Colonization of Aspergillus japonicus on synthetic materials and application to the production of fructooligosaccharides

The ability of Aspergillus japonicus ATCC 20236 to colonize different synthetic materials (polyurethane foam, stainless steel sponge, vegetal fiber, pumice stones, zeolites, and foam glass) and to produce fructooligosaccharides (FOS) from sucrose (165 g/L) is described. Cells were immobilized in situ by absorption, through direct contact with the carrier particles at the beginning of fermentation. Vegetal fiber was the best immobilization carrier as A. japonicus grew well on it (1.25 g/g carrier), producing 116.3 g/L FOS (56.3 g/L 1-kestose, 46.9 g/L 1-nystose, and 13.1 g/L 1-β-fructofuranosyl nystose) with 69% yield (78% based only in the consumed sucrose amount), giving also elevated activity of the β-fructofuranosidase enzyme (42.9 U/mL). In addition, no loss of material integrity, over a 2 day-period, was found. The fungus also immobilized well on stainless steel sponge (1.13 g/g carrier), but in lesser extents on polyurethane foam, zeolites, and pumice stones (0.48, 0.19, and 0.13 g/g carrier, respectively), while on foam glass no cell adhesion was observed. When compared with the FOS and β-fructofuranosidase production by free A. japonicus, the results achieved using cells immobilized on vegetal fiber were closely similar. It was thus concluded that A. japonicus immobilized on vegetal fiber is a potential alternative for high production of FOS at industrial scale.     

Metabolism of Fructooligosaccharides by Lactobacillus paracasei 1195

Fermentation of fructooligosaccharides (FOS) and other oligosaccharides has been suggested to be an important property for the selection of bacterial strains used as probiotics. However, little information is available on FOS transport and metabolism by lactic acid bacteria and other probiotic bacteria. The objectives of this research were to identify and characterize the FOS transport system of Lactobacillus paracasei 1195. Radiolabeled FOS was synthesized enzymatically from [³H]sucrose and purified by column and thin-layer chromatography, yielding three main products: glucose (G) α-1,2 linked to two, three, or four fructose (F) units (GF₂, GF₃, and GF₄, respectively). FOS hydrolysis activity was detected only in cell extracts prepared from FOS- or sucrose-grown cells and was absent in cell supernatants, indicating that transport must precede hydrolysis. FOS transport assays revealed that the uptake of GF₂ and GF₃ was rapid, whereas little GF₄ uptake occurred. Competition experiments showed that glucose, fructose, and sucrose reduced FOS uptake but that other mono-, di-, and trisaccharides were less inhibitory. When cells were treated with sodium fluoride, iodoacetic acid, or other metabolic inhibitors, FOS transport rates were reduced by up to 60%; however, ionophores that abolished the proton motive force only slightly decreased FOS transport. In contrast, uptake was inhibited by ortho-vanadate, an inhibitor of ATP-binding cassette transport systems. De-energized cells had low intracellular ATP concentrations and had a reduced capacity to accumulate FOS. These results suggest that FOS transport in L. paracasei 1195 is mediated by an ATP-dependent transport system having specificity for a narrow range of substrates.     

Comparison of Fructooligosaccharide Utilization by Lactobacillus and Bacteroides Species

The utilization of 1-kestose (GF₂) and nystose (GF₃), the main components of fructooligosaccharides (FOS), by Lactobacillus and Bacteroides species was examined. Of seven Lactobacillus and five Bacteroides strains that utilized FOS, L. salivarius, L. rhamnosus, L. casei, and L. gasseri utilized only GF₂, whereas L. acidophilus and all the Bacteroides strains utilized both GF₂ and GF₃. Only the strains able to utilize both GF₂ and GF₃ had β-fructosidase activity in the culture supernatants. The culture supernatants of the Lactobacillus strains had higher β-fructosidase activity for GF₂ than for GF₃, whereas those of the Bacteroides strains had higher activity for GF₃ than for GF₂. Furthermore, β-fructosidase activity of the culture supernatants of the Lactobacillus cells grown in the GF₃ medium was much higher than that of the cells grown in the GF₂ medium, whereas the activity of the culture supernatants of the Bacteroides cells grown in the GF₃ medium was almost the same as that of the cells grown in the GF₂ medium. These results indicate that Lactobacillus species metabolize FOS in a different way from that of Bacteroides species.     

Theoretical calculation of the sugar concentrations during enzymatic production of fructooligosaccharides

Summary In a batch production of fructooligosaccharides from sucrose, the concentrations of residual sucrose, glucose and fructooligosaccharides at a given reaction time(t) and initial sucrose concentration(S₀) were theoretically calculated by the following correlation equations: Glucose(t) = 0.0653 S₀ × ln(t); Fructooligosaccharides(t) = 0.1636 S₀ × ln(t); Sucrose(t)=S₀ - Glucose(t) + FOS(t).     

Production of fructooligosaccharides by mycelium-bound transfructosylation activity present in Cladosporium cladosporioides and Penicilium sizovae

Different filamentous fungi isolated from molasses and jams (kiwi and fig) were screened for fructooligosaccharides (FOS) producing activity. Two strains, identified as Penicilium sizovae (CK1) and Cladosporium cladosporioides (CF₂15), were selected on the basis of the FOS yield and kestose/nystose ratio. In both strains the activity was mostly mycelium-bound. Starting from 600 g/L of sucrose, maximum FOS yield was 184 and 339 g/L for P. sizovae and C. cladosporioides, respectively. Interestingly, the highest FOS concentration with C. cladosporioides was reached at 93% sucrose conversion, which indicated a notable transglycosylation to hydrolysis ratio. The main FOS in the reaction mixtures were identified by HPAEC–PAD chromatography. C. cladosporioides synthesized mainly 1-kestose (158 g/L), nystose (97 g/L), ¹F-fructosylnystose (19 g/L), 6-kestose (12 g/L), neokestose (10 g/L) and a disaccharide (34 g/L) that after its purification and NMR analysis was identified as blastose [Fru-β(2 → 6)-Glc]. P. sizovae was very selective for the formation of ¹F-FOS (in particular 1-kestose) with minor contribution of neoFOS and negligible of levan-type FOS.     

Response surface methodology: Synthesis of short chain fructooligosaccharides with a fructosyltransferase from Aspergillus aculeatus

A transferase was isolated, purified and characterised from Aspergillus aculeatus. The enzyme exhibited a pH and temperature optima of 6.0 and 60 °C, respectively and under such conditions remained stable with no decrease in activity after 5 h. The enzyme was purified 7.1 fold with a yield of 22.3% and specific activity of 486.1 U mg^?1 after dialysis, concentration with polyethyleneglycol (30%) and DEAE-Sephacel chromatography. It was monomeric with a molecular mass of 85 kDa and K_m and V_max values of 272.3 mM and 166.7 μmol min^?1 ml^?1. The influence of pH, temperature, reaction time, and enzyme and sucrose concentration on the formation of short-chain fructooligosaccharides (FOS) was examined by statistical response surface methodology (RSM). The enzyme showed both transfructosylation and hydrolytic activity with the transfructosylation ratio increasing to 88% at a sucrose concentration of 600 mg ml^?1. Sucrose concentration (400 mg ml^?1) temperature (60 °C), and pH (5.6) favoured the synthesis of high levels of GF₃ and GF₄. Incubation time had a critical effect on the yield of FOS as the major products were GF₂ after 4 h and GF₄ after 8 h. A prolonged incubation of 16 h resulted in the conversion of GF₄ into GF₂ as a result of self hydrolase activity.     

Production, purification and identification of fructooligosaccharides produced by β-fructofuranosidase from Aspergillus niger IMI 303386

Aspergillus niger IMI 303386 produced higher levels of intra- and extracellular -fructofuranosidase and inulinase on inulin than on sucrose. Intracellular -fructofuranosidase from sucrose medium catalysed the best transfructosylation reaction. The concentration of fructooligosaccharides (FOS) reached a maximum in 72 h with 25% (w/v) sucrose. The FOS were purified and the main products were kestose and nystose. Inulinase hydrolysed inulin in an exofashion and released mainly fructose.     

Preparative separation of alkaloids from Nelumbo nucifera leaves by conventional and pH-zone-refining counter-current chromatography

Two modes of high-speed counter-current chromatography (HSCCC) were successfully applied to the separation of alkaloids from crude extract of Nelumbo nucifera leaves. The conventional HSCCC separations were performed with a two-phase solvent system composed of tetrachloromethane–CHCl₃–methanol–0.1 M HCl at a volume ratio of 1:3:3:2 (v/v/v/v), and 120 mg crude extract could be successfully separated. pH-Zone-refining CCC was performed with a two-phase solvent system composed of petroleum ether (60–90 °C)–ethyl acetate–methanol–water (5:5:2:8, v/v/v/v) where triethylamine (10 mM) was added to the upper organic stationary phase as a retainer and hydrochloric acid (5 mM) to the aqueous mobile phase as an eluent. From 4.0 g of the crude extract, 120 mg N-nornuciferine, 1020 mg nuciferine and 96 mg roemerine were obtained in a single run each with a purity of over 98% as determined by HPLC. The structures of the isolated compounds were identified by ESI-MS, ¹H NMR and ¹³C NMR.     

Industrial production of fructooligosaccharides by immobilized cells of <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis> in a packed bed reactor

Continuous production of fructooligosaccharides (FOS) by Aureobasidium pullulans immobilized on calcium alginate beads with a packed bed was investigated at a plant scale reactor. Optimum conditions were with 770 g sucrose/l, being fed at 200 l/h at 50°C which gave a productivity of 180 g FOS/l h. Initial activity was maintained for more than 100 days. The reactor was successfully scaled up to a production scale of 1.2 m³.     

The Production of β-Fructofuranosidase from Bifidobacterium spp.

The productions of β-fructofuranosidase from Bifidohacterium longum A1, B. adolescentis G1, and four other strains of Bifidobacteria were investigated. All strains used in this study were grown in modified BL broth containing a mixture of fructooligosaccharides [1^F (1-β-D-fructofuranosyl)_n-1sucrose, GF_n (n = 2 – 5)] as the only carbon source. Hydrolyses of 1-kestose, sucrose, and inulin were detected in the extract of the cell. The highest activity on 1-kestose was detected in the extract of B. longum A1 followed by B. adolescentis G1. The other extracts weakly attacked 1-kestose. The relative activities of the extract of B. adolescentis G1 for 1-kestose, nystose, 1^F-fructosylnystose, sucrose, and inulin were 100, 82.5, 50.8, 28.3, and 15.0, respectively. The relative activities for various substrates differed from invertases (yeast β-fructofuranosidases) and exo-inulinase from Penicillium trzehinskii.     

Production of 6-kestose by the filamentous fungus Gliocladium virens as affected by sucrose concentration

The filamentous fungus Gliocladium virens is able to produce fructooligosaccharides (FOS), fructose-containing sugars, used as functional ingredients to improve nutritional and technological properties of foods. In this work we evaluated FOS production by G. virens when grown in a wide range of sucrose concentrations (10–400 g l^?1). High sucrose concentrations increased both biomass and FOS production, including 6-kestose, a trisaccharide comprising β (2 → 6) linked fructosyl units, with enhanced stability and prebiotic activity when compared to the typical FOS β (2 → 1) linked. The highest 6-kestose yield (3 g l^?1) was achieved in media containing 150 g l^?1 sucrose after 4–5 days of culture, production being 90% greater than in media containing 10, 30, or 50 g l^?1 sucrose. After 5 days, FOS production declined markedly, following complete sucrose depletion in the medium. Although most of the β-fructofuranosidases preferentially catalyze sucrose hydrolysis, FOS production in G. virens grown in high sucrose concentration, might be attributed to a reverse hydrolysis by these enzymes. In conclusion, high sucrose concentrations increase growth of G. virens whilst 6-kestose accumulation in the medium seems to be controlled both by specific properties of β-fructofuranosidases and on the sucrose concentration.     

Biohydrogen production in a three-phase fluidized bed bioreactor using sewage sludge immobilized by ethylene–vinyl acetate copolymer

Ethylene–vinyl acetate (EVA) copolymer was used to immobilize H₂-producing sewage sludge for H₂ production in a three-phase fluidized bed reactor (FBR). The FBR with an immobilized cell packing ratio of 10% (v/v) and a liquid recycle rate of 5 l/min (23% bed expansion) was optimal for dark H₂ fermentation. The performance of the FBR reactor fed with sucrose-based synthetic medium was examined under various sucrose concentration (C_so) and hydraulic retention time (HRT). The best volumetric H₂ production rate of 1.80 ± 0.02 H₂ l/h/l occurred at C_so = 40 g COD/l and 2 h HRT, while the optimal H₂ yield (4.26 ± 0.04 mol H₂/mol sucrose) was obtained at C_so = 20 g COD/l and 6 h HRT. The H₂ content in the biogas was stably maintained at 40% or above. The primary soluble metabolites were butyric acid and acetic acid, as both products together accounted for 74–83% of total soluble microbial products formed during dark H₂ fermentation.     

Enzymatic synthesis of fructooligosaccharides from date by-products using an immobilized crude enzyme preparation of <Emphasis Type="Italic">β</Emphasis>-D-fructofuranosidase from <Emphasis Type="Italic">Aspergillus awamori</Emphasis> NBRC 4033

Aqueous extracts from date by-products of the sucrose-rich variety “Deglet Nour” were used as a starting substrate to achieve the enzymatic synthesis of fructooligosaccharides (FOS) commonly used as prebiotics. A crude β-fructofuranosidase (Ffase) preparation from Aspergillus awamori NBRC4033 was immobilized on chitosan by covalent binding through glutaraldehyde linkages (Yi = 88%, Ya = 54%), and used for this purpose. The effect of water-extraction volume on the FOS synthesis by transfructosylation was studied. It was found that 150 mL/100 g of date by-products gave the best FOS concentration and productivity (123 g/L and 18.5 g/h/100 g respectively), related to an optimal sucrose conversion of 53.26%. The main FOS product was purified via a biogel-P2 gel filtration column. Its structure was determined as 1-kestose: α-Dglucopyranosyl-( 1→2)-β-D-fructofuranosyl-(2→1)-β-Dfructofuranoside by combination of ¹H, ¹³C and 2D-NMR techniques. Our results provide new insights into the enzymatic synthesis of FOS from an alternative source of sucrose, namely date by-products.     

Biological properties of fructooligosaccharides with different contents of kestose and nystose in rats

Abstract

In a four-week experiment on rats' diets containing 5% of sucrose or fructooligosaccharides (FOS) diversified in terms of kestose and nystose contents: 6:1 (FOS-K), 3:1 (FOS-KN), and 0.5:1 (FOS-N) were applied. All FOS preparations, primarily FOS-N, considerably increased the mass of caecum, lowered pH of caecal digesta, and increased concentrations of protein. The glycolytic activity of the caecal digesta was generally alike in all groups, except for the control group where the activity of β-glucosidase was negligibly lower and that of α-galactosidase higher. The administration of FOS preparation with a diet increased the concentration and the pool of total VFA in the caecal digesta, especially in the case of butyric and propionic acids and decreased the concentration of iso-butyric and valeric acids. When compared with the kestose-rich preparation, the nystose-rich preparation increased the production of total VFA in the caecum, primarily of n-butyrate and propionate. Different length of kestose and nystose chains had no effect on the activity of bacterial enzymes in the caecum nor the biochemical indices of serum, concentration of cholesterol, glucose, urea, Ca, P and Mg.     

Method for Enrichment of Rhodopseudomonas sphaeroides from Fresh Water

An inulinase was highly purified from the culture broth of Penicillium purpurogenum by chromatographies on DEAE-Sepharose CL-6B, Toyopearl HW-65, and Bio-Gel P-100. The enzyme was homogeneous by disc electrophoretic analysis. The molecular weight was 6.4 × 10⁴ by SDS-disc electrophoresis and gel filtration on Bio-Gel P-150. The isoelectric point was pH 3.6 by isoelectric focusing. The enzyme hydrolyzed inulin rapidly, but did not affect sucrose. By paper chromatography analysis, the major products from inulin were tri-, tetra-, penta-, and hexa-saccharides. The substrate specificity of the enzyme on hydrolyses of fructo-oligosaccharides[1^F(1-β-d-fructofuranosyl)n sucrose (n = 1 to 6 and n (average of polymerization degree) = 8)] were examined. The Km values and relative maximum velocities for the hydrolyses of inulin and fructo-oligosaccharides (GF_n, n = 2 to 7 and n = 9) were as follows: inulin, (DP = 35) 0.21 mM and 100; GF₉, 0.24 mM and 86.5; GF₇, 0.33 mM and 132; GF₆, 0.85 mM and 71.2; GF₅, 3.8 mM and 25.4; GF₄, 2.8 mM and 28.8; GF₃, (nystose) 16 mM and 0.8; GF₂ (1-kestose), 8.4 mM and 0.2. The molecular activities for the hydrolyses of fructo-oligosaccharides (GF_n, n = 2 to 6) were increased depending on the degree of polymerization of fructosyl residues, and were nearly constant if the polymerization degree was over seven. These results strongly suggested that the endo-type inulinase from Penicillium purpurogenum had a subsite structure consisting of at least seven subsites.     

Production and properties of inulinase from Penicillium sp. NFCC 2768 grown on inulin-rich vegetal infusions

Inulinase production by Penicillium sp. NFCC 2768 isolated from the rhizosphere soil of dahlia was studied on media containing inulin-rich plant extracts. The maximum inulinase activity (64.54 nkat/ml) was observed with the tuber extract of dahlia (Dahlia pinnata). The fungus produced substantial inulinase activity on asparagus root powder (45.23 nkat/ml) and garlic extracts (41.32 nkat/ml). The apparent molecular weight of the purified inulinase was 68 kDa. The optimum pH and temperature for enzyme activity were 5.0 and 50°C, respectively. Mn²⁺ and Ca²⁺ were found to enhance the inulinase activity, while Hg²⁺ was found to be a strong inhibitor. Inulinase liberated fructose, glucose, sucrose, kestose (GF₂), nystose (GF₃), and inulooligosaccharides (IOS). This study suggested the use of dahlia tuber extract and asparagus root powder as suitable substrates for inulinase production by the newly isolated Penicillium sp. NFCC 2768, and its application in the generation of fructose and IOS.     

Structural analysis and optimised production of fructo- oligosaccharides by levansucrase from Acetobacter diazotrophicus SRT4

Major fructo-oligosaccharides (FOS) produced by levansucrase (EC 2.4.1.10) from Acetobacter diazotrophicus SRT4 were characterised as 1-kestose and nystose by acid hydrolysis and 13C-NMR spectroscopy. The highest yields of 1-kestose (481 mM; 241 g/l) and nystose (81 mM; 54 g/l) were achieved at initial sucrose concentration of 1754 mM (600 g/l), pH 5.5 and 40°C. The synthesized FOS reached 50% (w/w) of total sugars in the reaction mixture, with a conversion efficiency over 70% (w/w) based on the amount of sucrose converted to 1-kestose.     

Electrochemical assay for the determination of nitric oxide metabolites using copper(II) chlorophyllin modified screen printed electrodes

This work presents a novel electrochemical assay for the collective measurement of nitric oxide (NO) and its metabolites nitrite (NO₂⁻) and nitrate (NO₃⁻) in volume miniaturized sample at low cost using copper(II) chlorophyllin (CuCP) modified sensor electrode. Zinc oxide (ZnO) incorporated screen printed carbon electrode (SPCE) was used as a host matrix for the immobilization of CuCP. The morphological changes of the ZnO and CuCP modified electrodes were investigated using scanning electron microscopy. The electrochemical characterization of CuCP–ZnO–SPCE exhibited the characteristic quasi-reversible redox peaks at the potential +0.06 V versus Ag/AgCl. This biosensor electrode showed a wide linear range of response over NO concentrations from 200 nM to 500 μM with a detection limit of 100 nM and sensitivity of 85.4 nA μM⁻¹. Furthermore, NO₂⁻ measurement showed linearity of 100 nM to 1 mM with a detection limit of 100 nM for NO₂⁻ and sensitivity of 96.4 nA μM⁻¹. Then, the concentration of NO₃⁻ was measured after its enzymatic conversion into NO₂⁻. Using this assay, the concentrations of NO, NO₂⁻, and NO₃⁻ present in human plasma samples before and after beetroot supplement were estimated using suitable membrane coated CuCP–ZnO–SPCE and validated with the standard Griess method.     

Continuous production of high-purity fructooligosaccharides and ethanol by immobilized Aspergillus japonicus and Pichia heimii

High-purity fructooligosaccharides (FOS) were produced from sucrose by an innovative process incorporating immobilized Aspergillus japonicus and Pichia heimii cells. Intracellular FTase of A. japonicus converted sucrose into FOS and glucose, and P. heimii fermented glucose mainly into ethanol. The continuous production of FOS was carried out using a tanks-in-series bioreactor consisting of three stirred tanks. When a solution composed of 1 g L^?1 yeast extract and 300 g L^?1 sucrose was fed continuously to the bioreactor at a dilution rate of 0.1 h^?1, FOS at a purity of up to 98.2 % could be achieved and the value-added byproduct ethanol at 79.6 g L^?1 was also obtained. One gram of sucrose yielded 0.62 g FOS and 0.27 g ethanol. This immobilized dual-cell system was effective for continuous production of high-purity FOS and ethanol for as long as 10 days.