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.     

Characterization of the activity of penicillin G acylase immobilized onto nylon membranes grafted with different acrylic monomers by means of γ-radiation

Penicillin G acylase (PGA) has been immobilized onto nylon membranes grafted with methylmethacrylate (MMA) or diethyleneglycoldimethacrylate (DGDA) monomers by means of γ-radiation. Hexamethylenediamine (HMDA) has been used as spacer between the grafted membranes and the enzyme. Glutaraldehyde (GA) was used as crosslinking to couple the enzyme to the HMDA. The catalytic membranes so prepared were studied as a function of pH and temperature of the solution containing the substrate. The membranes showing the best characteristics were the ones grafted with DGDA. The dependence of the behavior of these membranes on several experimental conditions was studied, i.e., the temperature and duration of the aminoalkylation process, spacer concentration, the glutaraldehyde concentration and the enzyme concentration. The experimental conditions giving the best performance of the catalytic membranes have been deduced. The time requested to obtain 50% of substrate conversion, i.e., hydrolysis of cephalexin, has been studied as a function of its initial concentration.     

Cephalexin synthesis by immobilised penicillin G acylase under non-isothermal conditions: reduction of diffusion limitation

The effect of thermodialysis on the enzymatic kinetic synthesis of the antibiotic cephalexin was investigated. As reference points, two existing models for an immobilised enzyme (Assemblase^®) and for the free enzyme were used. For Assemblase^®, it is known that diffusion limitation occurs and that therefore considerably more of the undesired side-product phenylglycine is formed.

The enzyme was immobilised on a membrane, and under isothermal conditions (293 K) the course of the reaction resembled that of the Assemblase^® enzyme. However, if a temperature gradient was applied across the membrane, with an average temperature of 293 K for the enzyme, than the course of the reaction changed. For large temperature gradients (30° and more), the course of the reaction resembled that of free enzyme. Thermodialysis enhances mass transfer across the membrane and therewith reduces diffusion limitations in the immobilised enzyme on the membrane.

The stability of the immobilised enzyme is such that the reactor can be re-used repeatedly. This, together with the positive effect of the temperature gradient on the course of the reaction, makes thermodialysis an interesting new technique that has potential to be applied on a larger scale if the membrane surface area per volume of reactor can be improved.     

Purification of hepatocyte growth factor using polyvinyldiene fluoride-based immobilized metal affinity membranes: equilibrium adsorption study

Polyvinyldiene fluoride (PVDF)-based affinity membranes with immobilized copper ions were developed in this study. The resulting membranes were tested for their adsorption properties using a model protein, lysozyme, in batch mode. First, different lengths of diamine were utilized as spacer arms to immobilize the metal ions onto the membranes. It was found that the application of 1,8-diaminooctane as the spacer arm led to the highest adsorption capacity. Moreover, the effects of pH and salt concentration were investigated to distinguish the proportion of specific and nonspecific interactions. A big fraction of lysozyme adsorption capacity for the immobilized metal affinity membranes was considered to come from nonspecific electrostatic interactions, which could be reduced by increasing salt concentration. Lastly, the purification of hepatocyte growth factor (HGF) from insect cell supernatant was performed using the immobilized metal affinity membranes in batch mode. HGF was found in the elution condition using EDTA, indicating the successful purification of HGF.     

Rational design of a more stable penicillin G acylase against organic cosolvent

We have used a simple and efficient approach by combining the known functional and structural properties of penicillin G acylase (PGA) from E. coli, and tried to mutate PGA of Bacillus megaterium with the goal of increasing the stability of the enzyme in organic solvents or at acidic pH. The PGA mutants Kβ427A, Kβ430A and Kβ427A/Kβ430A obtained have higher stability in DMF than the wild-type PGA.     

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.     

Variation of penicillin acylase partition coefficient with phase volume ratio in poly(ethylene glycol)–sodium citrate aqueous two-phase systems

The influence of phase volume ratio on partition and purification of penicillin acylase from Escherichia coli on poly(ethylene glycol)–sodium citrate aqueous two-phase systems was studied. In PEG 1000 systems both partition coefficients of the enzyme and total protein increased with decreasing phase volume ratio. However, in PEG 3350 containing NaCl, penicillin acylase follows a reverse trend, while total protein behaves in the same way. Implications for protein purification designs are discussed.     

Efficient preparation of enantiopure l-tert-leucine through immobilized penicillin G acylase catalyzed kinetic resolution in aqueous medium

Racemic _DL-tert-leucine (_DL-Tle) was resolved to obtain enantiopure _L-Tle through enantioselective hydrolysis of its N-phenylacetyl derivative with immobilized penicillin G acylase (PGA). The effects of pH, reaction temperature, substrate concentration and reaction time on the reaction were investigated. The reaction was conveniently carried out at 0.4 M substrate concentration in water at pH 8.0 and 30 °C. Under the optimized reaction conditions, _L-Tle was obtained in an enantiopure form (>99% ee) with 45.8% substrate conversion after 4 h. The thermal stability and operational stability of immobilized PGA were examined. Furthermore, the preparation of _L-Tle was successfully performed in a recirculating packed bed reactor (RPBR) system and immobilized PGA exhibited a long-term stability for 51 days with a slight decrease of activity. The isolated _D-enantiomer was racemized at 160 °C for 15 min and reused as substrate. The results obtained clearly demonstrated a potential for industrial application of immobilized PGA in the preparation of _L-Tle through enantioselective hydrolysis of its N-phenylacetyl derivative.     

Immobilization of penicillin G acylase on macro-mesoporous silica spheres

In this study, macro-mesoporous silica spheres were prepared with a micro-device and used as the support for the immobilization of penicillin G acylase (PGA). To measure the enzymatic activity, the silica spheres with immobilized PGA were placed into a packed-bed reactor, in which the hydrolysis of penicillin G was carried out. The influences of the residence time, the initial concentration of the substrate, the accumulation of the target product 6-aminopenicillanic acid, and the enzyme loading amount on the performance of the immobilized PGA were investigated. The introduction of macropores increased the enzyme loading amount and decreased the internal mass transfer resistance, and the results showed that the enzyme loading amount reached 895 mg/g (dry support), and the apparent enzymatic activity achieved up to 1033 U/g (dry support). In addition, the immobilized PGA was found to have great stability.     

Modifying the substrate specificity of penicillin G acylase to cephalosporin acylase by mutating active-site residues

The penicillin G acylase (PGA) and cephalosporin acylase (CA) families, which are members of the N-terminal (Ntn) hydrolases, are valuable for the production of backbone chemicals like 6-aminopenicillanic acid and 7-aminocephalosporanic acid (7-ACA), which can be used to synthesize semi-synthetic penicillins and cephalosporins, respectively. Regardless of the low sequence similarity between PGA and CA, the structural homologies at their active-sites are very high. However, despite this structural conservation, they catalyze very different substrates. PGA reacts with the hydrophobic aromatic side-chain (the phenylacetyl moiety) of penicillin G (PG), whereas CA targets the hydrophilic linear side-chain (the glutaryl moiety) of glutaryl-7-ACA (GL-7-ACA). These different substrate specificities are likely to be due to differences in the side-chains of the active-site residues. In this study, mutagenesis of active-site residues binding the side-chain moiety of PG changed the substrate specificity of PGA to that of CA. This mutant PGA may constitute an alternative source of engineered enzymes for the industrial production of 7-ACA.     

Use of neural networks in the mathematical modelling of the enzymic synthesis of amoxicillin catalysed by penicillin G acylase immobilized in chitosan

This study focuses in the mathematical modelling of the enzymic synthesis of amoxicillin by the reaction of p-hydroxyphenylglycine methyl ester and 6-aminopenicillanic acid (6APA), catalyzed by penicillin G acylase (PGA) immobilized on glutaraldehyde-chitosan, at 25°C and pH 6.5. Previous work on the kinetics and mechanism of reaction showed that the use of neural networks seems to be an interesting alternative to simulate experimental data of antibiotic production. Therefore, two feedforward neural networks, with one hidden layer, were trained and used to forecast the rates of amoxicillin and p-hydroxyphenylglycine (POHPG) net production. First of all, some parameters that affect the network performed were investigated, such as the number of nodes between the input and hidden layers and the number of interactions during the learning phase. Afterwards, hybrid models that coupled artificial neural networks to mass-balance equations were used to reproduce the performance of batch reactors for the production of amoxicillin. This approach provided accurate results, within the range of substrate concentration studied.     

Immobilization of penicillin G acylase on paramagnetic aldehyde-functionalized mesostructured cellular foams

Paramagnetic aldehyde-functionalized mesostructured cellular foams (PAMCFs), synthesized by grafting 3-aminopropyltriethoxysilane modified Fe₃O₄ (NH₂-Fe₃O₄) nanoparticles with larger particle size than the window pore size of MCFs on the outer surface of aldehyde-functionalized mesostructured cellular foams (AMCFs), were investigated as efficient supports for immobilization of penicillin G acylase (PGA). The results show that NH₂-Fe₃O₄ nanoparticles were successfully grafted on the outer surface of AMCFs and PGA molecules were mainly immobilized covalently on the inner surface of PAMCFs, which was because amino groups of NH₂-Fe₃O₄ nanoparticles or PGA molecules reacted with aldehyde groups of AMCFs or PAMCFs to form imine bonds. PGA/PAMCFs-15 showed a rather high initial activity of 9563 U g⁻¹ and retained 89.1% of its initial activity after recycled for 10 times. PGA/PAMCFs are easily recycled by magnetic field in order to replace tedious separation of high-speed centrifugation for mesoporous materials.     

A new biocatalyst: Penicillin G acylase immobilized in sol-gel micro-particles with magnetic properties

The present work focuses on the development and basic characterization of a new magnetic biocatalyst, namely penicillin G acylase (PGA), immobilized in sol-gel matrices with magnetic properties, ultimately aimed for application in cephalexin (CEX) synthesis. A mechanically stable carrier, based on porous xerogels silica matrixes starting from tetramethoxysilane (TMOS), was prepared leading to micro-carriers with medium sized particles of 30 μm, as determined by scanning electron microscopy. An immobilization yield of 95–100% and a recovered activity of 50–65% at 37°C, as determined by penicillin G (PG) hydrolysis (pH STAT method), were observed. These results clearly exceed those reported in a previous work on PGA immobilization in sol-gel, where only 10% of activity was recovered. The values of activity were kept constant for 6 months. Immobilized PGA (682 U/g_{dry weight}) retained high specific activity throughout ten consecutive runs for PG hydrolysis, suggesting adequate biocatalyst stability. The CEX synthesis was performed at 14°C, using the free and immobilized PGA in aqueous medium. Phenylglycine methyl ester was used as acyl donor at 90 mM and 7-aminodeacetoxycephalosporanic acid was the limiting substrate at 30 mM. The CEX stoichiometric yield after 1-h reaction was close to 68% (23 mM CEX/h) and 65% (19 mM CEX/h), respectively.     

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.     

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)     

Protein fractionation using fast flow immobilized metal chelate affinity membranes

A new group-specific affinity membrane using metal chelates as ligands and inorganic glass hollow fiber microfiltration membranes as support matrices is developed and tested. The study focused on developing the optimum activation and coupling procedures to bind the chelating agent (iminodiacetic acid, IDA) to the surface of the microporous glass hollow fiber membrane and testing the resultant affinity membrane. Starting with three different glass surfaces, five modification reactions were evaluated. All the modified "active surfaces" were first tested for their protein adsorptive properties in batch mode with suspended microporous glass grains using model proteins with known binding characteristics with Cu-IDA systems. The metal loading capacities of the surfaces exhibiting favorable fractionation were then measured by atomic absorption spectroscopy.The results were compared with the results obtained with a commercial material used in immobilized metal affinity column chromatography. The protein binding characteristics of the hollow fiber affinity membranes were also evaluated under conditions of convective flow. This was performed by flowing single solute protein solutions through the microporous membrane at different flow rates. These results were then used to estimate the optimum loading and elution times for the process. A mathematical model incorporating radial diffusion was solved using a finite difference discretization method. Comparison between model predictions and experimental results was performed for four different proteins at one flow rate. These results suggested that the kinetics of adsorption was concentration dependent. Finally, the hollow fiber affinity membranes were challenged with two component mixtures to test their ability to fractionate mixed protein solutions. Efficient separation and good purity were obtained.The results presented here represent the development of a new fast flow affinity membrane process-immobilized metal affinity membranes (IMAM). (c) 1994 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.     

Leakage of recombinant penicillin G acylase from Escherichia coli by adding chloroform under fermentation conditions

A simple method was developed to release periplasmic penicillin G acylase from Escherichia coli BL21(DE3) during the fermentation process. More than 80% of the total penicillin G acylase was released into the broth when 3% (v/v) chloroform was added at 3 h after induction. The activity of extracellular penicillin G acylase reached 20699 U/l. This method was efficient and would facilitate further investigation of penicillin G acylase for industrial applications.     

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.     

金属螯合亲和层析法纯化抗乙肝核心抗原单克隆抗体

采用金属螯合亲和层析法,纯化了小鼠腹水来源的抗乙肝核心抗原单克隆抗体,对上样缓冲液的pH和离子强度、洗脱液种类和洗脱方式进行优化。结果表明,采用降低pH分步洗脱时,最佳上样缓冲液为pH8.0,20mmol/LPB+0.5mol/LNaCl,抗体在pH5.0被洗脱下来,抗体回收率80%,纯度85%。采用咪唑浓度梯度洗脱时,最佳的上样缓冲液为pH8.0,20mmol/LPB+5mmol/L咪唑,抗体纯度大于95%,回收率65%;在上样缓冲液中不添加NaCl而添加少量的咪唑,更有利于抗体分离。以上洗脱方式都能较好地保持mAb的生物学活性,为该抗体的应用提供了必要的实验基础。