Enhancement of penicillin G hydrolysis using penicillin acylase to 6-aminopenicillanic acid by simultaneous chromatographic separation

Penicillin G (Pen-G) was hydrolyzed to 6-aminopenicillanic acid (6-APA) and phenylacetic acid (PAA) in a chromatographic reactor-separator using the mixture of immobilized Escherichia coli cells and a macroporous adsorbent as stationary phase and a phosphate buffer of pH 7.8 as eluant. Pen-G conversion of 98% was observed without adjustment of the eluant pH due to the effective separation of 6-APA from Pen-G and PAA. At a sample load of 600 mg Pen-G, the volume overload gave higher Pen-G conversion (86%) than the mass overload (68%), while their difference in product resolution (0.9 and 1.0, respectively) was insignificant.     

聚丙烯腈纤维固定化青霉素酰化酶性质的研究

将巨大芽孢杆菌（Bacillusmegaterium）青霉素酞化酶连接到聚丙烯腈纤维载体上,制成固定化青霉素酰化酶。其表现活力约为2000u／g。水解青霉素G的最适温度为50℃;最适PH为9．0;在PHS．5～10．3、温度50℃以下酶的活力稳定;表观米氏常数Ka为1．33×10-8mol／L;最大反应速度Vm为2．564mmol·min-1;苯乙酸为竞争性抑制剂,抑制常数为0．16mol／L。水解10％的青霉素G钾盐溶液,使用20批,保留酶活力80％。     

颗粒状固定化青霉素酰化酶的研究

将巨大芽孢杆菌 (Bacillusmegaterium)胞外青霉素酰化酶通过共价键结合到聚合物载体EupergitC颗粒环氧基团上 ,制成的颗粒状固定化青霉素酰化酶表现活力达 1 40 0 μ/g左右。固定化酶水解青霉素的最适 pH8 0 ,最适温度为 55℃。在pH6 0～ 8 5、温度低于 40℃时固定化酶活力稳定。在 pH8 0、温度 37℃时 ,固定化酶对青霉素的表现米氏常数Ka为 2×1 0 - 2 mol/L ;苯乙酸为竞争性抑制剂 ,抑制常数Kip为 2 8× 1 0 - 2 mol/L ;6 APA为非竞争性抑制剂 ,抑制常数Kia为 0 1 2 5mol/L。固定化酶水解青霉素 ,投料浓度为 8% ,在使用 2 0 0批后 ,保留活力 80 %左右 ,6 APA收率平均达 89 48%。     

Kinetic behavior of immobilized Penicillin acylase

Penicillin acylase has been immobilized to carboxymethylcellulose and to the resin Amberlite XAD7. The reaction kinetics of the enzyme were affected by both intrinsic (molecular) and microenvironmental effects. The Michaelis constant for the enzyme increased after immobilization as a result of an intrinsic effect of the reagent, glutaraldehyde, used for enzyme immobilization. Microenvironmental effects were of two types: diffusional limitation of access of substrate and a reaction-generated pH depression in the support particles. This depression of internal pH was observed in all the preparations and could be reduced by addition of pH buffering salts to reactor. An adsorbed pH-indicating dyc was used to determine the surface and internal pH of particles of XAD7–penicillin acylase under various reaction conditions. The extent of diffusional rate limitation in XAD7–penicillin acylase was related to the penetration depth of protein into the porous support particles. The penetration depth of protein and thus the diffusional limitation of the reaction rate could be controlled by the conditions of preparation of the immobilized enzyme. A staining technique was used to observe the location of the protein.     

Enzymes in polyelectrolyte complexes. The effect of phase transition on thermal stability

Penicillin amidase, alpha-chymotrypsin and urease have been immobilized in water-soluble nonstoichiometric polyelectrolyte complexes (N-PEC). N-PEC are formed by modified poly(N-ethyl-4-vinyl-pyridinium bromide) (polycation) and excess poly(methylacrylic acid) (polyanion). N-PEC are a new class of polymers capable, characteristically, of phase transitions solution in equilibrium precipitate induced by slight change in pH or ionic strength. Neither the chemical structure of the carrier nor the number of cross-linkages between an enzyme and a carrier change on phase transition. That gives an unique opportunity to elucidate the difference between enzymes immobilized on water-soluble and water-insoluble supports. A detailed study of the phase transition effect on thermal stability of the enzymes and protein-protein interactions has been carried out. The following effects were found. Pronounced thermal stabilization of penicillin amidase and urease may be achieved on two conditions: the enzyme is in the precipitate; (b) the enzyme is linked to the N-PEC nucleus. Then the thermal stability of N-PEC-bound penicillin amidase increases 7-fold at pH 5.7, 60 degrees C, and 300-fold at pH 3.1, 25 degrees C, compared to the native enzyme. For urease, the thermal stabilization increases 20-fold at pH 5.0, 70 degrees C. The localization of enzyme on N-PEC has been established by titration of alpha-chymotrypsin bound to a polycation or polyanion with basic pancreatic trypsin inhibitor. Both in solution (pH 6.1) and in N-PEC precipitate (pH 5.7), an alpha-chymotrypsin molecule bound to a polyanion is fully exposed to the solution. If the enzyme is bound to a polycation, only 20% of alpha-chymotrypsin molecules in the precipitate and 40% in solution retain their ability for protein-protein interactions. This means that a polycation-bound enzyme is localized in the hydrophobic nucleus of the complex, whereas the polyanion-bound enzyme sits on the hydrophilic shell of the complex. On pH-induced phase transition (pH decreases from 6.1 to 5.7), there occurs a stepwise decrease in penicillin amidase activity which is due to a 9.8-fold increase in the Km for 2-nitro-4-phenylacetamidobenzoic acid. Change of the catalytic activity and thermal stability of N-PEC-bound penicillin amidase is fully reversible and reproducible. Such soluble-insoluble immobilized enzymes with controllable thermal stability and activity may be used for simulating events in vivo and in biotechnology.     

Urea hydrolysis by immobilized urease in a fixed-bed reactor: analysis and kinetic parameter estimation

Urea hydrolysis by urease immobilized onto ion exchange resins in a fixed-bed reactor has been studied. A modified Michaelis-Menten rate expression is used to describe the pH-dependent, substrate- and product-inhibited kinetics. Ionic equilibria of product and buffer species are included to account for pH changes generated by reaction. An isothermal, heterogeneous plug-flow reactor model has been developed. An effectiveness factor is used to describe the reaction-diffusion process within the particle phase. The procedure for covalent immobilization of urease onto macroporous cation exchangers is described. Urea conversion data are used to estimate kinetic parameters by a simplex optimization method. The best-fitted parameters are then used to predict the outlet conversions and pH values for systems with various inlet pH values, inlet urea and ammonia concentrations, buffers, particle sizes, and spacetimes. Very good agreement is obtained between experimental data and model predictions. This immobilized urease system exhibits quite different kinetic behavior from soluble urease because the pH near the enzyme active sites is different from that of the pore fluid. This effect results in a shift of the optimal pH value of the V(max) (pH) curve from 6.6 (soluble urease) to ca. 7.6 in dialysate solution, and ca. pH 8.0 in 20mM phosphate buffer. The reactor model is especially useful for estimating intrinsic kinetic parameters of immobilized enzymes and for designing urea removal columns.     

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.     

Equilibrium modeling of extractive enzymatic hydrolysis of penicillin G with concomitant 6-aminopenicillanic acid crystallization

In the present downstream processing of penicillin G, penicillin G is extracted from the fermentation broth with an organic solvent and purified as a potassium salt via a number of back-extraction and crystallization steps. After purification, penicillin G is hydrolyzed to 6-aminopenicillanic acid, a precursor for many semisynthetic beta-lactam antibiotics. We are studying a reduction in the number of pH shifts involved and hence a large reduction in the waste salt production. To this end, the organic penicillin G extract is directly to be added to an aqueous immobilized enzyme suspension reactor and hydrolyzed by extractive catalysis. We found that this conversion can exceed 90% because crystallization of 6-aminopenicillanic acid shifts the equilibrium to the product side. A model was developed for predicting the equilibrium conversion in batch systems containing both a water and a butyl acetate phase, with either potassium or D-p-hydroxyphenylglycine methyl ester as counter-ion of penicillin G. The model incorporates the partitioning equilibrium of the reactants, the enzymatic reaction equilibrium, and the crystallization equilibrium of 6-aminopenicillanic acid. The model predicted the equilibrium conversion of Pen G quite reasonably for different values of pH, initial penicillin G concentration and phase volume ratio. The model can be used as a tool for optimizing the enzymatic hydrolysis.     

Inhibition of chitosan-immobilized urease by slow-binding inhibitors: Ni, F and acetohydroxamic acid

The inhibitions by Ni²⁺ and F⁻ ions and by acetohydroxamic acid of jack bean urease covalently immobilized on chitosan membrane was studied (pH 7.0, 25°C) and compared with those of the native enzyme. The reaction progress curves of the immobilized urease-catalyzed hydrolysis of urea were recorded in the absence and presence of the inhibitors. They revealed that the inhibitions are of the competitive slow-binding type similar to those of native urease. The immobilization weakened the inhibitory effect of the inhibitors on urease as measured by the inhibition constants K_i^*. The increase in their values: 17.9-fold for Ni²⁺, 26.5-fold for F⁻ and 1.7-fold for acetohydroxamic acid, was accounted for by environmental effects generated by heterogeneity of the urease–chitosan system: (1) mass transfer limitations imposed on substrate and reaction product in the external solution, and (2) the increase in local pH on the membrane produced by both the enzymatic reaction and the electric charge of the support. By relating the K_M/K_i^* ratio to the electrostatic potential of chitosan it was found that while the reduced Ni²⁺ inhibition is mainly brought about by the potential, inhibition by acetohydroxamic acid is independent of the potential, and the acid inhibits urease in its non-ionic form. The reduction in F⁻ inhibition was ascribed to the increased pH in the local environment of the immobilized enzyme.     

活性炭吸附固定化粪产碱杆菌青霉素G酰化酶

目的：以活性炭为载体固定化粪产碱杆菌来源的青霉素G酰化酶,考察固定化酶的性质。方法：对影响酶固定化的因素优化筛选,确定有显著影响的因素：pH、离子强度、酶量、固定化时间进行L934的正交实验,获得最佳固定化条件,并对固定化酶的最适反应温度、pH及批次稳定性进行研究。结果：最佳固定化条件为：载体0.3g,酶量5mL,总反应体系为12mL,离子强度1mol/L,温度4℃,pH 7.0,固定化40h;最高固定化酶活性为135.9U/g湿载体。固定化酶性最适反应温度为55℃,最适pH为10,重复使用12次后没有活性损失。结论：活性炭吸附固定化青霉素G酰化酶的活性高,批次反应稳定,具有工业应用潜力。     

Properties of urease immobilized on the functional organic silica surface

The paper deals with kinetics of the urea hydrolysis by microbial-origin urease dissolved and immobilized on the organic silica surface. It is shown that hydrolysis kinetics for soluble urease is described by the Michaelis-Menten equation until the concentration of urea reaches 1 M. Two fractions differing in the Michaelis constant are revealed for silochrome immobilized urease. The rate of urea hydrolysis by native and immobilized urease was studied depending on the pH value in presence of the substrate in the 1 M and 5 mM concentration. The hydrolysis rate of 1 M urea in the buffer-free solution by silochrome-immobilized urease is practically independent of pH within 4.5-6.5. Application of a 2.5 mM phosphate-citrate buffer as a solvent causes an increase in the hydrolysis rate within this pH range. For a soluble urease the 1 M urea hydrolysis rate dependence on pH is ordinary at pH 5.8-6.0. If the substrate concentration is 5 mM, the pH-dependences for the rate of the urea hydrolysis by silochrome- and aerosil-immobilized urease are close and at pH above 6.0 coincide with those for a soluble enzyme. The found differences in the properties of soluble and immobilized ureases are explained by the substrate and reaction products diffusion.     

Urease immobilized on an aminated polysulphone membrane – inhibition by boric acid

An enzymatic membrane for application in the processes of decomposition and removal of urea from aqueous solutions was prepared: jack bean urease was immobilized on an aminated polysulphone membrane by adsorption. The inhibition of the system by boric acid was studied using procedures based on the MICHAELIS-MENTEN integrated equation (non-linear regression, and the linear transformations of WALKER and SCHMIDT, JENNINGS and NIEMANN, and BOOMAN and NIEMANN). The reaction was carried out in a 100 mM phosphate buffer of pH 7.0, containing 2 mM EDTA, obtained by neutralization of orthophosphoric acid with NaOH, at an initial urea concentration of 10 mM, and a temperature of 25 °C. The reaction was initiated by the addition of the enzyme to the urea solution, and was monitored by removing samples of the reaction mixture for NH₃ determinations by the phenol-hypochlorite method until the urea was exhausted. The results were compared with those obtained earlier under the same reaction conditions for free urease and urease covalently immobilized on chitosan. The inhibition was found to be competitive, similar to that of the free enzyme and urease immobilized on chitosan, with inhibition constants K_i equal to 0.36, 0.19 and 0.60 mM. The results show that adsorption of the enzyme on a polysulphone membrane changed the enzyme to a lesser degree than covalent immobilization of the enzyme on a chitosan membrane.     

固定化青霉素酰化酶在光-pH敏感可回用两水相中裂解青霉素G为6-APA

两水相体系在发展中存在的关键问题是相体系回收困难.由于生产成本及降低污染的原因, 用过的相体系需要回收和重复使用.用环境敏感型溶解可逆聚合物形成可回用两水相体系是当前是为可行的回收方法。本文在光敏感可回用高聚物PNBC与pH敏感型可回用高聚物PADB形成的两水相体系中进行固定化青霉素酰化酶的相转移催化青霉素G产生6-APA的反应。在这个两水相体系中,通过优化,在1% NaCl 存在下,６－ＡＰＡ的分配系数可达5.78。催化动力学显示,达平衡的时间近7h,反应最高得率约85.3%（pH 7.8, 20℃）。较相近条件下的单水相反应得率提高近20%。在反应过程中,通过底物及产物的分配系数检测,发现底物分配系数变化不大,而产物6-APA及苯乙酸的分配系数发生很大变化,从而引起产物的得率变化。在两水相中,底物及产物主要分配在上相,固定化酶分配在下相,底物青霉素G进入下相经酶催化产生的6-APA及苯乙酸又转入上相,从而解除了青霉素酰化酶催化反应的底物及产物抑制作用,达到提高产物得率的效果。此外,采用固定化酶较固定化细胞效率高,占用下相体积小,较游离酶稳定性高,且完全单侧分配在下相。因此,在两水相中进行固定化酶的催化反应具有明显的优越性。形成两水相的高聚物PNBC通过488 nm 的激光照射或经滤光的450nm 光源照射得到回收;pH敏感型成相聚合物PADB可通等电点 4.1沉淀可实现循环利用,高聚物的回收率在95%-98%之间,按此回收率计算,聚合物可使用60次以上。     

Effects of immobilization on the kinetics of enzyme-catalyzed reactions. II. Urease in a packed-column differential reactor system.

Urease from Jack bean was immobilized on nonporous glass beads by covalent bonding and its kinetics were studied in a packed-column differential reactor. To facilitate comparison, the urease was immobilized by both diazo and glutaraldehyde coupling. The kinetic properties of immobilized urease were similar to those of the soluble enzyme and different immobilization methods did not appreciably alter the kinetic properties. The affects of three different amino acid activators appear to follow predictions obtained from a relatively simple competitive model, except at very low substrate levels.     

High throughput covalent immobilization process for improvement of shelf-life,operational cycles,relative activity in organic media and enzymatic kinetics of urease and its application for urea removal from water samples

High throughput covalent urease immobilization was performed through the amide bond formation between the urease and the amino-functional MNPs. The enzyme’s performances, including shelf-life, reusability, enzymatic kinetics, and the enzyme relative activity in organic media was improved. At optimal conditions, the immobilization efficiency was calculated about 95.0% with keeping 94.7% of the urease initial specific activity. The optimal pH for maximum activity of the free and immobilized urease was calculated as 7.0 at 37.0 °C and 8.0 at 60.0 °C, respectively. The kinetics studies showed the K_m of 26.0 mM and 8.0 mM and the V_max of 5.31 μmol mg⁻¹ min⁻¹ and 3.93 μmol mg⁻¹ min⁻¹ for the free and immobilized urease, respectively. The ratio K_cat/K_m as a measure of catalytic efficiency and enzyme specificity was calculated as 0.09 mg mL⁻¹ min⁻¹ and 0.22 mg mL⁻¹ min⁻¹ for the free and immobilized urease, respectively, indicating an improvement in the enzymatic kinetics. The shelf-life and operational studies of immobilized urease indicated that approximately 97.7% and 88.5% of its initial activity was retained after 40 days and 17 operational cycles, respectively. The immobilized urease was utilized to urea removal from water samples with an efficiency between 91.5–95.0%.     

Investigation of the operational stabilities and kinetics of glucoamylase immobilized on alkylamine derivatives of titanium(IV)-activated porous inorganic supports

Glucoamylase (exo-1,4-α-d-glucosidase, EC 3.2.3.1) was coupled to several porous silica matrices by an improved metal-link/chelation process using alkylamine derivatives of titanium(IV)-activated supports. In order to select the titanium activation procedure which gave stable enzyme preparations, long-term stability tests were performed. The immobilized glucoamylase preparations, in which the carrier was activated to dryness with a 15% w/v TiCl₄ solution, displayed very stable behaviour, with half-lives of ～60 days. The optimum operating conditions were determined for these preparations. There are significant differences between the behaviour of the immobilized enzyme and the free enzyme. The apparent K_m increased on immobilization due to diffusional resistances. The pH optimum for the immobilized preparation showed a slight shift to acid pH relative to that of the soluble enzyme. Also, the optimum temperature descreased to 60°C after immobilization. In order to test Michaelis-Menten kinetics at high degrees of conversion, time-course analysis of soluble starch hydrolysis was performed. It was observed that simple Michaelis-Menten kinetics are not applicable to the free/immobilized glucoamylase-starch system at high degrees of conversion.     

The kinetics of penicillin-V deacylation on an immobilized enzyme

An immobilized Penicillin-V-acylase (commercial name, Novozym 217) with high specificity for the phenoxyacetyl-(V)- side chain was investigated in a recycle reactor and in a batch reactor to find the enzymatic reaction rate as a function of conversion, x, substrate concentration, c(A) (0) and pH. The reaction rate depends strongly on pH, and both products, phenoxy-acetic acid and 6-APA, inhibit the reaction. Nonspecific side reactions amount to only a few per cent when c(A) (0) <150mM and pH& gt; 6.5. The effectiveness factor for commercial-size particles is found to be about 0.65, and a value of 1.3mM is obtained for the equilibrium constant, K(eq), of the deacylation reaction. A kinetic model for the deacylation process which includes the effect of pH and of the reverse (acylation) reaction is proposed. Rate data for particles of different size are fitted to the nonlinear model. Five kinetic parameters and an effective diffusivity for the immobilized enzyme particles are determined.     

Modification and characterization of cellulosic cotton fibers for efficient immobilization of urease

Cotton fibers were first grafted by polyacrylonitril in the presence of KMnO(4) and oxalic acid as a combined redox initiator. Moreover, modification of the grafted cotton fibers was done by changing the nitrile group (-CN) into hydrazidine group through the reaction with hydrazine hydrate, then the fibers were activated by glutaraldehyde to introduce free aldehyde groups which were able to react with amino groups of urease to form Schiff's base, and result in cotton fibers immobilized urease. The efficiency of the immobilization was evaluated by examining the relative enzymatic activity of enzyme before and after the immobilization of urease. The results showed that the optimum temperature of immobilized urease was 35°C, which was higher than that of the free enzyme (30°C), and the immobilized urease exhibited a higher relative activity than that of free urease over 35°C. The optimal pH for immobilized urease was 6.5, which was lower than that of the free urease (pH 7.0), and the immobilization resulted in stabilization of enzyme over a wider pH range. The kinetic constant value (K(m)) of immobilized urease was higher than that of the free urease. However, the thermal and operational stabilities of immobilized urease have been improved greatly.     

Hydrolysis of starch particles using immobilized barley α-amylase

Barley α-amylase has been immobilized on silica particles with diameters between 0.5 and 10 μm using a covalent binding method. Immobilization procedures were adjusted to optimize enzyme activity. The effects of product inhibition, thermal stability and operational stability have been determined. The feasibility of using the immobilized enzyme to hydrolyze wheat starch particles at temperatures below the gelatinization temperature (<55 °C) was proven. The optimal conditions for the hydrolysis were found to be: pH 4.5, 40 °C, calcium ion concentration 0.002 M and immobilized enzyme loading of 30 mg/ml. At these conditions, the immobilized enzyme was able to hydrolyze wheat starch particles at concentrations as high as 100 mg/ml with a final conversion of 90% after 24 h of operation. Maltose and glucose were found to inhibit the immobilized enzyme in a similar manner as reported previously using soluble enzyme. Although the thermostability of the immobilized enzyme was superior to the soluble enzyme, the immobilized enzyme degraded at the same rate as the soluble enzyme during cold wheat starch hydrolysis (operational stability unchanged). Model equations are presented for product inhibition, hydrolysis kinetics and enzyme degradation. Using best-fit parameters, the equations are shown to fit the experimental data well.     

Hydrolysis of urea by gelatin-immobilized urease: separation of kinetic and diffusion phenomena in a model immobilized-enzyme reactor system.

Experiments and appropriate mathematical models are presented in an attempt to elucidate and separate the effects of mass transfer and immobilization on the apparent kinetics of hydrolysis of urea by urease immobilized within a crosslinked gelatin film. Diffusion of urea through the gelatin matrix appears to exert the major influence on the observed kinetics. Diffusion coefficients are measured, and a model for the "effectiveness factor" is presented, accounting for this aspect of mass transfer control. A secondary, but significant, influence on apparent kinetics arises because the reaction products lead to an increased pH level which, because of diffusion resistance, remains high within the gelatin matrix. For pH levels in the 6.7 to 9.0 range the activity of urease is a strongly decreasing function of pH. An approximate model accounting for ionic equilibrium allows this pH-diffusion effect to be introduced in such a way as to lead to predictions of the apparent kinetics that are compared with experimental observations. Examination of these results indicates that the immobilization procedure leads to some loss of activity due to an interaction of the gelatin crosslinking reaction with the enzyme itself.