Enzymatic hydrolysis of penicillin in mixed ionic liquids/water two-phase system

In this paper, an integrated process involving the mixed ionic liquids/water two-phase system (MILWS) is proposed to improve the efficiency for enzymatic hydrolysis of penicillin G. First, hydrophilic [C4mim]BF4 (1-butyl-3-methylimidazolium tetrafluoraborate) and NaH2PO4 salt form an ionic liquids aqueous two-phase system (ILATPS), which could extract penicillin from its fermentation broth efficiently. Second, a hydrophobic [C4mim]PF6 (1-butyl-3-methylimidazolium hexafluoraphosphate) is introduced into the ionic liquids-rich phase of ILATPS containing penicillin and converses it into MILWS. Penicillin is hydrolyzed by penicillin acylase in the water phase of MILWS at pH 5. The byproduct phenylacetic acid (PAA) is partitioned into the ionic liquids mixture phase, while the intended product 6-aminopenicillanic acid (6-APA) is precipitated at this pH. In comparison with a similar butyl acetate/water system (BAWS) at pH 4, MILWS exhibits two advantages. (1) The selectivity between PAA and penicillin is greatly optimized at pH 5 by varying the mole ratio of [C4mim]PF6/[C4mim]BF4 in MILWS, whereas in BAWS the unalterable nature of the organic solvent restricts the optimized pH for maximum selectivity between PAA and penicillin at pH 4. (2) The pH for 6-APA precipitation in BAWS is 4, whereas it shifts to pH 5 in MILWS due to the complexation between negatively charged 6-APA and the cationic surface of the ionic liquids micelle. As a result, the removal of the two products from the enzyme sphere at relatively high pH is permitted in MILWS, which is beneficial for enzymatic activity and stability in comparison with the acidic pH 4 environment in BAWS.     

Thermodynamics of the conversion of penicillin G to phenylacetic acid and 6-aminopenicillanic acid

The thermodynamics of the enzymatic conversion (penicillin acylase) of aqueous penicillin G to phenylacetic acid and 6-aminopenicillanic acid have been studied using both high-pressure liquid-chromatography and microcalorimetry. The reaction was carried out in aqueous phosphate buffer over the pH range 6.0-7.6, at ionic strengths from 0.10 to 0.40 mol kg-1, and at temperatures from 292 to 322 K. The data have been analyzed using a chemical equilibrium model with an extended Debye-Hückel expression for the activity coefficients. For the reference reaction, penicillin G- (aq) + H2O(l) = phenylacetic acid-(aq) + 6-aminopenicillanic acid-(aq) + H+ (aq), the following parameters have been obtained: K = (7.35 +/- 1.5) X 10(-8) mol kg-1, delta G0 = 40.7 +/- 0.5 kJ mol-1, delta H0 = 29.7 +/- 0.6 kJ mol-1, and delta C0p = -240 +/- 50 J mol-1 K-1 at 298.15 K and at the thermochemical standard state. The extent of reaction for the overall conversion is highly dependent upon the pH.     

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.     

Enzymatic conversion of benzylpenicillin to 6-aminopenicillanic acid in concentrated ultrafiltered broths

Benzylpenicillin filtered broths purified by ultrafiltration and fermented broths clarified by ultrafiltration and afterwards concentrated by reverse osmosis were used directly for enzymatic conversion of benzylpenicillin to 6-aminopenicillanic acid and phenylacetic acid by immobilised penicillin G acylase or amidase. It was concluded that, when the ultrafiltration operation retained 100% of protein, the concentrates from reverse osmosis could be successfully directly fed to the enzymatic reactor, giving high enzymatic conversion yield of benzylpenicillin to 6-aminopenicillanic acid.     

One-pot, two-step enzymatic synthesis of amoxicillin by complexing with Zn2+

A one-pot, two-step enzymatic synthesis of amoxicillin from penicillin G, using penicillin acylase, is presented. Immobilized penicillin acylase from Kluyvera citrophila was selected as the biocatalyst for its good pH stability and selectivity. Hydrolysis of penicillin G and synthesis of amoxicillin from the 6-aminopenicillanic acid formed and d-p-hydroxyphenylglycine methyl ester were catalyzed in situ by a single enzyme. Zinc ions can react with amoxicillin to form complexes, and the yield of 76.5% was obtained after optimization. In the combined one-pot synthesis process, zinc sulfate was added to remove produced amoxicillin as complex for shifting the equilibrium to the product in the second step. By controlling the conditions in two separated steps, the conversion of the first and second step was 93.8% and 76.2%, respectively. With one-pot continuous procedure, a 71.5% amoxicillin yield using penicillin G was obtained.     

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.     

Enzymic acylation of 6-aminopenicillanic acid

The enzymic synthesis of benzylpenicillin from 6-aminopenicillanic acid in the presence of poly (ethylene glycol) has been studied. With equimolar initial concentrations (20 mM) of 6-aminopenicillanic acid and phenylacetic acid a 60% conversion to benzylpenicillin can be achieved at 10°C and pH 5.2 in the presence of 45% (w/v) poly(ethylene glycol). Under these conditions the lactam ring of the benzylpenicillin and 6-aminopenicillanic acid and the enzyme, penicillin acylase (penicillin amidase, penicillin amidohydrolase, EC 3.5.1.11), were more stable than in the absence of the polyol.     

Production of 6-aminopenicillanic acid in aqueous two-phase systems by recombinant Escherichia coli with intracellular penicillin acylase

Bioconversion of penicillin G in PEG 20000/dextran T 70 aqueous two-phase systems was achieved using the recombinant Escherichia coli A56 (ppA22) with an intracellular penicillin acylase as catalyst. The best conversion conditions were attained for: 7% (w/v) substrate (penicillin G), enzyme activity in bottom phase 52 U ml(-1), pH 7.8, temperature 37 degrees C, reaction time 40 min. Five repeated batches could be performed in these conditions. Conversions ratios between 0.9-0.99 mol of 6-aminopenicillanic acid (6-APA) per mol of penicillin G, were obtained and volumetric productivity was 3.6-4.6 micromol min(-1) ml(-1). In addition the product 6-APA could be directly crystallized from the top phase with a purity of 96%.     

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).     

A two-step, one-pot enzymatic synthesis of ampicillin from penicillin G potassium salt

A two-step, one-pot synthesis of ampicillin from penicillin G potassium salt (PGK) in aqueous buffer/organic co-solvent has been achieved. Ethylene glycol (EG) was chosen as the organic co-solvent. Factors including co-solvent content, enzyme loading, reaction temperature and substrate concentration were investigated. The optimum conditions were as follow: pH 8.0 phosphate buffer solution, 50% EG (v/v), 25 °C, 100 mM PGK and 300 mM d-phenylglycine methyl ester (D-PGM), 43.2 IU/ml IPA-750. The maximum yield was 57.3% after a reaction time of 17 h. It is the first report about the synthesis of ampicillin from penicillin G potassium salt in one-pot combining the enzymatic hydrolysis and the subsequent enzymatic condensation, and the novel methodology will have important application in the β-lactam antibiotics industry.     

Application of cross-linked enzyme aggregates of Bacillus badius penicillin G acylase for the production of 6-aminopenicillanic acid

AIMS: Optimization of 6-aminopenicillanic acid (6-APA) production using cross-linked enzyme aggregates (CLEA) of Bacillus badius penicillin G acylase (PAC). METHODS AND RESULTS: CLEA-PAC was prepared using purified/partially purified PAC with phenylacetic acid as active-site blocking agent and glutaraldehyde as cross-linker. Conversion of penicillin G to 6-APA by CLEA-PAC was optimized using response surface methodology (RSM) (central composite rotatable design) consisting of a three-factor-two-level pattern with 20 experimental runs. CONCLUSION: Nearly, 80% of immobilization yield was obtained when partially purified enzyme was used for the preparation of CLEA-PAC. Quantitative conversion of penicillin G to 6-APA was observed within 60 min and the CLEA-PAC was reusable for 20 repeated cycles with 100% retention of enzyme activity. SIGNIFICANCE AND IMPACT OF THE STUDY: The faster conversion of penicillin G to 6-APA by CLEA-PAC and efficient reusability holds a strong potential for the industrial application.     

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.     

Antibacterial and toxicological evaluation of beta-lactams synthesized by immobilized beta-lactamase-free penicillin amidase produced by Alcaligenes sp

Search for anti-beta-lactamase and synthesis of newer penicillin were suggested to overcome resistance to penicillin in chemotherapy. It was found that clavulanic acid, an ant-beta-lactamase was ineffective due to its structural modification by bacteria. Thus, there is a need for the synthesis of newer pencillins. Retro-synthesis was inspired by the success of forward reaction i.e.conversion of penicillin G to 6-aminopenicillanic acid (6-APA) by biological process. In the present study a better enzymatic method of synthesis of newer pencillin by a beta-lactamase-free penicillin amidase produced by Alcaligenes sp. is attempted. Antibacterial and toxicological evaluation of the enzymatically synthesized beta-lactams are reported. Condensation of 6-APA with acyl donor was found to be effective when the reaction is run in dimethyl formamide (DMF 50% v/v) in acetate buffer (25 mM pH 5.0) at 37 degrees C. Periplasm entrapped in calcium alginate exihibited the highest yield (approximately 34%) in synthesis. The minimum inhibitory concentration of the synthetic products against Staphylococcus aureus and Salmonella typhi varied between 20-80 microg/ml. Some of the products exhibited antibacterial activity against enteric pathogens. It was interesting to note that product A was potent like penicillin G. LD50 value of three products (product A, B and C) was more than 12 mg/kg. Furthermore, these synthetic beta-lactams did not exihibit any adverse effect on house keeping enzymes viz., serum glutamate oxalacetate-trans-aminase, serum glutamate pyruvate -trans-aminase, acid phosphatase, alkaline phosphatase of the test animals. The hematological profile (RBC and WBC) of the test animals also remained unaffected.     

Kinetics of the enzymatic synthesis of benzylpenicillin

The kinetics of the enzymatic synthesis of benzylpenicillin catalysed by penicillin amidase (EC 3.5.1.11) from Escherichia coli have been studied. Both free phenylacetic acid (PAA) and its activated derivative, phenylacetylglycine (PAG), were used in the synthesis as acylating agents for 6-aminopenicillanic acid (6-APA). The catalytic rate constants for synthesis carried out at pH 6.0 were 11.2 and 25.2 s⁻¹, respectively, i.e. they are close and have high absolute values. The main feature of the enzymatic synthesis of benzylpenicillin from phenylacetylglycine, compared with the synthesis from phenylacetic acid, is the shape of the progress curve of antibiotic accumulation. In the former case, benzylpenicillin gradually accumulates until equilibrium is reached. Thus, if the reaction is carried out at the thermodynamically optimum pH of synthesis (low pH), penicillin can be obtained in high yield. In the case of phenylacetylglycine, the kinetic curves are more complex and are characterized by a clear-cut maximum. The presence of the maximum, its value and position on the time axis depend on reagent concentration and on the pH used. A kinetic scheme is proposed which describes well the experimental dependencies. The possibility of using activated acid derivatives in synthesis and the advantages of using computer calculations for process optimization are discussed.     

Specificity of Penicillin Acylase of Fusarium and of Penicillium chrysogenum

Extracts containing penicillin acylase were obtained by shaking the mycelium of Fusarium avenaceum and of Penicillium chrysogenum in 0.2 M sodium acetate or sodium chloride solution. The optimum pH for conversion of penicillin V into 6-aminopenicillanic acid (6-APA) by the enzyme of Fusarium was about 7.5, and the reaction velocity was increased by a rise in temperature from 27 to 37 C. Penicillin G and penicillins with an aliphatic side chain were cleaved much less readily than was penicillin V. With the enzyme preparation obtained from a nonpenicillin-producing strain of P. chrysogenum, the reaction rate was higher at pH 8.5 than at pH 7.5 and pH 6.5. The acylase of P. chrysogenum hydrolyzes penicillin V more readily than penicillin G. In a series of aliphatic penicillins, the amount of 6-APA formed through the action of this enzyme increased with the number of carbon atoms of the side chain. Penicillins with a glutaryl or an adipyl group as side chain were unaffected by the enzyme of Fusarium and of Penicillium. No reaction was observed upon incubation of penicillin N (with a D-aminoadipyl side chain) or isopenicillin N (with an L-aminoadipyl side chain) with Fusarium and Penicillium extract. When the carboxy group of the side chain of these penicillins was esterified, formation of 6-APA was observed upon incubation with Penicillium extract, whereas no 6-APA or only very small amounts were obtained by acylase of Fusarium.     

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.     

The isolation and characterization of 60 nm vesicles (''nanovesicles'') produced during ionophore A23187-induced budding of human erythrocytes.

1. Penicillin N was synthesized by coupling alpha-amino-alpha-p-nitrobenzyl-N-p-nitro-benzyloxycarbonyl-D-adipate with 6-aminopenicillanic acid benzyl ester, followed by removal of the protecting groups through hydrogenolysis. 2. alpha-Amino-alpha-p-nitrobenzyl-N-p-nitrobenzyloxycarbonyl-D-[5-14C]adipate was prepared by treating alpha-p-nitrobenzyl-N-p-nitrobenzyloxycarbonyl-D-glutamic acid with [14C]diazomethane followed by rearrangement with silver trifluoromethanesulphonate. 3. Coupling of alpha-amino-alpha-p-nitrobenzyl-N-p-nitrobenzyloxycarbonyl-D-[5-14C]adipate with 6-aminopenicillanic acid benzyl ester gave triprotected [10-14C]penicillin N. 4. 3H was introduced at C-6 of the Schiff's base derivative (10) by oxidation followed by reduction with NaB3H4. 5. The so-derived (6 alpha-3H)-labelled Schiff's base was hydrolysed to give 6-amino [6 alpha-3H]penicillanic acid benzyl ester p-toluenesulphonic acid salt, which after coupling as the free amine with alpha-amino-alpha-p-nitrobenzyl-N-pnitrobenzyloxycarbonyl-D-adipate and then hydrogenolysis, yielded [6alpha-3H]penicillin N. 6. Triprotected [10-14C]penicillin N and triprotected [6alpha-3H]penicillin N in admixture were hydrogenolysed to give [10-14C,6alpha-3H]penicillin N.     

Course of pH during the formation of amoxicillin by a suspension-to-suspension reaction

Amoxicillin can be produced in an enzymatic suspension-to-suspension reaction in which the substrate(s) and product(s) are mainly present as solid particles, while the reaction takes place in the liquid phase. During these suspension-to-suspension reactions different subprocesses take place, such as dissolution/crystallization of substrates and products, enzymatic synthesis of the product(s), and undesired enzymatic hydrolysis of substrates and/or products. All these subprocesses are influenced by pH and also influence the pH because the reactants are weak electrolytes. This paper describes a quantitative model for predicting pH and concentrations of reactants during suspension-to-suspension reactions. The model is based on mass and charge balances, pH-dependent solubilities of the reactants, and enzyme kinetics. For the validation of this model, the kinetically controlled synthesis of amoxicillin from 6-aminopenicillanic acid and D-(p)hydroxyphenylglycine methyl ester was studied. The pH and the dissolved concentrations took a very different course at different initial substrate amounts. This was described quite reasonably by the model. Therefore, the model can be used as a tool to optimize suspension-to-suspension reactions of weak electrolytes.     

Characterization of the beta-lactam binding site of penicillin acylase of Escherichia coli by structural and site-directed mutagenesis studies

The binding of penicillin to penicillin acylase was studied by X-ray crystallography. The structure of the enzyme-substrate complex was determined after soaking crystals of an inactive betaN241A penicillin acylase mutant with penicillin G. Binding of the substrate induces a conformational change, in which the side chains of alphaF146 and alphaR145 move away from the active site, which allows the enzyme to accommodate penicillin G. In the resulting structure, the beta-lactam binding site is formed by the side chains of alphaF146 and betaF71, which have van der Waals interactions with the thiazolidine ring of penicillin G and the side chain of alphaR145 that is connected to the carboxylate group of the ligand by means of hydrogen bonding via two water molecules. The backbone oxygen of betaQ23 forms a hydrogen bond with the carbonyl oxygen of the phenylacetic acid moiety through a bridging water molecule. Kinetic studies revealed that the site-directed mutants alphaF146Y, alphaF146A and alphaF146L all show significant changes in their interaction with the beta-lactam substrates as compared with the wild type. The alphaF146Y mutant had the same affinity for 6-aminopenicillanic acid as the wild-type enzyme, but was not able to synthesize penicillin G from phenylacetamide and 6-aminopenicillanic acid. The alphaF146L and alphaF146A enzymes had a 3-5-fold decreased affinity for 6-aminopenicillanic acid, but synthesized penicillin G more efficiently than the wild type. The combined results of the structural and kinetic studies show the importance of alphaF146 in the beta-lactam binding site and provide leads for engineering mutants with improved synthetic properties.