Production of inulo-oligosaccharides from inulin by recombinant E. coli containing endoinulinase activity

To utilize intracellular endoinulinase for inulo-oligosaccharide (IOS) production from inulin, the endoinulinase gene (inu1) of Pseudomonas sp. was successfully cloned into the plasmid pBR322 by using EcoRI restriction endoinulinase and E. coli HB101 as a host strain. The endoinulinase from E. coli HB101/pKMG50 was constitutively expressed, showing similar reaction modes as compared to those of the original strain. However, some critical differences existed in optimal reaction conditions and oligosaccharide compositions between the two products catalyzed by the native enzyme of original strain and those by intact cells from recombinant cells. The IOS compositions produced by recombinant E. coli were quite different due to the diffusional restriction of the substrate and products within the cell wall. Optimal reaction conditions for batchwise production of IOS were as follow : optimum temperature, 55v°C; pH, 7.5; substrate concentration, 100 g/l inulin; enzyme dosage, 20 units/g substrate. Continuous production of IOS from inulin was also carried out at 50v°C using a bioreactor packed with the recombinant cells immobilized on calcium alginate gel. The optimal feed concentration and the feed flow rate were 100 g/l inulin and 0.6 h^у as a superficial space velocity, respectively. Under the optimum operation conditions, continuous production of IOS was successfully performed with productivity of 166.7 g/l·h for 15 days at 50v°C without significant loss of initial activity.     

Continuous production of inulo-oligosaccharides from chicory juice by immobilized endoinulinase

Several carrier materials were examined for endoinulinase immobilization. A polystyrene carrier material (UF93^®) gave the best immobilization capacity (217 units/g carrier) and operational stability. Carbohydrate compositions in the reaction product were quite similar irrespective of the support materials even though each carrier material has different pore structure associated with diffusional restriction. After immobilization the optimal pH for enzyme activity was shifted from 5.0 to 4.5, whereas optimal temperature (55v°C) was unaltered. Continuous production of inulo-oligosaccharides from chicory juice was carried out using the polystyrene-bound endoinulinase. The recommended operating conditions of the enzyme reactor for maximizing productivity were as follows: feed concentration, 100 g/l chicory juice; flow rate, as superficial space velocity 2.0 h^у; temperature, 55v°C. The enzyme reactor was run for 28 days at 55v°C achieving an oligosaccharide yield of 82% without any significant loss of initial enzyme activity, where the volumetric productivity was 200 g/l · h. Furthermore, there was no marked difference in operational stability between the two reactors fed with pure inulin solution and with chicory juice as a substrate even though chicory juice contains a lot of impurities.     

Production of inulooligosaccharides from inulin by a novel endoinulinase from Xanthomonas sp.

A novel inulinolytic microorganism, Xanthomonas sp. produced an endoinulinase, to be used for inulooligosaccharide (IOS) formation from inulin, at an activity of 11 units ml^–1 (1.2 mg protein ml^–1). The endoinulinase was optimally active at 45°C and pH 6.0. Batchwise production of IOS was carried out by the partially purified endoinulinase with a maximum yield of about 86% on a total sugar basis with 10 g inulin l^–1. The major IOS components were DP (degree of polymerization) 5 and 6 with trace amount of smaller oligosaccharides.     

Production of inulo-oligosaccharides using endo-inulinase from a pseudomonas sp.

Inulo-oligosaccharides were produced from inulin by using high activities of an endo-acting inulinase. The total yields of oligosaccharide were slightly decreased as the concentration of inulin increased from 50 to 200g/l. Under the optimal reaction conditions, the products consist of inulo-oligosaccharides ranging from DP (degrees of polymerization)2 to DP7, where the major oligosaccharides are 29.8% DP2, 21.4% DP3, and 8.1% DP4 oligomer, respectively. The maximum yield was 75.6% when 50g inulin/l and 15 units/g substrate were used.     

Production of inulooligosaccharides from chicory extract by endoinulinase from Xanthomonas oryzae No. 5

Inulooligosaccharides (IOS) production from chicory extract was carried out using endoinulinase obtained from a new isolate, Xanthomonas oryzae No. 5. The IOS production from chicory extract was maximum when 50 g/liter of chicory extract was utilized as the substrate. As the substrate concentration increased, the IOS production accordingly decreased probably due to substrate inhibition. For a comparative study, enzyme reactions were carried out from pure inulin as substrate. Though total IOS contents indicated higher IOS yield with pure inulin compared to that of chicory extract, the distribution of inulooligosaccharide components between pure inulin and chicory extract was not significantly different; i.e. DP5 and higher oligosaccharides are major products in case of both chicory extract and pure inulin as substrate. A considerable amount of oligofructose (about 30%, w/w), which were originally present in chicory extract, resulted in the change of the enzyme kinetics. A reaction pH 7 was found to be most suitable for enzyme reaction. The initial reaction rates increased with increasing enzyme dosage, although the relative composition of the IOS produced remain unchanged.     

Production of high-content fructo-oligosaccharides by an enzymatic system from Penicillium rugulosum

Summary The production of high-content fructo-oligosaccharides from sucrose by a crude FTF from a new strain of Penicillium isolated in our Laboratory was investigated. The optimum conditions for the production of the enzyme and for the enzymic reaction have been determined. It has been demonstrated that the crude enzyme acts as a mixed enzyme system of fructosyl transferase (FTF; Class 2 of Enzyme Nomenclature) and glycosidases (Class 3 of Enyme Nomenclature). Under optimum conditions: pH 5.5, temperature 55°C, sucrose concentration 750 g/l, enzyme concentration 5 FTF units/g sucrose, conversion yield up to 80% were obtained and high concentration of nystose (412 g/l) and fructofuranosyl-nystose (176 g/l) were accumulated.     

Enzymatic production of inulo-oligosaccharides from chicory juice

Batchwise production of inulo-oligosaccharide from chicory juice was carried out by an endoinulinase from Pseudo-monas sp. The maximum yield of oligosaccharides (OS) was about 80% in total sugar basis with substrate at 30–100 g/l. Compared with pure inulin of the same origin as a substrate, the same OS yield was obtained but it showed quite a different product distribution in degree of polymerization (DP) and sugar composition, where DP2, DP3 and DP4 were major components. © Rapid Science Ltd. 1998     

Production of inulotriose from inulin by inulin-degrading enzyme from Streptomyces rochei E87

A. YOKOTA, O. YAMAUCHI AND F. TOMITA. 1995. A strain of streptomycctes producing an extracellular inulin-degrading enzyme was isolated from a soil sample. This strain was identified as Streptomyces rochei E87. The inulin-degrading enzyme was found to degrade inulin into inulotriose as the main end product. This enzyme was induced by inulin. Under favourable culture conditions, the enzyme activity in the culture supernatant fluid reached 1.0 U ml^-1after incubation for 3 d. Using this enzyme, inulotriose was produced in a weight yield of over 70% from an initial 10–50 gl^-1of inulin.     

Production of a tumor-specific xenoantiserum from partially purified immunoprotective tumor antigen

Summary Rabbits imunized with the immunoprotective TSTA fraction partially purified by preparative isoelectric focusing of 3 M KCl extracts from a chemically induced murine sarcoma, MCA-F, produced specific xenoantisera as assessed by an indirect membrane immunofluorescence assay. Only the immunizing tumor, MCA-F, and not the antigenically distinct MCA-D or MCA-T target cells were stained by the xenoantiserum. Absorption of anti-MCA-F antiserum with the antigenically distinct MCA-D or MCA-T cells did not reduce its capacity to bind to MCA-F cells. The immunofluorescence reaction was competitively inhibited by MCA-F fractions that induced specific immunoprotection: crude 3 M KCl extract, isoelectrically focused TSTA (fraction 15), and intact irradiated MCA-F cells. The TSTA specificity of these xenoantisera suggests that they may provide useful reagents for rapid isolation and characterization of the immunoprotective moiety. Abbreviations used: TSTA, tumor-specific transplantation antigens; MCA, 3-methylcholanthrene; MCA-F, MCA-D, MCA-T, methylcholanthrene-induced fibrosarcoma of C3H/HeJ mice; pIEF, preparative isoelectric focusing; PBS, 0.15 M phosphate-buffered saline (pH 7.2); MEM, minimum essential medium; MTD, minimum tumorigenic dose; Fr 15, fraction 15 of pIEF containing TSTA; FI, fluorescence index; FITC, fluorescein isothiocynate     

In vitro synthesis of fractofuranosyl-only oligosaccharides from inulin and fructose by purified chicory root fructan:fructan fructosyl transferase

Besides the non-reducing inulin series of gluco-frueto oligosaccharides which are common in Asteraceae, two series of reducing fructofuranosyl-only oligosaccharides occur in overwintering, forced, and sprouting chicory roots. Such inulo-n-oses could be produced by the action of an endo-inulinase on gluco-fructo oligosaccharides. We show here that similar series of inulo-n-oses as found in vivo can be produced by incubating fructose and inulin with a purified fructamfructan tructosyl transferase (FFT; EC 2.4.1.100) from chicory roots ( Cichorium intybus L.). Therefore fructose (but not glucose) can act as an acceptor for FFT. Since the inulo-n-oses only appear in vivo once the endogenous fructose concentration increases, we conclude that they are not the result of a putative endo-inulinase but of FFT activity.     

Production of organic acids from fermentation of mannitol, fructooligosaccharide and inulin by a cholesterol removing Lactobacillus acidophilus strain

AIMS: Assessment of individual production of organic acids by Lactobacillus acidophilus ATCC 4962 in the presence of mannitol, fructooligosaccharide (FOS) and inulin. METHODS AND RESULTS: The production patterns of individual organic acids by L. acidophilus ATCC 4962 were assessed using the experimental region for optimum cholesterol removal from the interaction between L. acidophilus ATCC 4962 and prebiotics selected in our previous study. The production of acetic and formic acids was growth associated and was greatly influenced by the inoculum size of the organism and the concentration of mannitol. The growth of the organism was repressed with the fermentation end products of FOS and inulin, which subsequently exhibited repressed production of acetic and formic acids as well. The inoculum size, mannitol and FOS linearly affected the formation of butyric acid and the response surface generated showed a correlation between butyric acid and acetic acid. The experimental regions with increased production of lactic acid showed cessation of growth of the organism, indicating inhibition of growth at high concentration of lactic acid. CONCLUSIONS: The production of individual organic acids was dependent on growth and the fermentability of prebiotics. Mannitol, FOS and inulin favoured the production of formic, lactic and butyric acids respectively. SIGNIFICANCE AND IMPACT OF THE STUDY: The fermentability of prebiotics to produce metabolites has been a controversial issue. Information gathered in this study provides a better understanding on the production of organic acids from fermentation of mannitol, FOS and inulin by L. acidophilus ATCC 4962, and on changes in their production as a response from interaction of factors.     

Purification and some properties of endoinulinase from Chrysosporium pannorum

One endoinulinase (2,1-β-d-fructan fructanohydrolase EC 3.2.1.7) was purified from Chrysosporium pannorum AHU 9700. The enzyme was a glycoprotein having an isoelectric point around pH 3.8. The molecular weight was 58,000 and 56,000 by SDS-polyacrylamide gel electrophoresis and gel filtration on Sephacryl S-200, respectively. The endoinulinase was most active between pH 6.0–7.0 at 50°C, and was stable at 45°C (10 min) and from pH 4.5 to 8.5 (24 h). This enzyme was active only on inulin, not on levan, sucrose, raffinose, or melezitose. The main products from inulin were inulotriose, inulotetraose, and inulopentaose.     

Continuous production of high-content fructooligosaccharides by a complex cell system

A complex biocatalyst system with a bioreactor equipped with a microfiltration (MF) module was employed to produce high-content fructooligosaccharides (FOS) in a continuous process initiated by a batch process. The system used mycelia of Aspergillus japonicus CCRC 93007 or Aureobasidium pullulans ATCC 9348 with beta-fructofuranosidase activity and Gluconobacter oxydans ATCC 23771 with glucose dehydrogenase activity. Calcium carbonate slurry was used to control pH to 5.5, and gluconic acid in the reaction mixture was precipitated as calcium gluconate. Sucrose solution with an optimum concentration of 30% (w/v) was employed as feed for the complex cell system, and high-content FOS was discharged continuously from a MF module. The complex cell system was run at 30 degrees C with an aeration rate of 5 vvm and produced more than 80% FOS with the remainder being 5-7% glucose and 8-10% sucrose on a dry weight basis, plus a small amount of calcium gluconate. The system worked for a 7-day continuous production process with a dilution rate of 0.04 h(-1), and the volumetric productivity for total FOS was more than 160 g L(-1) h(-1).     

Production of cyclodextrin from starch by cyclodextrin glycosyltransferase from Bacillus firmus and characterization of purified enzyme

During screening for cyclodextrin-forming microorganisms, an alkalophilic Bacillus sp, which produced high activity of cyclodextrin glycosyltransferase, was isolated and identified as Bacillus firmus. The crude enzyme transformed starch to mainly β-and γ-cyclodextrin. The purified enzyme had an optimum pH of 7.5–8.5 and its optimum temperature was 65°C, which is the highest optimum temperature as compared to other cyclodextrin glycosyltransferases except that produced by Bacillus amyloliquefaciens. Received 06 January 1997/ Accepted in revised form 20 March 1997     

Production of highly purified hydroxytyrosol from Olea europaea leaf extract biotransformed by hyperthermophilic beta-glycosidase

A large amount of highly purified hydroxytyrosol (91-94% in weight) is obtained in short time by a simple biotransformation of Olea europaea leaf extract by a partially purified hyperthermophilic beta-glycosidase immobilized on chitosan support. The biotransformation conditions have been modulated for increasing the hydroxytyrosol yield, whilst chitosan and chitin matrices are used as adsorbent materials in liquid phase hydroxytyrosol extraction from the biotransformed mixtures. Natural and non-toxic hydroxytyrosol has been by this way produced from a vegetal source, and this compound appeared for the first time highly purified by natural and biocompatible safe biopolymers in comparison to previous results. Moreover, the GC analyses have displayed that the eluates from a two-step bioreactor have qualitative composition very similar to that of the extra-virgin olive oil polar fraction. The proposed bioreactor could also find application in the utilization of olive mill waste waters (OMWW), medium rich in large amounts of oleuropein, which can be converted in pharmacologically active compounds.     

Characterization of a novel fructosyltransferase from Lactobacillus reuteri that synthesizes high-molecular-weight inulin and inulin oligosaccharides

Fructosyltransferase (FTF) enzymes produce fructose polymers (fructans) from sucrose. Here, we report the isolation and characterization of an FTF-encoding gene from Lactobacillus reuteri strain 121. A C-terminally truncated version of the ftf gene was successfully expressed in Escherichia coli. When incubated with sucrose, the purified recombinant FTF enzyme produced large amounts of fructo-oligosaccharides (FOS) with beta-(2-->1)-linked fructosyl units, plus a high-molecular-weight fructan polymer (>10(7)) with beta-(2-->1) linkages (an inulin). FOS, but not inulin, was found in supernatants of L. reuteri strain 121 cultures grown on medium containing sucrose. Bacterial inulin production has been reported for only Streptococcus mutans strains. FOS production has been reported for a few bacterial strains. This paper reports the first-time isolation and molecular characterization of (i) a Lactobacillus ftf gene, (ii) an inulosucrase associated with a generally regarded as safe bacterium, (iii) an FTF enzyme synthesizing both a high molecular weight inulin and FOS, and (iv) an FTF protein containing a cell wall-anchoring LPXTG motif. The biological relevance and potential health benefits of an inulosucrase associated with an L. reuteri strain remain to be established.