Reaction heat measurements in the enzymatic hydrolysis reaction of penicillin GK to obtain 6-APA

The purpose of this study was to measure heats involved in the hydrolysis process for the industrial production of 6-aminopenicillanic acid (6-APA) using dynamic calorimetry techniques. The experimental design was planned using Hess' law. The information derived from the calorimeter was correlated mathematically to determine the heat released during enzymatic hydrolysis. This is important for temperature control systems and reactor design. The results obtained with the calorimetric measurements at 308 K and pH 7.5 are the penicillin hydrolysis, ΔH_hydrol, at 35.9 ± 5.7 kJ mol⁻¹ and phenyl acetic acid neutralization, ΔH_neut, at −47.1 ± 3.8 kJ mol⁻¹.     

Hydrogel coated monoliths for enzymatic hydrolysis of penicillin G

The objective of this work was to develop a hydrogel-coated monolith for the entrapment of penicillin G acylase (E. coli, PGA). After screening of different hydrogels, chitosan was chosen as the carrier material for the preparation of monolithic biocatalysts. This protocol leads to active immobilized biocatalysts for the enzymatic hydrolysis of penicillin G (PenG). The monolithic biocatalyst was tested in a monolith loop reactor (MLR) and compared with conventional reactor systems using free PGA, and a commercially available immobilized PGA. The optimal immobilization protocol was found to be 5 g l(-1) PGA, 1% chitosan, 1.1% glutaraldehyde and pH 7. Final PGA loading on glass plates was 29 mg ml(-1) gel. For 400 cpsi monoliths, the final PGA loading on functionalized monoliths was 36 mg ml(-1) gel. The observed volumetric reaction rate in the MLR was 0.79 mol s(-1) m(-3) (monolith). Apart from an initial drop in activity due to wash out of PGA at higher ionic strength, no decrease in activity was observed after five subsequent activity test runs. The storage stability of the biocatalysts is at least a month without loss of activity. Although the monolithic biocatalyst as used in the MLR is still outperformed by the current industrial catalyst (immobilized preparation of PGA, 4.5 mol s(-1) m(-3) (catalyst)), the rate per gel volume is slightly higher for monolithic catalysts. Good activity and improved mechanical strength make the monolithic bioreactor an interesting alternative that deserves further investigation for this application. Although moderate internal diffusion limitations have been observed inside the gel beads and in the gel layer on the monolith channel, this is not the main reason for the large differences in reactor performance that were observed. The pH drop over the reactor as a result of the chosen method for pH control results in a decreased performance of both the MLR and the packed bed reactor compared to the batch system. A different reactor configuration including an optimal pH profile is required to increase the reactor performance. The monolithic stirrer reactor would be an interesting alternative to improve the performance of the monolith-PGA combination.     

Enzymatic splitting of penicillin V for the production of 6-APA using immobilized penicillin V acylase

Penicillin V acylase from Fusarium sp. SKF 235 was immobilized on several cation-exchange resins, of which Amberlite CG-50 was preferred. Maximum activity of the immobilized penicillin V acylase was 250 to 280 IU/g dry beads. The pH and temperature optima of the enzyme shifted from 6.5 to 6.8 and 55°C to 60°C, respectively, as a result of immobilization. However, the K _m for penicillin V remained at 10mm. Parameters for producing 6-aminopenicillanic acid were investigated and the immobilized penicillin V acylase was used for 68 cycles in a stirred tank reactor.     

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.     

Kinetically controlled acylation of 6-APA catalyzed by penicillin acylase from Streptomyces lavendulae: effect of reaction conditions in the enzymatic synthesis of penicillin V

Abstract

Enzymatic synthesis of penicillin V (penV) by acylation of 6-aminopenicillanic acid (6-APA) was carried out using methyl phenoxyacetate (MPOA) as activated acyl donor and soluble penicillin acylase from Streptomyces lavendulae (SlPVA) as biocatalyst. The effect of different reaction conditions on penV synthesis was investigated, such as enzyme concentration, pH, molar ratio of 6-APA to MPOA, as well as presence of DMSO as water-miscible co-solvent at different concentrations. Time-course profiles of all reactions followed the typical pattern of kinetically controlled synthesis (KCS) of β-lactam antibiotics: penV concentration reached a maximum (highest yield or Y_max) and then decreased gradually. Such maximum was higher at pH 7.0, observing that final penV concentration was abruptly reduced when basic pH values were employed in the reaction. Under the selected conditions (100?mM Tris/HCl buffer pH 7.0, 30?°C, 2.7% (v/v) DMSO, 20?mM MPOA, 0.3 UI/ml of SlPVA), Y_max was enhanced by increasing the substrate molar ratio (6-APA to MPOA) up to 5, reaching a maximum of 94.5% and a S/H value of 16.4 (ratio of synthetic activity to hydrolytic activity). As a consequence, the use of an excess of 6-APA as nucleophile has allowed us to obtain some of the highest Y_max and S/H values among those reported in literature for KCS of β-lactam antibiotics. Although many penicillin G acylases (PGAs) have been described in kinetically controlled acylations, SlPVA should be considered as a different enzyme in the biocatalytic tool-box for novel potential synthetic processes, mainly due to its different substrate specificity compared to PGAs.     

Asymmetric enzymatic oxidoreductions in organic solvents

It is now beyond doubt that enzymes can vigorously work even in neat organic solvents containing little or no water. Switching the enzymatic reaction medium from aqueous to nonaqueous can make previously problematic processes feasible through, for example, increased substrate solubility or diminished side reactions. Moreover, when placed in this highly unnatural milieu, enzymes exhibit new and potentially valuable properties, including greater stability, markedly altered selectivity that can be readily controlled by the solvent, and molecular memory. Consequently, novel synthetic and biotechnological opportunities ensue, as illustrated herein by those based on enzymatic oxidoreductions such as the asymmetric peroxidase-catalyzed sulfoxidation of organic sulfides.     

Effect of organic solvents on penicillin acylase-catalyzed reactions: interaction of organic solvents with enzymes

The effects of various organic solvents on penicillin acylase-catalyzed synthesis of β-lactam antibiotics (pivampicillin and ampicillin) have been investigated in water-solvent mixtures. The rates of penicillin acylase-catalyzed reactions were found to be significantly reduced by the presence of a small amount of organic solvent. In particular, the rate of enzyme catalysis was extremely low in the presence of ring-structured solvents and acids while enzyme activities were fully restored after removing the solvents. This indicates that interactions between the solvents and the enzyme are specific and reversible. To correlate the inhibitory effects of organic solvents with solvent properties the influence of solvent hydrophobicities and solvent activity on the rate of pivampicillin synthesis was examined. The reaction rate was found to decrease with increasing solvent hydrophobicities, and a better correlation was observed between the reaction rate and solvent activity. The effects of ionic strength on the synthesis of pivampicillin and ampicillin were also examined. The ionic strength dependence indicates that electrostatic interactions are involved in the binding of ionic compounds to the enzyme. On the basis of the active site structure of penicillin acylase, a possible mechanism for molecular interactions between the enzyme and organic solvents is suggested.     

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)     

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.     

Advances in enzymatic transformation of penicillins to 6-aminopenicillanic acid (6-APA)

This article elaborates on the important recent developments in the enzymatic transformation of penicillins to 6-aminopenicillanic acid (6-APA), which is the basic raw material for the industrial production of semisynthetic penicillins such as amoxycillin and ampicillin. Particular emphasis is placed on the improvements in purification, stability, and immobilization of the enzymes, (i.e. penicillin acylases) used for these transformations.     

Enzyme stability in the presence of organic solvents

Summary The thermal stability of vacuum-dried acid-phosphatase has been investigated, both in the absence and in the presence of pure hexadecane. Preliminary experimental results indicate that: i) in both solid-phase runs, acid-phosphatase is much more stable than the free enzyme in aqueous solution, ii) the presence of the organic solvent slightly reduces thermal stability of the solid-phase enzyme. As regards the deactivation mechanism, when acid-phosphatase operates in free aqueous solution it follows a two-step in series deactivation. Initially the native configuration decays towards an intermediate, still active form. This, in turn, irreversibily yields a totally inactive structure. In the thermal deactivation of solid-phase enzyme it has been observed that: i) the first step is substantially retarded, ii) the final transition is completely hindered, iii) the intermediate configuration is more active than that produced in aqueous solution, by more than one order of magnitude.     

Aldolase stability in the presence of organic solvents

Rabbit muscle aldolase (RAMA) and trout muscle aldolase (TRMA) retained 100% activity in the presence of hexane, cyclohexane and toluene. Both enzymes retained greater than 80% activity in the presence of 20% (v/v) methanol. In the presence of 20% (v/v) N,N-dimethylformamide RAMA and TRMA were inactive, but at least 50% activity could be restored by returning the enzymes to an aqueous environment.     

青霉素G酰化酶工业进化的研究进展

青霉素G酰化酶是近几十年来β内酰胺类抗生素领域应用最广、开发最成功的酶之一。伴随着β-内酰胺类抗生素由化学合成法变更为酶法在中国的大规模产业化,得到了充分的开发与应用,取得了成功。青霉素G酰化酶不但用于水解制备6-APA、7-ADCA,更重要的是用于氨苄西林、头孢氨苄、阿莫西林、头孢拉定、头孢克洛等抗生素的制备。本文综述了近15年青霉素G酰化酶在我国研究与应用的历史沿革、基因与蛋白质结构、工业应用表达体系、工业评价标准与进化研究,还对各种突变株在具体医药工业领域的开发应用进行了综述,旨在梳理青霉素G酰化酶结构与性能的进化趋势以及在医药工业领域取得的巨大成就,同时也为相关人员在此领域进行深耕提供参考。     

Enzyme reaction engineering: synthesis of antibiotics catalysed by stabilized penicillin G acylase in the presence of organic cosolvents.

By using very active and very stable penicillin G acylase (PGA)--agarose derivatives we have studied the industrial design of equilibrium-controlled synthesis of lactamic antibiotics. In the presence of high concentrations of organic cosolvents we have carried out the direct enzymatic condensation of phenylacetic acid and 6-aminopenicillanic acid to yield the model antibiotic penicillin G. We have mainly studied the integrated effect of different variables that define the reaction medium on a number of parameters of industrial interest:time course of antibiotic synthesis, highest synthetic yields, stability of the catalyst, and solubility and stability of substrates and products. The main variables tested were the nature and concentration of the organic cosolvent, pH, and temperature. The effects of the variables tested on different parameters were quite different and sometimes opposite. Hence, the optimal experimental conditions for antibiotic synthesis catalysed by PGA were established, as a compromise solution, in order to obtain good values for every parameter of industrial interest. These conditions seem to be important parameters for scale-up (e.g. we have been able to reach more than 95% of synthetic yields with productivities around 0.5 tons of model antibiotic per year per liter of catalyst).     

Growth of Gram-negative bacteria in the presence of organic solvents

The growth behavior of Gram-negative bacteria when exposed to high concentrations (50% v/v) of water-insoluble organic solvents was investigated. The solvents were chosen according to their polarity values as denoted by a logarithmically expressed parameter log P, where P is the partition coefficient of a given solvent in an equimolar mixture of octanol and water. The cell growth was measured by the number of colonies developed on a solid agar medium in direct contact with the solvents. All 31 strains tested showed characteristic growth patterns. The survival and subsequent growth of bacteria increased with the increase in the log P value and was found to be strain specific. For all the strains, 100% cell growth was reached from 0% within 0.1–0.4 log P units. Log P₅₀ values, defined as the log P values at which 50% of the cells form colonies, were determined for each bacterial strain. On the whole, Pseudomonas strains were found to be more resistant to apolar solvents than all other bacteria tested. This resistance was dependent not only on the polarities but also on the toxic nature of different organic solvents, the cell membrane components, and to a limited extent, the growth medium. A tenfold increase in the Mg²⁺ concentration in the growth medium enhanced the solvent resistance of E. coli but had no such effect on Pseudomonads. In general, different growth temperatures had no impact on the solvent resistance of the Gram-negative bacteria tested.     

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     

Dramatic enhancement of enzymatic activity in organic solvents by lyoprotectants

When seven different hydrolytic enzymes (four proteases and three lipases) were lyophilized from aqueous solution containing a ligand, N-Ac-L-Phe-NH(2), their catalytic activity in anhydrous solvents was far greater (one to two orders of magnitude) than that of the enzymes lyophilized without the ligand. This ligand-induced activation was expressed regardless of whether the substrate employed in organic solvents structurally resembled the ligand. Furthermore, nonligand lyoprotectants [sorbitol, other sugars, and poly(ethylene glycol)] also dramaticaliy enhanced enzymatic activity in anhydrous solvents when present in enzyme aqueous solution prior to lyophilization. The effects of the ligand and of the lyoprotectants were nonadditive, suggesting the same mechanism of action. Excipient activated and nonactivated enzymes exhibited identical activities in water. Also, addition of the excipients directly to suspensions of nonactivated enzymes in organic solvents had no appreciable effect on catalytic activity. These observations indicate that the mechanism of the excipient-induced activation is based on the ability of the excipients to alleviate reversible denaturation of enzymes upon lyophilization. Activity enhancement induced by the excipients is displayed even after their removal by washing enzymes with anhydrous solvents. Subtilisin Carlsberg, lyophilized with sorbitol, was found to be a much more efficient practical catalyst than its "regular" counterpart. (c) 1993 John Wiley & Sons, Inc.     

Perspectives for the industrial enzymatic production of glycosides

Glycosides are of commercial interest for industry in general and specifically for the pharmaceutical and food industry. Currently chemical preparation of glycosides will not meet EC food regulations, and therefore chemical preparation of glycosides is not applicable in the food industry. Thus, enzyme-catalyzed reactions are a good alternative. However, until now the low yields obtained by enzymatic methods prevent the production of glycosides on a commercial scale. Therefore, high yields should be established by a combination of optimum reaction conditions and continuous removal of the product. Unfortunately, a bioreactor for the commercial scale production of glycosides is not available. The aim of this article is to discuss the literature with respect to enzymatic production of glycosides and the design of an industrially viable bioreactor system.