The addition of Co2+ enhances the catalytic efficiency and thermostability of recombinant glucose isomerase from Thermobifida fusca

Glucose isomerase is an important industrial enzyme that catalyzes the reversible isomerization of glucose to fructose. In this study, the effect of cobalt ions (Co²⁺) on the catalytic efficiency and thermostability of recombinant glucose isomerase from Thermobifida fusca was analyzed. The activity of glucose isomerase from engineered Escherichia coli supplemented with 1 mM Co²⁺ (C-GI) reached 41 U/ml, 2.1-fold higher than enzyme prepared from E. coli without additive (GI). The purified C-GI also exhibited an increased specific activity (23.8 U/mg compared to 12.1 U/mg for GI) and a greater thermostability (half-life of 17 h at 75 °C, 11.3-fold higher than GI (1.5 h)). The optimal temperature for C-GI shifted from 80 °C to 85 °C and demonstrated higher activity over pH 7.0–9.0. The k_cat/K_m value of C-GI (89.3 M^?1 s^?1) for the isomerization of glucose to fructose was nearly 1.75-fold higher than that of GI. In addition, the engineered cells were immobilized with the method of flocculation-cross linking. The immobilized cells supplemented with 1 mM Co²⁺ (C-IGI) had a better operational performance than cells without additives (IGI); at the end of 6 cycles, the conversion rate of C-IGI was still 43.1%, meeting the conversion rate requirement.     

Immobilization of glucose isomerase

The immobilization of glucose isomerase (D-xylose ketol isomerase, EC 5.3.1.5) by covalently bonding to various carriers and by adsorption to ion exchange resins was attempted in order to obtain a stable immobilized enzyme which can be used for continuous isomerization of glucose in a column. Of the covalent bonding methods, the colloidal silica-glutaraldehyde method showed the highest binding capacity and gave the most stable immobilized glucose isomerase. The Ludox HS-30 bound glucose isomerase column showed a half-life of 24 days and an enzyme usage of 0.07 units per gram of isomerized sugar (d.s, fructose 45%). Of the resins used, the macromolecular type or porous type strongly basic anion exchange resins showed the highest binding capacity and gave the most stable immobilized glucose isomerase. The Amberlite IRA-904 resine-bound glucose isomerase showed a half-life of 23 days and an enzyme usage of 0.06 units per gram of isomerized sugar (d.s., fructose 45%). Based on the ease of the immobilization process, the possibility of carrier reuse and the extensive use already achieved by ion exchange resins in the sugar industry, IRA-904 resin was selected as the candidate for commercialization.     

Production of l-rhamnulose,a rare sugar,from l-rhamnose using commercial immobilized glucose isomerase

Abstract

A commercial immobilized d-glucose isomerase from Streptomyces murines (Sweetzyme) was used to produce l-rhamnulose from l-rhamnose in a packed-bed reactor. The optimal conditions for l-rhamnulose production from l-rhamnose were determined as pH 8.0, 60?°C, 300?g L^?1 l-rhamnose as a substrate, and 0.6?h^?1 dilution rate. The half-life of the immobilized enzyme at 60?°C was 809?h. Under the optimal conditions, the immobilized enzyme produced an average of 135?g L^?1 l-rhamnulose from 300?g L^?1 l-rhamnose after 16 days at pH 8.0, 60?°C, and 0.6?h^?1 dilution rate, with a productivity of 81?g/L/h and a conversion yield of 45% in a packed-bed reactor.     

Heterologous expression and biochemical characterization of glucose isomerase from Thermobifida fusca

Glucose isomerase (GIase) catalyzes the isomerization of d-glucose to d-fructose. The GIase from Thermobifida fusca WSH03-11 was expressed in Escherichia coli BL21(DE3), and the purified enzyme took the form of a tetramer in solution and displayed a pI value of 5.05. The temperature optimum of GIase was 80 °C and its half life was about 2 h at 80 °C or 15 h at 70 °C. The pH optimum of GIase was 10 and the enzyme retained 95 % activity over the pH range of 5–10 after incubating at 4 °C for 24 h. Kinetic studies showed that the K _m and K _cat values of the enzyme are 197 mM and 1,688 min^?1, respectively. The maximum conversion yield of glucose (45 %, w/v) to fructose of the enzyme was 53 % at pH 7.5 and 70 °C. The present study provides the basis for the industrial application of recombinant T. fusca GIase in the production of high fructose syrup.     

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.     

Immobilized glucose oxidase on different supports for biotransformation removal of glucose from oligosaccharide mixtures

Four immobilized forms of glucose oxidase (GOD) were used for biotransformation removal of glucose from its mixture with dextran oligosaccharides. GOD was biospecifically bound to Concanavalin A-bead cellulose (GOD-ConA-TBC) and covalently to triazine-bead cellulose (GOD-TBC). Eupergit C and Eupergit CM were used for preparation of other two forms of immobilized GOD: GOD-EupC and GOD-EupCM. GOD-ConA-TBC and GOD-EupC exhibited the best operational and storage stabilities. pH and temperature optima of these two immobilized enzyme forms were broadened and shifted to higher values (pH 7 and 35 °C) in comparison with those of free GOD. The decrease of V_max values after immobilization was observed, from 256.8 ± 7.0 μmol min⁻¹ mg_GOD⁻¹ for free enzyme to 63.8 ± 4.2 μmol min⁻¹ mg_GOD⁻¹ for GOD-ConA-TBC and 45 ± 2.7 μmol min⁻¹ mg_GOD⁻¹ for GOD-EupC, respectively. Depending on the immobilization mode, the immobilized GODs were able to decrease the glucose content in solution to 3.8–15.6% of its initial amount The best glucose conversion, was achieved by an action of GOD-EupCM on a mixture of 100 g dextran with 9 g of glucose (i.e. 98.7% removal of glucose).     

Immobilized glucose dehydrogenase for cofactor regeneration in heme-catalyzed demethylation and hydroxylation reactions

Glucose dehydrogenase (E.C. 1.1.1.47) from B. megaterium M 1286 was immobilized together with mutarotase (E.C. 5.1.3.3) on several organic carriers and by different methods. The storage stability of the enzyme at pH-values > 6 is slightly improved by immobilization and the pH-optimum is shifted from 8.3 to 8.0. Kinetic constants of the immobilized enzyme are: K′_M(NAD⁺) = 5.36 × 10^?4 mol/l K′_M(glucose) = 3.76 · 10^?2 mol/l and V′_max = 5.54 · 10^?5 mol/(l min g carrier) for the most active preparation (2.16 mg enzyme/g carrier). In reactor experiments the immobilized glucose dehydrogenase was used with glucose to regenerate NADPH in NADPH-dependent iron-III-protoporphyrin-IX-imidazole catalyzed hydroxylation and demethylation of model substrates of cytochrome P-450. The advantages of the coupling of both reactions with cofactor recycling are shown and discussed.     

Purification, immobilization and characterization of linoleic acid isomerase on modified palygorskite

Linoleic acid isomerase from Lactobacillus delbrueckii subsp. bulgaricus 1.1480 was purified by DEAE ion-exchange chromatography and gel filtration chromatography. An overall 5.1% yield and purification of 93-fold were obtained. The molecular weight of the purified protein was ~41 kDa which was analyzed by SDS-PAGE. The purified enzyme was immobilized on palygorskite modified with 3-aminopropyltriethoxysilane. The immobilized enzyme showed an activity of 82 U/g. The optimal temperature and pH for the activity of the free enzyme were 30 °C and pH 6.5, respectively; whereas those for the immobilized enzyme were 35 °C and pH 7.0, respectively. The immobilized enzyme was more stable than the free enzyme at 30–60 °C, and the operational stability result showed that more than 85% of its initial activity was retained after incubation for 3 h. The K _m and V _max values of the immobilized enzyme were found to be 0.0619 mmol l⁻¹ and 0.147 mmol h⁻¹ mg⁻¹, respectively. The immobilized enzyme had high operational stability and retained high enzymatic activity after seven cycles of reuse at 37 °C.     

Immobilization of β-amylase on polystyrene cation exchange resin equilibrated with Al3+ions (IR-120 Al3+)

A simple procedure for the immobilization of β-amylase (EC3.2.1.2) on IR-120 Al³⁺ is described. Immobilization brought about a slight shift in the optimum pH towards the alkaline side relative to that of the soluble enzyme. Immobilized β-amylase showed a broader temperature optima (45–55°C) compared with the soluble enzyme (45°C). A six-fold increase in the K_m was also noticed. On storage and repeated use the immobilized enzyme retained approximately 60% of its initial activity up to 120 days at room temperature.     

Immobilization of Kluyveromyces marxianus cells containing inulinase activity in open pore gelatin matrix: 1. Preparation and enzymatic properties

Kluyveromyces marxianus cells with inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7) activity have been immobilized in open pore gelatin pellets with retention of > 90% of the original activity. The open pore gelatin pellets with entrapped yeast cells were obtained by selective leaching out of calcium alginate from the composite matrix, followed by crosslinking with glutaraldehyde. Enzymatic properties of the gelatin-entrapped cells were studied and compared with those of the free cells. The immobilization procedure did not alter the optimum pH of the enzymatic preparation; the optimum for both free and immobilized cells was pH 6.0. The optimum temperature of inulin hydrolysis was 10°C higher for immobilized cells. Activation energies for the reaction with the free and immobilized cells were calculated to be 6.35 and 2.26 kcal mol^?1, respectively. K_m values were 8 mM inulin for the free cells and 9.52 mM for the immobilized cells. The thermal stability of the enzyme was improved by immobilization. Free and immobilized cells showed fairly stable activities between pH 4 and 7, but free cell inulinase was more labile at pH values below 4 and above 7 compared to the immobilized form. There was no loss of enzyme activity of the immobilized cells on storage at 4°C for 30 days. Over the same period at room temperature only 6% of the original activity was lost.     

Immobilization of glucose isomerase to ion-exchange materials

Glucose isomerase (D -xylose ketol-isomerase EC 5.3.1.5) from Bacillus Coagulans was partially purified and immobilized by adsorption to anion exchangers. The highest activities were obtained when the enzyme was adsorbed to DEAE-cellulose. On immobilization to DEAE-cellulose the measured optimum pH value for enzyme activity shifted from 7.2 to 6.8. There was no appreciable difference between the heat stabilities of soluble and immobilized enzyme. The K_{m app} values for the immobilized enzyme were found to be 0.25M in the presence of 0.01M Mg²⁺ and 0.19M with 0.005M Mg²⁺, while those enzyme were 0.11 and 0.17M, re spectively. Under conditions of contimuous of D -glucose, a decrease of activity with time was observed, but this decrease was less at a low Mg²⁺ concentration and was affected by column geometry. There were no appreciable diffusional limitation effects in packed-bed columns.     

Immobilized xanthine oxidase: Kinetics, (in)stability,and stabilization by coimmobilization with superoxide dismutase and catalase

Milk xanthine oxidase was immobilized by covalent attachment to CNBr-activated Sepharose 4B and by adsorption to n-octylamine-substituted Sepharose 4B. The amounts of activity immobilized for the two preparations were 30 and 90%, respectively. The pH optima for free and adsorbed xanthine oxidase were at 8.6 and 8.2, respectively. Both free and immobilized xanthine oxidase show substrate inhibition. The apparent inhibition constant (K_i′) found for adsorbed xanthine oxidase with xanthine as substrate was higher than the K_i for the free enzyme, which was shown to be due to substrate diffusion limitation in the pores of the carrier beads (internal diffusion limitation). Higher substrate concentrations, as desirable for practical application in organic synthesis, can therefore be used with the immobilized enzyme without decreasing the rate. As a result of the internal diffusion limitation the apparent Michaelis constant (K_m′) for adsorbed xanthine oxidase was also higher than the K_m for the free enzyme. Immobilized xanthine oxidase was more stable than the free enzyme during storage at 4 and 30°C. Both forms rapidly lost activity during catalysis. The loss was proportional to the amount of substrate converted. Coimmobilization of xanthine oxidase with superoxide dismutase and catalase improved the operational stability, suggesting that O₂^? and H₂O₂ side-products of the enzymatic reaction were involved in the inactivation. Coimmobilization with albumin also had some stabilizing effect. Complete surrounding of xanthine oxidase by protein, however, by means of etrapment in a glutaraldehyde-crosslinked gelatin matrix, considerably enhanced the operational half-life. This system was less efficient than the Sepharose preparations either because much activity was lost during the immobilization procedure and/or because it had poor flow properties. Xanthine (15 mg)was converted by an adsorbed xanthine oxidase preparation and product (uric acid) was isolated in high yield (84%).     

Isomerization of glucose to fructose: production and some properties of glucose isomerase from Streptomyces sp. strain C7

Nine strains of actinomycetes isolated from Iraqi soils were investigated for glucose isomerase production. Only one strain, Streptomyces sp., C₇, was active. The maximum conversion ratio of the enzyme for the cells grown in d-xylose medium after 24 h incubation at 70°C and pH 6.9, was 64 and 48% for crude extract and cell-bound enzyme, respectively. The optimum pH value and temperatures for both enzymes were 8.0 and 70°C.     

Stability evaluation of 6-phosphogluconate dehydrogenase immobilized on amino-functionalized magnetic nanoparticles

Abstract

In this study, 6-phosphogluconate dehydrogenase was covalently immobilized onto the N-2-aminoethyl-3-aminopropyltriethoxysilane (APTES) modified core-shell Fe₃O₄@SiO₂ magnetic nanoparticles (ASMNPs) using glutaraldehyde (GA). Immobilization of 6PGDH on ASMNPs was confirmed using fourier transform-infrared spectroscopy (FT-IR) and scanning electron microscopy (SEM) analysis. The NADP⁺ conversion ratio, the reusability, thermal, and storage stability of the immobilized 6PGDH were determined and compared with those of the free enzyme. The maximum retention of enzyme activity reached to 96% when the enzyme was immobilized on ASMNPs activated with monomer form of GA. Although the thermal stability of free and immobilized enzymes was similar, at 30?°C, the immobilized 6PGDH showed the improved thermal stability at 40?°C and 50?°C compared with free 6PGDH. While the free 6PGDH only converted 33% of NADP⁺ in reaction medium upon 480?s, the immobilized 6PGDH performed 56% conversion of NADP⁺ at same time. The immobilized 6PGDH retained 62% of its initial activity up to the fifth cycle and 35% of its initial activity after 22?days of storage at 4?°C.     

Immobilization of apricot pectinesterase (Prunus armeniaca L.) on porous glass beads and its characterization

Pectinesterase isolated from Malatya apricot pulp was covalently immobilized onto glutaraldehyde-containing amino group functionalized porous glass beads surface by chemical immobilization at pH 8.0. The amount of covalently bound apricot PE was found 1.721 mg/g glass support. The properties of immobilized enzyme were investigated and compared to those of free enzyme. The effect of various parameters such as pH, temperature, activation energy, heat and storage stability on immobilized enzyme were investigated. Optimum pH and temperature were determined to be 8.0 and 50 °C, respectively. The immobilized PE exhibited better thermostability than the free one. Kinetic parameters of the immobilized enzyme (K_m and V_max values) were also evaluated. The K_m was 0.71 mM and the V_max was 0.64 μmol min^?1 mg^?1. No drastic change was observed in the K_m and V_max values. The patterns of heat stability indicated that the immobilization process tends to stabilize the enzyme. Thermal and storage stability experiments were also carried out. It was observed that the immobilized enzyme had longer storage stability and retained 50% of its initial activity during 30 days.     

Optimization of operating temperature for continuous glucose isomerase reactor system

The Optimal temperature control policy for an immobilized glucose isomerase reactor system was studied. This optimization study takes into consideration the enzyme deactivation during the continuous reactor operation. The Kinetic parameters including reduced Michaelis–Menten constant (K?_m), reduced maximum reaction rate (V?_m), equilibrium constant (K_e), and enzyme deactivation constant (k_d) and their functional relationships to temperature were determined experimentally. The optimization problem was formulated in terms of maximization of fructose productivity as the objective function. The optimization problem was solved by making use of a maximum principle and the control vector iteration method. Approximately optimal temperature control policy was employed as compared with the reactor operation at an optimum constant temperature.     

Properties and applications of immobilized snake venom NAD glycohydrolase

The NAD glycohydrolase (NADase) from Bungarus fasciatus snake venom was adsorbed on concanavalin A-Sepharose, and demonstrated to retain both hydrolase and transglycosidase activities in the bound form. The matrix-bound enzyme was stable to repeated washing with buffer and storage at 4°C. The bound enzyme exhibited the same K_m value for hydrolysis of nicotinamide-1,N⁶-ethenoadenine dinucleotide as previously measured with the soluble, purified form of the enzyme. The bound NADase was used repeatedly for a preparative-scale synthesis of 3-acetylpyridine adenine dinucleotide. It was further demonstrated that the immobilized enzyme could be prepared directly from crude snake venom, thus avoiding the time required for purification. The application of the immobilized snake venom NADase for the preparation of pyridine nucleotide coenzyme analogs has many advantages over procedures used previously for analog synthesis.     

Cloning of <Emphasis Type="Italic">Escherichia coli</Emphasis> K12 xylose isomerase (glucose isomerase) gene and studying the enzymatic properties of its expression product

The coding region of Escherichia coli K12 xylose (glucose) isomerase gene was inserted into the pRAC expression vector and cloned in E. coli BL21(DE3) cells. After induction of expression of the cloned gene, the proportion of recombinant xylose isomerase accounted for 40% of the total protein content. As a result of one-stage purification by affinity chromatography, a protein preparation of 90% purity was obtained. The recombinant enzyme catalyzed the isomerization of glucose to fructose and exhibited maximum activity (0.8 U/mg) at 45°C and pH 6.8. The enzyme required Mg²⁺ ions as a cofactor. When Mg²⁺ and Co²⁺ ions were simultaneously present in the reaction medium, the enzyme activity increased by 15–20%. Complete replacement of Mg²⁺ with Co²⁺ decreased the enzyme activity. In the presence of Ca²⁺ at concentrations comparable to the concentration of Mg²⁺, the enzyme was not inhibited, although published data reported inhibition of similar enzymes by Ca²⁺. The recombinant enzyme exhibited a very low thermostability: it underwent a slow inactivation when incubated at 45°C and was completely inactivated after incubation at 65°C for 1 h.     

Continuous production of l-phenylalanine from acetamidocinnamic acid using co-immobilized cells of Corynebacterium sp. and Paracoccus denitrificans

In order to produce l-phenylalanine efficiently from acetamidocinnamic acid with immobilized microbial cells, a two-step enzyme reaction using the acetamidocinnamate amidohydrolase activity of Corynebacterium sp. C-23 cells and the aminotransferase activity of Paracoccus denitrificans pFPr-1 cells was investigated. It was found that the useage of co-immobilized Corynebacterium sp. and P. denitrificans cells with κ-carrageenan was superior to that of the mixture of immobilized Corynebacterium sp. cells and immobilized P. denitrificans cells. When the space velocity was 0.06 h⁻¹ at 30°C, 147 mml-phenylalanine were produced with a 98% conversion ratio from acetamidocinnamic acid. The half-life of the l-phenylalanine-forming activity of the column was calculated to be ≈ 14 days at 30°C.     

Catalytic properties of d-xylose isomerase from Streptomyces violaceoruber

The catalytic properties and stability of d-xylose isomerase from Streptomyces violaceoruber have been studied. The enzyme was activated by Mg²⁺, Co²⁺ and Mn²⁺ but Ni²⁺, Ca²⁺, Zn²⁺, Cu²⁺ and Hg were ineffective. Optimum catalytic conditions were obtained at 80°C in the pH range 7.5–9.5 and in the presence of 10 mm Mg²⁺. The specific activity of the enzyme increased after treatment with 10 mm EDTA (factor 2.4). A further increase of activity (factor 2.0–2.8) was observed after preincubation of the enzyme with Mg²⁺ or Co²⁺, the preincubation time depending on the incubation temperature. The thermal stability of the enzyme is very high. At 60°C the enzyme retained optimum activity following 30 days of storage in the presence of 1 mm Co²⁺ or 10 mm Mg²⁺. At 80°C, Co²⁺ is superior as a protector against thermal denaturation. At saturating concentrations of Mg²⁺ (35°C) the K_m-values of the EDTA-treated enzyme with respect to d-xylose and d-glucose were 2.8 and 149 mm and the dissociation constants of the enzyme-Mg²⁺ complex for xylitol and d-sorbitol were 0.455 and 4.47 mm, respectively.