strain carrying an acr::cat insertion mutation was constructed. As expected, the loss of ACR activity led to an accumulation of acetoin in the supernatants of acr:: cat mutant cultures. Additionally, the productivity of acetoin was improved by high concentration of CSL. The results above demonstrate the feasibility of using B. subtilis for the production of not only 2,3-BD but also acetoin as a major product.     

An in vivo, label-free quick assay for xylose transport in Escherichia coli

Efficient use of xylose is necessary for economic production of biochemicals and biofuels from lignocellulosic materials. Current studies on xylose uptake for various microorganisms have been hampered by the lack of a facile assay for xylose transport. In this work, a rapid in vivo, label-free method for measuring xylose transport in Escherichia coli was developed by taking advantage of the Bacillus pumilus xylosidase (XynB), which cleaved a commercially available xylose analog, p-nitrophenyl-β-d-xylopyranoside (pNPX), to release a chromogenic group, p-nitrophenol (pNP). XynB was expressed alone or in conjunction with a Zymomonas mobilis glucose facilitator protein (Glf) capable of transporting xylose. This XynB-mediated transport assay was demonstrated in test tubes and 96-well plates with submicromolar concentrations of pNPX. Kinetic inhibition experiments validated that pNPX and xylose were competitive substrates for the transport process, and the addition of glucose (20 g/L) in the culture medium clearly diminished the transmembrane transport of pNPX and, thus, mimicked its inhibitory action on xylose uptake. This method should be useful for engineering of the xylose transport process in E. coli, and similar assay schemes can be extended to other microorganisms.     

Biofunctionalization of cellulosic fibres with l-cysteine: Assessment of antibacterial properties and mechanism of action against Staphylococcus aureus and Klebsiella pneumoniae

The main purpose of this work is to obtain a cotton-based textile material functionalized with l-cysteine (l-cys) to achieve an antimicrobial effect with potential application in biomedical, geriatric or pediatric textiles. The binding capacity of l-cys to cotton fibres was assessed through different functionalization strategies—surface activation and exhaustion processes. A subsequent analysis of the possible antibacterial action against Staphylococcus aureus and Klebsiella pneumoniae was performed according with the Japanese International standard ( JISL, 2008). To determine the mechanism of action of l-cys on the selected strains, flow cytometry was used.     

Alteration of xylose reductase coenzyme preference to improve ethanol production by Saccharomyces cerevisiae from high xylose concentrations

A K270R mutation of xylose reductase (XR) was constructed by site-direct mutagenesis. Fermentation results of the F106X and F106KR strains, which carried wild type XR and K270R respectively, were compared using different substrate concentrations (from 55 to 220 g/L). After 72 h, F106X produced less ethanol than xylitol, while F106KR produced ethanol at a constant yield of 0.36 g/g for all xylose concentrations. The xylose consumption rate and ethanol productivity increased with increasing xylose concentrations in F106KR strain. In particular, F106KR produced 77.6g/L ethanol from 220 g/L xylose and converted 100 g/L glucose and 100g/L xylose into 89.0 g/L ethanol in 72h, but the corresponding values of F106X strain are 7.5 and 65.8 g/L. The ethanol yield of F106KR from glucose and xylose was 0.42 g/g, which was 82.3% of the theoretical yield. These results suggest that the F106KR strain is an excellent producer of ethanol from xylose.     

Synergistic anti-bacterial and proteomic effects of epigallocatechin gallate on clinical isolates of imipenem-resistant Klebsiella pneumoniae

Imipenem-resistant Klebsiella pneumoniae (IRKP) were used to explore the synergistic anti-bacterial and proteomic effects of imipenem alone or in combination with epigallocatechin gallate (EGCg). The minimal inhibitory concentrations (MICs) of EGCG for 12 clinically isolated IRKP strains ranged from 300 to 650 μg/ml. Each of the 12 IRKP strains experienced a 4- to 64-fold reduction in the MIC of imipenem upon co-incubation with 0.25 × MIC level of EGCg. The time-kill method was used on the 12 IRKP clinical isolates to evaluate the bactericidal activities of imipenem alone or with EGCg. Compared to imipenem alone, EGCg with imipenem demonstrated enhanced bactericidal activity. Two-dimensional polyacrylamide gel electrophoresis identified eight down-regulated and four up-regulated proteins in the IRKP strain upon exposure to 1 × MIC of EGCg. Analysis of the outer membrane protein profiles of IRKP cultures treated with EGCg revealed unique changes in outer membrane proteins. In addition, scanning electron microscopic analysis demonstrated the presence of cells with wrinkled surfaces containing perforations and irregular rod-shaped forms after treatment with EGCg or imipenem. These studies demonstrate that EGCg can synergize the bacterial activity of imipenem and differentially stimulate the expression of various proteins in IRKP.