Properties and repeated use of a reversibly soluble-insoluble yeast lytic enzyme

Summary A yeast lytic enzyme was covalently immobilized on an enteric coating polymer, Eudragit S, that is reversibly soluble and insoluble (S-IS) depending on the pH of the reaction medium. The yeast lytic enzyme immobilized on Eudragit S (Y-E) showed a sharp response of solubility to slight changes in pH without decrease in enzymatic activity. The specific activity per amount of enzyme protein of Y-E for dry yeast cells was about two-thirds that of the native enzyme. In both lysis reactions of dry and pressed baker's yeast cells, changing the pH of the reaction medium from 7.0 to 4.8 at an appropriate interval allows the insoluble Y-E and the reaction products (soluble protein for dry yeast cells and invertase and soluble protein for pressed baker's yeast cells) to be repeatedly separated. The reaction method using a reversible S-IS enzyme is a promising procedure for repeated use of the enzyme in a heterogeneous reaction system containing yeast cells as a substrate.     

Kinetcs and decay of fumarase activity of immobilized Brevibacterium ammoniagenes cells for continuous production of L-malic acid

The kinetics of the reversible fumarase reaction of immobilized Brevibacterium ammoniagenes cells and the decay behavior of enzyme activity were investigated in a plug flow system. The time course of the reaction in the immobilized cell column was well explained by the time-conversion equation including the apparent kinetic constants of the immobilized cell enzyme. The decay rate of fumarase activity was faster in the upper sections of the column (inlet side of the substrate solution) compared with the lower sections when 1M sodium fumarate (pH 7.0) was continuously passed through the column at 37°C. It was shown that the decay rate of the fumarase activity in the immobilized cell column depends on the flow rate of the substrate solution. The effect of flow rate on the decay rate of enzyme activity was considered to be related to the rate of contamination of enzyme with poisonous substances derived from the substrate solution or to the rate of leakage of enzyme stabilizers and/or enzyme itself from the immobilized cells.     

The properties of invertase,covalently immobilized at activated carbon

The covalent immobilization of yeast invertase with glutaraldehyde at activated carbon, modified preliminarily by urea and dimethyl formamide treatment, has been established. Some physicochemical properties of the immobilized and native enzyme in water and water-organic solutions have been studied. Hydrolytic, as well as transferase enzyme characteristics have changed after immobilization. The optimal conditions for hydrolytic and transferase activity of immobilized invertase are pH 6.0 and 7.0, respectively. The optimum temperature for the immobilized enzyme is 30°C. The conversion degree of isoamyl alcohol depends on the substrate and enzyme concentrations in medium, holdup time and organic phase quantity in the reaction medium.     

纳米磁性壳聚糖微球固定化酵母醇脱氢酶的研究

建立了以纳米级磁性壳聚糖微球(magnetic chitosan microspheres , M-CS)为载体固定化酵母醇脱氢酶(yeast alcohol dehydrogenase,YADH)的方法,优化了YADH的固定化条件,考察了固定化酶的性质。结果表明,M-CS 呈规则的圆球形,粒径在30nm 左右,具有较好的磁响应性。酵母醇脱氢酶固定化适宜条件为:50 mg 磁性壳聚糖微球,加入20mL 0.25 mg/mL 酵母醇脱氢酶(蛋白质含量)磷酸盐缓冲液(0.05 mol/L ,pH 7.0) ,在4 ℃固定2h。M-CS 容易吸附酵母醇脱氢酶,但吸附的酶量受载体与酶的比例、溶液的离子浓度、溶液pH的影响明显,而温度对吸附的酶量的影响则相对较弱。相对于游离的酵母醇脱氢酶,固定化酶的最适温度略有升高,可明显改善其热稳定性、酸碱稳定性、操作稳定性和贮存稳定性。     

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.     

固定化嗜热脂肪芽孢杆菌连续合成半乳糖寡糖的研究

利用固定了产β-半乳糖苷酶的嗜热脂肪芽孢杆菌,以乳糖为底物,在纤维床反应器中连续合成半乳糖寡糖(GOS),最高得率为50.7%。在连续反应体系中,研究了底物浓度、pH、反应温度和停留时间对半乳糖寡糖合成的影响,确定最佳反应条件为底物浓度450 g/L、反应温度55℃、pH7.0、停留时间100 min。在连续反应24h后,流加1.5%的D-半乳糖能提高合成GOS的能力,固定化细胞反应体系中连续稳定操作120 h。     

Some properties of a papain–agarose reactor provided with a pH monitor

A small reactor of immobilized papain was used to gain some knowledge about the effect of immobilization upon the reactivity of the enzyme towards one substrate and various types of inhibitors. A buffer solution containing benzoyl–arginine ethyl ester as substrate was run through a small column of papain immobilized by attachment to agarose beads. The pH of the effluent was measured continuously and provided the data used to calculate the substrate conversion during passage through the reactor. The operation of the system was checked by determining the substrate conversion as a function of flow rate. It proved to operate as theory demanded. The rate and extent of inhibition were measured after addition of various inhibitors to the buffer–substrate solution. The following quantities of immobilized papain were found to be equal within ±20% to those of the free enzyme in solution: the overall activity, the K_m of benzoyl–arginine ethyl ester, the K_i of the competitive inhibitor benzoylamino-acetonitrile, the rate of inactivation by chloroacetic acid and by chloroacetamide, the rate of activation by cysteine of the mixed disulfide of papain and cysteine, and the rate of spontaneous reactivation of the KCNO–papain adduct. The inactivation by KCNO proved to be strongly pH dependent. This may explain why the rate of the latter reaction is only 66% of the rate with free enzyme. It is concluded that the rates and equilibrium constants measured in the present reactor system are within ±20% of the values of the dissolved enzyme, provided that the reactions are not strongly pH dependent. Calculation showed there was no diffusion limitation.     

Flow analysis for determination of paraoxon with use of immobilized acetylcholinesterase reactor and new type of chemiluminescent reaction

A highly sensitive flow analysis method for determination of acetylcholinesterase (AChE) inhibitors like organophosphorous pesticides using a new chemiluminescent reaction was developed and optimized. This method is fast, sensitive, and cheap, because it requires only one enzyme and its substrate. The system incorporates a reactor with immobilized AChE on controlled pore glass (CPG) and a chemiluminometric detector. Variations in enzyme activity due to inhibition are measured from the changes of concentrations of thiocholine produced when the substrate (acetylthiocholine chloride) is pumped before and after the passage of the solution containing the pesticide through the immobilized AChE reactor. Thiocholine is determined by a new chemiluminescent reaction with luminol in the presence of potassium ferricyanide. The percentage inhibition of enzyme activity is correlated to the pesticide concentration. The inhibited enzyme is reactivated by 10 mM pyridine-2-aldoxime methiodide (2-PAM). The experimental conditions were first optimized for activity determination of the effect of pH, flow rates, and Tris concentrations. For the measurement of AChE inhibition, the appropriate concentration of the substrate is selected such that the rate of noninhibited reaction can be considered unchanged and could be used as a reference. For optimization of experimental conditions for inhibition, several parameters of the system are studied and discussed: flow rate, enzyme-pesticide contact time, luminol concentration, ferricyanide concentration, 2-PAM concentration, and configuration of the FIA manifold. Paraoxon, an organophosphorous pesticide was tested. For an inhibition time of 10 min the calibration graph is linear from 0.1 to 1 ppm paraoxon with a relative standard deviation (n = 5) of 4.6% at 0.5 ppm. For an inhibition time of 30 min the calibration graph is linear from 25 to 250 ppb paraoxon.     

The preparation and characterization of an immobilized l-glutamic decarboxylase and its application for determination of l-glutamic acid

This paper is to study the preparation and characterization of an immobilized L-glutamic decarboxylase (GDC) and develop a sensitive method for the determination of L-glutamate using a new biosensor, which consists of an enzyme column reactor of GDC immobilized on a novel ion exchange resin (carboxymethyl-copolymer of allyl dextran and N.N'-methylene-bisacrylamide CM-CADB) and ion analyzer coupled with a CO(2) electrode. The conditions for the enzyme immobilization were optimized by the parameters: buffer composition and concentration, adsorption equilibration time, amount of enzyme, temperature, ionic strength and pH. The dynamic response of Na(2)HPO(4)-citric acid buffer system selected is much better than that of the others, 0.10 M HAc-0.10 M NaAc and 0.10 M sodium citrate-0.10 M citric acid. The initial rate of the enzyme reaction v(0) in this buffer system is 1.76 mol. l(-1) min(-1), moreover, the rate of the enzyme reaction appears linear in the first 4 min. The optimum adsorption equilibrium time is around 6 h. The amount of enzyme adsorbed on CM-CADB resin affects the response to substrate L-glutamic acid, the widest range of linearity is obtained with over 30 mg (GDC)/g(resin). The GDC activity immobilized on CM-CADB reaches a maximum when the immobilization temperature was kept around 40 degrees C. pH was kept at 4.4 when measuring the activity of the immobilized GDC. No variation of the activity of immobilized GDC is observed when the capacity is over 2.5 meq/g.(CM-CADB resin). The properties of the immobilized enzyme on CM-CADB were characterized. No significant improvement can be achieved when the substrate concentration exceeds 12.00 mmol/l, where the activity of immobilized GDC is equal to 1.58 mmol/l.min.g. The optimum pH is found to be 5.2, which changes 0.2 unit, comparing with that of the free GDC (5.0). The optimum temperature is found to be around 48 degrees C, which is lower than that of free GDC (55 degrees C). The critical temperature of the free GDC and the immobilized GDC is approximately 50 degrees C and 45 degrees C, respectively. The half-life of the activity is 127 days when the immobilized enzyme was stored in the cold (4 degrees C). An immobilized GDC enzyme column reactor matched with a flow injection system-ion analyzer coupled with CO(2) electrode-data collection system made up the original form of the apparatus of biosensor for determining of L-glutamic acid. The determination conditions are that the buffer solution is 0.10 M Na(2)HPO(4)-0.05 M citric acid at pH 4.4 and t = 37 degrees C. The limit of detection is 1.0 x 10(-)(5) M. The linearity response is in the range of 5 x 10 (-2) - 5 x 10 (-5) M. The equation of linear regression of the calibration curve is y = 43.3x + 181.6 (y is the milli-volt of electrical potential response, x is the logarithm of the concentration of the substrate of L-glutamic acid). The correlation coefficient equals 0.99. The coefficient of variation equals 2.7%.     

A comparative study of immobilized amyloglucosidase in a packed bed reactor and a continuous feed stirred tank reactor

The catalytic activity of amyloglucosidase covalently attached to DEAE-cellulose was studied in a packed bed reactor and a continuous feed stirred tank reactor (CSTR) for the reaction maltose → glucose. At low flow rates mass-transfer limitations in the bed reactor lead to lower conversions for this reactor compared to the CSTR. Simple theoretical expressions for these reactors were compared with the experimental results. There are significant differences between the kinetic parameters and pH profile of the immobilized and free enzyme. The immobilized enzyme also showed greater stability at 50°C than did free amyloglucosidase. The temperature dependence of the reaction rate was the same for immobilized and free enzyme.     

Urokinase bound to fibrocollagenous tubes: an in vitro kinetic study

Urokinase (UK) has been immobilized to the inner surfaces of fibrocollagenous tubes (FCT) in an attempt to develop a fibrinolytic biomaterial which may be suitable for use as a small diameter vascular prosthesis. The enzyme was bound by adsorption followed by glutaraldehyde crosslinking. An in virto kinetic study of immobilized urokinase was conducted by employing the tubular material as a flow through reactor operated in a batch recycle mode in which the esterolysis of the model substrate, N-alpha-acetyl-L-lysine methyl ester (ALME), was monitored as a function of substrate concentration, recycle flow rate, and temperature. Results were compared with data from the soluble enzyme reaction, which was conducted in the presence and absence of 10% swine skin gelatin, in order to identify the specific effects of a collagenous microenvironment. Observed rates for the UK-FCT catalyzed reaction were observed to be dependent on recycle flow rates below 12 mL/min (Re = 107). Apparent Michaelis-Menten rate parameters were determined by a nonlinear search technique for two flow rates: one above the critical point for external diffusion effects (Re = 282) and one within the mass-transfer-limited region (Re = 71). When the latter data were corrected for external diffusion by applying the Graetz correlation for laminar flow in tubes to estimate themass transfer coefficient, the corrected K(m) of 6.45 +/- 0.38 mM agreed very closely with the diffusion free parameter (i.e. 6.13 +/- 0.63). Furthermore, this value was observed to be an order of magnitude higher than that of the soluble enzyme but approximately equal to the K(m) of the soluble enzyme in a 10% gelatin environment (8.13 +/- 1.53 mM). It is postulated that the difference in kinetic parameters between soluble and collagen immobilized UK is due to an inherent interaction between collagen and enzyme rather than to mass transfer effects. Such aninteraction is supported by the effects of collagen on thermal stability and energy of activation.     

Comparative studies on soluble and immobilized yeast hexokinase

Comparative studies have been carried out on soluble and immobilized yeast hexokinase (ATP: D-hexose 6-phosphotransferase, EC 2.7.1.1). The enzyme was immobilized by covalent attachment to a polyacrylamide type support containing carboxylic functional groups. The effects of immobilization on the catalytic properties and stability of hexokinase were studied. As a result of immobilization, the pH optimum for catalytic activity was shifted in the alkaline direction to ～pH 9.7. The apparent optimum temperature of the immobilized enzyme was higher than that of the soluble enzyme. The apparent K_m value with D-glucose as substrate increased, while that with ATP as substrate decreased, compared with the data for the soluble enzyme. Differences were found in the thermal inactivation processes and stabilities of the soluble and immobilized enzymes. The resistance to urea of the soluble enzyme was higher at alkaline pH values, while that for the immobilized enzyme was greatest at ～pH 6.0.     

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.     

Fatty acid specificity of immobilized kid goat pre-gastric esterase: Effects of pH

Summary Kid goat pre-gastric esterase immobilized in a hollow fiber reactor was used to hydrolyse butteroil at buffer pH values of 5.0, 6.0 and 7.0. Overall hydrolysis proceeded fastest at pH 6.0, but changes in volatile fatty acid ratios with pH suggest that the same enzyme:substrate system can produce different flavor profiles, e. g., at pH 6.0 the relative rate of production of undesirable soaplike flavors is minimized.     

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.     

Kinetic modeling of lactose hydrolysis with an immobilized beta-galactosidase from Kluyveromyces fragilis

The kinetic model of the hydrolysis of lactose with a beta-galactosidase from Kluyveromyces fragilis immobilized on a commercial silica-alumina (KA-3, from Südchemie) has been determined. A wide experimental range of the main variables has been employed: temperature, concentrations of substrate, and products and concentration of enzyme. The runs were performed in a complex buffer with the salt composition of milk. The effect of pH and temperature on the stability and the activity of the enzyme have been studied. The optimum pH for the enzyme activity was, approximately, seven. The immobilized enzyme was more stable than the free one at acidic pH, but more instable at basic pH. The maximum temperature used for the hydrolysis runs performed to select the kinetic model was 40 degrees C, so inactivation of the enzyme during the kinetic runs has been avoided. Agitation, concentration of enzyme in the solid and particle size were selected to ensure that the overall rate was that of the chemical reaction. Eleven kinetic models were proposed to fit experimental data, from first order to more complex ones, such as those taking into account inhibition by one of the compounds involved in the hydrolysis reaction. Applying statistical and physical criteria, a Michaelis-Menten model with a competitive inhibition by galactose has been selected. The model is able to fit the experimental data correctly in the wide experimental range studied. Finally, the model obtained is compared to the one selected in a previous work for the hydrolysis of lactose with the free enzyme.     

Activity and operational stability of immobilized mandelonitrile lyase in methanol/water mixtures

Summary The enzyme mandelonitrile lyase was covalently immobilized on solid support materials using different methods. Immobilization on porous silica using coupling with glutaraldehyde afforded preparations with high enzyme loading (up to 9% (w/w)). The immobilized enzyme was used in a packed bed reactor for the continuous production of d-mandelonitrile from benzaldehyde and cyanide. The influence of the flow rate, pH, substrate concentrations and enzyme loading on the reaction yield and the enantiomeric purity of the product was investigated. In order to suppress the competing spontaneous reaction, the enzymatic reaction must be rapid. A flow rate of 9.5 ml/min (0.1 M benzaldehyde and 0.3 M HCN) through a 3 ml reactor afforded a 86% yield of mandelonitrile with 92% enantiomeric excess. No leakage of enzyme occurred under continuous operation. One column was used continuously for 200 h without any decrease in yield or enantiomeric purity of the product. High concentrations of benzoic acid were shown to decrease the operational stability of the system.     

Immobilized enzymes: electrokinetic effects on reaction rates in a porous medium

The effect of the internal diffusion and electrical surface charge on the overall rate of a reaction catalyzed by an enzyme immobilized on a porous medium are examined. Effectiveness factors have been calculated which compare the global reaction rate to that existing in the absence of the internal diffusion and/or the electrical field. The surface charge, assumed to arise from the dissociation equilibria of the acidic and basic surface groups of the enzyme, generates an electrical double layer at the pore surface. The double-layer potential is governed by the Poisson-Boltzmann equation. It is shown that the diffusion potential can be characterized by a modulus which depends upon the surface reaction rate, the charges and diffusivities of the substrate and products, the ionic strength, and the pore dimensions. The flux of a charged species in the pore occurs under the influences of the concentration gradient and the electrical potential gradient. The governing equations are solved by an iterative numerical method. The effects of pH, enzyme concentration, and substrate concentration on the rates of two different hydrolysis reactions catalyzed by immobilized papain are examined. The release of H(+) in one of the reactions causes the lowering of internal pH, and also a constancy of the internal pH when the external pH in creases beyond a certain value. The latter reaction also shows a maximum in the reaction rate with respect to enzyme concentration. The reaction not involving H(+) as a product shows a maximum in the reaction rate with respect to external pH, but a monotonic increase in the reaction rate as the enzyme concentration increases.     

Immobilization of alpha-glucosidase in chitosan coated polygalacturonic acid

Crude alpha-glucosidase from Baker's yeast was immobilized in polygalacturonic acid beads and coated with chitosan. Chemical and physical characterization were performed by using p-nitrophenyl-alpha-D-glucopyranoside (pNPG) as an artificial substrate. Operation, thermal, pH, and strorage stabilities of the free and immobilized enzyme were also examined. The stabilities of immobilized enzyme were found to be better than that of the free enzyme. Furthermore, the hydrolysis rate of the chitosan coated alpha-glucosidase polygalacturonic acid beads were studied. In conclusion, the enzyme beads appear to have good characteristics and offer the prospect that this system may find application in enzyme immobilization, in addition to controlled drug release studies.     

Improved octyl glucoside synthesis using immobilized β-glucosidase on PA-M with reduced glucose surplus inhibition

A β-glucosidase extracted from bitter almond (Prunus dulcis var. amara) was immobilized on polyamine microspheres (PA-M) for catalytic octyl glucoside (OG) synthesis from glucose and octanol through reversed hydrolysis. The immobilization increased the activity of enzyme at pH 6.0–7.0, and the optimal reaction temperature for immobilized enzyme was identical to the free enzyme. The thermal stability and solvent tolerance of enzyme were increased by its immobilization. In the co-solvent system using 10% t-butyl alcohol and 10% (v/v) water, the yield of OG was increased by 1.7-fold compared to the yield from the system without co-solvent. Based on dynamic and Dixon plot analyses, the initial reaction velocity (V₀) increased approximately three-fold on immobilization and the OG synthesis was inhibited by surplus glucose. The inhibition dissociation constants for free and immobilized enzyme were 219?mM and 116?mM, respectively. A fed-batch mode was applied in the OG synthesis to minimize substrate inhibition. After 336?h of reaction, the OG yield and the conversion rate of glucose reached 134?mM and 59.6%, respectively. Compared to the batch operation, the fed-bath operation increased the OG yield and the conversion rate of glucose by 340% and 381%, respectively.