固定化青霉素酰化酶在光-pH敏感可回用两水相中裂解青霉素G为6-APA

两水相体系在发展中存在的关键问题是相体系回收困难.由于生产成本及降低污染的原因, 用过的相体系需要回收和重复使用.用环境敏感型溶解可逆聚合物形成可回用两水相体系是当前是为可行的回收方法。本文在光敏感可回用高聚物PNBC与pH敏感型可回用高聚物PADB形成的两水相体系中进行固定化青霉素酰化酶的相转移催化青霉素G产生6-APA的反应。在这个两水相体系中,通过优化,在1% NaCl 存在下,６－ＡＰＡ的分配系数可达5.78。催化动力学显示,达平衡的时间近7h,反应最高得率约85.3%（pH 7.8, 20℃）。较相近条件下的单水相反应得率提高近20%。在反应过程中,通过底物及产物的分配系数检测,发现底物分配系数变化不大,而产物6-APA及苯乙酸的分配系数发生很大变化,从而引起产物的得率变化。在两水相中,底物及产物主要分配在上相,固定化酶分配在下相,底物青霉素G进入下相经酶催化产生的6-APA及苯乙酸又转入上相,从而解除了青霉素酰化酶催化反应的底物及产物抑制作用,达到提高产物得率的效果。此外,采用固定化酶较固定化细胞效率高,占用下相体积小,较游离酶稳定性高,且完全单侧分配在下相。因此,在两水相中进行固定化酶的催化反应具有明显的优越性。形成两水相的高聚物PNBC通过488 nm 的激光照射或经滤光的450nm 光源照射得到回收;pH敏感型成相聚合物PADB可通等电点 4.1沉淀可实现循环利用,高聚物的回收率在95%-98%之间,按此回收率计算,聚合物可使用60次以上。     

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%.     

Immobilization of permeabilized Escherichia coli cells with penicillin acylase activity.

Escherichia coli cells with penicillin acylase activity were sequentially treated at pH 7.8 with aqueous solutions of N-cetyl-N,N,N-trimethylammonium bromide and glutaraldehyde and then immobilized within porous polyacrylamide beads. The immobilized whole cells showed enhanced hydrolysis rates in the conversion of benzylpenicillin to 6-aminopenicillanic acid (6-APA) compared to untreated cells immobilized and used under identical conditions. The immobilized system showed no apparent loss in enzyme activity when used repeatedly over 90 cycles for 6-APA production from 4% benzylpenicillin.     

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.     

Formation of 6-Aminopenicillanic Acid, Penicillins, and Penicillin Acylase by Various Fungi

Several penicillin-producing fungi were examined for ability to produce 6-aminopenicillanic acid (6-APA) and penicillin acylase. 6-APA was found in corn steep liquor fermentations of Trichophyton mentagrophytes, Aspergillus ochraceous, and three strains of Penicillium sp. 6-APA was not detected in fermentations of Epidermophyton floccosum although penicillins were produced. 6-APA formed a large part of the total antibiotic production of T. mentagrophytes. The types of penicillins produced by various fungi were identified by paper chromatography, and it was found that all cultures produced benzylpenicillin. T. mentagrophytes and A. ochraceous showed increased yields of benzylpenicillin and the formation of phenoxymethylpenicillin in response to the addition to the fermentation medium of phenylacetic acid and phenoxyacetic acid, respectively. Washed mycelia of the three Penicillium spp. and two high penicillin-yielding strains of P. chrysogenum possessed penicillin acylase activity against phenoxymethylpenicillin. A. ochraceous, T. mentagrophytes, E. floccosum, and Cephalosporium sp. also had penicillin acylase activity against phenoxymethylpenicillin. Only two of the above fungi, T. mentagrophytes and E. floccosum, showed significant penicillin acylase activity against benzylpenicillin; in both cases it was very low. The acylase activity of A. ochraceous was considerably increased by culturing in the presence of phenoxyacetic acid. It is concluded that 6-APA frequently but not invariably accompanies the formation of penicillin, and that penicillin acylase activity against phenoxymethylpenicillin is present in all penicillin-producing fungi.     

颗粒状固定化青霉素酰化酶的研究

将巨大芽孢杆菌 (Bacillusmegaterium)胞外青霉素酰化酶通过共价键结合到聚合物载体EupergitC颗粒环氧基团上 ,制成的颗粒状固定化青霉素酰化酶表现活力达 1 40 0 μ/g左右。固定化酶水解青霉素的最适 pH8 0 ,最适温度为 55℃。在pH6 0～ 8 5、温度低于 40℃时固定化酶活力稳定。在 pH8 0、温度 37℃时 ,固定化酶对青霉素的表现米氏常数Ka为 2×1 0 - 2 mol/L ;苯乙酸为竞争性抑制剂 ,抑制常数Kip为 2 8× 1 0 - 2 mol/L ;6 APA为非竞争性抑制剂 ,抑制常数Kia为 0 1 2 5mol/L。固定化酶水解青霉素 ,投料浓度为 8% ,在使用 2 0 0批后 ,保留活力 80 %左右 ,6 APA收率平均达 89 48%。     

Mutagenic effect of acridine orange on the expression of penicillin G acylase and beta-lactamase in Escherichia coli

AIMS: The present work aimed to improve the production of penicillin G acylase (PGA) and reduce the beta-lactamase activity through acridine orange (AO) induced mutation in Escherichia coli. METHODS AND RESULTS: Three wild E. coli strains BDCS-N-FMu10, BDCS-N-S21 and BDCS-N-W50, producing both the enzymes PGA and beta-lactamase were treated by AO. Minimum inhibitory concentration of AO was 10 microg ml(-1) and it was noted that bacterial growth was gradually suppressed by increasing the concentration of AO from 10 to 100 microg ml(-1). The highest concentration that gave permissible growth rate was 50 microg ml(-1). The isolated survivals were screened on the bases of PGA and beta-lactamase activities. Among the retained mutants, the occurrence of beta-lactamase deficient ones (91%) was significantly higher than penicillin acylase deficient ones (27%). CONCLUSIONS: In seven of the mutants, PGA activity was enhanced with considerable decrease in beta-lactamase activity. One of the mutant strains (BDCS-N-M36) exhibited very negligible expression of beta-lactamase activity and twofold increase in PGA activity [12.7 mg 6-amino-penicillanic acid (6-APA) h(-1) mg(-1) wet cells] compared with that in the wild-type strain (6.3 mg 6-APA h(-1) mg(-1) wet cells). SIGNIFICANCE AND IMPACT OF THE STUDY: The treatment of E. coli cells with AO resulted in mutants with enhanced production of PGA and inactivation of beta-lactamase. These mutants could be used for industrial production of PGA.     

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.     

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.     

Penicillin Acylase of Pseudomonas melanogenum KY 3987

Partially purified penicillin acylases (EC 3.5.1.11) were prepared from Pseudomonas melanogenum KY 3987 and Kluyvera citrophila KY 3641 capable of synthesizing d(–)-α-amino-benzylpenicillin (APc) from 6-aminopenicillanic acid (6-APA) and phenylglycine methyl ester. As the cell-free extract of P. melanogenum contained high levels of penicillinase (EC 3.5.2.6), the acylase was separated completely from the penicillinase by use of Sephadex column chromatography or electrofocusing. The most salient property of the P. melanogenum penicillin acylase was its substrate specificity to penicillin substrates: it could form 6-APA only from APc but not from penicillin G, penicillin V and p-aminobenzylpenicillin, whereas the K. citrophila acylase acted on all of these penicillins. The P. melanogenum enzyme is hence considered a novel type of penicillin acylase.     

Highly efficient synthesis of ampicillin in an "aqueous solution-precipitate" system: repetitive addition of substrates in a semicontinuous process

The synthesis of ampicillin catalyzed by Escherichia coli penicillin acylase was optimized in an aqueous system with partially dissolved antibiotic nucleus 6-aminopenicillanic acid (6-APA). The yields of both 6-APA and acyl donor could be improved by repetitively adding substrates to the reaction, allowing the concentration of 6-APA to remain saturated throughout. In this reaction concept, with four subsequent additions of substrates, 97% conversion of 6-APA and 72% of D-(-)-phenylglycine methyl ester (D-PGM) to ampicillin was achieved. The synthetic potential of this concept was estimated using a mathematical model which showed that by increasing the amount of added substrates a nearly quantitative conversion of 6-APA and 85% conversion of acyl donor into ampicillin could be achieved.     

Enzymatic conversion in aqueous two-phase systems: deacylation of benzylpenicillin to 6-aminopenicillanic acid with penicillin acylase

The conversion of benzylpenicillin (BP) to 6-aminopenicillanic acid (6-APA) using penicillin acylase (penicillin amidohydrolase, EC 3.5.1.11) has been studied in aqueous two-phase systems. In a system composed of 8.9% (w/w) PEG 20000/7.6% (w/w) potassium phosphate the enzyme was almost completely partitioned to the bottom phase (K < 0.01), which allowed repeated batch conversions, recirculating the enzyme several times. The initial specific productivities were 0.31–1.47 μmol 6-APA mg protein^?1 min^?1 in repeated conversions over five steps. The yield obtained from the top phase was 0.47–0.71 mol 6-APA mol BP^?1. The results are discussed in relation to recirculating the enzyme by immobilizing it to a solid matrix. Despite the high phosphate concentration in the bottom phase the system needs to be titrated in order for the reaction to proceed. Titration of the top phase alone protected the enzyme from denaturation by strong alkali used for the titration.     

生物法合成达泊西汀

通过固定化青霉素G酰化酶(PGA)对(±)-N-苯乙酰基-3-氨基-3-苯基丙酸进行酶法拆分,得到合成达泊西汀的中间体(S)-3-氨基-3-苯基丙酸,(S)-3-氨基-3-苯基丙酸经过还原、甲基化、缩合等多步化学合成得到最终产物达泊西汀。(±)-N-苯乙酰基-3-氨基-3-苯基丙酸的最佳拆分条件:底物(±)-N-苯乙酰基-3-氨基-3-苯基丙酸2.83 g,固定化的青霉素酰化酶2.66 g,pH 7.5,25℃反应4 h,(S)-3-氨基-3-苯基丙酸收率为89.4%,e.e.值99.3%。达泊西汀的总收率25.5%,e.e.值96.7%。     

Biotransformation of penicillin V to 6-aminopenicillanic acid using immobilized whole cells of E. coli expressing a highly active penicillin V acylase

The production of 6-aminopenicillanic acid (6-APA) is a key step in the manufacture of semisynthetic antibiotics in the pharmaceutical industry. The penicillin G acylase from Escherichia coli has long been utilized for this purpose. However, the use of penicillin V acylases (PVA) presents some advantages including better stability and higher conversion rates. The industrial application of PVAs has so far been limited due to the nonavailability of suitable bacterial strains and cost issues. In this study, whole-cell immobilization of a recombinant PVA enzyme from Pectobacterium atrosepticum expressed in E. coli was performed. Membrane permeabilization with detergent was used to enhance the cell-bound PVA activity, and the cells were encapsulated in calcium alginate beads and cross-linked with glutaraldehyde. Optimization of parameters for the biotransformation by immobilized cells showed that full conversion of pen V to 6-APA could be achieved within 1?hr at pH 5.0 and 35°C, till 4% (w/v) concentration of the substrate. The beads could be stored for 28 days at 4°C with minimal loss in activity and were reusable up to 10?cycles with 1-hr hardening in CaCl₂ between each cycle. The high enzyme productivity of the PVA enzyme system makes a promising case for its application for 6-APA production in the industry.     

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.     

Some Problems Involved in Ampicillin Formation by Kluyvera’s Penicillin Acylase

The cell growth of Kluyvera citrophila KY3641, capable of producing α-aminobenzyl-penicillin (APc) from 6-aminopenicillanic acid (6-APA) and phenylglycine, was stimulated by glutamic acid, serine or proline, or by pH control with tartaric acid or fumaric acid.

Penicillinase produced in an early stage of growth or pH-controlled culture was inactivated by alkaline treatment (incubation of cells at 40°C for 5 to 24 hr in pH 7.5 to 9.5) without inactivation of penicillin acylase. Surface active agents enhanced APc production. On the other hand, phenylalanine and some inorganic compounds inhibited this production.

This bacterium formed APc from penicillin G, but amounts of APc formed were only 9 μg from 20 mg of penicillin G.     

Immobilization of penicillin acylase on acrylic carriers

Penicillin acylase obtained from E. Coli (E. C. 3.5.1.11) was covalently bound via glutaric aldehyde to acrylic carriers crosslinked with divinylbenzene or ethylene glycol dimethacrylate. The best enzymatic preparation was obtained by using ethyl acrylate/ ethylene glycol dimethacrylate copolymer. 1 cm³ of the carrier bound 6.4 mg of protein, having 72% activity in relation to the native enzyme. The preparation lost only 10% of its initial activity after 100 d of storage at 4°C. A negligible effect of immobilization on the enzyme activity at different temperatures or pH as well as significant increase of the stability of the immobilized enzyme at elevated temperatures were observed.Abbreviations BA butyl acrylate - AE ethyl acrylate - PA penicillin acylase - 6-APA 6-aminopenicillanic acid - EGDMA ethylene glycol dimethacrylate - DVB divinylbenzene     

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.     

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.     

Simple strategy of reactivation of a partially inactivated penicillin g acylase biocatalyst in organic solvent and its impact on the synthesis of β‐lactam antibiotics

Some reactions of organic synthesis require to be performed in rather aggressive media, like organic solvents, that frequently impair enzyme operational stability to a considerable extent. We have studied the option of developing a reactivation strategy to increase biocatalyst lifespan under such conditions, under the hypothesis that organic solvent enzyme inactivation is a reversible process. Glyoxyl agarose immobilized penicillin G acylase and cross‐linked enzyme aggregates of the enzyme were considered as biocatalysts performing in dioxane medium. Reactivation strategy consisted in re‐incubation in aqueous medium of the partly inactivated biocatalysts in organic medium, best conditions of reactivation being studied with respect to dioxane concentration and level of enzyme inactivation attained prior to reactivation. Best results were obtained with glyoxyl agarose immobilized penicillin G acylase at all levels of residual activity studied, with reactivations up to 50%; for the case of a biocatalyst inactivated down to 75% of its initial activity, full recovery of enzyme activity was obtained after reactivation. The potential of this strategy was evaluated in the thermodynamically controlled synthesis of deacetoxycephalosporin G in a sequential batch reactor operation, where a 20% increase in the cumulative productivity was obtained by including an intermediate stage of reactivation after 50% inactivation. Biotechnol. Bioeng. 2009;103: 472–479. © 2009 Wiley Periodicals, Inc.