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We have previously demonstrated the production of glucooligosaccharides via a fermentation of sucrose with Leuconostoc mesenteroides NRRL B-742 using sodium hydroxide (NaOH) to control the pH. Because NaOH is expensive, we sought to minimize the cost of our process by substituting hydrated lime and saccharate of lime (lime sucrate) in its place. The yield of glucooligosaccharides using either 5 % lime (41.4 ± 0.5 g/100 g) or 5 % lime sucrate (40.0 ± 1.4 g/100 g) were both similar to the NaOH control (42.4 ± 1.5 g/100 g). Based on this, it appears that the cost associated with pH control in our process can be reduced by a factor of approximately 2.4 using lime instead of NaOH. Because our chromatographic stage is based on a Ca(2+)-form resin to separate glucooligosaccharides, the use of lime not only negates the need for costly de-salting via ion-exchange (elimination of two ion-exchange sections) prior to separation, but also greatly reduces the resin regeneration cost.

In this study, sugarcane bagasse was pretreated with ammonium hydroxide, and the effectiveness of the pretreatment on enzyme hydrolysis and ethanol production was examined. Bagasse was soaked in ammonium hydroxide and water at a ratio of 1:0.5:8 for 0-4 days at 70 °C. Approximately, 14-45 % lignin, 2-6 % cellulose, and 13-22 % hemicellulose were removed during a 0.5- to 4-day ammonia soaking period. The highest glucan conversion of sugarcane bagasse soaked in dilute ammonia at moderate temperature by cellulase was accomplished at 78 % with 75 % of the theoretical ethanol yield. Under the same conditions, untreated bagasse resulted in a cellulose digestibility of 29 and 27 % of the theoretical ethanol yield. The increased enzymatic digestibility and ethanol yields after dilute ammonia pretreatment was related to a combined effect of the removal of lignin and increase in the surface area of fibers.

A challenge facing the biofuel industry is to develop an economically viable and sustainable biorefinery. The existing potential biorefineries in Louisiana, raw sugar mills, operate only 3 months of the year. For year-round operation, they must adopt other feedstocks, besides sugar cane, as supplemental feedstocks. Energy cane and sweet sorghum have different harvest times, but can be processed for bio-ethanol using the same equipment. Juice of energy cane contains 9.8% fermentable sugars and that of sweet sorghum, 11.8%. Chemical composition of sugar cane bagasse was determined to be 42% cellulose, 25% hemicellulose, and 20% lignin, and that of energy cane was 43% cellulose, 24% hemicellulose, and 22% lignin. Sweet sorghum was 45% cellulose, 27% hemicellulose, and 21% lignin. Theoretical ethanol yields would be 3,609 kg per ha from sugar cane, 12,938 kg per ha from energy cane, and 5,804 kg per ha from sweet sorghum.

A series of oligosaccharides (cellobio-oligosaccharides) ranging from degrees of polymer 3 to 6 were synthesized by Leuconostoc mesenteroides B-512 FMCM in the presence of cellobiose. The major oligosaccharides were the trisaccharides, α-D-glucopyranosyl-(1 → 2)-β-D-glucopyranosyl-(1 → 4)-D-glucopyranose and α-D-glucopyranosyl-(1 → 6)-β-D-glucopyranosyl-(1 → 4)-D-glucopyranose. These cellobio-oligosaccharides were inhibitory on mutansucrase, an enzyme that causes dental caries. They were also found to be effective antifungal agents against Aspergillus terreus acting by inhibiting β-(1 → 3)-glucan synthase, which is required for fungal cell wall formation.

The economics driving biorefinery development requires high value-added products such as cellobiose for financial feasibility. This research describes a simple technology for increasing cellobiose yields during lignocellulosic hydrolysis. The yield of cellobiose produced during cellulose hydrolysis was maximized by modification of reaction conditions. The addition of an inhibitor from the group that includes glucose oxidase, gluconolactone, and gluconic acid during cellulase hydrolysis of cellulose increased the amount of cellobiose produced. The optimal conditions for cellobiose production were determined for four factors; reaction time, cellulase concentration, cellulose concentration, and inhibitor concentration using a Box-Behnken experimental design. Gluconolactone in the cellulase system resulted in the greatest production of cellobiose (31.2%) from cellulose. The yield of cellobiose was 23.7% with glucose oxidase, similar to 21.9% with gluconic acid.

Sugarcane bagasse is the major by-product of the sugar industry. It has a great potential for the production of biofuels and chemicals due to its considerable amount of cellulose and hemicellulose. In this study, we investigated a simple and economic pretreatment process using dilute ammonia for the storage of sugarcane bagasse. Sugarcane bagasse was stored in 0, 0.03, and 0.3% (w/w) ammonium hydroxide in a closed bottle for 40 days at 30 degrees C under atmospheric pressure without any agitation or circulation. Samples were taken every 10 days and analyzed for changes on lignin, cellulose, hemicellulose composition, ammonia concentration, and microbial counts. Biomass storage for 40 days at 0.3% ammonium hydroxide removed 46% of lignin and retained 100% cellulose and 73% hemicellulose.

Reactive oxygen species (ROS) such as singlet oxygen ((1)O(2)), superoxide (O(2)(-)), hydroxyl radicals (OH(*)), or hypochlorite ion (OCl(-)), can remove both hemicellulose and lignin from lignocellulose. Ox-B (US Patent 6,866,870), an ROS producing solution containing sodium hypochlorite and hydrogen peroxide, was investigated for its ability to oxidize sugarcane bagasse. Treatment with equivalent amounts of hypochlorite produced similar results. Ox-B differentiated from hypochlorite when low concentration treatments were used and they were followed by a caustic wash. Cellulases hydrolyzed 80-100% of the cellulose present after Ox-B/caustic treatment compared to 40% or less for NaOCl/caustic treatment. Ox-B treatment was temperature independent and complete within 3h. It was pH dependent, with best results obtained when the pH was controlled at 8. Although highly effective, in order for Ox-B to be industrially feasible for alcohol production, the chemical cost must decrease to justify its use.

There is a growing market for oligosaccharides as sweeteners, prebiotics, anticariogenic compounds, and immunostimulating agents in both food and pharmaceutical industries. Interest in novel carbohydrate-based products has grown because of their reduced toxicity and low immune response. Cellobiose is potentially valuable as a nondigestible sugar. The reaction of cellobiose, as an acceptor with a sucrose as a donor, catalyzed by a dextransucrase from Leuconostoc mesenteroides B-512FMCM, produced a series of cellobio-oligosaccharides. This production system was optimized using a Box-Behnken experimental design for 289 mM of sucrose and 250 mM of cellobiose and 54 U of the enzyme at pH 5.2 and 30 degrees C, to produce maximum yields of oligosaccharide.

Sugar cane bagasse consists of hemicellulose (24%) and cellulose (38%), and bioconversion of both fractions to ethanol should be considered for a viable process. We have evaluated the hydrolysis of pretreated bagasse with combinations of cellulase, beta-glucosidase, and hemicellulase. Ground bagasse was pretreated either by the AFEX process (2NH(3): 1 biomass, 100 degrees C, 30 min) or with NH(4)OH (0.5 g NH(4)OH of a 28% [v/v] per gram dry biomass; 160 degrees C, 60 min), and composition analysis showed that the glucan and xylan fractions remained largely intact. The enzyme activities of four commercial xylanase preparations and supernatants of four laboratory-grown fungi were determined and evaluated for their ability to boost xylan hydrolysis when added to cellulase and beta-glucosidase (10 filter paper units [FPU]: 20 cellobiase units [CBU]/g glucan). At 1% glucan loading, the commercial enzyme preparations (added at 10% or 50% levels of total protein in the enzyme preparations) boosted xylan and glucan hydrolysis in both pretreated bagasse samples. Xylanase addition at 10% protein level also improved hydrolysis of xylan and glucan fractions up to 10% glucan loading (28% solids loading). Significant xylanase activity in enzyme cocktails appears to be required for improving hydrolysis of both glucan and xylan fractions of ammonia pretreated sugar cane bagasse.

Aims: To evaluate a sodium hypochlorite and hydrogen peroxide solution (Ox-B7) as a potential decontaminant of Bacillus subtilis spore-contaminated surface materials (porous and nonporous)., Methods and Results: Test materials were contaminated with B. subtilis spores to a final concentration in the range of 5.7-6.6 log CFU cm(-2). Ox-B7 reduced spore counts by 99.999% (5 log) for both porous and nonporous surfaces within a 5-min contact. Treatment with equivalent concentrations of only sodium hypochlorite reduced spore counts by 99% (2 log) on porous materials and by 99.99% (4 log) on nonporous materials. Hydrogen peroxide treatments reduced spores by less than 90% (<1 log) on both porous and nonporous materials when compared with untreated samples., Conclusions: A combination of sodium hypochlorite and hydrogen peroxide (Ox-B7) effectively killed B. subtilis spores on both porous and nonporous surface materials., Significance and Impact of the Study: The combination of sodium hypochlorite and hydrogen peroxide can be used as an alternative disinfectant of spore-contaminated surface materials, as it is more effective than when hydrogen peroxide or sodium hypochlorite are used separately.

Aims: To evaluate both the antimicrobial activity and the effectiveness of a combination of sodium hypochlorite and hydrogen peroxide (Ox-B) for killing Pseudomonas aeruginosa ATCC 19142 cells and removing P. aeruginosa biofilms on aluminum or stainless steel surfaces., Methods and Results: Pseudomonas aeruginosa biofilms were developed in tryptic soy broth containing vertically suspended aluminium or stainless steel plates. Biofilms were exposed to a mixed sodium hypochlorite and hydrogen peroxide solution as a sanitizer for 1, 5 and 20 min. The sanitizer was then neutralized, the cells dislodged from the test surfaces, and viable cells enumerated. Cell morphologies were determined using scanning (SEM) and transmission electron microscopy (TEM). Cell viability was determined by confocal scanning laser microscopy (CSLM). Biofilm removal was monitored by Fourier transform infrared (FTIR) spectrophotometry. Cell numbers were reduced by 5-log to 6-log after 1 min exposure and by 7-log after 5 min exposure to Ox-B. No viable cells were detected after a 20 min exposure. Treatment with equivalent concentrations of sodium hypochlorite reduced viable numbers by 3-log to 4-log after 1 min exposure and by 4-log to 6-log after 5 min, respectively. A 20 min exposure achieved a 7-log reduction. Hydrogen peroxide at test concentration treatments showed no effect. FTIR analysis of treated pseudomonad biofilms on aluminium or stainless steel plates showed either a significant reduction or complete removal of biofilm material after a 5 min exposure to the mixed sodium hypochlorite and hydrogen peroxide solution. SEM and TEM images revealed damage to cell wall and cell membranes., Conclusions: A combination of sodium hypochlorite and hydrogen peroxide effectively killed P. aeruginosa cells and removed biofilms from both stainless steel and aluminium surfaces., Significance and Impact of the Study: The combination of sodium hypochlorite and hydrogen peroxide can be used as an alternative disinfectant and/or biofilm remover of contaminated food processing equipment.

In this study, three epigallocatechin gallate glycosides were synthesized by the acceptor reaction of a glucansucrase produced by Leuconostoc mesenteroides B-1299CB with epigallocatechin gallate (EGCG) and sucrose. Each of these glycosides was then purified, and the structures were assigned as follows: epigallocatechin gallate 7-O-alpha-D-glucopyranoside (EGCG-G1); epigallocatechin gallate 4'-O-alpha-D-glucopyranoside (EGCG-G1'); and epigallocatechin gallate 7,4'-O-alpha-D-glucopyranoside (EGCG-G2). One of these compounds (EGCG-G1) was a novel compound. The EGCG glycosides exhibited similar or slower antioxidant effects, depending on their structures (EGCG > or = EGCG-G1 > EGCG-G1' > EGCG-G2), and also manifested a higher degree of browning resistance than was previously noted in EGCG. Also, EGCG-G1, EGCG-G1', and EGCG-G2 were 49, 55, and 114 times as water soluble, respectively, as EGCG.

A newly developed compound derived by fermentation, isomaltooligosaccharide (IMO), was hypothesized to enrich cecal bifidobacterial populations and reduce colonization levels of Salmonella in the ceca of broiler chickens. Broiler starter diets were prepared with final IMO concentrations of 1% (wt/wt), 2% (wt/wt), and 4% (wt/wt) and a control diet without IMO supplementation. Chickens were divided into 4 groups and challenged with 10(8) cell of Salmonlella enterica ser. Typhimurium with 200 microg/mL nalidixic acid resistant (S. Typhimurium Nalr) after 7 d of placement. The experiment was done in 3 replications. IMO-supplemented diets resulted in significantly higher cecal bifidobacteria compared with the control diet (P < 0.05). However, there was no significant difference in bifidobacteria counts among the treatment groups. Chickens fed diets with 1% IMO had a significant 2-log reduction in the level of inoculated S. Typhimurium Nalr (P < 0.05) present in, the ceca compared with the control group, but no differences were found between the control group and the groups fed 2 or 4% IMO for S. Typhimurium Nalr. No differences in feed consumption, feed conversion, or feed efficiency compared with the control group were observed; however, the result showed a significant reduction in weight for birds fed 1% IMO diet compared with those fed the control diet.

Leuconostoc mesenteroides B-512 FMC produces dextran and levan using sucrose. Because of the industrial importance of dextrans and oligosaccharides synthesized by dextransucrase (one of glycansucrases from L. mesenteroides), much is known about the dextransucrase, including expression and regulation of gene. However, no detailed report about levansucrase, another industrially important glycansucrase from L. mesenteroides, and its gene was available. In this paper, we report the first-time isolation and molecular characterization of a L. mesenteroides levansucrase gene (m1ft). The gene m1ft is composed of 1272-bp nucleotides and codes for a protein of 424 amino acid residues with calculated molecular mass of 47.1 kDa. The purified protein was estimated to be about 51.7 kDa including a His-tag based on SDS-PAGE. It showed an activity band at 103 kDa on a non-denaturing SDS-PAGE, indicating a dimeric form of the active M1FT. M1FT levan structure was confirmed by NMR and dot blot analysis with an anti-levan-antibody. M1FT converted 150 mM sucrose to levan (18%), 1-kestose (17%), nystose (11%) and 1,1,1-kestopentaose (7%) with the liberation of glucose. The M1FT enzyme produced erlose [O-alpha-D-glucopyranosyl-(1-->4)-O-alpha-D-glucopyranosyl-(1-->2)-beta-D-fructofuranoside] as an acceptor product with maltose. The optimum temperature and pH of this enzyme for levan formation were 30 degrees C and pH 6.2, respectively. M1FT levansucrase activity was completely abolished by 1 mM Hg2+ or Ag2+. The Km and Vmax values for levansucrase were calculated to be 26.6 mM and 126.6 micromol min-1 mg-1.

Metabolic acids produced by oral pathogens demineralize tooth surfaces, leading to dental caries. Glucosyltransferases are the key factor in this process. We synthesized various modified oligosaccharides and tested them for their inhibitory effects on glucosyltransferase activity. Oligosaccharides were produced using a mixed-culture fermentation of Lipomyces starkeyi and Leuconostoc mesenteroides and then further modified as iron- and sulfate-oligosaccharides. Iron- and sulfate-oligosaccharides reduced glucosyltransferase activity of Streptococci from 17% to 43% and prevented the formation of insoluble biomass on the surface of glass vials or stainless steel wires in the presence of sucrose. They also reduced the growth and acid productions of oral pathogens including S. mutans, S. sobrinus, Eikenella corrodens, Prevotella intermedia, and Actinobacillus actinomycetemcmitans.

The complex dietary carbohydrates, called prebiotics, have been used to control Salmonella and improve intestinal bacterial balance in broilers. Leuconostoc mesenteroides (ATCC 13146) isomaltooligosaccharides (IMO) stimulate growth of Bifidobacterium and Lactobacillus and are not used by Salmonella or Escherichia coli. We tested the efficacy of these IMO as a prebiotic. IMO, compared with fructooligosaccharides (FOS) as sole carbon source, promoted growth of chicken cecal isolates and Bifidobacterium. Cecal isolates and Salmonella typhimurium grown in mixed culture on IMO reduced the Salmonella population. Cecal isolates grown on IMO showed higher viable counts and faster growth than Salmonella, indicating a potential value for these oligomers for poultry intestinal microflora modification.

The Lipomyces starkeyi alpha-amylase (LSA) gene encoding soluble starch-degrading alpha-amylase was cloned and characterized from a derepressed and partially constitutive mutant for both dextranase and amylase activities. The nucleotide (nt) sequence of the cDNA fragment reveals an open reading frame of 1944 bp encoding a 619 amino acid (aa) mature protein (LSA) with a calculated molecular weight of 68.709 kDa that was estimated to be about 73 kDa, including His tag (4 kDa) based on SDS-PAGE (10% acrylamide gel), activity staining, and the Western blotting, using anti-amylase-Ab. LSA had a sequence similar to other alpha-amylases in four conserved regions of the alpha-amylase family: (I) (287)DIVVNH(292), (II) (372)GLRIDTVKH(380), (III) (399)GEVFD(403), (IV) (462)FLENQD(467). Polymerase chain reaction and sequence analysis showed one intron of 60 nucleotides in the genomic lsa at positions between 966 and 967 of cDNA. The cloned LSA amylase showed a maximum activity at pH 6 and optimum temperature of 40 (o)C, with greater than 90% stability between pH 5 and pH 8 for 16 h. It was inhibited by Cu(2+) and stimulated by Ca(2+) and Mg(2+). Enzyme activity was not affected by 1 mM EGTA but was inhibited by 1 mM EDTA. LSA did not hydrolyze maltodextrins of G2 to G4, yet formed G2+G3 from G5, G2+G4 or G3+G3 from G6, and G3+G4 from G7. LSA did not hydrolyze soluble starch in the present of 2% (w/v) of acarbose. Kinetics of LSA was carried out by using starch as a substrate and the inhibition type of acarbose was the mixed non-competitive type (ki = 3.4 microM).

There is an emerging market for functional oligosaccharides for use in foods. Currently, technology for the production of oligosaccharides is limited to extraction from plant sources, acid or enzymatic hydrolysis of polysaccharides or synthesis by transglycosylation reactions. Oligosaccharides can also be produced using a Leuconostoc fermentation and restricting the polymer size by addition of maltose. Maltose limits the dextransucrase reaction, yielding high concentrations of alpha-glucooligosaccharides. Branched oligomers produced by this process were readily catabolized by bifidobacteria and lactobacilli but were not readily utilized by either Salmonella sp. or Escherichia coli, pointing toward their use in intestinal microflora modification.

Pseudomonas syringae pathovar phaseolicola, which produces alginate during stationary growth phase, displayed elevated extracellular alginate lyase activity during both mid-exponential and late-stationary growth phases of batch growth. Intracellular activity remained below 22% of the total activity during exponential growth, suggesting that alginate lyase has an extracellular function for this organism. Extracellular enzyme activity in continuous cultures, grown in either nutrient broth or glucose-simple salts medium, peaked at 60% of the washout rate, although nutrient broth-grown cultures displayed more than twice the activity per gram of cell mass. These results imply that growth rate, nutritional composition, or both initiate a release of alginate lyase from viable P. syringae pv. phaseolicola, which could modify its entrapping biofilm.

A novel glucanhydrolase from a mutant of Lipomyces starkeyi ATCC 74054 was purified. The single protein (100 kDa) showed either dextranolytic or amylolytic activity. We referred to the glucanhydrolase as a DXAMase. The DXAMase was produced in a starch medium and it was 3.75-fold more active for hydrolysis of the purified insoluble-glucan of Streptococcus mutans than Penicillium funiculosum dextranase. Aggregation of S. mutans cells with dextran and adherence to glass were eliminated by incubating with the DXAMase. The addition of DXAMase (0.1 IU/ml) to the mutansucrase reaction digest with sucrose reduced the formation of insoluble-glucan about 80%. Also the DXAMase (0.5 IU/ml) removed 80% of the pre-formed sucrose-dependent adherent film. These in vitro properties of L. starkeyi KSM 22 DXAMase are desirable for its application as a dental plaque control agent.

A derepressed and partially constitutive mutant for dextranase of Lipomyces starkeyi was selected after ethyl methane sulphonate mutagenesis by zone clearance on blue dextran agar plates. The mutant produced dextranase when grown on glucose, fructose and sucrose as well as on dextran, and more enzyme was produced by the mutant than by the parental strain when grown on 1% dextran. The pH and temperature optima for the mutant dextranase were 5.5 and 55 degrees C, respectively. Dextranase produced on sucrose produced more isomaltose and less glucose after dextran hydrolysis than the equivalent enzyme produced on dextran. The clinical size dextran (average mol. wt of 75,000 +/- 25,000) yield of mixed culture fermentation with the mutant and Leuconostoc mesenteroides was 94% of the total dextran produced.

Seaweed alginate was acetylated by intact, resting cells of Pseudomonas syringae ATCC 19304. Maximum acetylation of this polymer occurred at a pH of 6.0 and a temperature of 25 deg C. Aeration and gluconic acid were required for an optimal reaction. A reactor which contained carbon-immobilized cells was constructed to continuously acetylate alginate. The maximal yield of acetylation was about 90%, and the half-life of this system was 6.5 days.

A mixed-culture fermentation system was designed for the production of size-limited dextrans. This process was simpler and more economical than traditional methods. It required the establishment of microbial consortia of Lipomyces starkeyi ATCC 74054 and Leuconostoc mesenteroides ATCC 10830. Controlling initial conditions, growth, and enzyme production by both organisms controlled the product size. In this process, both strains were grown separately and then mixed. Dextran fermentation was then allowed to proceed. At the desired time (and molecular size), the fermentation was harvested. The optimum pH and temperature for production of clinical dextran (75,000 MW) were 5.2 (+/- 0.1) and 28 (+/- 0.5) degrees C, respectively. Varying the ratio of L. mesenteroides to L. starkeyi in the inoculum did not significantly affect either the final cell ratios or dextran production.

Vancomycin in combination with ciprofloxacin exhibited synergy against 7 of 10 strains of Pseudomonas aeruginosa. MICs for the microbial strains used in this study ranged from 0.0325 to 3.0 micrograms/ml for ciprofloxacin and from 23.5 to > 188 micrograms/ml for vancomycin. Combinations of these antibiotics, tested in a checkerboard pattern, gave fractional inhibitory concentrations of 0.5 or less for 7 of the 10 strains tested.

A beta-glucosidase (EC 3.2.1.21) from the fungus Aspergillus terreus was purified to homogeneity as indicated by disc acrylamide gel electrophoresis. Optimal activity was observed at pH 4.8 and 50 degrees C. The beta-glucosidase had K(m) values of 0.78 and 0.40 mM for p-nitrophenyl-beta-d-glucopyranoside and cellobiose, respectively. Glucose was a competitive inhibitor, with a K(i) of 3.5 mM when p-nitrophenyl-beta-d-glucopyranoside was used as the substrate. The specific activity of the enzyme was found to be 210 IU and 215 U per mg of protein on p-nitrophenyl-beta-d-glucopyranoside and cellobiose substrates, respectively. Cations, proteases, and enzyme inhibitors had little or no effect on the enzyme activity. The beta-glucosidase was found to be a glycoprotein containing 65% carbohydrate by weight. It had a Stokes radius of 5.9 nm and an approximate molecular weight of 275,000. The affinity and specific activity that the isolated beta-glucosidase exhibited for cellobiose compared favorably with the values obtained for beta-glucosidases from other organisms being studied for use in industrial cellulose saccharification.

Inulin, a polyfruction, is found as the reserve carbohydrate in the roots and tubers of various plants (i.e. Jerusalem artichoke, chicory, and dahlia tubers). The beta-fructofuranosidase (inulase) from the yeast Kluyveromyces fragilis is of interest because of its industrial potential in fructose syrup and alcohol production from inulin containing plants. We have found that the inulase of K. fragilis can be immobilized in the yeast cells by glutaraldehyde treatment. These cells are resistant to physical and enzymatic destruction. Although the exact nature of the immobilization is not fully understood, the kinetic parameters of the immobilized enzyme are similar to those of the soluble enzyme. No reduction of enzyme activity was observed after glutaraldehyde treatment and glutaraldehyde concentration did not affect enzyme activity. A 96% hydrolysis of dahlia inulin was achieved in 10.5 h with a 9.5% (w/v) fixed enzyme suspension. A Jerusalem artichoke extract containing 16.8%polyfructan was completely hydrolyzed in 3.5 h with a 0.24% (w/v)fixed enzyme suspension. This is a time frame feasible for industrial consideration.

Lysozyme (EC 3.2.1.17) complexes with extracted Pseudomonas aeruginosa LPS in two distinct stages. The initial stage does not produce turbidity detectable by nephelometry (measured as nephelos units (N) per time) but does permit low-speed sedimentation of the lysozyme-lipopolysaccharide (LPS) complex. This association is 100% disrupted by the action of 0.1 M Mg2+. Monovalent cations at equal ionic strength to the Mg2+ concentration used for these studies failed to alter significantly the lysozyme-LPS complex, indicating that the role of Mg2+ was not strictly an ionic one. The study of lysozyme-LPS complexes may provide a model system for investigating in vivo protein-LPS interactions.

An alkaline phosphatase mutant of Pseudomonas aeruginosa exhibiting both regulatory and catalytic changes was isolated. Under repression conditions (i.e. high inorganic phosphate (Pi)) the mutant culture produced an alkaline phosphatase (APase) displaying significant activity against both beta-glycerol phosphate (betaGP) and p-nitrophenyl phosphate (pNPP), while the wild type displayed no activity directed towards these substrates under the same conditions. In vivo, the mutant enzyme's ratio of specific activities was 45:1 in favour of betaGP versus pNPP, whereas this ratio was reversed to 1:9 betaGP versus pNPP for the same enzyme isolated from mutant cells. In addition, the kinetic parameters and stability requirements for the mutant-derived enzyme was altered in comparison with those of the wild type. A study of lipopolysaccharide (LPS) preparations from both the mutant and wild type indicated the mutant to be deficient in the core region of its LPS. The authors propose that the modifications in the catalytic activity of the mutant enzyme, demonstrated in vivo, are due to a change in the enzyme's microenvironment.

A novel exocellular glucoamylase produced by a thermophilic fungus,Cephalosporium eichhorniae, was purified by a combination of membrane filtration and Sephadex chromatography. The enzyme was a glycoprotein, 28% carbohydrate by weight. It was composed of a single polypeptide chain with a molecular weight of 26,850. The enzyme was thermostable with optimum activity between 45 and 62°C. It had a substrate preference of amylose>amylopectin. Analysis by thin-layer and gas-liquid chromatography showed the major hydrolytic product of starch was glucose, classifying this enzyme as a thermophilic glucoamylase.

Glutaraldehyde, the biological fixative of choice in the cytochemical localization of the phosphatases, was investigated for its effects on Pseudomonas aeruginosa alkaline phosphatase. Comparative studies on the inactivation of alkaline phosphatase by glutaraldehyde showed significant differences when the purified protein was compared with whole, cell-bound enzyme. The effects of the reagent on the kinetics of the purified enzyme were studied and some conclusions drawn as to the mode of inactivation. The reaction of glutaraldehyde with the cell envelope of P. aeruginosa was also investigated, and it was found not to modify the extraction of lipopolysaccharides from the outer membrane. This study emphasizes the care that must be taken to interpret data, cytochemical or otherwise, obtained when glutaraldehyde is used as a fixative or cross-linking reagent.

A washing procedure that removed maximum numbers of contaminating microorganisms from whole surgical gloves was developed. Washing, coupled with membrane filtration, proved to be a simple and effective method for bioburden determinations on whole gloves.

The beta-fructofuranosidase from Kluyveromyces fragilis was purified to one band on electrophoresis by 3 different methods. Two of the preparations were found to be impure by isoelectric focusing. This demonstrates the need for more than one criteria of homogeneity when purifying this enzyme. The enzyme was found to be a glycoprotein, stable at 50 degrees C, with a pH optimum of 4.5. The cations Hg2+, Ag+, Cu2+ and Cd2+ exhibited a marked inhibition of the enzyme. Competitive inhibition was observed with the fructose analog 2,5-anhydro-D-mannitol suggesting that the enzyme is inhibited by the furanose form of fructose.

The relationship between proton motive force and the secretion of dextransucrase in Leuconostoc mesenteroides was investigated. L. mesenteroides was able to maintain a constant proton motive force of -130 mV when grown in batch fermentors at pH values 5.8 to 7.0. The contribution of the membrane potential and the transmembrane pH gradient varied depending on the pH of the growth medium. The differential rate of dextransucrase secretion was relatively constant at 1,040 delta mU/delta mg (dry weight) when cells were grown at pH 6.0 to 6.7. Over this pH range, the internal pH was alkaline with respect to the external pH. When cells were grown at alkaline pH values, dextransucrase secretion was severely inhibited. This inhibition was accompanied by an inversion of the pH gradient as the internal pH became more acidic than the external pH. Addition of nigericin to cells at alkaline pH partially dissipated the inverted pH gradient and produced a fourfold stimulation of dextransucrase secretion. Treatment of cells with the lipophilic cation methyltriphenylphosphonium had no effect on the rate of dextransucrase secretion at pH 5.5 but inhibited secretion by 95% at pH 7.0. The reduced rate of secretion correlated with the dissipation of the proton motive force by this compound. Values of proton motive force greater than -90 mV were required for maximal rates of dextransucrase secretion. The results of this study indicate that dextransucrase secretion in L. mesenteroides is dependent on the presence of a proton gradient across the cytoplasmic membrane that is directed into the cell.

Production of extracellular proteolytic activity by Aeromonas hydrophila was influenced by temperature, pH, and aeration. Conditions which produced maximal growth also resulted in maximal protease production. Enzyme production appeared to be modulated by an inducer catabolite repression system whereby NH4+ and glucose repressed enzyme production and complex nitrogen and nonglucose, carbon energy sources promoted it. Under nutritional stress, protease production was high, despite poor growth.

The mixture of polysaccharides in the gelling component of agar (agarose) is hydrolyzed to D-galactose and 3,6-anhydro-L-galactose by a series of hydrolytic enzymes obtained from Pseudomonas atlantica. The final degradative step in the pathway of agarose decomposition is the hydrolysis of the alpha-linkage in the dissaccharide neoagarobiose yielding D-galactose and 3,6-anhydro-L-galactose. Pseudomonas atlantica when grown on agar produces two specific enzymes, p-nitrophenyl alpha-galactose hydrolase and neoagarobiose hydrolase. The purification and partial characterization of both enzymes are presented.

Alkaline phosphatase (APase) of Pseudomonas aeruginosa exists primarily in the periplasmic region of the cell, i.e., between the cytoplasmic membrane and the outer tripartite layer. The enzyme is also found in the culture filtrate or associated with the outer layer of the cell wall. APase forms a complex with released outer cell wall material, and lipopolysaccharide (LPS) is associated with the complex. Since the enzyme was purified to homogeneity, it became desirable to determine whether complex formation with LPS , or the outer cell wall, affected any properties of the purified phosphatase. The ratio of activities of purified APase with p-nitrophenylphosphate and beta-glycerolphosphate as substrates is about 4:1. The ratio of activities with enzyme complexed with LPS is about 1:1. The energy of activation of sucrose or magnesium released enzyme is 9500 cal/mol whereas the values for purified enzyme plus LPS, purified enzyme, purified enzyme plus phosphatidylethanolamine (PE), and purified enzyme plus LPS plus PE range from 3400 to 8700 cal/mol. These changes occur in the physiological temperature range, 27 to 39C, of this organism. Sucrose-released enzyme in the presence of substrate is inactivated at 47C whereas pure enzyme plus substrate is affected at 41C. The addition of LPS, PE, or a combination of both increases the temperature of inactivation from 45 to 51C. The results suggest that certain properties of the purified enzyme differ from those of the enzyme released from whole cells by either sucrose or magnesium resuspension. The addition of cell wall components such as LPS and PE to purified APase restores these properties. The addition of cell wall components such as LPS and PE to purified APase restores these properties. The evidence suggests that artificial complex formation changes the environment of the enzyme protein such that the environment now resembles that which exists within the whole cell wall.

A p-nitrophenyl alpha-galactoside hydrolase is partially released when whole cells of Pseudomonas atlantica are converted to spheroplasts. The p-nitrophenyl alpha-glactoside hydrolase is completely inactivated by treatment of whole cells with diazonaphthalene -- disulfonic acid (NDS), a reagent which does not penetrate the cytoplasmic membrane. Under the conditions used no inactivation of lactic acid dehydrogenase was observed. A specific staining procedure for this enzyme for use in electron microscopy was developed. The results with this technique in conjunction with the results of spheroplasting and NDS localization suggest that p-nitrophenyl alpha-galactoside hydrolase is located in or on the double-track membranes, primarily on the outer double track.

Conditions are reported for efficient protoplast formation and regeneration in four strains of Leuconostoc mesenteroides. Protoplasts were produced from each strain at frequencies greater than 99%, although the rate of their production was variable from strain to strain. Bovine serum albumin and Mg were required for maximal regeneration, while the presence of Ca was inhibitory. Regeneration frequencies of 16% could be obtained with strain ATCC 10830. This frequency was four- to eightfold higher than the frequencies of the other strains examined.

Lipomyces starkeyi ATCC 20825 is a derepressed mutant derived from L. starkeyi ATCC 12659. It requires the presence of an inducer before it produces dextranase. This study was undertaken to determine the most efficient, commercially feasible method for inducing this enzyme. The following compounds induced dextranase synthesis: 1-O-beta-methyl-glucopyranoside, 1-O-alpha-methyl-glucopyranoside, dextran, isomaltopentose, isomaltotetraose, isomaltotriose, and isomaltose. 1-O-beta-Methyl-glucopyranoside was found to be a gratuitous inducer. Early in the growth phase, cells produced higher specific levels of enzyme than they did in late log phase. The length of exposure of the yeast cells to the inducer also affected the amount of dextranase produced. The maximum amount of enzyme was produced after 12 h of exposure to the inducer. The saturation concentration was the same for all inducers tested, i.e., approximately 1 mg of inducer for every 2 x 10 cells.

The yeast Kluyveromyces fragilis (ATCC 12424) was grown on a 2% inulin-1% yeast extract medium for 36 h and subsequently fixed with 0.5% glutaraldehyde. The glutaraldehyde treatment did not affect the beta-fructofuranosidase (inulinase, EC 3.2.1.7) activity of the cells but it did make the cells resistant to chemical and physical treatments that normally release beta-fructofuranosidase from untreated cells. The enzyme in the treated cells exhibited Km values for sucrose and raffinose identical to those obtained for the free enzyme. The cell wall of the treated cells exhibited the same diffusion properties for sucrose, raffinose, and inulin as those observed for untreated cells. The beta-fructofuranosidase was not bound covalently to the cell by the glutaraldehyde treatment. The results support the permeability barrier model for the enzyme retention in the yeast cell wall.

Current hospital practice for testing renal function is to use the creatinine clearance test. Inulin clearance, an inherently more accurate procedure, currently is only carried out by specialized laboratories because there is not a simple biochemical assay for inulin, that is, an assay that could be carried out by any laboratory without special facilities. We have developed a simple enzymatic assay system for measuring inulin in plasma and urine. The procedure uses a beta-fructofuranosidase immobilized on Concanavalin A to convert inulin to fructose. Fructose is then measured by measuring the NADH----NAD conversion produced when fructose is converted to sorbitol by the enzyme sorbitol dehydrogenase. Kinetic parameters, binding capacities, and operating conditions for the immobilized beta-fructofuranosidase were determined as well as general operating parameters for the complete assay system. This system offers the potential for replacing the creatinine clearance test as the assay of choice for renal function.