Inversion of sucrose with β- -fructofuranosidase (invertase) immobilized on bead DEAHP-cellulose: Batch process

The inversion of sucrose with β- -fructofuranosidase (EC 3.2.1.26) immobilized by an ionic bond on bead cellulose containing weak basic N,N-diethylamino-2-hydroxypropyl groups has been investigated. The immobilized enzyme is strongly bound at an ionic strength up to 0.1 M in the pH range 3–6. The amount adsorbed is proportional to porosity and to the exchange capacity of the ion exchange cellulose, reaching values up to 200 mg/g dry carrier, with an activity in 10% sucrose solution at 30°C, pH 5, >8000 μmol min⁻¹ g⁻¹. The inversion of sucrose with immobilized β- -fructofuranosidase was carried out in a stirred reactor. The dependence of activity on pH (3–7), temperature (0–70°C) and concentration of the substrate (2–64 wt%) were determined, and the inversion was compared with that obtained using non-immobilized enzyme under similar conditions. The rate of inversion at low substrate concentration (2–19 wt%) was described by Michaelis-Menten kinetics.     

Inversion of sucrose in a continuous process with β-d-fructofuranosidase (invertase) immobilized on bead DEAHP-cellulose

Inversion of sucrose with β-d-fructofuranosidase (EC 3.2.1.26) immobilized by the ionic bond on bead DEAHP-cellulose has been studied under flow conditions. Under these conditions, the inversion of sucrose is affected by the concentration and flow rate of the substrate and by the reaction temperature. The effect of substrate concentration on the reaction was investigated in the range 19.5–64.2 wt %; the effect of flow rate was examined in the range 0.25–5.57 g solution per min, and the temperature range used was 25–50°C. It was found that the activities of immobilized β-d-fructofuranosidase in stirred and flow reactors were the same. The lower activities of β-d-fructofuranosidase in the case of concentrated solutions, and of immobilized β-d-fructofuranosidase compared with the native enzyme are attributed to more difficult diffusion through the beads of the ion exchanger, especially of the strongly viscous substrate. A long-term investigation of the enzyme activity over a period of three months demonstrated the stability of the β-d-fructofuranosidase immobilized by the ionic bond on bead DEAHP-cellulose; the half-life of the enzyme was 215 days. It was also found that the immobilization of the enzyme on a carrier was more effective under flow conditions, i.e. through an ion exchanger in the column, than under the equilibrium conditions of a stirred reactor.     

Inversion of sucrose with β-d-fructofuranosidase (invertase) immobilized on bead DEAHP-cellulose: Batch process

The inversion of sucrose with β-d-fructofuranosidase (EC 3.2.1.26) immobilized by an ionic bond on bead cellulose containing weak basic N,N-diethylamino-2-hydroxypropyl groups has been investigated. The immobilized enzyme is strongly bound at an ionic strength up to 0.1 M in the pH range 3–6. The amount adsorbed is proportional to porosity and to the exchange capacity of the ion exchange cellulose, reaching values up to 200 mg/g dry carrier, with an activity in 10% sucrose solution at 30°C, pH 5, >8000 μmol min^?1 g^?1. The inversion of sucrose with immobilized β-d-fructofuranosidase was carried out in a stirred reactor. The dependence of activity on pH (3–7), temperature (0–70°C) and concentration of the substrate (2–64 wt%) were determined, and the inversion was compared with that obtained using non-immobilized enzyme under similar conditions. The rate of inversion at low substrate concentration (2–19 wt%) was described by Michaelis-Menten kinetics.     

Batch production of high-content fructo-oligosaccharides from sucrose by the mixed-enzyme system of β-fructofuranosidase and glucose oxidase

The production of high-content fructo-oligosaccharides from sucrose by the mixed-enzyme system of β-fructofuranosidase and glucose oxidase was investigated. The mixed-enzyme reaction was carried out in a stirred tank reactor containing 0.7 l of sucrose solution with coupled β-fructofuranosidase and glucose oxidase for 25 h. The optimum conditions for the mixed-enzyme reaction were as follows: pH, 5.5; temperature, 40°C; sucrose concentration, 400 g/l; agitation speed, 550 rpm; oxygen flow rate, 0.7 l/min; enzyme dosage, 10 units of β-fructofuranosidase with the combination of 15 units of glucose oxidase per gram sucrose. Under optimum conditions, high-content fructo-oligosaccharides up to 98% were obtained with complete consumption of sucrose and glucose by the mixed-enzyme system. Compared with the fructo-oligosaccharides produced by the β-fructofuranosidase, the high-content fructo-oligosaccharides produced by the mixed-enzyme system showed a significant difference with respect to sugar composition; i.e., a higher content of nystose was accumulated and only a trace amount of fructofuranosyl nystose was detected.     

Immobilization of invertase on a new type of macroporous glycidyl methacrylate

Invertase was immobilized via its carbohydrate moiety. The immobilized enzyme has a specific activity of 5500 IU g^–1, with 45% activity yield on immobilization. In a packed bed reactor, 90% 2.5 M sucrose was converted at a flow rate of 4 bed volumes h^–1. The obtained specific productivity at 40 °C of 3 kg l^–1 h^–1 is the best one so far. Long-term stability was 290 days in 2.5 M sucrose at 40 °C and at a flow rate of 3 bed volumes h^–1.     

On-line deconjugation of glucuronides using an immobilized enzyme reactor based upon β-glucuronidase

An immobilized enzyme reactor based upon β-glucuronidase (BG–IMER) has been developed for the on-line deconjugation of substrates. The activity of the BG–IMER and its applicability to on-line deconjugation was investigated. The BG–IMER was coupled to a reversed-phase column (C₈ or C₁₈) and the latter column was used to separate substrates and products eluted from the β-glucuronidase reactor. The activity of the BG–IMER was followed by measurement of percent deconjugation and the parameters investigated were: substrate concentration, pH (4 to 6), temperature (r.t., 37°C), enzyme–substrate contact time using flow-rates of 0.1 to 1.0 ml/min (15–1.5 min). The glucuronides used in the evaluation of the BG–IMER were: 4-methylumbelliferyl-β- -glucuronide, p-acetaminophen-β- -glucuronide, 3′-azido-3′-deoxythymidine-β- -glucuronide, phenyl-β- -glucuronide, chloramphenicol-β- -glucuronide, estradiol-17-β- -glucuronide and morphine-β- -glucuronide. The development of on-line HPLC deconjugation of glucuronide substrates using the BG–IMER will facilitate the identification of metabolites and quantification of aglycones in metabolic and pharmacokinetic studies.     

Molecular and Biochemical Characterization of a β-Fructofuranosidase from Xanthophyllomyces dendrorhous

An extracellular β-fructofuranosidase from the yeast Xanthophyllomyces dendrorhous was characterized biochemically, molecularly, and phylogenetically. This enzyme is a glycoprotein with an estimated molecular mass of 160 kDa, of which the N-linked carbohydrate accounts for 60% of the total mass. It displays optimum activity at pH 5.0 to 6.5, and its thermophilicity (with maximum activity at 65 to 70°C) and thermostability (with a T₅₀ in the range 66 to 71°C) is higher than that exhibited by most yeast invertases. The enzyme was able to hydrolyze fructosyl-β-(2→1)-linked carbohydrates such as sucrose, 1-kestose, or nystose, although its catalytic efficiency, defined by the k_cat/K_m ratio, indicates that it hydrolyzes sucrose approximately 4.2 times more efficiently than 1-kestose. Unlike other microbial β-fructofuranosidases, the enzyme from X. dendrorhous produces neokestose as the main transglycosylation product, a potentially novel bifidogenic trisaccharide. Using a 41% (wt/vol) sucrose solution, the maximum fructooligosaccharide concentration reached was 65.9 g liter⁻¹. In addition, we isolated and sequenced the X. dendrorhous β-fructofuranosidase gene (Xd-INV), showing that it encodes a putative mature polypeptide of 595 amino acids and that it shares significant identity with other fungal, yeast, and plant β-fructofuranosidases, all members of family 32 of the glycosyl-hydrolases. We demonstrate that the Xd-INV could functionally complement the suc2 mutation of Saccharomyces cerevisiae and, finally, a structural model of the new enzyme based on the homologous invertase from Arabidopsis thaliana has also been obtained.     

Immobilization studies of whole microbial cells on transition metal activated inorganic supports

Summary Whole cells of Saccharomyces bayanus, Saccharomyces cerevisiae and Zymomonas mobilis were immobilized by chelation/metal-link processes onto porous inorganic carriers. The immobilized yeast cells displayed much higher sucrose hydrolyzing activities (90–517 U/g) than the bacterial, Z. mobilis, cells (0.76–1.65 U/g). The yeast cells chelated on hydrous metal oxide derivative of pumice stone presented higher initial -d-fructofuranosidase (invertase, EC 3.2.1.26) activity (161–517 U/g) than on other derivatives (90–201 U/g). The introduction of an organic bridge between the cells and the metal activator led to a decrease of the initial activity of the immobilized cells, however S. cerevisiae cells immobilized on the carbonyl derivative of titanium (IV) activated pumice stone, by covalent linkage, displayed a very stable behaviour, which in continuous operation at 30° C show only a slightly decrease on invertase activity for a two month period (half-life=470 days). The continuous hydrolysis of a 2% w/v sucrose solution at 30° C in an immobilized S. cerevisiae packed bed reactor was described by a simple kinetic model developed by the authors (Cabral et al., 1984a), which can also be used to predict the enzyme activity of the immobilized cells from conversion degree data.     

Semirational Directed Evolution of Loop Regions in Aspergillus japonicus β-Fructofuranosidase for Improved Fructooligosaccharide Production

The Aspergillus japonicus β-fructofuranosidase catalyzes the industrially important biotransformation of sucrose to fructooligosaccharides. Operating at high substrate loading and temperatures between 50 and 60°C, the enzyme activity is negatively influenced by glucose product inhibition and thermal instability. To address these limitations, the solvent-exposed loop regions of the β-fructofuranosidase were engineered using a combined crystal structure- and evolutionary-guided approach. This semirational approach yielded a functionally enriched first-round library of 36 single-amino-acid-substitution variants with 58% retaining activity, and of these, 71% displayed improved activities compared to the parent. The substitutions yielding the five most improved variants subsequently were exhaustively combined and evaluated. A four-substitution combination variant was identified as the most improved and reduced the time to completion of an efficient industrial-like reaction by 22%. Characterization of the top five combination variants by isothermal denaturation assays indicated that these variants displayed improved thermostability, with the most thermostable variant displaying a 5.7°C increased melting temperature. The variants displayed uniquely altered, concentration-dependent substrate and product binding as determined by differential scanning fluorimetry. The altered catalytic activity was evidenced by increased specific activities of all five variants, with the most improved variant doubling that of the parent. Variant homology modeling and computational analyses were used to rationalize the effects of amino acid changes lacking direct interaction with substrates. Data indicated that targeting substitutions to loop regions resulted in improved enzyme thermostability, specific activity, and relief from product inhibition.     

Glutaraldehyde-fixation of yeast cells: Kinetics of a model system for enzyme cytochemistry

The kinetics of glutaraldehyde inactivation of a protoplasmic (-fructofuranosidase) and an extracytoplasmic (acid phosphatase) enzyme inSaccharomyces rouxii cells were studied at pH 5.5 and 30°C. The effects of glutaraldehyde concentration (0.5–3%), pH value, and temperature were surveyed by varying the fixation conditions. Cells from 1- to 10-day cultures retained 50–75% of their acid phosphatase activity and 15–24% of their -fructofuranosidase activity after 1-h exposures to 0.5% glutaraldehyde. The surviving -fructofuranosidase activity remained physically cryptic and was revealed only after further membrane perturbation with ethyl acetate. This crypticity barrier disappeared after overnight incubation of the treated cells at 4°C, with or without added glutaraldehyde, during which time the enzyme was resistant to further inactivation. The velocity ratio for raffinose versus sucrose, as substrate, decreased in treated cells, and changes inV _max andK _m were indicative of frank destruction of some enzyme molecules as well as modification of survivors. A comparable set of changes was also generated by treating cell-free extract with glutaraldehyde. Glutaraldehyde (0.5%) killed all yeast cells at 30°C within 5 min; at 4°C survival rates were quite high—81% after 15 min and 65% after 1 h. The bearing of these examples of enzyme inactivation, permeability barrier abolition, and structural stabilization on the general problems of yeast cytochemistry is discussed.     

MenD as a versatile catalyst for asymmetric synthesis

The thiamine diphosphate (ThDP)-dependent enzyme 2-succinyl-5-enolpyruvyl-6-hydroxy-3-cyclohexene-1-carboxylate synthase (MenD) from Escherichia coli K12, formerly known as SHCHC-synthase, catalyses the decarboxylation of α-ketoglutarate and the subsequent addition of the resulting succinyl-THDP to isochorismate. Here, the enzyme is tested for unphysiologial C–C bond-forming reactions.Condensation of α-ketoglutarate after decarboxylation to a broad range of aldehydes gave α-hydroxyketones with isolated yields from 26 to 87% and 94 to 98% ee for addition to aromatic aldehydes. MenD accepts a wide range of aldehydes as acceptor substrates to produce chiral α-hydroxyketones with conserved regioselectivity where the activated succinylsemialdehyde serves selectively as the donor. Regioselectivity is inverted only for condensation of α-ketoglutarate with pyruvate (activated acetaldehyde) as donor. Besides α-ketoglutarate, pyruvate and oxalacetate are accepted as donors in combination with benzaldehyde and 2-fluorobenzaldehyde as acceptors, however with decreased activity of C–C bond formation.The physiological 1,4-addition of α-ketoglutarate to isochorismate was investigated for acceptor substrate variability. (2S,3S)-2,3-Dihydroxy-2,3-dihydrobenzoate (2,3-CHD), which lacks the pyruvyl found in isochorismate, is converted to (5S,6S)-2-succinyl-5,6-dihydroxycyclohex-2-enecarboxylate. In contrast to the addition to carbonyls, the active site of MenD does appear to impose specific constraints on the acceptor substrate for 1,4-addition with α,β-unsaturated carboxylic acids.     

Improved productivity of <Emphasis Type="Italic">β</Emphasis>-fructofuranosidase by a derepressed mutant of <Emphasis Type="Italic">Aspergillus niger</Emphasis> from conventional and non-conventional substrates

Summary Wild-type cultures of Aspergillus niger produced a basal level of β-fructofuranosidase on glucose of 1 IU l⁻¹ h⁻¹. In contrast, a catabolite-derepressed mutant strain of the same organism produced a markedly higher level (25 IU l⁻¹ h⁻¹) of this enzyme when grown on the same carbon source. Wheat bran induced both the wild type (252 IU l⁻¹ h⁻¹) and the mutant strain (516 IU l⁻¹ h⁻¹) to produce 252- to 516-fold higher levels of this enzyme than was observed with the wild-type grown on glucose and was the best carbon source. When corn steep liquor served as a nitrogen source, the wild-type organism showed a higher activity of enzyme on monosaccharides and disaccharides comparable to that produced by corncobs in the basal medium and that mutant was a potentially improved (> 2-fold) organism for the production of β-fructofuranosidase on all carbon sources. Enhanced substrate consumption and product formation kinetic parameters suggest that the mutant organism may be exploited for bulk production of this useful enzyme.     

Kinetic behaviour of α-galactosidase produced by Absidia griseola: a comparison between free and immobilized forms of the enzyme

In this research the characteristics of free (partially purified) and immobilized (mould pellets of Absidia griseola) -galactosidase have been investigated. Inhibition studies of the enzyme showed that p-nitrophenol and sucrose do not have any inhibitory effect on the enzyme, but that galactose is a competitive inhibitor. In the immobilized form, inhibition was lower than in the free enzyme and the level of inhibition decreased as the temperature increased. The activity and stability of free and immobilized enzyme were investigated with respect to temperature, and the results showed that the optimal temperature range of the free enzyme was 45–50 °C, while the immobilized enzyme had an optimum at 55–60 °C. The optimum pH for the free enzyme was 6.0 and the value was decreased to 5.0 by immobilizing. The experimental effectiveness factors were found to be represented as a single function of the modified Thiele modulus, including parameters such as pellet size, enzyme concentration in the pellets and substrate concentration. Both experimental and theoretical data concerning effectiveness factors are nearly the same.     

Performance of Aspergillus niger B 03 β-xylosidase immobilized on polyamide membrane support

The dynamics of β-xylosidase biosynthesis from Aspergillus niger B 03 was investigated in laboratory bioreactor. Maximum xylosidase activity 5.5 U/ml was achieved after 80 h fermentation at medium pH 4.0. The isolated β-xylosidase was immobilized on polyamide membrane support and the basic characteristics of the immobilized enzyme were determined. Maximum immobilization and activity yield obtained was 30.0 and 6.8%, respectively. A shift in temperature optimum and pH optimum was observed for immobilized β-xylosidase compared to the free enzyme. Immobilized enzyme exhibited maximum activity at 45 °C and pH 4.5 while its free counterpart at 70 °C and pH 3.5, respectively. Thermal stability at 40 and 50 °C and storage stability of immobilized β-xylosidase were investigated at pH 5.0. Kinetic parameters K_m, V_max and K_i were determined for both enzyme forms. Free and immobilized β-xylosidase were tested for xylose production from birchwood xylan. The substrate was preliminarily depolymerized with xylanase to xylooligosaccharides and the amount of xylose obtained after their hydrolysis with free and immobilized β-xylosidase was determined by HPLC analysis. Continuous enzyme hydrolysis of birchwood xylan was performed with xylanase and free or immobilized β-xylosidase. The maximum extent of hydrolysis was 25 and 30% with free and immobilized enzyme, respectively. Immobilized preparation was also examined for reusability in 20 consecutive cycles at 40 °C.     

Continuous production of fructooligosaccharides from sucrose by immobilized fructosyltransferase

The productivity of the continuous production of fructooligosaccharides from sucrose was investigated by fructosyltransferase immobilized onto a high-porous ion exchange resin was optimal with 600 g sucrose/l at a flow rate of 2.7 h^–1 expressed as a superficial space velocity. When the column was operated at 50 °C, about 8% loss of the initial activity of immobilized enzyme was observed after 30 days continuous operation, achieving high productivity of 1174 g/l · h.     

Purification and properties of a novel raw starch degrading-cyclodextrin glycosyltransferase from Klebsiella pneumoniae AS- 22

A novel raw starch degrading α-cyclodextrin glycosyltransferase (CGTase; E.C. 2.4.1.19), produced by Klebsiella pneumoniae AS-22, was purified to homogeneity by ultrafiltration, affinity and gel filtration chromatography. The specific cyclization activity of the pure enzyme preparation was 523 U/mg of protein. No hydrolysis activity was detected when soluble starch was used as the substrate. The molecular weight of the pure protein was estimated to be 75 kDa with SDS-PAGE and gel filtration. The isoelectric point of the pure enzyme was 7.3. The enzyme was most active in the pH range 5.5–9.0 whereas it was most stable in the pH range 6–9. The CGTase was most active in the temperature range 35–50°C. This CGTase is inherently temperature labile and rapidly loses activity above 30°C. However, presence of soluble starch and calcium chloride improved the temperature stability of the enzyme up to 40°C. In presence of 30% (v/v) glycerol, this enzyme was almost 100% stable at 30°C for a month. The K_m and k_cat values for the pure enzyme were 1.35 mg ml⁻¹ and 249 μM mg⁻¹ min⁻¹, respectively, with soluble starch as the substrate. The enzyme predominantly produced α-cyclodextrin without addition of any complexing agents. The conditions employed for maximum α-cyclodextrin production were 100 g l⁻¹ gelatinized soluble starch or 125 g l⁻¹ raw wheat starch at an enzyme concentration of 10 U g⁻¹ of starch. The α:β:γ-cyclodextrins were produced in the ratios of 81:12:7 and 89:9:2 from gelatinized soluble starch and raw wheat starch, respectively.     

Identification of Prebiotic Fructooligosaccharide Metabolism in Lactobacillus plantarum WCFS1 through Microarrays

Short-chain fructooligosaccharides (scFOS) and other prebiotics are used to selectively stimulate the growth and activity of lactobacilli and bifidobacteria in the colon. However, there is little information on the mechanisms whereby prebiotics exert their specific effects upon such microorganisms. To study the genomic basis of scFOS metabolism in Lactobacillus plantarum WCFS1, two-color microarrays were used to screen for differentially expressed genes when grown on scFOS compared to glucose (control). A significant up-regulation (8- to 60-fold) was observed with a set of only five genes located in a single locus and predicted to encode a sucrose phosphoenolpyruvate transport system (PTS), a β-fructofuranosidase, a fructokinase, an α-glucosidase, and a sucrose operon repressor. Several other genes were slightly overexpressed, including pyruvate dehydrogenase. For the latter, no detectable activity in L. plantarum under various growth conditions has been previously reported. A mannose-PTS likely to encode glucose uptake was 50-fold down-regulated as well as, to a lower extent, other PTSs. Chemical analysis of the different moieties of scFOS that were depleted in the growth medium revealed that the trisaccharide 1-kestose present in scFOS was preferentially utilized, in comparison with the tetrasaccharide nystose and the pentasaccharide fructofuranosylnystose. The main end products of scFOS fermentation were lactate and acetate. This is the first example in lactobacilli of the association of a sucrose PTS and a β-fructofuranosidase that could be used for scFOS degradation.     

Monitoring and control of enzymic sucrose hydrolysis using on-line biosensors

Summary Previously reported flow microcalorimeter devices for enzymic reaction heat measurement, enzyme thermistors, have here been extended with systems for on-line sample treatment. Glucose analysis was performed by intermittent flow injections of 50 l samples through such an enzyme thermistor device containing immobilized glucose oxidase and catalase. Sucroce analysis was performed by allowing diluted samples to continuously pass through an additional enzyme thermistor containing immobilized invertase. The reaction heats were recorded as temperature changes in the order of 10–50 m°C for concentrations of 0.05–0.30 M glucose or sucrose present in the original non-diluted samples.The performance of this system was investigated by its ability to follow concentration changes obtained from a gradient mixer. The system was applied to monitoring and controlling the hydrolysis of sucrose to glucose and fructose in a plug-flow reactor with immobilized invertase. The reactor was continuously fed by a flow of scurose of up to 0.3 M (100 g/l). Glucose and remaining sucrose were monitored in the effluent of the column. By using flow rate controlled feed pumps for sucrose and diluent the influent concentration of sucrose was varied while the overall flow rate remained constant.On-line control of the effluent concentration of lucose and sucrose was achieved by a proportional and integral regulator implemented on a microcomuter. Preset concentration of glucose in the effluent could be maintained over an extended period of time espite changes in the overall capacity of the invertase reactor. Long delay times in the sensor system and the enzyme column made it necessary to carefully tune the control parameters. Changes of set-point value and temperature disturbances were used to verify accuracy of controlling performance.     

Synthesis of Oligosaccharides by β-Fructofuranosidase in Biphasic Medium Containing Organic Solvent as Bulk Phase

The effect of four organic solvents on β-fructofuranosidase mediated synthesis of oligosaccharides from sucrose were investigated. Amongst the solvents examined, butyl acetate proved to be the best for oligosaccharide synthesis. Starting with the equivalent of 44.6 g/L of sucrose, 247 U of enzyme and 91.6% (by vol.) of butyl acetate results in the production of 8.8 g/L of oligosaccharides within 30 min, with trisaccharides constituting more than 60% of the oligosaccharides. The efficiency for conversion of sucrose to oligosaccharides is greater than 19%, and this exceeds the 11.6% (in 24 h) previously achieved with 1271 U of the same enzyme in aqueous medium. Use of butyl acetate as the bulk phase therefore modifies the reaction environment in favour of enhanced and accelerated rate of oligosaccharide synthesis by this β-fructofuranosidase.