Lime application for the efficient production of nutraceutical glucooligosaccharides from Leuconostoc mesenteroides NRRL B-742 (ATCC13146).

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.

Enhancement of the Enzymatic Digestibility and Ethanol Production from Sugarcane Bagasse by Moderate Temperature-Dilute Ammonia Treatment.

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.

Composition of sugar cane, energy cane, and sweet sorghum suitable for ethanol production at Louisiana sugar mills.

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.

Potential physiological functions of acceptor products of dextransucrase with cellobiose as an inhibitor of mutansucrase and fungal cell synthase.

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)-ß-D-glucopyranosyl-(1 → 4)-D-glucopyranose and α-D-glucopyranosyl-(1 → 6)-ß-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 ß-(1 → 3)-glucan synthase, which is required for fungal cell wall formation.

Use of cellulase inhibitors to produce cellobiose.

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.

Compositional changes in sugarcane bagasse on low temperature, long-term diluted ammonia treatment.

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.

Sugarcane bagasse oxidation using a combination of hypochlorite and peroxide.

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.

Hydrolysis of ammonia-pretreated sugar cane bagasse with cellulase, beta-glucosidase, and hemicellulase preparations.

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.

Optimization of oligosaccharide synthesis from cellobiose by dextransucrase.

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.

Synthesis, structure analyses, and characterization of novel epigallocatechin gallate (EGCG) glycosides using the glucansucrase from Leuconostoc mesenteroides B-1299CB.

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.

Cloning and expression of levansucrase from Leuconostoc mesenteroides B-512 FMC in Escherichia coli.

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.

Modified oligosaccharides as potential dental plaque control materials.

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.

Cloning and expression of Lipomyces starkeyi alpha-amylase in Escherichia coli and determination of some of its properties.

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).

Induction of Lipomyces starkeyi Dextranase.

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.