Physical and reactive extraction equilibria of penicillin G in a hydrogen-bond acceptor solvent system

Physical and reactive extraction equilibria of penicillin G were investigated experimentally and theoretically in the existence of n-butyl acetate as a hydrogen-bond acceptor solvent. Physical extraction equilibrium experiments were carried out varying the pH of aqueous phase and overall penicillin concentration. We compared the experimental data with the calculated results from four physical extraction equilibrium models suggested here and obtained the most reasonable model. Also, penicillin G was reactively extracted using Amberlite LA-2 in n-butyl acetate. The experimental variables were pH of the aqueous phase, overall amine concentration, and overall penicillin concentration. A combined equilibrium model including our physical extraction equilibrium expression and the reactive extraction equilibrium expression suggested by Reschke and Schügerl was used so as to analyze the current reactive extraction equilibrium system. The calculated results from the reactive extraction equilibrium model were in good agreement with the experimental data.     

Recovery of penicillin G from fermentation broth with reactive extraction in a mixer-settler

Summary In a laboratory countercurrent mixer-settler, penicillin was recovered from its fermentation broth by extraction with Amberlite LA-2 in n-butylacetate at pH 5.0 and reextracted from the ion-pair complex containing a solvent phase with a buffer at 7.2–7.5 with an overall degree of extraction above 90 %.Symbols A amine - AHP complex - c concentration - C partition coefficent - E degree of extraction - HP penicillin acid - K_G equilibrium constant - P, P^– penicillin acid anion Indices aq aqueous phase - org organic phase - A amine - AHP complex - G overall - HP free acid - P penicillin     

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.     

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     

Removal of organic solvent from antibiotics with supercritical carbon dioxide

Organic solvents were rapidly extracted from penicillin G potassium and streptomycin sulfate with supercritical carbon dioxide (SC-CO₂) at 200 atm and 35°C without loss of antibiotic activities. The amounts of organic solvents remaining in the antibiotics depended upon pressure and temperature for a given extraction time. A semilogarithmic plot of remaining amounts of organic solvents against extraction time gave a straight line in the early extraction stage, allowing prediction of the extraction time required for decreasing amounts of organic solvent. The addition of water as an entrainer to SC-CO₂ resulted in a significant increase in extraction rates.     

Reactive extraction of penicillin G in a pilot plant Karr-column II. Fermentation broths

Summary Penicillin G was extracted from mycelfree fermentation broths by means of the carrier (Amberlite LA-2) in n-butylacetate at pH 5 in a 7.6 m high pilot plant Karr-column with degrees of extraction E=98–99% and penicillin enrichments up to 3. The reextraction was carried out with phosphate buffer at pH-values above 7.5 with degree of extractions E=86–88% and penicillin enrichments up to 3. The penicillin and carrier losses were negligible. The influence of the process variables on the extraction degree was investigated. The penicillin extraction of the model medium and the fermentation broths were compared. Recommendations are given for the optimal penicillin recovery with reactive extraction.Symbols a specific interfacial area with regard to the volume of the continuous phase - cA concentration of carrier - cAHP,O concentration of complex in feed - cP,cP,O concentration of penicillin acid anion in theaqueous phase, in the feed - d ₃₂ Sauter droplet diameter - E degree of extraction - f stroke frequency - V _aq throughput of the aqueous phase - V ₀ throughput of the organic phase - Z dimensionsless longitudinal coordinate of the column with regard to its active length (4m) - holdup of the organic phase     

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.     

Determination of penicillin G in bovine plasma by high-performance liquid chromatography after pre-column derivatization

A simple, selective, and sensitive liquid chromatographic method with ultraviolet detection was developed for the analysis of penicillin G in bovine plasma. The assay utilizes a simple extraction of penicillin G from plasma (with a known amount of penicillin V added as internal standard) with water, dilute sulphuric acid and sodium tungstate solutions, followed by concentration on a conditioned C₁₈ solid-phase extraction column. After elution with 500 μl of elution solution, the penicillins are derivatized with 500 μl of 1,2,4-triazole—mercuric chloride solution at 65°C for 30 min. The penicillin—mercury mercaptide complexes are separated by reversed-phase liquid chromatography on a C₁₈ column. The method, which has a detection limit of 5 ng/ml (ppb) in bovine plasma, was used to quantitatively measure the concentrations of penicillin G in plasma of steers at a series of intervals after the intramuscular administration of a commercial formulation of procaine penicillin G.     

Novel reactive perstraction system applied to the hydrolysis of penicillin G

The activity of penicillin acylase has been studied in aqueous and organic solvents, as free enzyme as well as immobilized within the membrane of liquid-core capsules. The activity of the enzyme is inhibited by the accumulation of the products of the hydrolysis reaction, namely phenyl acetic acid (PAA). In order to overcome this inhibition a range of organic solvents were tested for use in in situ product recovery. Of these solvents dibutyl sebacate (DBS) was chosen due to the rapid extraction rate, the high logP and to facilitate capsule production. The extraction efficiency at pH 3.5 for PAA was >80% for phase ratios of >50% free solvent with partition coefficients of 8 and 0.7 for PAA and penicillin G (PenG), respectively, thereby showing that PAA could be selectively extracted at pH 3.5 and 25 degrees C. Liquid-core capsules containing DBS were shown to efficiently remove PAA selectively and the PAA could be effectively back-extracted and the capsules re-used in a three-stage process resulting in high product separation. Immobilization of penicillin acylase onto the capsule membranes resulted in increased operational stability of the enzyme and a very high enzyme activity. Over 53.3% of the PAA formed could be recovered in the capsule core with a concentration over sevenfold higher than in the aqueous phase. Higher extraction efficiencies could be obtained by varying the substrate concentration and number of capsules. The enzyme immobilized on capsules could be stored for over 4 months at pH 8 and 4 degrees C with no loss of activity. Over 80% of the initial activity could be recovered over five repeated batch cycles of the bioconversion process. The importance of capsular perstraction and reactive capsular perstraction has been clearly demonstrated.     

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.     

高浓度底物下青霉素扩环酶的活性评价与底物抑制现象

本文对青霉素扩环酶(Penicillin expandase,也称Deacetoxycephalosporin C synthase,DAOCS)在高浓度青霉素G下的底物抑制现象进行初步评价与表征,筛选适合工业应用条件的高活力突变体。我们通过HPLC对已报道的几个DAOCS高活力突变体在青霉素G浓度5.6至500 mmol/L间的比活力进行定量测定,并与不同催化反应动力学模型的理论推测变化趋势比较,发现DAOCS野生型酶及高活力突变体H4、H5、H6与H7在高浓度青霉素G条件下均表现出明显的底物抑制现象,但是变化趋势不同。野生型酶与突变体H4的比活力先上升后下降,与竞争性抑制模型预测不符。突变体H5、H6与H7的比活力变化呈现更复杂的变化趋势。在所有测试的突变体中,H6的活性显著高于其他突变体酶。青霉素G对野生型DAOCS的底物抑制现象符合非竞争性抑制模型的预测。而部分突变体表现出复杂的底物抑制行为,表明其具有更复杂的作用机制。在高底物浓度下筛选具有较强催化活性的青霉素扩环酶突变体对于推动其在工业生产中的应用具有重要指导作用。     

Reactive extraction of penicillin G in a pilot plant Karr-column

Summary Penicillin G was extracted from a model medium with a secondary amine (Amberlite LA-2) as carrier in n-butylacetate as solvent in a 7.6 m high pilot plant Karr-column at different stroke frequencies, throughput of the phases, concentrations of Penicillin G and carrier and ratios of the throughputs of the aqueous and organic phases. Up to penicillin concentrations of 30 gl^–1, throughputs of the aqueous phase of 100 lh^–1 and throughput ratios of the aqueous phase-to-organic phase of 3, very high degrees of extraction (99%) can be achieved with a penicillin loss below 1%.Symbols a specific interfacial area with regard to the volume of the continuous phase - C partition coefficient - cA, cA, i concentration of carrier (sec. amine) in the bulk at the interface - cAHP, cAHP, i concentration of complex in the bulk at the interface - cH proton concentration - cHP_a, cHP_a,i concentration of free acid in the bulk of the aqueous phase at the interface - cHP_o, cHP_{o, i} concentration of free acid in the bulk of the organic phase, at the interface - cP, cP, i concentration of acid anions in the bulk of the aqueous phase, at the interface - d₃₂ Sauter droplet diameter - E degree of extraction - f stroke frequency - KG reaction equilibrium constant - K_phys distribution coefficient - N number of stages in cascade - t mean residence time of the aqueous phase - _aq throughput of the aqueous phase - _o throughput of the organic phase - Z dimensionless longitudinal coordinate of the column with regard to its active length (4 m) - holdup of the organic phase     

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.     

High-performance liquid chromatographic identification of beta-lactam antibiotics produced by dermatophytes

Thirteen of 48 dermatophyte isolates were found by bioassay to produce beta-lactam antibiotics and seven produced other antibiotics. Estimation and detection of specific beta-lactams in culture broths by derivatization and HPLC was only possible following concentration and extraction procedures. Analysis of the concentrated broths demonstrated the production of penicillin X and penicillin G by two Trichophyton mentagrophytes strains and by one Microsporum canis strain; one further T. mentagrophytes strain produced only penicillin X. Additions of the beta-lactam side-chain precursors, phenylacetic acid and phenoxyacetic acid, to fermentation media failed to increase the antibiotic titres.     

High-performance liquid chromatographic identification of beta-lactam antibiotics produced by dermatophytes

Thirteen of 48 dermatophyte isolates were found by bioassay to produce beta-lactam antibiotics and seven produced other antibiotics. Estimation and detection of specific beta-lactams in culture broths by derivatization and HPLC was only possible following concentration and extraction procedures. Analysis of the concentrated broths demonstrated the production of penicillin X and penicillin G by two Trichophyton mentagrophytes strains and by one Microsporum canis strain; one further T. mentagrophytes strain produced only penicillin X. Additions of the beta-lactam side-chain precursors, phenylacetic acid and phenoxyacetic acid, to fermentation media failed to increase the antibiotic titres.     

Engineering the Substrate Specificity of a Thermophilic Penicillin Acylase from Thermus thermophilus

A homologue of the Escherichia coli penicillin acylase is encoded in the genomes of several thermophiles, including in different Thermus thermophilus strains. Although the natural substrate of this enzyme is not known, this acylase shows a marked preference for penicillin K over penicillin G. Three-dimensional models were created in which the catalytic residues and the substrate binding pocket were identified. Through rational redesign, residues were replaced to mimic the aromatic binding site of the E. coli penicillin G acylase. A set of enzyme variants containing between one and four amino acid replacements was generated, with altered catalytic properties in the hydrolyses of penicillins K and G. The introduction of a single phenylalanine residue in position α188, α189, or β24 improved the K_m for penicillin G between 9- and 12-fold, and the catalytic efficiency of these variants for penicillin G was improved up to 6.6-fold. Structural models, as well as docking analyses, can predict the positioning of penicillins G and K for catalysis and can demonstrate how binding in a productive pose is compromised when more than one bulky phenylalanine residue is introduced into the active site.     

Simultaneous determination of seven penicillins in muscle, liver and kidney tissues from cattle and pigs by a multiresidue high-performance liquid chromatographic method

A high-performance liquid chromatographic (HPLC) method based on solid-phase extraction (SPE) was developed for determination of amoxicillin, penicillin G (benzylpenicillin), ampicillin, oxacillin, cloxacillin, nafcillin and dicloxacillin in muscle, liver and kidney tissues of pigs and cattle. The compounds were extracted in aqueous solution by precipitation of organic materials with a mixture of sulphuric acid and sodium tungstate. The extract was cleaned up by SPE on a divinylbenzene-co-N-vinylpyrrolidone polymeric sorbent. Further clean-up was performed by liquid–liquid partition with diethyl ether. The extract was derivatised with benzoic anhydride and 1,2,4-triazole mercury (II) reagent. Chromatography was performed by reversed-phase gradient HPLC on a C₁₈ column with ultraviolet detection at 323 nm. The limits of detection estimated by a conservative model were in the range 8.9–11.1 μg/kg for amoxicillin, penicillin G, ampicillin, oxacillin, cloxacillin and nafcillin and 18.3–20.9 μg/kg for dicloxacillin. The mean recovery range was 66–77% for amoxicillin, 73–75% for penicillin G, 81–82% for ampicillin, 73–76% for oxacillin, 74–75% for cloxacillin, 66–72% for nafcillin and 58–65% for dicloxacillin.     

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.     

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.     

Alterations induced by penicillin in the protein profile and cell structure of Group GStreptococcus

We investigated the effect of a subminimal concentration of penicillin on the ultrastructure and protein profile of Group G streptococci. In cells treated with penicillin (1/3 MIC), the protein content increased by 50%, and several protein bands with a molecular mass of 14–70 kDa were detected. In the hydrophilic phase, carbohydrate-containing proteins were detected by PAS staining, and in the hydrophobic phase, a group of proteins that reacted strongly with homologous antisera were observed. In terms of cell structure, Triton X-114 extraction was found to induce alterations in the cross wall of untreated cells. In bacteria treated with penicillin but not extracted with Triton X-114, the cell wall was observed to detach itself, and regions with reduced amounts of cellular material appeared in the cytoplasm. After Triton-X114 extraction, these penicillin-treated cells exhibited profound morphological changes, leading in some cases to lysis.