Metabolic Conversion of Castasterone and Brassinolide into Their Glucosides in Higher Plants

Castasterone (CS) and brassinolide (BL) were administered to mung bean (Vigna radiata) explants, Arabidopsis thaliana seedlings, and cultured Catharanthus roseus cells, and the glucosylated metabolites were analyzed using LC/MS/MS. In mung bean and C. roseus, CS-2-O-glucoside (CS-2G), -3-O-glucoside (CS-3G), -22-O-glucoside (CS-22G), and -23-O-glucoside (CS-23G) were identified as metabolites of CS, whereas BL-2G, BL-3G, and BL-23G were identified as metabolites of BL. In A. thaliana, CS and BL were converted into their respective 2-O- and 23-O-glucosides. Of the metabolites identified with BL and CS administration, BL-23G was the predominant metabolite in mung bean and A. thaliana, whereas the 3-O-glucoside of BL was abundant in C. roseus. This is the first report of the metabolic conversion of CS into CS-2G, CS-3G, CS-22G, and CS-23G, and of BL into BL-2G and BL-3G. Our results indicate that the glucosylation profiles of BL and CS vary with plant species, and that the glucosylation of CS is rather limited quantitatively, compared with that of BL.     

Production of 5′-dRiboflavin-α-d-glucopyranoside in Growing Cultures by the Mold Mucor

During the investigations on riboflavin glycoside formation by Aspergillus, Mucor, Penicillium and Rhizopus, a remarkable production of 5′-d-riboflavin-α-d-glucopyranoside was observed in several strains belonging to the genus Mucor when grown on a, medium containing maltose and riboflavin. Several conditions on 5′-d-riboflavin-α-d-glucopyranoside formation were also investigated with washed mycellium of M. javanicus. Maltosyl compounds such as maltose, dextrin, amylose and soluble starch were the effective glucosyl donor, whereas glucose, fructose, sucrose, lactose and dextran were inactive.     

α-Glucosidase synthesis in batch and continuous culture ofSaccharomyces cerevisiae

Glucose prevented maltose utilization in batch culture ofSaccharomyces cerevisiae whereas in a mixed carbohydrate-limited system, maltose and glucose were consumed simultaneously. The specific activity of -glucosidase depended on the dilution rate as well as the proportion of maltose in the mixture. The chemostat provides a way of reaching the low residual concentrations of glucose in the broth that are necessary to release catabolite repression and permit maltose induction of -glucosidase.     

Physiological and genetic factors for process development of cyclosporine fermentations

Summary The new immunosuppressive agent cyclosporine (Cyclosporin A, Cy) is the most prominent member of a group of cyclic peptide fungal metabolites (cyclosporins) produced byTolypocladium inflatum in submerged fermentations. In the present study, kinetics and physiology of mycelial growth and Cy production byT. inflatum were examined. A new semi-synthetic medium was formulated, consisting of a single carbon/energy source, Bacto-peptone, potassium phosphate and potassium chloride. A wide variety of carbon sources supported growth and Cy production. 3% (w/v) sorbose gave the highest final Cy titer (105.5 mg/l), based on 10-day fermentations. The best specific Cy production was observed with 2% sorbose (14.3 mg Cy/g biomass) followed by 5%myo-inositol (13.4 mg Cy/g biomass). A feeding strategy consisting of sequential addition of two carbon sources such as sorbose and maltose was developed in order to reach higher volumetric production. Genetic studies were also conducted, focussing on the development of mutants for increased Cy production and for the synthesis of novel cyclosporins. In the course of these studies, viable protoplasts ofT. inflatum have been isolated and regenerated.     

Regulation and genetic enhancement of beta-amylase production in Clostridium thermosulfurogenes.

We studied the general mechanism for regulation of beta-amylase synthesis in Clostridium thermosulfurogenes. beta-Amylase was expressed at high levels only when the organism was grown on maltose or other carbohydrates containing maltose units. Three kinds of mutants altered in beta-amylase production were isolated by using nitrosoguanidine treatment, enrichment on 2-deoxyglucose, and selection of colonies with large clear zones on iodine-stained starch-glucose agar plates. beta-Amylase was produced only when maltose was added to cells growing on sucrose in wild-type and catabolite repression-resistant mutant strains, but the differential rate of enzyme synthesis in constitutive mutants was constant regardless of the presence of maltose. In carbon-limited chemostats of wild-type and catabolite repression-resistant mutant stains, beta-amylase was expressed on maltose but not on glucose or sucrose. beta-Amylase synthesis was immediately repressed by the addition of glucose. Therefore, we concluded that beta-amylase synthesis in C. thermosulfurogenes was inducible and subject to catabolite repression. The addition of cAMP did not eliminate the repressive effect of glucose. The mutants were generally characterized in terms of beta-amylase production, growth properties, fermentation product formation, and alterations in glucose isomerase and glucoamylase activities. A hyperproductive mutant produced eightfold more beta-amylase on starch medium than the wild type and more rapidly fermented starch to ethanol.     

Thermostable amylolytic enzymes from a cellulolytic fungusMyceliophthora thermophila D14 (ATCC 48 104)

Summary The production of amylolytic enzymes by a thermophilic cellulolytic fungus,Myceliophthora thermophila D14 was investigated by batch cultivation in Czapek-Dox medium at 45° C. Among various nitrogenous compounds used, NaNO₃ and KNO₃ were found to be the best for amylase production. Starch, cellobiose and maltose induced the synthesis of amylase while glucose, fructose, galactose, lactose, arabinose, xylose, sorbitol, mesoinositol and sucrose did not. Calcium ions had the most stimulating effect on enzyme formation amongst many ions investigated. The synthesis of amylolytic enzymes was dependent on growth and occurred predominantly in the mid-stationary phase. The enzyme was active in a broad temperature range (50° C–60° C) and displayed activity optima at 60° C and pH 5.6.     

Derepression of a baker's yeast strain for maltose utilization is associated with severe deregulation of HXT gene expression

Aims: We undertook to improve an industrial Saccharomyces cerevisiae strain by derepressing it for maltose utilization in the presence of high glucose concentrations. Methods and Results: A mutant was obtained from an industrial S. cerevisiae strain following random UV mutagenesis and selection on maltose/5‐thioglucose medium. The mutant acquired the ability to utilize glucose simultaneously with maltose and possibly also sucrose and galactose. Aerobic sugar metabolism was still largely fermentative, but an enhanced respirative metabolism resulted in a 31% higher biomass yield on glucose. Kinetic characterization of glucose transport in the mutant revealed the predominance of the high‐affinity component. Northern blot analysis showed that the mutant strain expresses only the HXT6/7 gene irrespective of the glucose concentration in the medium, indicating a severe deregulation in the induction/repression pathways modulating HXT gene expression. Interestingly, maltose‐grown cells of the mutant display inverse diauxy in a glucose/maltose mixture, preferring maltose to glucose. Conclusion: In the mutant here reported, the glucose transport step seems to be uncoupled from downstream regulation, because it seems to be unable to sense abundant glucose, via both repression and induction pathways. Significance and Impact of the Study: We report here the isolation of a S. cerevisiae mutant with a novel derepressed phenotype, potentially interesting for the industrial fermentation of mixed sugar substrates.     

Multistrain probiotic production by co‐culture fermentation in a lab‐scale bioreactor

Most commercial probiotic products intended for pharmaceutical applications consist of combinations of probiotic strains and are available in various forms. The development of co‐culture fermentation conditions to produce probiotics with the correct proportion of viable microorganisms would reduce multiple operations and the associated costs. The aim of this study was to develop a fermentation medium and process to achieve biomass comprising the desired proportion of two probiotic strains in co‐culture. Initially, a quantification medium was developed, and the method was optimized to allow the quantification of each strain's biomass in a mixture. The specific growth rates of Lactobacillus delbrueckii spp. bulgaricus and Lactobacillus plantarum were determined in media with different carbon sources. The inoculum volume was optimized to achieve equal proportion of biomass in co‐culture fermentation in test tubes. Next, fermentation was carried out in a 3‐L bioreactor. A biomass concentration of 2.06 g/L, with L. delbrueckii spp. bulgaricus and L. plantarum in the ratio of 47%:53% (by weight), was achieved with concomitant production of 12.69 g/L of lactic acid in 14 h. The results show that with careful manipulation of process conditions, it is possible to achieve the desired proportion of individual strains in the final biomass produced by co‐culture fermentation. This process may serve as a model to produce multistrain probiotic drugs at industrial scale.     

The high maltose-producing α-amylase of the thermophilic actinomycete,Thermomonospora curvata

The -amylase of Thermomonospora curvata catalyses the formation of very high levels of maltose from starch (73%, w/w) without the attendant production of glucose. The enzyme was produced extracellularly in high yield during batch fermentation in a 5-1 fermentor. Purification was achieved by ammonium sulphate fractionation, Superose-12 gel filtration and DEAE-Sephacel ionexchange chromatography. The enzyme exhibited maxima for activity at pH 6.0 and 65°C, had a relative molecular mass of 60900–62000 and an isoelecric point at 6.2. The exceptionally high levels of maltose produced and the unique action pattern exhibited on starch and related substrates indicate a very unusual maltogenic system. The predominance of maltose as the final end-product may be explained by the participation of reactions other than simple hydrolysis and the preferential cleavage of maltotriose from higher maltooligosaccharides. The enzyme exhibits very low affinity for maltotriose (K _m=7.7 × 10^–3 m) and its conversion to maltose is achieved by synthetic followed by hydrolytic events, which result in the very high levels of maltose observed and preclude glucose formation. This system is distinguished from other very high maltose-producing amylases by virtue of its high temperature maximum, very low affinity for maltotriose and the absence of glucose in the final saccharide mixture. Correspondence to: C. T. Kelly     

High-cell-density production of poly-β-hydroxybutyrate (PHB) from methanol by Methylobacterium extorquens: production of high-molecular-mass PHB

Methylobacterium extorquens ATCC 55366 was successfully cultivated at very high cell densities in a fed-batch fermentation system using methanol as a sole carbon and energy source and a completely minimal culture medium for the production of poly--hydroxybutyrate (PHB). Cell biomass levels were between 100 g/l and 115 g/l (dry weight) and cells contained between 40% and 46% PHB on a dry-weight basis. PHB with higher molecular mass values than previously reported for methylotrophic bacteria was obtained under certain conditions. Shake-flask and fermentor experiments showed the importance of adjusting the mineral composition of the medium for improved biomass production and higher growth rates. High-cell-density cultures were obtained without the need for oxygen-enriched air; once the oxygen transfer capacity of the fermentor was reached, methanol was thereafter added in proportion to the amount of available dissolved oxygen, thus preventing oxygen limitation. Controlling the methanol concentration at a very low level (less than 0.01 g/l), during the PHB production phase, led not only to prevention of oxygen limitation but also to the production of very high-molecular-mass PHB, in the 900–1800 kDa range. Biomass yields relative to the total methanol consumed were in the range 0.29–0.33 g/g, whereas PHB yields were in the range 0.09–0.12 g/g. During the active period of PHB synthesis, PHB yields relative to the total methanol consumed were between 0.2 g/g and 0.22 g/g. M. extorquens ATCC 55366 appears to be a promising organism for industrial PHB production.     

The influence of limiting and non-limiting growth conditions on glucose and maltose metabolism in Lactococcus lactis ssp. lactis strains

Three strains of Lactococcus lactis ssp. lactis, a dairy strain 65.1, a type strain ATCC 19435, and a mutant AS 211, were grown on glucose and on maltose under chemostat conditions. When the culture was shifted from glucose-limiting to non-limiting conditions, the product shifted from mixed acids to lactate. Mixed acids were obtained in all maltose cultures; however, an enhanced lactate formation was observed in 19435 and AS 211. An inorganic-phosphate (P_i)-dependent maltose phosphorylase activity was found to be responsible for the initial conversion of maltose. The activation of maltose phosphorylase by Pi was strain-specific. When growth was on maltose under non-limiting conditions, a correlation was found between high initial maltose phosphorylase and -phosphoglucomutase activities and lactate production. No such correlation was observed in maltose-limited cells. In glucose-grown cells under non-limiting conditions, homo-fermentative lactate formation coincided with high concentrations of fructose 1,6-bisphosphate (Fru1,6P ₂) and pyruvate (Pyr) and low concentrations of phosphoenolpyruvate (PPyr). Under limiting conditions, mixed acid formation coincided with low concentrations of Fru1,6P ₂ and Pyr and high concentrations of PPyr. In maltose-grown cells there was no correlation between intracellular intermediary metabolite concentrations and product formation. Therefore, in addition to intracellular intermediary metabolite concentrations, the product formation on maltose is suggested to be regulated by the transport and initial phosphorylating steps.     

Regulation of Amylase Synthesis in Bacillus circulans F-2

In the usual batch cultivation, Bacillus circulans F-2 produced amylase only when granular carbon sources such as raw starch or crosslinked starches (CLP) were added. In the dialysis cultivation, where CLP and partially purified amylase were incubated inside the dialysis tubing, the bacterium inoculated outside of the tubing grew and produced the amylase. Amylase production of this bacterium was further investigated in feeding cultivation, in which maltose was fed to the cultivation medium at various rates. The bacterial growth increased with the increase of the feeding rate of maltose, but maximum amylase production was observed at a feeding rate of 45 mg/hr/1. No amylase was produced on the media containing monosaccharides, sucrose, lactose, or isomaltose in the feeding cultivation although bacterial growth was observed. The amylase of this bacterium was found to be inducible. Replacement of 20% of the maltose with glucose resulted in a great decrease (70%) in the amylase production. This shows that the amylase synthesis of B. circulans F-2 is severely repressed by glucose.     

Purification and characterization of beta-cyanoalanine synthase and cysteine synthases from potato tubers: are beta-cyanoalanine synthase and mitochondrial cysteine synthase same enzyme?

beta-Cyanoalanine synthase (CAS; EC 4.4.1.9) and two kinds of cysteine synthases (CS; EC 4.2.99.8) have been purified from the particulate fraction of potato tubers. By DEAE Sephacel and Resource PHE chromatography, CAS activity was separated from two CS activities, designated as CS-1 and CS-2. The molecular masses of CAS, CS-1 and CS-2 were estimated to be 37, 39 and 34 kDa, respectively, by SDS-PAGE analysis. The purified CAS had CS activity, and both CS-1 and CS-2 had CAS activity. However, CAS and CSs had significant differences in kinetic characters. The antibody raised against purified CAS discriminated CAS from CSs, whereas the antibody raised against purified CS-2 recognized CS-1 and CS-2 but not CAS. The molecular mass and the partial amino acid sequence of CS-2 were similar to those of the cytosolic CS of potato, whereas the molecular mass of CS-1 was similar to that of the plastidic CS. The partial amino acid sequence of CAS was similar to those of CS isozymes, especially the mitochondrial CS isolated from spinach.     

Energetics and kinetics of maltose transport in Saccharomyces cerevisiae: a continuous culture study.

In Saccharomyces cerevisiae, maltose is transported by a proton symport mechanism, whereas glucose transport occurs via facilitated diffusion. The energy requirement for maltose transport was evaluated with a metabolic model based on an experimental value of YATP for growth on glucose and an ATP requirement for maltose transport of 1 mol.mol-1. The predictions of the model were verified experimentally with anaerobic, sugar-limited chemostat cultures growing on a range of maltose-glucose mixtures at a fixed dilution rate of 0.1 h-1. The biomass yield (grams of cells.gram of sugar-1) decreased linearly with increasing amounts of maltose in the mixture. The yield was 25% lower during growth on maltose than during that on glucose, in agreement with the model predictions. During sugar-limited growth, the residual concentrations of maltose and glucose in the culture increased in proportion to their relative concentrations in the medium feed. From the residual maltose concentration, the in situ rates of maltose consumption by cultures, and the Km of the maltose carrier for maltose, it was calculated that the amount of this carrier was proportional to the in situ maltose consumption rate. This was also found for the amount of intracellular maltose. These two maltose-specific enzymes therefore exert high control over the maltose flux in S. cerevisiae in anaerobic, sugar-limited, steady-state cultures.     

Effects of chondroitin sulfate and its oligosaccharides on toll-like receptor-mediated IL-6 secretion by macrophage-like J774.1 cells

The effects of two types of chondroitin sulphate (CS), CS-A and CS-C, their oligosaccharides (oligo-CSs), and disaccharides (Di-CSs) on toll-like receptor (TLR)-mediated secretion of interleukin (IL)-6 were compared using macrophage-like cell line J774.1. IL-6 secretion in the J774.1 cells was markedly increased by Pam3CS4, LPS, and CpG, the ligands to TLR1/2, 4, and 9 respectively. Among these three ligands, CpG-induced IL-6 was most clearly suppressed by CSs and their digests. Suppression of IL-6 secretion by smaller sized CS-A was stronger than that by intact CS-A, whereas no such size-dependent suppression was apparent for CS-C. Di-4S, the disaccharide unit of the CS-A digest, also showed much stronger suppression than Di-6S, the disaccharide unit of the CS-C digest, and the non-sulfated disaccharide unit, Di-0S. The suppressing activity of oligo-CSs, particularly Di-CSs, against TLR-mediated inflammation was dependent on the CS structure, including the sulfation site.     

Effects of Chondroitin Sulfate and Its Oligosaccharides on Toll-Like Receptor-Mediated IL-6 Secretion by Macrophage-Like J774.1 Cells

The effects of two types of chondroitin sulphate (CS), CS-A and CS-C, their oligosaccharides (oligo-CSs), and disaccharides (Di-CSs) on toll-like receptor (TLR)-mediated secretion of interleukin (IL)-6 were compared using macrophage-like cell line J774.1. IL-6 secretion in the J774.1 cells was markedly increased by Pam3CS4, LPS, and CpG, the ligands to TLR1/2, 4, and 9 respectively. Among these three ligands, CpG-induced IL-6 was most clearly suppressed by CSs and their digests. Suppression of IL-6 secretion by smaller sized CS-A was stronger than that by intact CS-A, whereas no such size-dependent suppression was apparent for CS-C. Di-4S, the disaccharide unit of the CS-A digest, also showed much stronger suppression than Di-6S, the disaccharide unit of the CS-C digest, and the non-sulfated disaccharide unit, Di-0S. The suppressing activity of oligo-CSs, particularly Di-CSs, against TLR-mediated inflammation was dependent on the CS structure, including the sulfation site.     

Influence of carbohydrates and polyols on l-lactic acid production and fatty acid formation by Rhizopus arrhizus

Growth and l-lactic acid production on 24 different carbohydrates and polyols (glycerol, mannitol and sorbitol) by Rhizopus arrhizus CCM 8109 were determined. The d- but not the l-forms of xylose, fructose, galactose, mannose, glucose, cellobiose, maltose and sucrose and partially hydrolysed starch were converted to l-lactic acid. Changes in lipid formation and fatty acid composition were detected in biomass grown on the different sugars. In the presence of polyols, growth and considerable production of lipids were observed with little or no lactate production. Invertase was mainly associated with the mycelium during growth on sucrose, whereas glucoamylase and -amylase were produced extracellularly during growth on starch.The authors are with the Department of Biochemical Technology, Faculty of Chemical Technology, Slovak Polytechnical University, Radlinského 9, SK-812 37 Bratislava, Slovak Republic     

Appetitive differential conditioning of the rabbit's jaw movement response. Effects of cue similarity and US magnitude

Two experiments examined appetitive differential conditioning of the rabbit's jaw movement response (JMR) in a two-phase procedure. The first phase entailed reinforced training with one conditioned stimulus (CS+), and the second phase involved intermixed presentations of CS+ and an unreinforced stimulus (CS-). In Experiment 1, CS+ was a 600-Hz tone, and CS- was either a 660-, 1,000-, or 2,100-Hz tone. In Experiment 2, the magnitude of the water unconditioned stimulus (US) paired with CS+ was either 1, 3, or 9 ml. The experiments revealed that 1) the level of responding to CS- rose for several days and then declined over the remainder of training; 2) the physical similarity between CS+ and CS- directly affected the level of responding to CS- but had no discernable effect on the level of responding to CS+; and 3) US magnitude positively affected the level of responding to CS+ and, to a lesser extent, CS-. The results are discussed in terms of their implications for Spence's gradient interaction theory and Pavlov's external inhibition hypothesis.     

Production of the fungal exopolysaccharide pullulan by batch-wise and continuous fermentation

A mutant strain of the deuteromycete Aureobasidium pullulans deficient in melanin synthesis was used to investigate the production of the exopolysaccharide pullulan and biomass, respectively. Shake-flask experiments with different carbon sources showed significant differences in pullulan elaboration. Sucrose was most suitable for pullulan synthesis among the carbon sources examined. Fermentations were carried out both batch-wise and continuously in a stirred vessel fermentator. In batch fermentations about 45% of the glucose offered was converted into pullulan at maximum formation rates of 0.16 g/l per hour using standard medium. The yield of polysaccharide could be maintained at 45% in continuous fermentations. At a dilution rate of 0.05 l/h, the formation rate of polysaccharide increased up to 0.35 g/l per hour. Alterations in the nitrogen content of the feed significantly affected the consumption rate of glucose and the production rate of polysaccharide, but final concentrations of biomass were hardly affected. Correspondence to: R. Schuster