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%.     

Technical improvement in the purification of enzymes from red algae using an aqueous two-phase partitioning system

The effective elimination of phycobiliproteins from crude enzyme preparation of the red alga Caloglossa continua (Okamura) King et Puttock (Ceramiales, Florideophyceae) was investigated in an aqueous two‐phase partitioning system (ATPS) by changing the concentrations of polyethylene glycol (PEG) and ammonium sulfate (AS). The phycobiliproteins shifted from the AS‐rich lower phase to the PEG‐rich upper phase in high PEG and AS concentrations. The best ATPS condition for the elimination of phycobiliproteins from the lower phase was obtained by the combination of 20% (weight/volume; w/v) PEG and 16% (w/v) AS. However, the recovery of aldolase and mannitol‐1‐phos‐phatase activities was significantly reduced. For purification of the enzymes, a combination of 15% (w/v) PEG and 16% (w/v) AS was the best ATPS condition, because a high specific activity and recovery of the enzymes were obtained. Under these conditions, 98% of the phycobiliproteins were removed from the lower phase. Therefore, the ATPS proved to be a very useful method as a first step in the purification of enzymes from red algae.     

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.     

Enhanced production of penicillin G acylase from a recombinant Escherichia coli

Penicillin G acylase (pac) gene was cloned into a stable asd ⁺ vector (pYA292) and expressed in Escherichia coli. This recombinant strain produced 1000 units penicillin G acylase g^–1 cell dry wt, which is 23-fold more than that produced by parental Escherichia coli ATCC11105. This enzyme was purified to 16 units mg^–1 protein by a novel two-step process.     

雷氏普罗威登斯菌青霉素G酰化酶基因在大肠杆菌中的克隆与表达

利用PCR和分子克隆技术从雷氏普罗威登斯菌（Prouidencia rettgeri)(ATCC29944)的基因组DNA中获得一个青霉素G酰化酶（penicillinGacylase,PGA)基因并将其装入表达质粒pET24a。携带有重组质粒pETPGA的Escherichia coli基因工程菌BL21（DE3）/pETPGA实现了PGA的高效表达,对发酵条件的研究表明基因工程菌在24℃,添加5g/L甘油条件下以1.0mmol/LIPTG诱导1.5h酶活力即达到993.4U/L,比野生菌酶活力（15U/L）提高了66倍。     

Stabilization of heterodimeric enzyme by multipoint covalent immobilization: Penicillin G acylase from Kluyvera citrophila

We have developed a strategy for immobilization-stabilization of penicillin G acylase (PGA) from Kluyvera citrophila by controlled multipoint covalent attachment to agarose-aldehyde gels. This enzyme is composed by two dissimilar subunits noncovalently bound. Thus, in this article we establish clear correlations between enzyme stabilization and the multipoint immobilization and/or between enzyme stabilization and the involvement of the two subunits in the attachment of them to the support. We have demonstrated that important thermal stabilizations of derivatives were only obtained through a very intense enzyme-support multipoint attachment involving the whole enzyme molecule. In this way, we have prepared derivatives preserving more than 90% of catalytic activity and being more than 1000-fold more stable than soluble and one-point attached enzyme. In addition, the involvement of the two subunits in the covalent attachment to the support has proved to be essential to develop interesting strategies for reactivation of inactivated enzyme molecules [e.g., by refolding of immobilized PGA after previous unfolding with urea and sodium dodecyl sulfate (SDS)]. (c) 1993 John Wiley & Sons, Inc.     

Continuous extraction of β-d-galactosidase from Escherichia coli in an aqueous two-phase system: effects of biomass concentration on partitioning and mass transfer

High concentrations of Escherichia coli disintegrate move the binodial of a poly(ethylene glycol) (PEG) 4000/potassium phosphate aqueous two-phase system towards lower concentrations. It has also been shown that the yield and purification factor of β-d-galactosidase (β-d-galactoside galactohydrolase, EC 3.2.1.23) in the PEG phase was gradually improved by moving the experimental system to a composition closer to the binodial. The mass transfer rates of cell debris, total protein, β-d-galactosidase and DNA have been studied and were found to be fast enough to reach equilibrium between the phases after 1.9 s of mixing in a static mixer with 24 mixing elements. A continuous extraction process for β-d-galactosidase from E. coli has been designed on the basis of these studies with a mean residence time of 6.3 min from the disintegrator inlet to the β-d-galactosidase containing PEG-phase outlet of the centrifuge. This PEG phase contained 83.5% of the total β-d-galactosidase with a purification factor of 13.6, and only 2.8% of the total protease activity of the disintegrate. All cell debris and almost all DNA were confined to the potassium phosphate phase.     

Immobilization of penicillin G acylase on aminoalkylated polyacrylic supports

A procedure is described for the immobilization of penicillin G acylase (PA) on Amberlite XAD7 modified by transamidation with 1,2-ethylenediamine and activated with glutaraldehyde. Reduction with sodium borohydride of the Schiff's bases formed between the amino groups of the protein and glutaraldehyde results in a dramatic improvement of the operational stability of the immobilized enzyme without affecting the catalytic activity. The enzyme kept in presence of the substrate, penicillin G, displays an increased stability with respect to that stored in pure phosphate buffer solution. The inactivation kinetics of the immobilized preparations of PA, determined in a continuous fixed bed reactor, as well as a discontinuous batch reactor, are reported.     

Application of surface response analysis to the optimization of penicillin acylase purification in aqueous two-phase systems

Penicillin acylase purification from an Escherichia coli crude extract using PEG 3350–sodium citrate aqueous two-phase systems (ATPS) was optimized. An experimental design was used to evaluate the influence of PEG, sodium citrate and sodium chloride on the purification parameters. A central composite design was defined centred on the previously found conditions for highest purification from an osmotic shock extract. Mathematical models for the partition coefficient of protein and enzyme, balance of protein and enzyme, yield and purification were calculated and statistically validated. Analysis of the contours of constant response as a function of PEG and sodium citrate concentrations for three different concentrations of NaCl revealed different effects of the three factors on the studied parameters. A maximum purification factor of 6.5 was predicted for PEG 3350, sodium citrate and NaCl concentrations of 15.1, 11.0 and 8.52% respectively. However, under these conditions the predicted yield was 61%. A better compromise between these two parameters can be found by superimposing the contour plots of the purification factor and yield for 10.3% NaCl. A region in the experimental space can be defined where the purification factor is always higher than 5.5 with yields exceeding 80%.     

Stabilization and functional properties of Escherichia coli penicillin G acylase by covalent conjugation of anionic polysaccharide carboxymethylcellulose

The stabilization of Escherichia coli penicillin G acylase (PGA) conjugated with carboxymethylcellulose (CMC) against temperature and pH was studied. The 2,3-dialdehyde derivative of CMC obtained by periodate oxidation was covalently conjugated to PGA via Schiff's base formation. The inactivation mechanism of both native and CMC-conjugated PGA appeared to obey first order inactivation kinetics during prolonged incubations at 40–60 °C and in the pH range 4–9. Inactivation rate constants of conjugated enzyme were always lower, and half-life times were always higher than that of native PGA. The activation free energy of inactivation (G _i values) of CMC-conjugated enzyme were found to be always higher than that of native PGA at all temperatures and pH values studied as another indicator of enzyme stabilization. Highest stability of CMC-conjugated enzyme was observed as nearly four-fold at 40 °C and pH 8.0. No changes were observed on the temperature and pH profiles of PGA after CMC conjugation. Lower K _m and higher k _cat values of PGA obtained after CMC conjugation indicates the improved effect of conjugation on the substrate affinity and catalytic performance of the enzyme.     

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.     

Purification of recombinant protein A by aqueous two-phase extraction integrated with affinity precipitation

Aqueous two-phase extraction incorporated affinity precipitation was examined as a technique for protein purification. An enteric coating polymer, Eudragit S100, was employed as a ligand carrier. Eudragit was specifically partitioned to the top phase in the aqueous two-phase systems. For application of this method to purification of recombinant protein A using human IgG coupled to Eudragit in an aqueous two-phase system, 80% of protein A added was recovered with 81% purity. The purity was enhanced 26-fold by thid method. The IgG-Eudragit could be used repeatedly for the purification process. This seperation method should be applicable to industrial-scale purification as a new purification procedure combining the advantages and compensating for the disadvantages of the aqueous two-phase method and affinity precipitation method. (c) 1992 John Wiley & Sons, Inc.     

Galactose induces the expression of penicillin acylase under control of the lac promoter in recombinant Escherichia coli

The expression of penicillin acylase (PA), cloned in the pPA102 plasmid under control of the wild-type lac promoter and using galactose as inducer in Escherichia coli JM101, JM103 and JM105 transformant cells, was analyzed. The E. coli JM101/pPA102 cultures attained the highest specific activity of PA. For large scale PA production based on E. coli JM101/pPA102 a culture media with galactose instead of isopropyl-thio-galactopyranoside as inducer would be as successful and less expensive.     

Affinity gel electrophoresis as a predictive technique in the fractionation of transgenic sheep milk proteins by affinity aqueous two-phase partitioning

Affinity electrophoresis in the presence of various triazine dyes of sheep milk proteins, including transgenically-introduced human ₁-antitrypsin, has been evaluated as a predictive technique for possible large scale affinity-driven aqueous two-phase purifications. The success of the approach suggested it has potential as a general method for the rapid screening of ligands using only g amounts of sample, that could be applied to many complex mixtures before embarking on more costly and time-consuming two-phase partitioning experiments.     

Partitioning of pristinamycins in aqueous two-phase systems: A first step toward the development of antibiotic production by extractive fermentation

The partitioning of pristinamycins was studied in dextran and polyethylene glycol (PEG) aqueous two-phases systems. Pristinamycins partitioned preferentially into the PEG-rich top phase. The partition coefficient was independent of molar mass of PEG and dextran and of antibiotic concentration, but, increased exponentially with the tieline length of the system. Partition of pristinamycins was greatly improved when fatty acids esters of PEG were mixed with PEG. In such mixtures, the partition of coefficient increased up to a value of 24, dependent on the carbon chain length of fatty acids and the modified PEG concentrations. Moreover, in such system, the two groups of pristinamycins, I and II, were extracted in accordance with their hydrophobicity. Recovery of pristinanamycins produced by Streptomyces pritinaespiralis in a fermentation broth was achieved with a dextran/PEG system. Cells were confined into the bottom phase and pristinamycins partitioned in the top phase. However, due to binding of the pristinamycins to the cells, the partition coefficient was slightly lower than of pure antibiotics solutions. (c) 1994 John Wiley & Sons, Inc.     

Effect of heat-shock proteins for relieving physiological stress and enhancing the production of penicillin acylase in Escherichia coli

High-level expression of recombinant penicillin acylase (PAC) using the strong trc promoter system in Escherichia coli is frequently limited by the processing and folding of PAC precursors (proPAC) in the periplasm, resulting in physiological stress and inclusion body formation in this compartment. Periplasmic heat-shock proteins with protease or chaperone activity potentially offer a promise for overcoming this technical hurdle. In this study, the effect of the two genes encoding periplasmic heat-shock proteins, that is degP and fkpA, on pac overexpression was investigated and manipulation of the two genes to enhance the production of recombinant PAC was demonstrated. Both DeltadegP and DeltafkpA mutants showed defective culture performance primarily due to growth arrest. However, pac expression level was not seriously affected by the mutations, indicating that the two proteins were not directly involved in the pathway for periplasmic processing of proPAC. The growth defect caused by the two mutations (i.e., DeltadegP and DeltafkpA) was complemented by either one of the wild-type proteins, implying that the function of the two proteins could partially overlap in cells overexpressing pac. The possible role that the two heat-shock proteins played for suppression of physiological stress caused by pac overexpression is discussed.     

Effect of complex nitrogen sources on the production of penicillin acylase byBacillus megaterium

The following complex nitrogen sources were evaluated for the production of penicillin acylase byBacillus megaterium: casein hydrolysate, corn steep liquor, stick water concentrate, blood meal and defatted sunflower meal. Experiments were run in shake flasks at 30‡C and pH 7.0. Best results were obtained with casein hydrolysate: 244 IU/I were produced with a productivity of 20.3 IU/l/h and yield of 717.6 IU/g of nitrogen. The lowest results correspond to sunflower meal with 39 IU/1.     

Partial purification of d-glucose-6-phosphate dehydrogenase from bakers' yeast by affinity partitioning using polymer-bound triazine dyes

d-Glucose-6-phosphate dehydrogenase (d-glucose-6-phosphate:NADP⁺ 1-oxidoreductase EC 1.1.1.49) has been purified from bakers' yeast by liquid-liquid extraction using phase-restricted triazine dyes (Procion Yellow HE-3G, Procion Olive MX-3G, Procion Navy MX-RB and Cibacron Blue F3G-A). This method was combined with fractional precipitation with poly(ethylene) glycol) and batchwise treatment with DEAE-cellulose. This rapid procedure gave an enzyme preparation with a specific activity of 0.92 kat per kg protein within 5 h. The affinity extraction step can easily be scaled up and the good recovery of ligand-poly(ethylene glycol) should make the process useful for larger amounts of enzyme. The technical possibilities are discussed.     

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.     

Partial purification of d-glucose-6-phosphate dehydrogenase from bakers' yeast by affinity partitioning using polymer-bound triazine dyes

d-Glucose-6-phosphate dehydrogenase (d-glucose-6-phosphate:NADP⁺ 1-oxidoreductase EC 1.1.1.49) has been purified from bakers' yeast by liquid-liquid extraction using phase-restricted triazine dyes (Procion Yellow HE-3G, Procion Olive MX-3G, Procion Navy MX-RB and Cibacron Blue F3G-A). This method was combined with fractional precipitation with poly(ethylene) glycol) and batchwise treatment with DEAE-cellulose. This rapid procedure gave an enzyme preparation with a specific activity of 0.92 kat per kg protein within 5 h. The affinity extraction step can easily be scaled up and the good recovery of ligand-poly(ethylene glycol) should make the process useful for larger amounts of enzyme. The technical possibilities are discussed.