Scalable preparation of silCoat‐biocatalysts by use of a fluidized‐bed reactor

SilCoat‐biocatalysts are immobilized enzyme preparations with an outstanding robustness against leaching and mechanical stress and therefore promising tools for technical synthesis. They consist of a composite material made from a solid enzyme carrier and silicone. In this study, a method has been found to enable provision of these catalysts in large scale. It makes use of easily scalable fluidized‐bed technology and, in contrast to the original method, works in almost complete absence of organic solvent. Thus, it is both a fast and safe method. When the Pt‐catalyst required for silicone formation is cast on the solid enzyme carrier before coating, resulting composites resemble the original preparations in morphology, catalytic activity, and stability against leaching and mechanical forces. Only the maximum total content of silicone in the composites lies about 10% w/w lower resulting in an overall leaching stability below the theoretical maximum. When the Pt‐catalyst is mixed with cooled siloxane solution before coating, surficial coating of the enzyme carriers is achieved, which provides maximum leaching stability at very low silicone consumption. Thus, the technology offers the possibility to produce both composite and for the first time also core‐shell silCoat‐particles, and optimize leaching stability over mechanical strength according to process requirements.     

Hydrolysis of Galacto-oligosaccharides in Soymilk by κ-carrageenan-entrapped α-galactosidase from Aspergillus Oryzae

Summary α-Galactosidase was immobilized in κ-carrageenan. The optimum pH of the soluble enzyme and immobilized enzyme was 4.8. The optimum temperature of the soluble enzyme was 50 °C and that of the immobilized enzyme was increased to 53 °C. The immobilized enzyme was used in batch, repeated batch, and in the continuous mode to degrade the raffinose family sugars present in soymilk. Two hours incubation with free and immobilized α-galactosidase resulted in 88 and 75% reduction in raffinose family oligosaccharides in soymilk respectively. In the repeated batch, 61% reduction was obtained in the fourth cycle. A fluidized bed reactor was designed to treat soymilk continuously. The performance of immobilized α-galactosidase was also tested in a fluidized bed reactor at different flow rates and 92% reduction of raffinose family oligosaccharides in soymilk was obtained at 25 ml h⁻¹ flow rate. The study revealed that immobilized α-galactosidase in continuous mode is efficient in reducing the oligosaccharides present in the soymilk.     

Removal of flatulence-inducing sugars by using free and polyvinyl alcohol immobilized α-Galactosidase from Aspergillus oryzae

Consumption of soymilk and soybean derived foods has been hampered due to the presence of RFOs (raffinose family oligosaccharides). Soy-based foods free from RFOs have positive impact on their acceptance as protein rich food. α-Galactosidase was entrapped in PVA (polyvinyl alcohol) cross linked with boric acid. Immobilized enzyme showed shift in optimum pH of 0.4 units and the activity yield of the immobilized α-galactosidase was found to be 76%. Immobilized enzyme was used to reduce RFOs in soymilk. In batch reaction after 12 h incubation soluble and immobilized enzyme showed 92 and 83% reduction of RFOs in soymilk, respectively. In repeated batch experiments immobilized enzyme showed 64% of its hydrolyzing activity after 6th cycle. PVA-immobilized α-galactosidase in fluidized bed reactor showed highest reduction (92%) of RFOs at a flow rate of 30 mL/h. The results of this study are interesting for their use in food processing industry.     

Glucose isomerase immobolized on porous glass

Partially purified glucose isomerase from a Streptomyces species was immobilized on porous glass particles and studied for various characteristics concerning its use as an industrial catalyst. The activities were investigated in relation to the reaction parameters and the enzyme deactivation was studied systematically under various reaction conditions. The half-life of the immobilized enzyme was found to exceed 200 days at 50°C. The rate equation of the reversible glucose ? fructose reaction was derived and the kinetic constants were determined. The rate equation was found to be in good agreement with experimental data for both forward and reverse reactions. The degree of diffusional effects was experimentally measured and theoretically analyzed.     

The use of α-galactosidase and invertase in hollow fiber reactors

Invertase and α-galactosidase have been immobilized in hollow fiber cartridges with no detectable enzyme leakage and used for the hydrolysis of sucrose and raffinose, respectively. For both hollow fiber immobilizes enzymes nearly complete substrate conversion is possible. Enzyme stabilities in polysulfone hollow fibers which have been preconditioned with bovine albumin approach the stabilities of the free enzymes.     

Electron transfer between galactose oxidase and an electrode via a redox polymer network

Galactose oxidase from Dactyllium dendroides was purified and immobilised on a carbon electrode in a redox polymer network of a polyvinylpyridine, partially N-complexed with osmiumbis(bipyridine)chloride (POsEA). The current density of the electrodes depended on the concentration of phosphate elution buffer. By additional crosslinking with a 1% glutaraldehyde solution in 50 mM phosphate buffer, pH 7.0, an electrode with an initial current density of 0.8 mA/cm² was obtained. Operational half life times were in the order of 1.2 h. The affinity of the immobilized enzyme for galactose,lactose, raffinose, glycerol and dihydroxyaceton was higher than described in literature for the enzyme in solution. Optimal temperature for the enzyme electrode was 30°C. The pH optimum for the immobilized enzyme was higher than for the enzyme in solution.     

Enzymatic removal of flatulence-inducing sugars in chickpea milk using free and polyvinyl alcohol immobilized α-galactosidase from <Emphasis Type="Italic">Aspergillus oryzae</Emphasis>

The treatment of chickpea milk was carried out in batch, repeated batch and continuous reaction by soluble and polyvinyl alcohol (PVA) immobilized Aspergillus oryzae alpha-galactosidase for the removal of raffinose family oligosaccharides (RFOs). In the batch mode of treatment 96 and 92% of RFOs hydrolysis was observed by soluble and immobilized enzyme, respectively. In repeated batch experiments, immobilized enzyme showed 70% RFOs hydrolysis up to sixth cycle. Polyvinyl alcohol immobilized alpha-galactosidase in fluidized bed reactor showed highest reduction of 94% at a flow rate of 30 ml/h. The results obtained from the present study are very interesting for industrial use of PVA-immobilized enzyme.     

A novel support for the immobilization of lipase and the effects of the details of its preparation on the hydrolysis of triacylglycerides

Summary The lipase from Candida cylindracea was immobilized by its adsorption on the internal surface of hydrophobic microporous poly(styrene-divinylbenzene) supports prepared by the concentrated emulsion polymerization method. The prepared supports have a surface area of the order of 200 m²/g. The immobilized enzyme catalyst is used for the hydrolysis of triacylglycerides. The effects of the amounts of surfactant and divinylbenzene used in the preparation of the hydrophobic support on the adsorption capacity for lipase and on the activity of the immobilized lipase have been investigated. The activity of the immobilized enzyme per enzyme molecule can be higher than that of the free lipase.     

Production, purification and characterization of an extracellular inulinase from Kluyveromyces marxianus var. bulgaricus

The yeast Kluyveromyces marxianus var. bulgaricus produced large amounts of extracellular inulinase activity when grown on inulin, sucrose, fructose and glucose as carbon source. This protein has been purified to homogeneity by using successive DEAE-Trisacryl Plus and Superose 6HR 10/30 columns. The purified enzyme showed a relative molecular weight of 57 kDa by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) and 77 kDa by gel filtration in Superose 6 HR 10/30. Analysis by SDS-PAGE showed a unique polypeptide band with Coomassie Blue stain and nondenaturing PAGE of the purified enzyme obtained from media with different carbon sources showed the band, too, when stained for glucose oxidase activity. The optimal hydrolysis temperature for sucrose, raffinose and inulin was 55°C and the optimal pH for sucrose was 4.75. The apparent K _m values for sucrose, raffinose and inulin are 4.58, 7.41 and 86.9 mg/ml, respectively. Thin layer chromatography showed that inulinase from K. marxianus var. bulgaricus was capable of hydrolyzing different substrates (sucrose, raffinose and inulin), releasing monosaccharides and oligosaccharides. The results obtained suggest the hypothesis that enzyme production was constitutive. Journal of Industrial Microbiology & Biotechnology (2000) 25, 63–69. Received 17 November 1999/ Accepted in revised form 30 May 2000     

Cloning,Expression, and Characterization of Rice α-Galactosidase

We have successfully cloned an α-galactosidase gene from a rice cDNA library and transformed it into Escherichia coli BL21. It was subsequently cloned to the pPIC9K vector and expressed in Pichia pastoris. A selected clone was found to result in high production yield of the galactosidase enzyme. The secreted enzyme was purified, and it revealed as a major protein band on an SDS-PAGE gel. The optimal pH value, enzyme stabilities, and substrate specificity were studied. The enzyme specificity toward the terminal α1→6, 1→4, and 1→3 linked galactosyl residue from various substrates was investigated. By determining the Michelis constant (Km) of the enzyme for melibiose, raffinose, and stachyose, our results showed that melibiose was hydrolyzed faster than raffinose, whereas the published data reported a reversed sequence, raffinose > melibiose. The enzyme also showed the ability of converting B red blood cells into O red cells. The objective of this work is to develop the Pichia system to produce a large quantity of enzyme for blood cell conversion for transfusion.     

Degradation of raffinose oligosaccharides in soymilk by immobilized alpha-galactosidase of Aspergillus oryzae

Alpha-galactosidase was immobilized in a mixture of k-carrageenan and locust bean gum. The properties of the free and immobilized enzyme were then determined. The optimum pH for both the soluble and immobilized enzyme was 4.8. The optimum temperature for the soluble enzymes was 50 degrees C, whereas that for the immobilized enzyme was 55 degrees C. The immobilized enzyme was used in batch, repeated batch, and continuous modes to degrade the raffinose-family sugars present in soymilk. Two hours of incubation with the free and immobilized alpha-galactosidases resulted in an 80% and 68% reduction in the raffinose oligosaccharides in the soymilk, respectively. In the repeated batch, a 73% reduction was obtained in the fourth cycle. A fluidized bed reactor was also designed to treat soymilk continuously and the performance of the immobilized alpha-galactosidase tested at different flow rates, resulting in a 90% reduction of raffinose-family oligosaccharides in the soymilk at a flow rate 40 ml/h. Therefore, the present study demonstrated that immobilized alpha-galactosidase in a continuous mode is efficient for reducing the oligosaccharides present in soymilk, which may be of considerable interest for industrial application.     

Purification and characterization of two alpha-galactosidases associated with catabolism of guar gum and other alpha-galactosides by Bacteroides ovatus.

When Bacteroides ovatus is grown on guar gum, a galactomannan, it produces alpha-galactosidase I which is different from alpha-galactosidase II which it produces when grown on galactose, melibiose, raffinose, or stachyose. We have purified both of these enzymes to apparent homogeneity. Both enzymes appear to be trimers and have similar pH optima (5.9 to 6.4 for alpha-galactosidase I, 6.3 to 6.5 for alpha-galactosidase II). However, alpha-galactosidase I has a pI of 5.6 and a monomeric molecular weight of 85,000, whereas alpha-galactosidase II has a pI of 6.9 and a monomeric molecular weight of 80,500. alpha-Galactosidase I has a lower affinity for melibiose, raffinose, and stachyose (Km values of 20.8, 98.1, and 8.5 mM, respectively) than does alpha-galactosidase II (Km values of 2.3, 5.9, and 0.3 mM, respectively). Neither enzyme was able to remove galactose residues from intact guar gum, but both were capable of removing galactose residues from guar gum which had been degraded into large fragments by mannanase. The increase in specific activity of alpha-galactosidase which was associated with growth on guar gum was due to an increase in the specific activity of enzyme I. Low, constitutive levels of enzyme II also were produced. By contrast, enzyme II was the only alpha-galactosidase that was detectable in bacteria which had been grown on galactose, melibiose, raffinose, or stachyose.     

Entrapment of purified novel dextransucrase obtained from newly isolated Acetobacter tropicalis and its comparative study of kinetic parameters with free enzyme

Abstract

Purified Acetobacter tropicalis dextransucrase was immobilized in different matrices viz. calcium-alginate, κ-carrageenan, agar, agarose and polyacrylamide. Calcium-alginate was proved to be superior to the other matrices for immobilization of dextransucrase enzyme. Standardization of immobilization conditions in calcium-alginate resulted in 99.5% relative activity of dextransucrase. This is the first report with such a large amount of relative activity as compared to the previous reports. The immobilized enzyme retained activity for 11 batch reactions without a decrease in activity which suggested that enzyme can be used repetitively for 11 cycles. The dextransucrase was also characterized, which revealed that enzyme worked best at pH 5.5 and 37?°C for 30?min in both the free as well as immobilized state. Calcium-alginate immobilized dextransucrase of A. tropicalis showed the K_m and V_max values of 29?mM and 5000?U/mg, respectively. Free and immobilized enzyme produced 5.7?mg/mL and 2.6?mg/mL of dextran in 2?L bench scale fermenter under optimum reaction conditions. This immobilization method is very unconventional for purified large molecular weight dextran-free dextransucrase of A. tropicalis as this method is used usually for cells. Such reports on entrapment of purified enzyme are rarely documented.     

Immobilization of glucoamylase and glucose oxidase in activated carbon: effects of particle size and immobilization conditions on enzyme activity and effectiveness

Glucoamylase and glucose oxidase have been immobilized on carbodiimide-treated activated carbon particles of various sizes. Loading data indicate nonuniform distribution of immobilized enzyme within the porous support particles. Catalysts with different enzyme loading and overall activities have been prepared by varying enzyme concentration in the immobilizing solution. Analysis of these results by a new method based entirely upon experimentally observable catalyst properties indicates that intrinsic catalytic activity is reduced by immobilization of both enzymes. Immobilized glucoamylase intrinsic activity decreases with increasing enzyme loading, and similar behavior is suggested by immobilized glucose oxidase data analysis. The overall activity data interpretation method should prove useful in other immobilized enzyme characterization research, especially in situations where the intraparticle distribution of immobilized enzyme is nonuniform and unknown.     

Immobilized horse liver alcohol dehydrogenase as an on‐line high‐performance liquid chromatographic enzyme reactor for stereoselective synthesis

Horse liver alcohol dehydrogenase (HLADH) has been non‐covalently immobilized on an immobilized artificial membrane (IAM) high‐performance liquid chromatography (HPLC) stationary phase. The resulting IAM‐HLADH retained the reductive activity of native HLADH as well as the enzyme's enantioselectivity and enantiospecificity. HLADH was also immobilized in an IAM HPLC stationary phase prepacked in a 13 × 4.1 mm ID column to create an immobilized enzyme reactor (HLADH‐IMER). The reactor was connected through a switching valve to a column containing a chiral stationary phase (CSP) based upon p‐methylphenylcarbamate derivatized cellulose (Chiralcel OJR‐CSP). The results from the combined HLADH‐IMER/CSP and chromatographic system demonstrate that the enzyme retained its activity and stereoselectivity after immobilization in the column and that the substrate and products from the enzymatic reduction could be transferred to a second column for analytical or preparative separation. The combined HLADH‐IMER/CSP system is a prototype for the preparative on‐line use of cofactor‐dependent enzymes in large‐scale chiral syntheses. Chirality 11:39–45, 1999. © 1999 Wiley‐Liss, Inc.     

Immobilized heparinase: In vitro reactor model

Heparinase immobilized to agarose has previously been shown to be useful in degrading heparin and thereby preventing thromboembolytic complications when this anticoagulant has been used in extracorporeal perfusions. The current study examined the kinetics of this immobilized enzyme. When heparinase is covalently bound to 8% agarose, the partition coefficient of heparin in the catalytic particle is 0.36 +/- 0.048 (N = 10). The immobilized enzyme has a K(m) of 0.15 +/- 0.03 mg/mL and an activation energy of 10.3 +/- 0.57 kcal/gmol (N = 5). These values are statistically indistinguishable from the values for the free enzyme. The immobilized enzyme showed a pH activity optimum between 7.0 and 7.4, compared to the optimum pH of 6.5 for the soluble enzyme. The activity optimum of immobilized heparinase with respect to salt concentration was between 0 and 0.1M. A reactor containing immobilized heparinase recirculating internally at 1300 mL/min behaved as a continuously stirred tank reactor (CSTR) when solutions at a flow rate of 120 mL/min were passed through the device. The residence time distribution was determined using blue dextran (molecular weight 2 x 10(6) daltons), which is sterically excluded from the agarose catalyst. A model of the heparinase reactor based on ideal CSTR behavior and the immobilized enzyme kinetic parameters was developed. It accurately predicted experimental conversions over a range of catalyst volumes, enzyme loadings, and substrate concentrations to within 7% in most cases and with a maximum deviation of 13%.     

Stachyose synthesis in leaves of Cucurbita pepo

An enzyme synthesizing stachyose, galactinol-raffinose galactosyltransferase (EC2.4.1.67), has been purified ca 40-fold from mature leaves of Cucurbita pepo using ammonium sulphate precipitation, Sephadex gel filtration and DEAE-Sephadex gel chromatography. The purified enzyme fraction was separated from all but 2 % of the total,α-galactosidase activity extracted from the tissue. The enzyme was optimally active at pH 6.9 and was stable for at least a month at 4° in the presence of 20 mM 2-mercaptoethanol. The enzyme displayed high specificity for the donor galactinol (K_m 7.7 mM) and the acceptor raffinose (K_m 4.6 mM) and was unable to effect synthesis of any other member of the raffinose series of galactosyl-sucrose oligosaccharides. Co²⁺, Hg²⁺, Mn²⁺ and Ni²⁺ ions were particularly inhibitory; no metal ion promotion was observed and 5 mM EDTA was ineffective. Myo-inositol was strongly inhibitory (K_i 2 mM), melibiose weakly so. Tris buffer (0. 1 M) was also inhibitory. Galactinol hydrolysis occurred in the absence of the acceptor raffinose but there was no hydrolysis of either raffinose or stachyose in the absence of the donor galactinol. The reaction was readily reversible and exchange reactions were detected between substrates and products. It is proposed that the synthesis of stachyose in mature leaves ofC. pepo proceeds via this galactosyltransferase and not via α-galactosidase.     

Polyvinylamine‐coated polyester fibers as a carrier matrix for the immobilization of peroxidases

Biocatalytic transformations that employ immobilized enzymes become increasingly important for industrial applications. Synthetic or natural textile fiber materials such as polyester, polyamide or viscose are support materials that are comparatively inexpensive. Contrary to traditional support materials, their flexibility enables their use in reactors of any geometry and a fast and residue‐free removal from batch reactors. In this study a permanently immobilized peroxidase (Baylase®) has been investigated on polyester felt as a solid support as a new heterogeneous catalyst system. The polyester felt was functionalized by coating with polyvinylamine and subsequent activation with glutaraldehyde as a crosslinking agent. The enzyme load on the textile surface, the activity of the immobilized protein after repeated use as well as the storage stability was evaluated. Scanning electron micrographs and UV Vis spectroscopy made it possible to verify the enzyme immobilization on the textile surface. Furthermore, the load of immobilized peroxidase was determined by ICP OE spectrometry to be 9–12 mg per gram of textile. The activity of immobilized Baylase® remained high over 35 reaction cycles and a storage period of 8 weeks.     

Properties of fibre-entrapped aspartase

Aspartase (l-aspartate ammonia lyase, EC 4.3.1.1) was extracted and purified from Escherichia intermedia cells. The enzyme was entrapped in cellulose triacetate porous fibres and the properties of the immobilized enzyme compared with those of the free enzyme. Similar behaviour was observed with regard to optimum pH, temperature, heat stability and kinetic constants. The stability of the entrapped enzyme was tested under operating conditions in a series of batch reactions. Good results were obtained for both the stability and the efficiency of the immobilized enzyme. The potential use of aspartase fibres for the production of l-aspartic acid is discussed.     

Silanized palygorskite for lipase immobilization

Lipase from Candida lipolytica has been immobilized on 3-aminopropyltriethoxysilane-modified palygorskite support. Scanning electron micrographs proved the covalently immobilization of C. lipolytica lipase on the palygorskite support through glutaraldehyde. Using an optimized immobilization protocol, a high activity of 3300 U/g immobilized lipase was obtained. Immobilized lipase retained activity over wider ranges of temperature and pH than those of the free enzyme. The optimum pH of the immobilized lipase was at pH 7.0–8.0, while the optimum pH of free lipase was at 7.0. The retained activity of the immobilized enzyme was improved both at lower and higher pH in comparison to the free enzyme. The immobilized enzyme retained more than 70% activity at 40 °C, while the free enzyme retained only 30% activity. The immobilization stabilized the enzyme with 81% retention of activity after 10 weeks at 30 °C whereas most of the free enzyme was inactive after a week. The immobilized enzyme retains high activity after eight cycles. The kinetic constants of the immobilized and free lipase were also determined. The K_m and V_max values of immobilized lipase were 0.0117 mg/ml and 4.51 μmol/(mg min), respectively.