Deacylation of benzylpenicillin by immobilized penicillin acylase

Immobilized penicillin acylase preparations have much higher activities per unit volume than immobilized cell preparations. Many parameters of the deacylation reaction are dependent on pH and both reactant and one of the products, 6-aminopenicillanic acid, are acid and alkali labile. Acid is produced as result of the deacylation reaction and must be neutralised. The influence of these pH effects on the design of the catalyst and the reactor is discussed.     

Continuous penicillin G hydrolysis in an electro-membrane reactor with immobilized penicillin G acylase

Penicillin G (2%, w/v in phosphate buffer, pH 8) was hydrolysed in a flow-through, miniature electro-membrane reactor with the penicillin G acylase immobilized in 5% (w/v) polyacrylamide (diam. 10 mm, thickness 2.6 mm, enzyme activity 24 U ml^–1). The conversion of penicillin G increased from 0.15 to almost 0.5 when the electric current applied to the reactor was changed from –600 to +600 A/m² with a substrate residency of 1 h. Symbols and abbreviations c _j ^p & concentration of component j in product stream (M) c _j ^s & concentration of component j in substrate stream (M) c _s ^o & substrate concentration at reactor inlet (M) C _j ^p=c _j ^p/c _S ⁰ & scaled concentration of component j in product stream C _j ^s=c _j ^s/c _S ⁰ & scaled concentration of component j in substrate stream i & electric current density (A/m²) j & reaction component, j P, Q or S P & main reaction product (6-aminopenicillanic acid) PGA & penicillin G acylase Q & side reaction product (phenylacetic acid) S & substrate (penicillin G) Y _s=C _P ^s+C _P ^p & substrate conversion & mean residence time of substrate and product streams in reactor (h) =C _Q ^s+C _Q ^p+C _S ^s+C _S ^s & check-sum of scaled concentrations =C _P ^p/(C _P ^s+C _P ^p) & separation factor of 6-aminopenicillanic acid (0 1)     

Conversion of benzylpenicillin to 6-aminopenicillanic acid in a batch reactor and continuous feed stirred tank reactor using immobilized penicillin amidase

A rate equation has been derived to describe the hydrolysis of benzylpenicillin to 6-aminopenicillanic acid by penicillin amidase. The integrated from of the rate equation has been shown to predict satisfactorily the progress of the reaction in a batch reactor using either soluble or immobilized penicillin amidase. The rate equation was also used to predict the performance of a continuous feed stirred tank reactor containing immobilized enzyme. There was good agreement with experimental measurements.     

Hydrolysis of penicillin G by combination of immobilized penicillin acylase and electrodialysis

Phenylacetic acid, as inhibitory product, was formed from a hydrolysis of penicillin G by immobilized penicillin acylase. In this article, electrodialysis was applied to remove phenylacetic acid continuously from the reaction mixture and to enhance an efficiency of the reaction. When 268 and 537 mM of penicillin G solution were used as the substrate, the concentration of phenylacetic acid in the reaction mixture could be maintained at less than 81 and 126 mM, respectively, and eventually, 86% and 88% of phenylacetic acid produced were removed from the reaction mixture at the end of the hydrolysis, respectively. Times required to reach 96% and 94.8% conversion from 268 and 537 mM of initial penicillin G could be reduced to 65% and 64% respectively, by means of electrodialysis; while 3.0% and 4.3% of initial penicillin G of 268 and 537 mM were permeated out of the reaction chamber during the hydrolysis, respectively. However, a loss of penicillin G by permeation could be reduced from 4.3% to 3.4% by a repeated addition of penicillin G.     

Efficient production of S-(+)-2-chlorophenylglycine by immobilized penicillin G acylase in a recirculating packed bed reactor

(S)-(+)-2-Chlorophenylglycine 1 is an important intermediate in the synthesis of Clopidogrel. A recirculating packed bed reactor (RPBR) was constructed for efficient production of (S)-1 by kinetic resolution of racemic N-phenylacetyl-2- chlorophenylglycine 2 using immobilized penicillin G acylase (PGA). The immobilized PGA exhibited maximum activity at 50 °C and pH 8.0 with (R,S)-2 as substrate. The kinetic constants (K_m and v_max) of immobilized PGA were calculated to be 20.61 mM and 83.2 mM/min/g, respectively. The substrate displayed inhibitory effect on immobilized PGA with inhibition constant of 221.23 mM. The immobilized PGA showed a strict enantiospecificity for substrate at different temperature, pH and substrate concentration examined. The performance and productivity of RPBR were evaluated by several critical parameters, including immobilized PGA load, substrate feeding rate, height to diameter ratio and so on. The kinetic resolution process shows higher initial reaction rate and conversion by recycling 100 mL of substrate solution (80 mM) through RPBRs packed with 6.0 g immobilized PGA with a feeding rate of 1.5 mL/min while the H/D ratio was 4.0. The immobilized PGA-catalyzed kinetic resolution of (R,S)-2 was successfully operated in the RPBR for 60 batches, with an average productivity of 1.2 g/L/h for (S)-1 in high optical purity (>97% enantiomeric excess) in semi-continuous operation. The residual (R)-2 can be easily racemized and then used as substrate.     

Enhancement of penicillin acylase activity by cultivating immobilized Kluyvera citrophila

Summary Whole cells of Kluyvera citrophila were immobilized in polyacrylamide gel. The penicillin acylase activity of immobilized whole cells was 60%–70% of native cells. When the immobilized cells were continuously cultivated for 40 h in an aerated fermentor containing peptone medium and were treated with alkali in order to remove -lactamase activity, the immobilized cells produced ampicillin up to 4.4 times faster than noncultivated cells.Ampicillin production was investigated in a column system using these cultivated immobilized whole cells. The cultivated immobilized cells showed excellent performance in continuous ampicillin production.     

Process of penicillin G hydrolysis catalyzed by penicillin acylase immobilized on acylic carrier

The usefulness of penicillin acylase immobilized onto butyl acrylate — ethyl glycol dimethacrylate (called in this paper acrylic carrier) in penicillin G hydrolysis performed in a stirred tank reactor is shown. The enzyme-acrylic carrier preparation does not deteriorate its own properties in the mixing condition of slurry reactor. The experiments were carried out in a batch and a continuous stirred tank reactor as well as continuous stirred tank reactors in series. It was found to be a satisfactory agreement between experimental and predicted results. It also indicated the optimal substrate concentration range which provides the most effective enzyme operation. A superiority of the three reactors in series over the batch reactor is shown.List of Symbols C_E g/m³ equivalent enzyme concentration - C_SO mol/m³ initial penicillin G concentration - K_A mol/m³ substrate affinity constant - K_iS mol/m³ substrate inhibitory constant - K_iP mol/m³ PhAA inhibitory constant - K_iQ mol/m³ 6-APA inhibitory constant - k₃ mol/g min constant rate of dissotiation of the active complex - r mol/m³ rate of reaction - t min. reaction time - t_j min. maintenance time - degree of conversion - _B, _F dimensionless time - min. residence time - PA penicillin acylase - PG penicillin G - PhAA phenylacetic acid - 6-APA 6-aminopenicillanic acid     

Deacylation of acylamino compounds other than penicillins by the cell-bound penicillin acylase of Escherichia coli

1. The action of the penicillin acylase enzyme of Escherichia coli N.C.I.B. 8743 on non-penicillin substrates suggests that the enzyme is an amidohydrolase. 2. The rates of hydrolysis for a small group of penicillins closely parallel those for a corresponding series of N-acylglycines. 3. For a series of E. coli strains, ability to cause rapid hydrolysis of phenylacetylglycine is correlated with ability to hydrolyse benzylpenicillin. 4. Amides and N-acylglycines are hydrolysed to the corresponding acids. The phenylacetyl group is hydrolysed most readily. Benzamide and beta-phenylpropionamide are not substrates. In a series of aliphatic acylglycines only valeryl- and hexanoyl-glycine are substrates. 5. Acylated l- but not d-alpha-amino acids are hydrolysed. d-alpha-Hydroxyphenylacetamide is a better substrate than the l compound.     

Enzymatic preparation of cefaclor with immobilized penicillin acylase

Enzymatic syntheses of cefaclor by immobilized penicillin acylase under kinetic control were carried out. According to the initial reaction rate ratio of synthesis to hydrolysis (Vs/Vh), penicillin acylase from Alcaligenes faecalis was chosen as the suitable catalyst for the synthesis of cefaclor. The reaction conditions, such as temperature, pH, and substrate concentration were investigated based on their Vs/Vh values. In the process of preparing cefaclor, in situ product removal (ISPR) and acyl donor feeding were used to achieve high yield. At the optimal conditions, the yield of cefaclor was 90%. In addition, the product were separated and purified, the total yield of cefaclor was 61%.     

Kinetic behavior of penicillin acylase immobilized on acrylic carrier

The usefulness of Lilly's kinetic equation to describe penicillin G hydrolysis performed by immobilized penicillin acylase onto the acrylic carrier has been shown. Based on the experimental results characteristic kinetic constants have been estimated. The effect of noncompetitive inhibition of 6-amino penicillanic acid has not been found. Five components of reaction resistance have been defined. These components were also estimated for the reaction of the native enzyme as well as the Boehringer preparation.List of Symbols C _E g/m³ enzyme concentration - C _P,C _Q mol/m³ product concentrations - C _S mol/m³ substrate concentration - C _SO mol/m³ initial substrate concentration - K _A mol/m³ constant which defines the affinity of a substrate to the enzyme - K _iS mol/m³ substrate inhibitory constant - K _iP mol/m³ PhAA inhibitory constant - K _iQ mol/m³ 6-APA inhibitory constant - k ₃ mol/g/min constant rate of dissociation of the active complex - R(1) concentrational component of reaction resistance - R(2) resistance component derived from substrate affinity - R(3) resistance component due to the inhibition of the enzyme by substrate - R(4) resistance component due to the inhibition of the enzyme by PhAA - R(5) resistance component due to inhibition of the enzyme by 6-APA - r = dC_s/dt mol/m³ min rate of reaction - t min reaction time - (i) relative resistance of reaction     

Non-isothermal cephalexin hydrolysis by penicillin G acylase immobilized on grafted nylon membranes

A new catalytic membrane has been prepared using a nylon membrane grafted by γ-radiation with methylmethacrylate (MMA) and using hexamethylenediamine (HMDA) as spacer. Penicillin G acylase (PGA) and cephalexin were employed as catalyst and substrate, respectively. Cephalexin hydrolysis was studied in bioreactors operated under isothermal and non-isothermal conditions. A hydrolysis increase was found when the temperature of the warm membrane surface was kept constant and the temperature of the other membrane surface was kept at a lower value. The hydrolysis increase was linearly proportional to the applied temperature difference. Cephalexin hydrolysis increased to about 10% when a temperature difference of 1°C was applied across the catalytic membrane. These results have been attributed to the non-isothermal cephalexin transport across the membrane, i.e., to the process of thermodialysis. In this way, the enzyme immobilized on and into the membrane reacts with a substrate concentration higher than that produced by simple diffusion under isothermal conditions.     

Preparation and kinetic properties of immobilized benzyl penicillin acylase]

An active insoluble preparation of immobilized benzyl penicillin acylase (IBA) EC 3.5.1.11 has been obtained by its entrapping into polyacrylamide gel lattice. Due to immobilization the preparation maintains up to 87% of its initial activity. The kinetics of IBA at low substrate concentrations obeys the Michaelis-Menten law; however, the apparent KM value decreases and the temperature optimum elevates. The inhibition by the reaction products--6-aminopenicillanic acid and phenylacetic acid--has been found to be 4.3 mM. The resultant IBA preparation proves to be suitable for hydrolysis of 5% benzyl penicillin solutions.     

Purification of penicillin G acylase using immobilized metal affinity membranes

The immobilized metal affinity membrane (IMAM) with modified regeneration cellulose was employed for purification of penicillin G acylase (PGA). For studying PGA adsorption capacity on the IMAM, factors such as chelator surface density, chelating metal, loading temperature, pH, NaCl concentration and elution solutions were investigated. The optimal loading conditions were found at 4 degrees C, 0.5 M NaCl, 32.04 micromol Cu(2+) per disk with 10 mM sodium phosphate buffer, pH 8.5, whereas elution conditions were: 1 M NH(4)Cl with 10 mM sodium phosphate buffer, pH 6.8. By applying these chromatographic conditions to the flow experiments in a cartridge, a 9.11-fold purification in specific activity with 90.25% recovery for PGA purification was obtained. Meanwhile, more than eight-times reusability of the membrane was achieved with the EDTA regeneration solutions.     

Dynamics of continuous stirred-tank biochemical reactor utilizing inhibitory substrate

The model of a continuous-stirred tank biochemical reactor was developed in which the instant uptake rate of substrate was used. The solutions of the model found for the oxidation of phenol by Pseudomonas putida fitted the experimental data better than the results obtained from the models cited in the literature. The model enables control of the culture parameters so that the unwanted washout of the biomass from the bioreactor can be avoided. A review of the models cited in the literature is also presented.     

Evaluation of immobilized metal affinity chromatography for purification of penicillin acylase

The aim of this work was to test immobilized metal affinity chromatography (IMAC) for the purification of penicillin acylase. After evaluation of different metals, Cu²⁺ was selected. Different samples were tested: pure penicillin acylase, industrial clarified feedstock and crude extract. After comparing two eluents, NH₄Cl and imidazole, it appeared that although both gave good results for recovery and activity, NH₄Cl was a more selective eluent with a higher fold purification than imidazole (4.64 versus 2.04). Moreover, we shown that a multistep gradient of NH₄Cl, greatly increased the degree of purification (12.36) compared with the one-step process as control (4.64). In addition, good recovery was obtained (97–100%).     

Factors affecting the synthesis of penicillins by the immobilized penicillin acylase from Escherichia coli

The effect of pH, temperature, reactant concentration, and reaction time has been investigated for the synthesis of N-benzhydryl-N′-acetamidopiperazyl-6-penicillanic acid and N-benzyl-N′-acetamidopiperazyl-6-penicillanic acid from 6-aminopenicillanic acid by the immobilized penicillin acylase from Escherichia coli. The synthesis of penicillins from carboxylic acids proceeds most rapidly at pH 5; with ethyl ester derivatives of carboxylic acids the pH optimum is higher (6–7). The most rapid synthesis of penicillins was obtained with ethyl ester derivatives of carboxylic acids. The optimum temperatures were 25–35°C.     

Rapid continuous colorimetric enzyme assay for penicillin G acylase

A rapid, continuous, colorimetric enzyme assay for penicillin G acylase has been developed. The assay measures the formation of the acidic products of penicillin G hydrolysis by following the decrease in pH using Phenol Red as an indicator. The activity measured is directly proportional to the amount of enzyme added to the assay, having a linear relationship with an R ² value of 0.9994.     

Thermal inactivation of immobilized penicillin acylase in the presence of substrate and products

Inactivation of immobilized penicillin acylase has been studied in the presence of substrate (penicillin G) and products (phenylacetic acid and 6-aminopenicillanic acid), under the hypothesis that substances which interact with the enzyme molecule during catalysis will have an effect on enzyme stability. The kinetics of immobilized penicillin acylase inactivation was a multistage process, decay constants being evaluated for the free-enzyme and enzyme complexes, from whose values modulation factors were determined for the effectors in each enzyme complex at each stage. 6-Aminopenicillanic acid and penicillin G stabilized the enzyme in the first stage of decay. Modulation factors in that stage were 0.96 for penicillin G and 0.98 for 6-aminopenicillanic acid. Phenylacetic acid increased the rate of inactivation in both stages, modulating factors being -2.31 and -2.23, respectively. Modulation factors influence enzyme performance in a reactor and are useful parameters for a proper evaluation. (c) 1996 John Wiley & Sons, Inc.     

Evaluation of the performance of immobilized penicillin G acylase using active-site titration

Penicillin G acylase from Escherichia coli was immobilized on Eupergit C with different enzyme loading. The activity of the immobilized preparations was assayed in the hydrolysis of penicillin G and was found to be much lower than would be expected on the basis of the residual enzyme activity in the immobilization supernatant. Active-site titration demonstrated that the immobilized enzyme molecules on average had turnover rates much lower than that of the dissolved enzyme. This was attributed to diffusion limitations of substrate and product inhibition. Indeed, when the immobilized preparations were crushed, the activity increased from 587 U g-1 to up to 974 U g-1. The immobilized preparations exhibited up to 15% lower turnover rates than the dissolved enzyme in cephalexin synthesis from 7-ADCA and D-(-)-phenylglycine amide. The synthesis over hydrolysis ratios of the immobilized preparations were also much lower than that of the dissolved enzyme. This was partly due to diffusion limitations but also to an intrinsic property of the immobilized enzyme because the synthesis over hydrolysis ratio of the crushed preparations was much lower than that of the dissolved enzyme.