Characterization of glucose oxidase immobilized on collagen

Summary The enzyme glucose oxidase (E.C. 1.1.3.4) was immobilized on collagen — a proteinaceous material found in biological systems as a structural material for a wide variety of cells and membranes. The novel technique of electrocodeposition, which utilizes the principles of electrophoresis, was used to deposit the enzyme-collagen complex on stainless steel helical supports. This technique has been developed in our laboratory. The mechanism of complex formation between collagen and enzyme involves multiple salt linkages, hydrogen bonds and van der Waals interactions.As a first step toward examining its feasible technical use, the kinetic behavior of the collagen-supported glucose oxidase was studied in a batch recycle type reactor and was compared with that for the soluble form. A novel reactor configuration consisting of multiple concentric electrocodeposited helical coils was used. The reactor was found to attain a stable level of activity which was maintained for several months under cyclic testing. The optimum levels of pH and temperature for the immobilized form of the enzyme were the same as those of the soluble enzyme, but the immobilized enzyme was more active than the soluble form at higher temperatures and pH. The values of the Michaelis-Menten parameters indicate that the overall reaction rate of the immobilized enzyme may be partially restricted by bulk and matrix diffusion.     

Studies on microbial glucose isomerase: 4. Characteristics of immobilized whole-cell glucose isomerase from Streptomyces spp.

Whole-cell glucose isomerase from a Streptomyces spp. was immobilized by entrapment in gelatin matrices crosslinked with glutaraldehyde. The resultant immobilized enzyme preparation had up to 40% recovery yield of the activity and showed relatively long stabilities during storage and the isomerizing reaction. The storage half-life of the preparation was 19 months at 5°C and the half-life of the enzyme during operation was 260 days in the presence of 1 mM Co²⁺ and 80 days in the absence of the metal ion. Optimum pH and temperature were 7.5 and 70–75°C, respectively. The K_m values for glucose and fructose were 0.29 and 0.46 m, respectively, with a maximum theoretical conversion yield of 56%. The simulation results based on the reversible one-substrate enzyme kinetic model agreed well with the experimental data obtained from a batch reactor. The continuous operation of packed bed reactors demonstrated that some effects of the external film diffusion resistance were apparent at low flow rates of the substrate feed solution, whereas the internal pore diffusion resistance was negligible up to the pellet size used in this work.     

Enzymatic modification of vegetable protein: Immobilization of Penicillium duponti enzyme on reconstituted collagen and the use of the immobilized-enzyme complex for solubilizing vegetable protein in a recycle reactor

Penicillium duponti enzyme was immobilized on reconstituted collagen by macromolecular complication, impregnation, and covalent crosslinking techniques. The immobilization of the enzyme on collagen has a twofold purpose: (1) providing a protein microenvironment for the proteolytic enzyme; and (2) extending the useful life the enzyme once immobilized on the collagen matrix. Two types of collagen were used, one produced by the United States Department of Agriculture and the other produced by FMC. The USDA collagen contained unhydrolyzed telepeptide linkages and required pretreatment to reduce collagenaselike activity of the enzyme. Activity analysis of the immobilized enzyme complex showed that membranes with enzyme loading less than 10 mg enzyme/g of wet membrane in the reactor were dimensionally stable. The degree of crosslinking was an important parameter. Membranes with structural opening up to three times the initial dry thickness were found to be the maximum limit for controlled release of enzyme from the collagen membrane during enzymatic reaction. Higher activities and better stability of the enzyme in collagen membrane were found for covalent crosslinking of the enzyme to treated collagen films. The hydrolysis of soybean vegetable protein with the immobilized enzyme in a recycle reactor at enzyme loading of mg/g of wet membrane at 40°C, pH 3.4, produced 56.5% of soluble protein in 10h. The production is equivalent to 1.84 h total contact time between the substrate and the immobilized enzyme. The average productivity based on a stable enzyme activity and 20g of dry membrane was 329 mg of protein/g/mg of active enzyme immobilized. The productivity of the free enzyme in a batch reactor was 62.5 mg protein/h/mg enzyme.     

Enzyme electrode for specific determination of L-lysine

L-Lysine alpha-oxidase from Trichoderma viride Y244-2 is immobilized in a gelatin support and fixed on a pO(2) sensor. The enzyme electrode obtained is used in a continuous flow system in order to measure the concentration of L-lysine in a fermentor. The sample oxygen-content dependance of the signal is minimized because of the enzyme support properties. The enzyme electrode response is set for lysine concentration from 0.2mM to 4mM. The specificity of lysine is tested with other amino acids. The enzyme membrane for lysine electrode can be used 3000 times or stored six months with good stability.     

Effects of immobilization on the kinetics of enzyme-catalyzed reactions. I. Glucose oxidase in a recirculation reactor system.

Glucose oxidase from Aspergillus niger was immobilized on nonporous glass beads by covalent bonding and its kinetics were studied in a packed-column recycle reactor. The optimum pH of the immobilized enzyme was the same as that of soluble enzyme; however, immobilized glucose oxidase showed a sharper pH-activity profile than that of the soluble enzyme. The kinetic behavior of immobilized glucose oxidase at optimum pH and 25 degrees C was similar to that of the soluble enzyme, but the immobilized material showed increased temperature sensitivity. Immobilized glucose oxidase showed no loss in activity on storage at 4 degrees C for nearly ten weeks. On continuous use for 60 hr, the immobilized enzyme showed about a 40% loss in activity but no change in the kinetic constant.     

Active protein and substrate flow effects in a tubular immobilized invertase reactor

Investigations of invertase (EC 3.2.1.26) immobilized inside modified nylon tubes showed that between 4% and 20% (w/w) of the protein exposed to binding sites on the tube was immobilized. An enhanced activity consistent with enzyme purification during immobilization was also evident, suggesting that, in scaled-up commercial applications, nylon tube invertase would be a more economical converter of sucrose than the free enzyme. The quantity and specific activity of the immobilized protein were not stochiometrical with the amount used in the coupling solution and, in the system studied, a concentration of 2 mg ml^?1 was optimal. K_m and V_max values confirmed higher rates of immobilized invertase catalysis when the rates of substrate flow through the reactor were higher. Higher rates of substrate flow imply a shortened residence time in the reactor and would lower the fractional conversion per pass of the substrate, reducing the efficiency of the reactor in flow-through situations. Thus, these higher catalysis rates, attributable at the higher flow rates to a reduction of the diffusion barrier between enzyme and substrate, would not translate into improved economy in the commercial flow-through processes at which the reactor is aimed.     

Immobilization of lactase from Kluyveromyces lactis greatly reduces the inhibition promoted by glucose. full hydrolysis of lactose in milk

The kinetic constants (Km, Vmax, and inhibition constants for the different products) of soluble and different immobilized preparations of beta-galactosidase from Kluyveromyces lactis were determined. For the soluble enzyme, the Km was 3.6 mM, while the competitive inhibition constant by galactose was 45 mM and the noncompetitive one by glucose was 758 mM. The immobilized preparations conserved similar values of Km and competitive inhibition, but in some instances much higher values for the noncompetitive inhibition constants were obtained. Thus, when glyoxyl or glutaraldehyde supports were used to immobilize the enzyme, the noncompetitive inhibition was greatly reduced (Ki approximately 15,000 and >40,000 mM, respectively), whereas when using sugar chains to immobilize the enzyme the behavior had an effect very similar to the soluble enzyme. These results presented a great practical relevance. While using the soluble enzyme or the enzyme immobilized via the sugar chain as biocatalysts in the hydrolysis of lactose in milk only around 90% of the substrate was hydrolyzed, by using of these the enzyme immobilized via the glyoxyl or the glutaraldehyde groups, more than 99% of the lactose in milk was hydrolyzed.     

Comparative study of immobilized and soluble NADH:FMN-oxidoreductase-luciferase coupled enzyme system

The properties of a coupled enzyme system (NAD(P)H:FMN-oxidoreductase and luciferase) from luminous bacteria were studied. The enzymes and their substrates were immobilized in polymer gels of different types: starch (polysaccharide) and gelatin (polypeptide). Maximum activity yield (100%) was achieved with the enzymes immobilized in starch gel. An increase in K _{m app} was observed in both immobilized systems as compared with the soluble coupled enzyme system. Immobilization in starch and gelatin gels increased the resistance of the NAD(P)H:FMN-oxidoreductase and luciferase coupled enzyme system to the effects of external physical and chemical factors. The optimum pH range expanded both to the acidic and alkaline regions. The resistance to concentrated salt solutions and high temperature also increased. The coupled enzyme system immobilized in starch gel (with activation energy 30 kJ/mol) was characterized by the best thermostability. The immobilized coupled enzyme system can be used to produce a stable and highly active reagent for bioluminescent analysis.     

A novel procedure for the preparation and characterization of catalytically active fatty acid synthetase immobilized on sepharose beads

A novel procedure for immobilization of enzymatically active fatty acid synthetase is presented. The enzyme is coupled to a Sepharose 4B matrix containing covalently attached antibodies which recognize, and bind specifically to, the thioesterase domain of this polyfunctional enzyme. A continuous flow system is described for assay of the immobilized enzyme. Fatty acid synthetase activity apparently is not limited by movement of substrates through the Nernst diffusion layer surrounding the matrix particles, since normal Michaelis-Menten kinetics are observed and reaction rates are independent of flow rate. The Km values for acetyl-CoA and malonyl-CoA, the pH/activity profile, and the reaction products are essentially the same as for the freely soluble enzyme, although the specific activity is lower by about 55%. The preparation and characterization of immobilized subunits of the enzyme could provide a valuable approach for studying the role of structural and functional subunit interactions in the enzyme. In addition, the immobilized enzyme offers a model for studying the properties of this enzyme in a highly structured environment such as might exist in vivo, permitting study of both physical and functional interactions of fatty acid synthetase with other lipogenic enzymes.     

Effects of fluid shear on immobilized enzyme kinetics.

There have been a number of reports concerning the damaging effects of shear on globular proteins in solution. Some recent work has indicated, however, that globular proteins in solution are relatively stable, but may be inactivated at air-liquid interfaces during shearing. This study investigated the effects of fluid shear on immobilized enzyme activity. Immobilized enzyme reactors were built to operate with the enzyme immobilized at the boundary of a fluid flow field. Two different enzymes, penicillinase and lactate dehydrogenase, were covalently bound to the interior surface of nylon tubes. Fluid shear rate was changed by varying the flow rate of substrate (reactant) solution through the tube, and fluid shear stresses were increased by increasing the viscosity of the recirculating solution. There were no observed effects of fluid shear on immobilized penicillinase or lactate dehydrogenase activity at shear rates of up to 10,350 s-1 or at shear stresses of up to 73 Pa.     

An enzyme electrode for on-line determination of ethanol and methanol

Since a stable alcohol oxidase with a high specific activity is not commercially available, we propose to produce and purify this enzyme from a strain of the yeast Hansenula polymorpha. This alcohol oxidase was immobilized into a gelatin matrix and its activity was estimated by a pO(2) sensor. The enzyme electrode obtained was then used in a continuous flow system to measure methanol or ethanol concentrations. The sample oxygen content dependence of the signal was minimized by the support properties. Measuring time for each sample were less than two minutes including response data treatment and rinsing step. The enzyme electrode response was set for ethanol from 0.5mM to 15mM and for methanol from 10mM to 300mM. On repeated use, the electrode signal for 10mM of ethanol was stable for at least 500 assays. Analysis have been performed in different beverages such as wine and beer, and the results compared to those obtained with classical methods of analysis.     

A rapid micro-assay method for gelatinolytic activity using tritium-labeled heat-denatured polymeric collagen as a substrate and its application to the detection of enzymes involved in collagen metabolism

A rapid micro-assay method for gelatinolytic activitiy has been developed using 3H-labeled heat-denatured polymeric collagen (gelatin) as a substrate to investigate enzymes involved in the post-collagenase catabolism of collagen. The method is based on the incubation of gelatin with enzyme followed by determination of the enzyme digestion products soluble in 67% dioxane. It is sensitive enough to detect microgram levels of gelatin fragments, and can be employed over wide ranges of pH and ionic strength. By applying the method to an embryonic chick skin culture system, three gelatinolytic enzyme fractions which showed high, limited and no caseinolytic activities were demonstrated to be separable by gel chromatography.     

Hydrolysis of soluble starch by rotary disc of immobilized glucoamylase

Immobilized glucoamylase sheet was prepared using soluble collagen prepared from cow hide powder as the support material. The immobilized glucoamylase sheet was attached to the rotary disc and the rates of hydrolysis of maltose and soluble starch in the tank were measured. Qualitative discussions are made of the effect of stirring speed of immobilized enzyme disc on the overall reaction rate.     

Purification and characterization of tadpole back-skin collagenase with low gelatinase activity

A collagenase secreted by tadpole (Rana catesbiana) back-skin explants in culture has been purified to electrophoretic homogeneity by successive chromatography on sulfopropyl Sephadex, Sephacryl S-200, collagen Sepharose, and heparin Sepharose. The purified enzyme has a molecular weight of approximately 49,000 and an isoelectric pH of 5.0. The enzyme is more active versus soluble collagen than reconstituted fibrils and exhibits very low activity against gelatin (specific activities: Type I collagen, 7660 units/mg; Type I gelatin, 66 units/mg). The collagenase obeys simple Michaelis-Menten kinetics using soluble type I collagen (Km), 0.35 microM; Vm, 1380 units/mg, at 25 degrees C and pH 7.4) and is inhibitable by chelating agents specific for transition metals. Methylene blue catalyzes the photoinactivation of this collagenase, suggesting the presence of essential histidine, tryptophan, tyrosine, or methionine residues.     

Thrombospondin interactions with fibronectin and fibrinogen. Mutual inhibition in binding

Thrombospondin synthesized and secreted by human endothelial cells in culture binds specifically to fibronectin immobilized on Sepharose beads. It can also bind to immobilized platelet-derived thrombospondin but not to immobilized gelatin or albumin. These interactions are not dependent on the presence of divalent cations or of other secreted materials. Purified platelet thrombospondin binds to fibronectin and fibrinogen immobilized on plastic surfaces with dissociation constants of 1.12 +/- 0.37 X 10(-7) M and 1.27 +/- 0.41 X 10(-7) M respectively, and to thrombospondin immobilized on plastic with dissociation constant of 4.82 +/- 1.01 X 10(-7) M. The affinities of interaction are not significantly affected by removal of divalent cations. Soluble fibrinogen inhibits binding of thrombospondin to fibronectin regardless of which of the latter two is surface-bound. Thrombospondin-fibronectin interaction is also inhibited by soluble thrombospondin. The binding of soluble thrombospondin to surface-bound fibrinogen is inhibited both by soluble fibronectin and soluble fibrinogen. These results suggest that thrombospondin plays a role both in platelet-platelet aggregation and in platelet-substratum adhesion, and that it may also take part in the construction of the extracellular matrix.     

Effect of pore diffusion limitation on dextrin hydrolysis by immobilized glucoamylase

Data reported here and previously indicate that when dextrin is hydrolyzed in the presence of immobilized glucoamylase, use of a larger average molecular weight substrate leads to lower overall rates of hydrolysis, while the maltose concentration during the bulk of the reaction and the maximum glucose concentration are lower than when the soluble form of the enzyme is employed under the same conditions. Computer simulation of the system demonstrated that all three observations were caused by pore diffusion limitation: the first by slow diffusion of substrate, the second by slow diffusion of intermediates, and the third by slow diffusion of glucose. Follow-up experiments with glucoamylase immobilized to particles of different sizes confirmed this finding, as results with the smallest beads were identical to those with soluble glucoamylase.     

Physico-Chemical Characterization of Watermelon Urease upon Immobilization in Alginate Beads

Watermelon (Citrullus vulgaris) urease was immobilized in 3.5% alginate leading to 72% immobilization. There was no leaching of the enzyme over a period of 15 days at 4°C. It continued to hydrolyse urea at a faster rate upto 90 min of incubation. The immobilized urease exhibited a shift of apparent pH optimum by one unit towards acidic side (from pH 8.0 to 7.0). The K_m was found to be 13.3 mM; 1.17 times higher than the soluble enzyme (11.4 mM). The beads were fairly stable upto 50°C and exhibited activity even at ?10°C. The enzyme was significantly activated by ME and it exhibited two peaks of activation; one at lower concentration and another at higher concentration. Time-dependent ureolysis in presence of ME progressed at a much elevated rate. Unlike soluble enzyme, which was inhibited at 200 mM urea, the immobilized enzyme was inhibited at 600 mM of urea and above, and about 47% activity was retained at 2000 mM urea. Moreover, the inhibition caused by high urea concentration was partially abolished by ME. The significance of the observations is discussed.     

Synthesis and degradation of collagens in skin of healthy and protein-malnourished rats in vivo, studied by 18O2 labelling.

To explore the effects of growth retardation, caused by restricted protein intake, on collagen turnover in the whole skin, Sprague-Dawley rats (n = 20) were labelled with 18O2 and fed on either an adequate (18%) or a low (3%) lactalbumin diet. Skin biopsies were obtained at intervals during the following 6 months. Independent groups of animals (n = 186) were used to determine the size of the 0.5 M-acetic acid-soluble and -insoluble collagen pools in the entire skin of healthy and malnourished rats. Collagen was estimated by measurement of hydroxyproline. Soluble-collagen synthesis rates were equivalent to 99 +/- 8 mumol of hydroxyproline/day in healthy animals and 11 +/- 2 mumol/day in malnourished rats. Insoluble-collagen synthesis rates were 32 and 5 mumol of hydroxyproline/day in the healthy and protein-depleted rats respectively. The degradation of soluble collagen amounted to 37 +/- 8 and 6 +/- 2 mumol of hydroxyproline/day in the healthy and malnourished groups respectively. Efflux of collagen from the soluble collagen, defined as the sum of the rate of soluble collagen that is degraded plus that which matures into insoluble collagen, was 70 +/- 8 and 11 +/- 2 mumol of hydroxyproline/day in the healthy and malnourished groups respectively. Insoluble collagen was not degraded in either group. The fraction of soluble collagen leaving the pool that was converted into insoluble collagen was 0.46 in both diet groups. It is concluded that the turnover of soluble collagen is markedly decreased with malnutrition, but degradation and conversion into insoluble collagen account for the same proportions of efflux from the soluble-collagen pool as in rapidly growing rats.     

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.     

Immobilization of β-galactosidase from Kluyveromyces lactis on silica and agarose: comparison of different methods

The covalent immobilization of β-galactosidase from Kluyveromyces lactis (β-gal) on to two different porous carriers, CPC-silica and agarose, is reported. CPC-silica was silanizated and activated with glutaraldehyde. The activation of agarose via a cyanylating agent (CDAP) was optimized. Gel-bound protein and gel-bound activity were both measured directly, allowing the determination of apparent specific activities (S.A.). Higher amounts of β-gal were immobilized on the activated CPC-silica (maximum capacity, 23 mg ml⁻¹ of packed support) than on the CDAP-activated agarose. For the lower enzyme loading assayed (12.6 mg ml⁻¹ packed support), 100% of the enzyme was immobilized but only 34% of its activity was expressed. This inactivation during immobilization was confirmed by the S.A. values (22–29 EU mg⁻¹ for the CPC-derivatives and 80 EU mg⁻¹ for soluble β-gal). The K_app (3.4 mM) for the CDAP-derivative with ONPG as substrate was higher than the K_M value for soluble β-gal (2 mM). When the enzyme loading was increased five-fold, the K_app increased four-fold, to 13 mM. The V_app values for the CPC-derivatives were remarkably lower than the V_max for soluble β-galactosidase. CDAP-derivatives showed better thermal stabilities than CPC-derivatives but neither of them enhanced the stability of the soluble enzyme. When stored at 4°C, the activity of both derivatives remained stable for at least 2 months. Both derivatives displayed high percentages of lactose conversion (90%) in packed bed mini-reactors. Glucose production was 3.3-fold higher for the CPC-derivative than for the CDAP-derivative, as a consequence of the higher flow rates achieved.