Fermentation of maltose and starch by Klebsiella oxytoca P2

Klebsiella oxytoca P2, which has genes from Zymomonas mobilis encoding the alcohol dehydrogenase and pyruvate decarboxylase integrated in its chromosome, fermented 50 g maltose/l to 25.4 g of ethanol/l. It also fermented 10, 20 and 40 g starch/l yielding 4, 8.4, and 17.7 g ethanol/l, respectively, representing 72, 75 and 78% of the theoretical yield. © Rapid Science Ltd. 1998     

Lethality and survival of Klebsiella oxytoca evoked by conjugative IncN group plasmids.

The transmission of plasmid pCU1 (or other IncN group plasmid) into a population of Klebsiella oxytoca cells reduces the viability of the population. A 2,400-bp region adjacent to traA is responsible for this phenotype and includes two regions, called kikA and kikC. Klebsiella cells which received this region and survived were found to acquire a chromosomal mutation which renders them immune to killing even after the plasmid is cured from the cells. To obtain insight into the mode of this apparent lethality, an appropriate pCU1lacZ derivative was constructed. It could be introduced with high efficiency into Klebsiella cells. Analyses of the resultant colonies indicate that the loss of viability is not a consequence of the death of plasmid-free segregants. On the contrary and unlike postsegregational killing by plasmids, cells survived by losing the plasmid or by acquiring, secondarily, a chromosomal mutation which confers immunity to killing.     

Fermentation of L-arabinose,D-xylose and D-glucose by ethanologenic recombinant Klebsiella oxytoca strain P2

Summary Recombinant Klebsiella oxytoca strain P2 carrying genes for pyruvate decarboxylase and alcohol dehydrogenase from Zymomonas mobilis was evaluated for its ability to ferment arabinose, xylose and glucose alone and in mixtures in pH-controlled batch fermentations. This organism produced 0.34–0.43 g ethanol/g sugar at pH 6.0 and 30°C on 8% sugar substrate and demonstrated a preference for glucose. Sugar utilization was glucose > arabinose > xylose and ethanol production was xylose > glucose > arabinose.     

Ethanol production from cellobiose, amorphous cellulose, and crystalline cellulose by recombinant Klebsiella oxytoca containing chromosomally integrated Zymomonas mobilis genes for ethanol production and plasmids expressing thermostable cellulase genes from Clostridium thermocellum.

The Zymomonas mobilis genes for ethanol production have been integrated into the chromosome of Klebsiella oxytoca M5A1. The best of these constructs, strain P2, produced ethanol efficiently from cellobiose in addition to monomeric sugars. Utilization of cellobiose and cellotriose by this strain eliminated the requirement for external beta-glucosidase and reduced the amount of commercial cellulase needed to ferment Solka Floc SW40 (primarily crystalline cellulose). The addition of plasmids encoding endoglucanases from Clostridium thermocellum resulted in the intracellular accumulation of thermostable enzymes as coproducts with ethanol during fermentation. The best of these, strain P2(pCT603T) containing celD, was used to hydrolyze amorphous cellulose to cellobiose and produce ethanol in a two-stage process. Strain P2(pCT603T) was also tested in combination with commercial cellulases. Pretreatment of Solka Floc SW40 at 60 degrees C with endoglucanase D substantially reduced the amount of commercial cellulase required to ferment Solka Floc. The stimulatory effect of the endoglucanase D pretreatment may result from the hydrolysis of amorphous regions, exposing additional sites for attack by fungal cellulases. Since endoglucanase D functions as part of a complex in C. thermocellum, it is possible that this enzyme may complex with fungal enzymes or bind cellulose to produce a more open structure for hydrolysis.     

Ethanol production from cellobiose, amorphous cellulose, and crystalline cellulose by recombinant Klebsiella oxytoca containing chromosomally integrated Zymomonas mobilis genes for ethanol production and plasmids expressing thermostable cellulase genes from Clostridium thermocellum.

The Zymomonas mobilis genes for ethanol production have been integrated into the chromosome of Klebsiella oxytoca M5A1. The best of these constructs, strain P2, produced ethanol efficiently from cellobiose in addition to monomeric sugars. Utilization of cellobiose and cellotriose by this strain eliminated the requirement for external beta-glucosidase and reduced the amount of commercial cellulase needed to ferment Solka Floc SW40 (primarily crystalline cellulose). The addition of plasmids encoding endoglucanases from Clostridium thermocellum resulted in the intracellular accumulation of thermostable enzymes as coproducts with ethanol during fermentation. The best of these, strain P2(pCT603T) containing celD, was used to hydrolyze amorphous cellulose to cellobiose and produce ethanol in a two-stage process. Strain P2(pCT603T) was also tested in combination with commercial cellulases. Pretreatment of Solka Floc SW40 at 60 degrees C with endoglucanase D substantially reduced the amount of commercial cellulase required to ferment Solka Floc. The stimulatory effect of the endoglucanase D pretreatment may result from the hydrolysis of amorphous regions, exposing additional sites for attack by fungal cellulases. Since endoglucanase D functions as part of a complex in C. thermocellum, it is possible that this enzyme may complex with fungal enzymes or bind cellulose to produce a more open structure for hydrolysis.     

产酸克雷伯氏菌M5al普鲁兰酶的异源表达及酶学性质研究

普鲁兰酶(EC 3.2.1.41)是一类淀粉脱支酶,能够特异性水解淀粉中的α-1,6-糖苷键,从而提高淀粉的利用率,在以淀粉为原料的食品、纺织、生物燃料和洗涤剂等行业中具有重要的应用价值。本研究以产酸克雷伯氏菌Klebsiella oxytoca M5al基因组DNA为模板,将PCR扩增得到的普鲁兰酶基因pul A克隆至表达载体p ET28a(+),构建好的重组质粒转化大肠杆菌Escherichia coli BL21(DE3),在培养基中添加0.5 mmol/L异丙基硫代半乳糖苷(IPTG)的条件下对该酶基因进行诱导表达,经镍柱纯化获得重组普鲁兰酶用于酶学性质研究。SDS-PAGE及Western Blot检测显示普鲁兰酶基因pul A在上述大肠杆菌宿主中成功获得了表达。该重组酶最适反应p H5.5,最适温度60℃。金属离子对酶活性有一定影响。Mn2+对酶活促进作用显著;Fe3+、Mg2+、Fe2+对酶活只有微弱的促进作用,而Cu2+对酶活造成强烈抑制。来源于Klebsiella oxytoca M5al的普鲁兰酶最适催化条件符合工业生产中淀粉糖化工艺的要求,具有应用于淀粉工业的潜力。     

Saccharification and fermentation of Sugar Cane bagasse by Klebsiella oxytoca P2 containing chromosomally integrated genes encoding the Zymomonas mobilis ethanol pathway

Pretreatment of sugar cane bagasse is essential for a simultaneous saccharification and fermentation (SSF) process which uses recombinant Klebsiella oxytoca strain P2 and Genencor Spezyme CE. Strain P2 has been genetically engineered to express Zymomonas mobilis genes encoding the ethanol pathway and retains the native ability to transport and metabolize cellobiose (minimizing the need for extracellular cellobiase). In SSF studies with this organism, both the rate of ethanol production and ethanol yield were limited by saccharification at 10 and 20 filter papaer units (FPU) g(-1) acid-treated bagasse. Dilute slurries of biomass were converted to ethanol more efficiently (over 72% of theoretical yield) in simple batch fermentations than slurries containing high solids albeit with the production of lower levels of ethanol. With high solids (i.e., 160 g acid-treated bagasse L(-1)), a combination of 20 FPU cellulase g(-1) bagasse, preincubation under saccharification conditions, and additional grinding (to reduce particle size) were required to produce ca. 40 g ethanol L(-1). Alternatively, almost 40 g ethanol L(-1) was produced with 10 FPU cellulase g(-1) bagasse by incorporating a second saccharification step (no further enzyme addition) followed by a second inoculation and short fermentation. In this way, a theoretical ethanol yield of over 70% was achieved with the production of 20 g ethanol 800 FPU(-1) of commercial cellulase. (c) 1994 John Wiley & Sons, Inc.     

Five additional genes in the pulC-O operon of the gram-negative bacterium Klebsiella oxytoca UNF5023 which are required for pullulanase secretion

Summary DNA sequence analysis, Tnpho and Tntac-1, mutagenesis, deletion analysis, expression under bacteriophage T7 gene 10 promoter control, subcellular fractionation and complementation tests were used to study the function of DNA located in the centre of thepulC-O operon fromKlebsiella oxytoca strain UNF5023. The characterized region of the operon includes five genes (pulG,pulH,pulI,pulJ andpulK) coding for apparently integral inner membrane proteins which are required for pullulanase secretion. The results presented here and previously show that thepulC-O operon contains at least 11 pullulanase secretion genes.     

Isolation and characterization of kikA, a region on IncN group plasmids that determines killing of Klebsiella oxytoca.

Transfer of the IncN group plasmid pCU1 from Escherichia coli to Klebsiella oxytoca by conjugation kills a large proportion (90 to 95%) of the recipients of plasmid DNA, whereas transfer to E. coli or even to the closely related Enterobacter aerogenes does not. Two regions, kikA and kikB, have been identified on pCU1 that contribute to the Kik (killing in klebsiellas) phenotype. We have localized the kikA region to 500 bp by deletion analysis and show by DNA-DNA hybridization that kikA is highly conserved among the plasmids of incompatibility group N. The expression in K. oxytoca of kikA under the control of the strong inducible E. coli tac promoter results in loss of cell viability. The nucleotide sequence showed two overlapping open reading frames (ORFs) within the kikA region. The first ORF codes for a putative polypeptide of 104 amino acids (ORF104). The second ORF codes for a 70-amino-acid polypeptide (ORF70). The properties of the putative protein encoded by ORF104 and gene fusions of kikA to alkaline phosphatase by using TnphoA suggest that killing may involve an association with the bacterial membrane; however, we could not rule out the possibility that ORF70 plays a role in the Kik phenotype.     

Fermentation and evaluation of Klebsiella pneumoniae and K. oxytoca on the production of 2,3-butanediol

Klebsiella is one of the genera that has shown unbeatable production performance of 2,3-butanediol (2,3-BD), when compared to other microorganisms. In this study, two Klebsiella strains, K. pneumoniae (DSM 2026) and K. oxytoca (ATCC 43863), were selected and evaluated for 2,3-BD production by batch and fed-batch fermentations using glucose as a carbon source. Those strains' morphologies, particularly their capsular structures, were analyzed by scanning electron microscopy (SEM). The maximum titers of 2,3-BD by K. pneumoniae and K. oxytoca during 10 h batch fermentation were 17.6 and 10.9 g L(-1), respectively; in fed-batch cultivation, the strains showed the maximum titers of 50.9 and 34.1 g L(-1), respectively. Although K. pneumoniae showed higher productivity, SEM showed that it secreted large amounts of capsular polysaccharide, increasing pathogenicity and hindering the separation of cells from the fermentation broth during downstream processing.     

Fermentation of 1,3-propanediol by a lactate deficient mutant of Klebsiella oxytoca under microaerobic conditions

Klebsiella oxytoca M5al is an excellent 1,3-propanediol (1,3-PD) producer, but too much lactic acid yielded greatly lessened the fermentation efficiency for 1,3-PD. To counteract the disadvantage, four lactate deficient mutants were obtained by knocking out the ldhA gene of lactate dehydrogenase (LDH) of K. oxytoca M5al. The LDH activities of the four mutants were from 3.85 to 6.92% of the parental strain. The fed-batch fermentation of 1,3-PD by mutant LDH3, whose LDH activity is the lowest, was studied. The results showed that higher 1,3-PD concentration, productivity, and molar conversion rate from glycerol to 1,3-PD can be gained than those of the wild type strain and no lactic acid is produced under both anaerobic and microaerobic conditions. Sucrose fed during the fermentation increased the conversion and sucrose added at the beginning increased the productivity. In fed-batch fermentation with sucrose as cosubstrate under microaerobic conditions, the 1,3-PD concentration, conversion, and productivity were improved significantly to 83.56 g l⁻¹, 0.62 mol mol⁻¹, and 1.61 g l⁻¹ h⁻¹, respectively. Furthermore, 60.11 g l⁻¹ 2,3-butanediol was also formed as major byproduct in the broth.     

PuIO, a component of the pullulanase secretion pathway of Klebsiella oxytoca, correctly and efficiently processes gonococcal type IV prepilin in Escherichia coli

The PulO protein required for extracellular secretion of pullulanase by Klebsiella oxytoca is known to be highly homologous to two type IV prepilin peptidases, namely XcpA(PilD) (Pseudomonas aeruginosa) and TcpJ (Vibrio cholerae). The predicted prepilin peptidase activity of PulO was confirmed by showing that it could correctly process the product of the cloned pilE.1 type IV pilin structural gene from Neisseria gonorrhoeae in Escherichia coli. The P. aeruginosa prepilin peptidase and another putative prepilin peptidase, ComC from Bacillus subtilis, also processed prePilE. Subcellular fractionation showed that the pilE gene product that had been processed by PulO remained associated with the cytoplasmic membrane, as did the unprocessed precursor. PulO was also shown to process three of the four prePilE-PhoA hybrids tested. Southern hybridization experiments suggest that a pulO homologue is present in the N. gonorrhoeae chromosome.     

Cloning of the pullulanase gene and overproduction of pullulanase in Escherichia coli and Klebsiella aerogenes.

The pullulanase gene (pul) of Klebsiella aerogenes was cloned into a pBR322 vector in Escherichia coli. Deletion analysis of the recombinant plasmid showed that the pul coding sequence, probably with the regulator gene, was located entirely within a 4.2-kilobase segment derived from the chromosomal DNA of K. aerogenes. E. coli cells carrying the recombinant plasmids produced about three- to sevenfold more pullulanase than did the wild-type strain of K. aerogenes W70. When the cloned cells of E. coli were grown with pullulan or maltose, most pullulanase was produced intracellularly, whereas K. aerogenes produced pullulanase extracellularly. Transfer of the plasmid containing the pul gene into K. aerogenes W70 resulted in about a 20- to 40-fold increase in total production of pullulanase, and the intracellular enzyme level was about 100- to 150-fold higher than that of the parent strain W70. The high level of pullulanase activity in K. aerogenes cells carrying the recombinant plasmid was maintained for at least 2 weeks.     

Properties of a cyclodextrin-specific, unusual porin from Klebsiella oxytoca.

The function of CymA, 1 of the 10 gene products involved in cyclodextrin uptake and metabolism by Klebsiella oxytoca, was characterized. CymA is essential for growth on cyclodextrins, but it can also complement the deficiency of a lamB (maltoporin) mutant of Escherichia coli for growth on linear maltodextrins, indicating that both cyclic and linear oligosaccharides are accepted as substrates. CymA was overproduced in E. coli and purified to apparent homogeneity. CymA is a component of the outer membrane, is processed from a signal peptide-containing precursor, and possesses a high content of antiparallel beta-sheet. Incorporation of CymA into lipid bilayers and conductance measurements revealed that it forms ion-permeable channels, which exhibit a substantial current noise. CymA-induced membrane conductance decreased considerably upon addition of alpha-cyclodextrin. Titration experiments allowed the calculation of a half-saturation constant, K(S), of 28 microM for its binding to CymA. CymA assembled in vitro to two-dimensionally crystalline tubular membranes, which, on electron microscopy, are characterized by a p1-related two-sided plane group. The crystallographic unit cell contains four monomeric CymA molecules showing a central pore. The lattice parameters are a = 16.1 nm, b = 3.8 nm, gamma = 93 degrees. CymA does not form trimeric complexes in lipid membranes and shows no tendency to trimerize in solution. CymA thus is an atypical porin with novel properties specialized to transfer cyclodextrins across the outer membrane.     

Export and secretion of the lipoprotein pullulanase by Klebsiella pneumoniae

Pullulanase, a secreted lipoprotein of Klebsiella pneumoniae, is initially localized to the outer face of the outer membrane, as shown by protease and substrate accessibility and by immunofluorescence tests. Freeze-thaw disruption of these cells released both membrane-associated and apparently soluble forms of pullulanase. Membrane-associated pullulanase co-fractionated with authentic outer membrane vesicles upon isopycnic sucrose-gradient centrifugation, whereas the quasi-soluble form had the same equilibrium density as inner membrane vesicles and extracellular pullulanase aggregates. The latter also contained outer membrane maltoporin, but were largely devoid of other membrane components including LPS and lipids. K. pneumoniae carrying multiple copies of the pullulanase structural gene (pulA) produced increased amounts of cell-associated and secreted pullulanase, but a large proportion of the enzyme was neither exposed on the cell surface nor released into the medium, even after prolonged incubation. This suggests that factors necessary for pullulanase secretion were saturated by the over-produced pullulanase. When pulA was expressed under lacZ promotor control, the pullulanase which was produced was not exposed on the cell surface at any time, suggesting that pullulanase secretion genes are not expressed constitutively, and raising the possibility that they, like pulA, may be part of the maltose regulon.     

Enhanced 2,3-Butanediol Production by Optimizing Fermentation Conditions and Engineering Klebsiella oxytoca M1 through Overexpression of Acetoin Reductase

Microbial production of 2,3-butanediol (2,3-BDO) has been attracting increasing interest because of its high value and various industrial applications. In this study, high production of 2,3-BDO using a previously isolated bacterium Klebsiella oxytoca M1 was carried out by optimizing fermentation conditions and overexpressing acetoin reductase (AR). Supplying complex nitrogen sources and using NaOH as a neutralizing agent were found to enhance specific production and yield of 2,3-BDO. In fed-batch fermentations, 2,3-BDO production increased with the agitation speed (109.6 g/L at 300 rpm vs. 118.5 g/L at 400 rpm) along with significantly reduced formation of by-product, but the yield at 400 rpm was lower than that at 300 rpm (0.40 g/g vs. 0.34 g/g) due to acetoin accumulation at 400 rpm. Because AR catalyzing both acetoin reduction and 2,3-BDO oxidation in K. oxytoca M1 revealed more than 8-fold higher reduction activity than oxidation activity, the engineered K. oxytoca M1 overexpressing the budC encoding AR was used in fed-batch fermentation. Finally, acetoin accumulation was significantly reduced by 43% and enhancement of 2,3-BDO concentration (142.5 g/L), yield (0.42 g/g) and productivity (1.47 g/L/h) was achieved compared to performance with the parent strain. This is by far the highest titer of 2,3-BDO achieved by K. oxytoca strains. This notable result could be obtained by finding favorable fermentation conditions for 2,3-BDO production as well as by utilizing the distinct characteristic of AR in K. oxytoca M1 revealing the nature of reductase.     

Biosynthesis and secretion of pullulanase, a lipoprotein from Klebsiella aerogenes

We constructed, by site-directed mutagenesis, a mutant pullulanase gene in which the cysteine residue in a pentapeptide sequence, Leu16-Leu-Ser-Gly-Cys20 within the NH2-terminal region of pullulanase from Klebsiella aerogenes, is replaced by serine (Ser20). The modification, processing, and subcellular localization of the mutant pullulanase were studied. Labeling studies with [3H]palmitate and immunoprecipitation with mouse antiserum raised against pullulanase showed that the wild form of both the extracellular and intracellular pullulanases contained lipids, whereas the mutant enzyme was not modified with lipids. Only the Cys20 was modified with glyceryl lipids. The bulk of the mutant pullulanase was located in the periplasm, but a portion of the unmodified, mutant pullulanase was secreted into the medium. Mutant pullulanases from the extracellular and the periplasm were purified and their NH2-terminal sequences were determined. Both the mutant pullulanases were cleaved between residues of Ser13 and Leu14 which is 6-amino acid residues upstream of the lipid modified pullulanase cleavage site. This new cleavage was resistant to globomycin, an inhibitor of the prolipoprotein signal peptidase of Escherichia coli. These results indicate that the pentapeptide sequence plays an important role in maturation and translocation of pullulanase in K. aerogenes. However, the modification of pullulanase with lipids seems to be not essential for export of the enzyme across the outer membrane.     

Conversion of xylan to ethanol by ethanologenic strains of Escherichia coli and Klebsiella oxytoca.

A two-stage process was evaluated for the fermentation of polymeric feedstocks to ethanol by a single, genetically engineered microorganism. The truncated xylanase gene (xynZ) from the thermophilic bacterium Clostridium thermocellum was fused with the N terminus of lacZ to eliminate secretory signals. This hybrid gene was expressed at high levels in ethanologenic strains of Escherichia coli KO11 and Klebsiella oxytoca M5A1(pLOI555). Large amounts of xylanase (25 to 93 mU/mg of cell protein) accumulated as intracellular products during ethanol production. Cells containing xylanase were harvested at the end of fermentation and added to a xylan solution at 60 degrees C, thereby releasing xylanase for saccharification. After cooling, the hydrolysate was fermented to ethanol with the same organism (30 degrees C), thereby replenishing the supply of xylanase for a subsequent saccharification. Recombinant E. coli metabolized only xylose, while recombinant K. oxytoca M5A1 metabolized xylose, xylobiose, and xylotriose but not xylotetrose. Derivatives of this latter organism produced large amounts of intracellular xylosidase, and the organism is presumed to transport both xylobiose and xylotriose for intracellular hydrolysis. By using recombinant M5A1, approximately 34% of the maximal theoretical yield of ethanol was obtained from xylan by this two-stage process. The yield appeared to be limited by the digestibility of commercial xylan rather than by a lack of sufficient xylanase or by ethanol toxicity. In general form, this two-stage process, which uses a single, genetically engineered microorganism, should be applicable for the production of useful chemicals from a wide range of biomass polymers.     

Conversion of xylan to ethanol by ethanologenic strains of Escherichia coli and Klebsiella oxytoca.

A two-stage process was evaluated for the fermentation of polymeric feedstocks to ethanol by a single, genetically engineered microorganism. The truncated xylanase gene (xynZ) from the thermophilic bacterium Clostridium thermocellum was fused with the N terminus of lacZ to eliminate secretory signals. This hybrid gene was expressed at high levels in ethanologenic strains of Escherichia coli KO11 and Klebsiella oxytoca M5A1(pLOI555). Large amounts of xylanase (25 to 93 mU/mg of cell protein) accumulated as intracellular products during ethanol production. Cells containing xylanase were harvested at the end of fermentation and added to a xylan solution at 60 degrees C, thereby releasing xylanase for saccharification. After cooling, the hydrolysate was fermented to ethanol with the same organism (30 degrees C), thereby replenishing the supply of xylanase for a subsequent saccharification. Recombinant E. coli metabolized only xylose, while recombinant K. oxytoca M5A1 metabolized xylose, xylobiose, and xylotriose but not xylotetrose. Derivatives of this latter organism produced large amounts of intracellular xylosidase, and the organism is presumed to transport both xylobiose and xylotriose for intracellular hydrolysis. By using recombinant M5A1, approximately 34% of the maximal theoretical yield of ethanol was obtained from xylan by this two-stage process. The yield appeared to be limited by the digestibility of commercial xylan rather than by a lack of sufficient xylanase or by ethanol toxicity. In general form, this two-stage process, which uses a single, genetically engineered microorganism, should be applicable for the production of useful chemicals from a wide range of biomass polymers.