Bacillus sphaericus Penicillin V Acylase: Purification,Substrate Specificity,and Active-Site Characterization

Penicillin V acylase from Bacillus sphaericus was purified to homogeneity with an overall yield of 15%. The enzyme exhibited comparatively high specificity for penicillin V, penicillin G, and other related compounds being hydrolyzed at less than 10% of the rate of penicillin V. Moreover, the high rate of hydrolysis was observed when the side chain of the substrate molecule was unsubstituted. Lysine-modifying reagents inactivated the enzyme rapidly. Kinetics and titration studies indicated the involvement of lysine in the catalytic activity of the enzyme. Received: 10 July 1996 / Accepted: 26 August 1996     

Computational Multiple Steady States of the Penicillin G Acylase‐Catalyzed Hydrolysis in an Isothermal CFSTR

A family of an enzymatically catalyzed reaction network was studied, which involves the hydrolysis of penicillin G by penicillin G acylase in an isothermal continuous flow stirred tank reactor (CFSTR). This system consisted of 10 coupled non‐linear equations and was found to be capable of exhibiting computational multiple steady states. A set of kinetic parameters determined from the existing experimental data were used to compute a set of rate constants and two corresponding steady states. This suggested that multiple steady states may occur in the system studied. The phenomena of bistability, hysteresis and bifurcation were discussed. Moreover, the capacity of steady state multiplicity was extended to its family of reaction networks.     

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.     

An Eco-Friendly and Sustainable Process for Enzymatic Hydrolysis of Penicillin G in Cloud Point System

Enzymatic hydrolysis of penicillin G by immobilized penicillin acylase in a nonionic surfactant mediated cloud point system was presented. The effect of the operation parameters on equilibrium pH of this enzymatic hydrolysis process without pH control was examined. A relatively high equilibrium pH in cloud point system without pH control can be obtained. The feasibility of recycling utilization of the nonionic surfactant, a novel green solvent, was also investigated experimentally. Enzymatic hydrolysis of penicillin G in a discrete semi-batch mode, which simulates a semi-continuous process, envisages a completely eco-friendly, sustainable and efficient process for production of 6-aminopenicillanic acid.     

Isolation and mapping of a mutant penicillin G acylase with altered substrate specificity from Escherichia coli

Summary Penicillin G acylase of Escherichia coli ATCC 11105 catalyzes hydrolysis as wellas synthesis of penicillin G. In this work a recombinant penicillin G acylase genewas mutagenized in vivo. A mutant with altered penicillin G acylase was selectedby its ability to grow with phthalyl-L-leucine as sole source of leucine. Themutant enzyme obtained was deficient in hydrolyzing penicillin G. A mutation ofGly359 to aspartic acid was mapped first by construction of chimeric pac genescomposed of wild type and mutant DNA, followed by nucleotide sequencing.     

Influence of penicillin instability on interpretation of feedback regulation experiments

Summary The stability of penicillin G during production is reviewed and compared to reports on end-product regulation of penicillin biosynthesis. From this analysis, it appears that penicillin control of its own synthesis when added exogenously at the beginning of the process has not been proven, since the apparent decrease of net accumulation can be explained by gradual hydrolysis of the added penicillin. It is also concluded that the maximum amount of penicillin accumulated normally is not controlled by penicillin, but rather by its stability and the ability of the cells to maintain a high synthetic rate over extended time periods.     

Effects of medium composition on penicillin-induced hydrolysis and loss of RNA and culture turbidity in group A streptococci.

Exposure to penicillin G of exponentially growing cultures of group A streptococci growing in chemically defined medium (CDM) can lead to extensive loss of culture turbidity. Significant reductions in culture turbidity did not accompany comparable treatments of group A streptococci growing in Todd-Hewitt broth (THB). Studies with THB and a high-molecular-weight (greater than 12,000) fraction of THB demonstrated that components in this complex medium inhibited the efflux of RNA hydrolysis products from otherwise intact cells. Hydrolysis products accumulated intracellularly and inhibited the extensive hydrolysis of RNA and consequently the loss of culture turbidity. Results of survival studies with cultures of group A streptococci exposed to penicillin G in THB demonstrated that this treatment protocol produces conditions of phenotypic tolerance relative to exposure in CDM. In combination, these findings provide further support for the hypothesis of RNA hydrolysis as the bactericidal mechanism of penicillin G action in this nonlytic death phenotype.     

ENHANCED PRODUCTION OF 6-AMINOPENICILLANIC ACID IN AQUEOUS METHYL ISOBUTYL KETONE SYSTEM WITH IMMOBILIZED PENICILLIN G ACYLASE

Enzymatic hydrolysis of penicillin G for production of 6-amino-penicillanic-acid (6-APA) was achieved by using penicillin G acylase as catalyst in an aqueous-methylisobutyl ketone (MIBK) system. The optimization was carried out and it was found that the best conversion was improved 10% more than the aqueous system, which was obtained at the conditions: initial pH 8.0, 5.0% (W/V) substrate (penicillin G), and temperature at 35°C, and the ratio of aqueous and organic phase was 3:1. The stability of the biocatalyst was studied at the operational conditions. After 5 cycles of semi-batch reactions, the residual activity of penicillin G acylase was 69.2% of the initial activity. There was no apparent loss of the yield of product. This process has a potential application in the industrial scale production of 6-APA because it simplifies the process effectively.     

Simultaneous extraction and concentration of penicillin G by hollow fiber renewal liquid membrane

In this article, hollow fiber renewal liquid membrane (HFRLM) technique was used for recovery of penicillin G from aqueous solution. The organic solution of 7 vol % di‐n‐octylamine (DOA) + 30 vol % iso‐octanol + kerosene was used as liquid membrane phase, and Na₂CO₃ aqueous solution was used as stripping phase. Experiments were performed as a function of carrier concentration in the organic phase, organic/aqueous volume ratio, pH, and initial penicillin G concentration in the feed phase, pH in the stripping phase, flow rates, etc. The results showed that the HFRLM process was stable and could carry out simultaneous extraction and concentration of penicillin G from aqueous solutions. As a carrier facilitated transport process, the addition of DOA in organic phase could greatly enhance the mass transfer rate; and there was a favorable organic/aqueous volume ratio of 1:20 to 1:30 for this system. The mass transfer flux and overall mass transfer coefficient increased with decreasing pH in the feed phase and increasing pH in the stripping phase, because of variation of the mass transfer driving force caused by pH gradient and distribution equilibrium. The flow rate of the shell side had significant influence on the mass transfer performance, whereas the effect of flow rate of lumen side on the mass transfer performance was slight because of the mass transfer intensification of renewal effect in the lumen side. The results indicated that the HFRLM process was a promising method for the recovery of penicillin G from aqueous solutions. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Treatment of gonorrheal urethritis with spectinomycin hydrochloride

One hundred and eighty-seven males with uncomplicated gonorrheal urethritis were treated with spectinomycin hydrochloride in a dosage of 2 g. given intramuscularly. A failure rate of 3.2% was observed and no complications of therapy were encountered. In addition, 310 strains of N. gonorrhoeae were tested for susceptibility to penicillin G and spectinomycin. All strains were sensitive to 20 μg./ml. of spectinomycin and this susceptibility appeared to decrease as penicillin resistance increased. A greater incidence of relative resistance to penicillin G was observed than in similar studies from other Canadian areas.     

Penicillin hydrolysis rate: Its effect on the kinetics of penicillin fermentation

The influence of the penicillin hydrolysis rate and dilution rate or specific growth rate on the productivity of a penicillin fermentation is quantified. Comparison of the theoretical with the experimental data suggests that hydrolysis largely accounts for the apparent critical minimum growth rate necessary to maintain maximum productivity.     

Selective transformations of penicillins and cephalosporins with pen G acylase

Summary Immobilised Penicillin G acylase from E. coli hydrolyses penicillin and cephalosporin derivatives protected at the carboxy group as the phenylacetoxymethylene esters. The corresponding hydrolysis of penicillin V retains the phenoxyacetyl moiety. Kinetic data of the hydrolysis are reported.     

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.     

Cross-linked aggregates of penicillin acylase: robust catalysts for the synthesis of β-lactam antibiotics

A novel method for the immobilization of penicillin G acylase (penicillin amidohydrolase, E.C. 3.5.1.11) is reported. It involves the physical aggregation of the enzyme, followed by chemical cross-linking to form insoluble cross-linked enzyme aggregates (CLEAs). Compared with conventionally immobilized penicillin G acylases, these CLEAs possess a high specific activity as well as a high productivity and synthesis/hydrolysis (S/H) ratio in the synthesis of semi-synthetic antibiotics in aqueous media. Moreover, they are active in a broad range of polar and apolar organic solvents.     

Alginate oligosaccharides as enhancers of penicillin production in cultures of penicillium chrysogenum

Oligosaccharide fragments were prepared by partial acid hydrolysis of sodium alginate and consisted of oligomannuronate (OM) and oligoguluronate (OG) blocks. Effects of the OM and OG blocks on penicillin G production by P. chrysogenum were investigated. The oligosaccharides were found to cause significant increases in penicillin G yields. OM blocks at concentrations 10 to 100 mug/mL were used to further evaluate the effects of the oligosaccharides, and were found to enhance the production of penicillin G in shaken flask cultures of P. chrysogenum P2 (high penicillin producer) and NRRL 1951 (low penicillin producer) at the test concentrations. There was an approximately 50% maximum increase in penicillin G yield from biomass in P. chrysogenum P2 cultures and 150% in P. chrysogenum NRRL 1951 cultures, when compared to control cultures without the oligosaccharides. (c) 1997 John Wiley & Sons, Inc.     

Kinetic characteristics and enantioselective action of penicillinase in the hydrolysis reaction of N-phenylacetyl derivatives of 1-aminoethylphosphonic acid and its esters

Penicillin acylase from E. coli (EC 3.5.1.11) was found to hydrolyze N-phenylacetylated 1-aminoethylphosphonic acid and its esters. The enzyme preferentially converts the R-form of the substrates: the ratios of the bimolecular rate constants of penicillin acylasecatalyzed hydrolysis of R- and S-forms of 1-(N-phenylacetamino)-ethylphosphonic acid and its dimethyl- and diisopropyl-esters are 58000, 2300, 1800; these derivatives were shown to have the greatest values of the catalytic constants for enzymatic hydrolysis of all known substrates for penicillin acylase: 237, 148 and 134 s-1; the corresponding Km values are 3.7 10(-5), 6.8 10(-4) and 6.2 10(-4) M at pH 7.0. The kinetics of enzymatic hydrolysis of 1-(N-phenylacetamino)-ethylphosphonic acid was investigated up to high degrees of conversion. The inhibition of penicillin acylase by high concentrations of the R-form of the substrate (with substrate inhibition constant of 0.07 M) and competitive inhibition by the reaction product, phenylacetic acid (Ki = 3.5 10(-5) M), was observed.     

Penicillin Acylase Activity of Penicillium chrysogenum

The penicillin acylase activity of Penicillium chrysogenum was studied. Washed mycelial suspensions of a high penicillin-producing and a nonproducing strain were found to be similar in respect to relative acylase activity on benzylpenicillin, 2-pentenylpenicillin, heptylpenicillin, and phenoxymethylpenicillin. The relative rates for both strains, as determined by 6-aminopenicillanic acid formation, were approximately 1.0, 2.5, 3.5, and 6.0 on the penicillins in the order given. The high producing strain formed both 6-aminopenicillanic acid and "natural" penicillins in fermentations to which no side-chain precursor had been added. Therefore, its demonstrated ability to cleave the natural penicillins, 2-pentenylpenicillin and heptylpenicillin, suggests that at least some of the 6-aminopenicillanic acid produced during such fermentations arises from the hydrolysis of the natural penicillins. At pH 8.5, the mycelial acylase activity of the nonproducing strain was about three times that at pH 6.0; at 35 C, it was about 1.5 times as active as it was at 30 C. When tested on penicillin G or V, no differences in either total or specific penicillin acylase activity were observed among mycelia harvested from cultures of the nonproducer to which penicillin G, penicillin V, or no penicillin had been added. Acetone-dried mycelium from both strains displayed acylase activity, but considerably less than that shown by viable mycelium. Culture filtrates were essentially inactive, although a very low order of activity was detected when culture filtrate from the nonproducer was treated with acetone and the acetone-precipitated material was assayed in a minimal amount of buffer.     

Resistance of Escherichia coli to penicillins. V. Physiological comparison of two isogenic strains, one with chromosomally and one with episomally mediated ampicillin resistance

Two essentially isogenic strains of Escherichia coli K-12 were compared: D31 had chromosomally and D1-R1 episomally mediated resistance to ampicillin. The two strains had the same ability to form colonies on ampicillin plates, but in other tests they were quite different. In serial dilution tests as well as in exponentially growing cultures, D1-R1 was far more resistant to ampicillin than was D31. The inoculum effect with D1-R1 was large and with D31 was rather small. On plates, D31 was more resistant to penicillin G than was D1-R1. The penicillinase activity of buffer suspended cells against dl-ampicillin was 15 times higher for D1-R1 than for D31, but the two strains showed about the same rate of hydrolysis of penicillin G. With dl-ampicillin as substrate, for D1-R1 the apparent K(m) was 1.7 x 10(-4)m, whereas D31 gave a slightly sigmoid curve with a half-saturation concentration of about 5 x 10(-3)m. No induction of penicillinase activity was found. When the growth rate was varied by a factor of four, the amount of penicillinase per cell mass was constant in both D1-R1 and D31, whereas in two wild-type strains the amounts of penicillinase increased with increasing growth rates. With exponentially growing D1-R1, ampicillin disappearance started within 3 min, but at low ampicillin concentrations the rate was less than 10% of the rate of hydrolysis by buffer-suspended cells. Before D31 started hydrolysis, there was a lag period that lasted at least one generation and depended on the concentration of ampicillin. After this lag period, the rate of hydrolysis was 10 times higher than that observed with buffer-suspended cells. These differences between growing and nongrowing cells indicate that both the chromosomally and the episomally mediated penicillinases are controlled by some products present in growing cells.     

Improving the industrial production of 6-APA: enzymatic hydrolysis of penicillin G in the presence of organic solvents

The hydrolysis of penicillin G in the presence of an organic solvent, used with the purpose of extracting it from the culture medium, may greatly simplify the industrial preparation of 6-APA. However, under these conditions, PGA immobilized onto Eupergit displays very low stability (half-life of 5 h in butanone-saturated water) and a significant degree of inhibition by the organic solvent (30%). The negative effect of the organic solvent strongly depended on the type of solvent utilized: water saturated with butanone (around 28% v/v) had a much more pronounced negative effect than that of methylisobutyl ketone (MIBK) (solubility in water was only 2%). These problems were sorted out by using a new penicillin G acylase derivative designed to work in the presence of organic solvents (with each enzyme molecule surrounded by an hydrophilic artificial environment) and a suitable organic solvent (MIBK). Using such solvent, this derivative kept its activity unaltered for 1 week at 32 degrees C. Moreover, the enzyme activity was hardly inhibited by the presence of the organic solvent. In this way, the new enzyme derivative thus prepared enables simplification of the industrial hydrolysis of penicillin G.