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.     

Effect of organic cosolvent on kinetic resolution of tert-leucine by penicillin G acylase from Kluyvera citrophila

Penicillin G acylase (PGA) from Kluyvera citrophila immobilized on Amberzyml was used for enantioselective hydrolysis of N-phenylacetylated-dl-tert-leucine (N-Phac-dl-Tle) to produce l-tert-leucine (l-Tle). The effects of various organic cosolvents on hydrolysis of N-Phac-dl-Tle have been investigated in aqueous-cosolvent medium. It was founded that the rate of PGA-catalyzed reaction was significantly affected by the presence of 2% (v/v) organic cosolvent concentration. The initial rate fell with increasing logP of the cosolvent, but for logP values less than −0.24 the rate was faster than in purely aqueous medium. Additionally, the relative rate increases with the increase of dielectric constant (ε) of organic cosolvents. The yields of l-Tle in all aqueous-cosolvent systems were above 95% with the enantiomeric excess (ee) of >99%.     

Evidence for involvement of arginyl residue at the catalytic site of penicillin acylase from Escherichia coli

Incubation of penicillin acylase from Escherichia coli with phenylglyoxal or 2,3-butanedione results in enzyme inactivation. Both benzylpenicillin and phenylacetate protect the enzyme against the inactivation, indicating the presence of arginine at or near the catalytic site. The reactions follow pseudofirst order kinetics and the inactivation kinetics indicate the presence of a single essential arginine moiety.     

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.     

Rapid continuous colorimetric enzyme assay for penicillin G acylase

A rapid, continuous, colorimetric enzyme assay for penicillin G acylase has been developed. The assay measures the formation of the acidic products of penicillin G hydrolysis by following the decrease in pH using Phenol Red as an indicator. The activity measured is directly proportional to the amount of enzyme added to the assay, having a linear relationship with an R ² value of 0.9994.     

微波对青霉素酰化酶催化反应性能的影响

运用动力学方法研究了微波对青霉素酰化酶(pK1和pK2分别为5.69-6.06和11.56)催化反应性能的影响。结果显示:使用微波解冻档对青霉素酰化酶进行一定时间的预处理后,能够加速酶的水解反应。酶液的最适处理时间为15 s,微波处理后,酶的最适温度为从原来的37℃上升到40℃,操作稳定性基本不变。对最适微波条件处理后的青霉素酰化酶pH值依赖性催化反应进行研究,从logVm和log(Vm/Km)与pH值关系曲线计算得到该酶的pK1和pK2分别为5.66-6.55和11.05。     

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。     

巨大芽孢杆菌青霉素G酰化酶的定点突变及其动力学性质研究

为了提高青霉素G酰化酶（PGA）在酸性及有机溶剂中的稳定性,以大肠杆菌的晶体结构为模板,用软件PMODELING同源模建巨大芽孢杆菌青霉素G酰化酶的三维结构结构并且选择PGA分子表面的合适碱性氨基酸突变为丙氨酸,通过三种不同的快速PCR介导定位突变的方法,将位于PGA的α亚基21位、128位和β亚基492位、512位的赖氨酸残基分别突变为丙氨酸,获得四个突变酶Kα021A、Kα128A、Kβ492A和Kβ512A。其中Kα128A和Kβ512A保持与野生型相近的酶活力,其动力学性质如最适温度、最适pH,Km及Kcat没有明显变化;突变酶Kα021A和Kβ492A则丧失 了酶活力。上述结果表明,PGA分子表面非活性中心的赖氨酸→丙氨酸点突变使突变子的性状发生了分化,突变效应呈现出丰富的多样性。该有理设计不但可以提高酶的稳定性,而且为揭示PGA结构和功能的关系提供了一个新的研究模型。     

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.     

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.     

巨大芽孢杆菌青霉素G酰化酶在新型环氧载体ZH-HA上的固定化

巨大芽孢杆菌青霉素G酰化酶共价结合在新型环氧-氨基型载体ZH-HA 上,通过对酶浓度、固定化时间、pH以及缓冲液浓度等条件的考察,确定了最优固定化条件:50 mg比活力6000 U/g的巨大芽孢杆菌青霉素G酰化酶蛋白和1g ZH-HA悬浮于pH 9.01 mol/L磷酸缓冲液,室温搅拌6 h,制得固定化巨大芽孢杆菌青霉素G酰化酶,活力2126 U/g湿载体,活力回收率7.67%.比较研究了固定化酶与原酶性质,原酶最适温度45℃,最适pH为8.0.固定化酶则分别是50℃和9.0,分别比溶液酶偏移5℃、1.0个pH单位.经过40批连续水解青霉素G钾盐,固定化巨大芽孢杆菌青霉素酰化酶仍保持80%的活力,显示出良好的工作稳定性.     

重组青霉素G酰化酶拆分制备（S）-邻氯苯甘氨酸

对产青霉素G酰化酶的重组枯草芽胞杆菌发酵产酶条件进行优化,确定优化后的发酵条件：可溶性淀粉10g/L、蛋白胨12g/L、酵母粉3g/L、NaCl10g,／L;pH7．5、培养温度37℃、装液量80mL（500mL三角瓶）、培养28h,青霉素G酰化酶的表达水平由最初的7．34U／mL提高至18．23U／mL。以表达青霉素G酰化酶的枯草芽胞杆菌发酵液为酶源,在水相中对映选择性催化N-苯乙酰-（R,S）-邻氯苯甘氨酸制备（S）-邻氯苯甘氨酸,当底物浓度为100mol／L时转化4h,转化率达44．2％。对底物浓度为80mmoL／L反应液中的（S）-邻氯苯甘氨酸进行分离,达到理论收率的94．29％（以N-苯乙酰-（R,S）-邻氯苯甘氨酸的0．5倍摩尔量为理论产率）,e．e．值大于99．9％。170℃条件下,N-苯乙酰-（R）-邻氯苯甘氨酸与苯乙酸共熔消旋为N-苯乙酰-（R,S）-邻氯苯甘氨酸可用于循环拆分。     

Expression, purification, and characterization of His-tagged penicillin G acylase from Kluyvera citrophila in Escherichia coli

The DNA fragment encoding Kluyvera citrophila penicillin G acylase (KcPGA) was amplified and cloned into the vector pET28b to obtain a C-terminus His-tagged fusion expression plasmid. The fusion protein KcPGA was successfully overexpressed in Escherichia coli BL21(DE3). The optimal induction concentration of isopropylthio-beta-D-galactoside (IPTG) was found to be 5 microM. The fusion protein was purified in a single step by Ni-IDA affinity chromatograph to a specific activity of 35.3U/mg protein with a final yield of 89% representing a 23-fold purification. The data presented here suggest that the purified fusion protein is stable with respect to pH and temperature. The optimal pH and temperature of recombinant KcPGA are 8.5 and 55 degrees C, respectively. The Km and Vmax are 17.6 microM and 23.8 U/mg, respectively. Therefore, the high yield and high specific activity of recombinant KcPGA produced in E. coli, together with other kinetic parameters, represent an excellent basis for further development of recombinant KcPGA as an immobilized biocatalyst for industrial applications.     

Substrate specificity of penicillin acylase from Streptomyces lavendulae

The kinetic parameters of several substrates of penicillin acylase from Streptomyces lavendulae have been determined. The enzyme hydrolyses phenoxymethyl penicillin (penicillin V) and other penicillins with aliphatic acyl-chains such as penicillin F, dihydroF, and K. The best substrate was penicillin K (octanoyl penicillin) with a k(cat)/K(m) of 165.3 mM(-1) s(-1). The enzyme hydrolyses also chromogenic substrates as NIPOAB (2-nitro-5-phenoxyacetamido benzoic acid), NIHAB (2-nitro-5-hexanoylamido benzoic acid) or NIOAB (2-nitro-5-octanoylamido benzoic acid), however failed to hydrolyse phenylacetil penicillin (penicillin G) or NIPAB (2-nitro-5-phenylacetamido benzoic acid) and penicillins with polar substituents in the acyl moiety. These results suggest that the structure of the acyl moiety of the substrate is more determinant than the amino moiety for enzyme specificity. The enzyme was inhibited by several organic acids and the extent of inhibition changed with the hydrophobicity of the acid. The best inhibitor was octanoic acid with a K(i) of 0.8 mM. All the results, taking together, point to an active site highly hydrophobic for this penicillin acylase from Streptomyces lavendulae.     

Modifying the substrate specificity of penicillin G acylase to cephalosporin acylase by mutating active-site residues

The penicillin G acylase (PGA) and cephalosporin acylase (CA) families, which are members of the N-terminal (Ntn) hydrolases, are valuable for the production of backbone chemicals like 6-aminopenicillanic acid and 7-aminocephalosporanic acid (7-ACA), which can be used to synthesize semi-synthetic penicillins and cephalosporins, respectively. Regardless of the low sequence similarity between PGA and CA, the structural homologies at their active-sites are very high. However, despite this structural conservation, they catalyze very different substrates. PGA reacts with the hydrophobic aromatic side-chain (the phenylacetyl moiety) of penicillin G (PG), whereas CA targets the hydrophilic linear side-chain (the glutaryl moiety) of glutaryl-7-ACA (GL-7-ACA). These different substrate specificities are likely to be due to differences in the side-chains of the active-site residues. In this study, mutagenesis of active-site residues binding the side-chain moiety of PG changed the substrate specificity of PGA to that of CA. This mutant PGA may constitute an alternative source of engineered enzymes for the industrial production of 7-ACA.     

Purification of penicillin G acylase using immobilized metal affinity membranes

The immobilized metal affinity membrane (IMAM) with modified regeneration cellulose was employed for purification of penicillin G acylase (PGA). For studying PGA adsorption capacity on the IMAM, factors such as chelator surface density, chelating metal, loading temperature, pH, NaCl concentration and elution solutions were investigated. The optimal loading conditions were found at 4 degrees C, 0.5 M NaCl, 32.04 micromol Cu(2+) per disk with 10 mM sodium phosphate buffer, pH 8.5, whereas elution conditions were: 1 M NH(4)Cl with 10 mM sodium phosphate buffer, pH 6.8. By applying these chromatographic conditions to the flow experiments in a cartridge, a 9.11-fold purification in specific activity with 90.25% recovery for PGA purification was obtained. Meanwhile, more than eight-times reusability of the membrane was achieved with the EDTA regeneration solutions.     

Rational design of a more stable penicillin G acylase against organic cosolvent

We have used a simple and efficient approach by combining the known functional and structural properties of penicillin G acylase (PGA) from E. coli, and tried to mutate PGA of Bacillus megaterium with the goal of increasing the stability of the enzyme in organic solvents or at acidic pH. The PGA mutants Kβ427A, Kβ430A and Kβ427A/Kβ430A obtained have higher stability in DMF than the wild-type PGA.     

Immobilization of penicillin G acylase on macro-mesoporous silica spheres

In this study, macro-mesoporous silica spheres were prepared with a micro-device and used as the support for the immobilization of penicillin G acylase (PGA). To measure the enzymatic activity, the silica spheres with immobilized PGA were placed into a packed-bed reactor, in which the hydrolysis of penicillin G was carried out. The influences of the residence time, the initial concentration of the substrate, the accumulation of the target product 6-aminopenicillanic acid, and the enzyme loading amount on the performance of the immobilized PGA were investigated. The introduction of macropores increased the enzyme loading amount and decreased the internal mass transfer resistance, and the results showed that the enzyme loading amount reached 895 mg/g (dry support), and the apparent enzymatic activity achieved up to 1033 U/g (dry support). In addition, the immobilized PGA was found to have great stability.     

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.