Effect of Internal Diffusional Restrictions on the Hydrolysis of Penicillin G: Reactor Performance and Specific Productivity of 6-APA with Immobilized Penicillin Acylase

A mathematical model that describes the heterogeneous reaction–diffusion process involved in penicillin G hydrolysis in a batch reactor with immobilized penicillin G acylase is presented. The reaction system includes the bulk liquid phase containing the dissolved substrate (and products) and the solid biocatalyst phase represented by glyoxyl-agarose spherical porous particles carrying the enzyme. The equations consider reaction and diffusion components that are presented in dimensionless form. This is a complex reaction system in which both products of reaction and the substrate itself are inhibitors. The simulation of a batch reactor performance with immobilized penicillin G acylase is presented and discussed for the internal diffusional restrictions impact on effectiveness and productivity. Increasing internal diffusional restrictions, through increasing catalyst particle size and enzyme loading, causes impaired catalyst efficiency expressed in a reduction of effectiveness factor and specific productivity. High penicillin G initial concentrations decrease the impact of internal diffusional restrictions by increasing the mass transfer towards porous catalyst until product inhibition becomes significant over approximately 50 mM of initial penicillin G, where a drop in conversion rate and a maximum in specific productivity are then obtained. Results highlight the relevance of considering internal diffusional restrictions, reactor performance, and productivity analysis for proper catalyst and reactor design.     

A scalable chemoenzymatic process for 7-amino-3-[Z-2-(4-methylthiazol-5-yl)vinyl]-3-cephem-4-carboxylic acid (ATCA)

An efficient chemoenzymatic process has been developed for preparation of 7-amino-3-[Z-2-(4-methylthiazol-5-yl)vinyl]-3-cephem-4-carboxylic acid, featuring removal of para-methoxybenzyl by trichloroacetic acid and cleavage of phenylacetyl E-isomer by immobilized penicillin acylase enzyme. The E-isomer of 7-amino-3-[Z-2-(4-methylthiazol-5-yl)vinyl]-3-cephem-4-carboxylic acid could be easily decreased to less than 0.2 % by salt formation. Importantly, trichloroacetic acid and immobilized penicillin acylase enzyme could be recovered and reused. The enzyme reaction could be run in a flow reactor. Only two crystallizations are involved as the purification procedure in the six-step sequence.     

不同介孔材料固定青霉素酰化酶的稳定性研究

介孔材料由于具有在2～30nm之间可调的纳米级规则孔道、大比表面积和强吸附性能而成为固定化酶的优良载体．将酶固定于介孔材料的孔道中制备成的固定化酶与溶液酶相比,有易于与产物分离,并可回收和反复使用,可降低生产成本,减少酶的自水解和保持酶的活性．青霉素酰化酶（Penicillin acylase,PGA,EC．3．5．1．11）又称为青霉素酰胺酶或青霉素氨基水解酶,该酶属于球蛋白,分子量较大,由2个亚基组成：分子量为19500的含有侧链结合位点的亚基和分子量为60000的含有催化位点的亚基．     

介孔材料MCFs的合成及组装青霉素酰化酶的性质研究

介孔材料由于具有纳米级规则孔道和巨大的比表面积而在催化、吸附及分离等方面存在较大的应用价值．近年来,由介孔分子筛如MCM-41和SBA-15州等组装功能性材料已成为研究的热点．酶作为高效催化剂有许多优点,但在溶液中易失活,使用后无法回收,有的酶在溶液中还存在自水解问题：将酶组装在介孔材料中制成固定化酶则可解决上述问题．目前已成功地将辣根过氧化物酶     

Batch and in-flow kinetic resolution of racemic 1-(N-acylamino)alkylphosphonic and 1-(N-acylamino)alkylphosphinic acids and their esters using immobilized penicillin G acylase

The kinetic resolution of racemic 1-(N-acylamino)alkylphosphonic acids 3 (R³ = OH) and their dimethyl esters 1, as well as 1-(N-acylamino)alkylphosphinic acids 4 (R³ = H or Ph) using penicillin G acylase (PGA) immobilized on three types of mesoporous silicas in both a batch slurry system and in a continuous-flow reactor was studied. The initial hydrolytic deacylation rates in the presence of those catalysts were measured and the relationships between the substrate structure and the enzyme efficiency are discussed. The stereospecific hydrolysis of the N-acyl group of both racemic N-acylated phosphorus analogues of amino acids and their esters catalyzed by the immobilized PGA proved to be a highly effective method for the kinetic resolution of all the investigated compounds, with the stereochemical preference of PGA for (R)-substrates.     

Synthesis of Cephalexin in Aqueous Medium with Carrier-bound and Carrier-free Penicillin Acylase Biocatalysts

The use of very high substrate concentrations favors the kinetically controlled synthesis of cephalexin with penicillin acylase (PA) not only by Michaelian considerations, but also because water activity is depressed, so reducing the rates of the competing reactions of product and acyl donor hydrolysis. Commercial PGA-450, glyoxyl agarose immobilized (PAIGA) and carrier-free cross-linked enzyme aggregates of penicillin acylase (PACLEA) were tested in aqueous media at concentrations close to the solubility of nucleophile and at previously determined enzyme to nucleophile and acid donor to nucleophile ratios. The best temperature and pH were determined for each biocatalyst based on an objective function considering conversion yield, productivity, and enzyme stability as evaluation parameters. Stability was higher with PAIGA and specific productivity higher with PACLEA, but best results based on such objective function were obtained with PGA-450. Yields were stoichiometric and productivities higher than those previously reported in organic medium, which implies significant savings in terms of costs and environmental protection. At the optimum conditions for the selected biocatalyst, operational stability was determined in sequential batch reactor operation. The experimental information gathered is being used for a technical and economic evaluation of an industrial process for enzymatic production of cephalexin in aqueous medium.     

Immobilization of whole-cell penicillin g acylase by entrapping within polymethacrylamide beads

Escherichia coli ATCC 11105 containing the periplasmic penicillin G acylase was entrapped within a copolymer of methacrylamide andN,N’- methylenebisacrylamide. A solution of monomer that was made up from methacrylamide andN,N’-methylenebisacrylamide dissolved in buffer was mixed with lyophilized cells and ammonium persulfate. This suspension was then pumped drop by drop into in soybean oil supplemented with 0.06% (v/v) 3-(dimethylamino)-propionitril. During submerging in the oil phase, the droplets were hardened and induced to polymerize within the droplets. Particles with a volume ranging from 0.013–0.017 mL per bead containing a biomass concentration up to 38.0 g/L were prepared. The optimal condition for the deacylation of penicillin G to 6-aminopencillanic acid (6-APA) catalyzed by the immobilized whole-cell penicillin G acylase was found to be 45‡C and pH 8.0. Product inhibition of this enzyme by 6-APA could be eliminated by controlling pH value at 8 during the course of penicillin G hydrolysis using a pH-stat. Conversion determined by the pH-stat method were 0.3% higher than that by p-dimethylaminobenzaldehyde method. Cell concentration in the matrix was found to be an important factor influencing the maximum velocity and the specific activity retained in the matrix. A kinetic model, in which the mass transfer resistances as a result of external film mass transfer and pore diffusion were assumed to be negligible, could properly describe the hydrolysis of penicillin G by the cells entrapped within the polymethacylamide beads.     

Cross-linked enzyme aggregates: a simple and effective method for the immobilization of penicillin acylase

[reaction--see text] Penicillin G acylase (penicillin amidohydrolase, E.C. 3.5.1.11) was immobilized in a simple and effective way by physical aggregation of the enzyme, using a precipitant, followed by chemical cross-linking to form insoluble cross-linked enzyme aggregates (CLEAs). These had the same activity in the synthesis of ampicillin as cross-linked crystals of the same enzyme, but the accompanying hydrolysis of the side-chain donor was much less. Penicillin G acylase CLEAs also catalyzed the synthesis of ampicillin in a broad range of organic solvents.     

Resolution of racemic 2-amino-1-butanol with immobilised penicillin G acylase

Racemic 2-amino-1-butanol has been resolved to obtain (S)-2-amino-1-butanol with >99% e.e. via enantioselective hydrolysis of its N-phenylacetyl derivative with penicillin G acylase immobilised on Eupergit C.     

Beaded reactive polymers 3 effect of triacrylates as crosslinkers on the physical properties of glycidyl methacrylate copolymers and immobilization of penicillin G acylase

Various glycidyl methacrylate (GMA) copolymers were synthesized by suspension polymerization, using pentaerythritol triacrylate (PETA), trimethylolpropane triacrylate (TMPTA), and trimethylolpropane trimethacrylate (TRIM) as crosslinking comonomers. These copolymers were evaluated for the immobilization of penicillin G acylase. Broad pore-size distribution that was observed was in the range 5-300 nm. Both surface area and pore volume increased with increase in the mole fraction of crosslinking comonomer (increasing crosslink density). The pore volume of the copolymers was more than doubled by including lauryl alcohol as porogen. Binding of penicillin G acylase (PGA) was quantitative on highly crosslinked copolymers. The expression of bound PGA was better on the relatively more hydrophilic GMA-TMPTA and GMA-PETA copolymer supports compared to the GMA-TRIM copolymers. Among the different copolymers studied, GMA-TMPTA copolymer 7411 exhibited highest activity of immobilized penicillin G acylase (167.4 IU/g) with 35.1% expression.     

Immobilized penicillin G acylase as reactor and chiral selector in liquid chromatography

In this paper, the use of penicillin G acylase (PGA) as a biocatalyst and as a chiral selector is described. Penicillin G-acylase is an interesting enzyme used in the manufacture of semisynthetic antibiotics and, in particular, in the production of 6-APA by hydrolysis of penicillin G. Five PGA-based HPLC columns have been prepared by using two different silica supports by employing two immobilization methods, namely "in situ" and "in batch". The effects of the immobilization techniques and of different silica pore size on the catalytic properties of the enzyme as well as the applicability of the PGA-bonded stationary phases as chiral selectors for a number of chiral drugs have been investigated. The HPLC columns based on immobilized PGA combine the hydrolytic activity and the chiral recognition properties of PGA, therefore they have been used for the development of a combined reaction-separation system for chiral and achiral substrates.     

A Process to Produce Penicillin G Acylase by Surface-Adhesion Fermentation Using <Emphasis Type="Italic">Mucor griseocyanus</Emphasis> to Obtain 6-Aminopenicillanic Acid by Penicillin G Hydrolysis

The production of extracellular and mycelia-associated penicillin G acylase (maPGA) with Mucor griseocyanus H/55.1.1 by surface-adhesion fermentation using Opuntia imbricata, a cactus, as a natural immobilization support was studied. Enzyme activity to form 6-aminopencillanic acid (6-APA) from penicillin G was assayed spectrophotometrically. The penicillin G hydrolysis to 6-APA was evaluated at six different times using PGA samples recovered from the skim milk medium at five different incubation times. Additionally, the effect of varying the penicillin G substrate concentration level on the PGA enzyme activity was also studied. The maximum reaction rate, V _max, and the Michaelis constant, K _M, were determined using the Michaelis–Menten model. The maximum levels for maPGA and extracellular activity were found to be 2,126.50 international unit per liter (IU/l; equal to 997.83 IU/g of support) at 48 h and 755.33 IU/l at 60 h, respectively. Kinetics of biomass production for total biomass showed a maximum growth at 60 h of 3.36 and 2.55 g/l (equal to 0.012 g of biomass per gram of support) for the immobilized M. griseocyanus biomass. The maPGA was employed for the hydrolysis of penicillin G to obtain 6-APA in a batch reactor. The highest quantity of 6-APA obtained was 226.16 mg/l after 40-min reaction. The effect of substrate concentration on maPGA activity was evaluated at different concentrations of penicillin G (0–10 mM). K _M and V _max were determined to be 3.0 × 10⁻³ M and 4.4 × 10⁻³ mM/min, respectively.     

A kinetic study of synthesis of amoxicillin using penicillin G acylase immobilized on agarose

We presenta kinetic model for the synthesis of amoxicillin from p-hydroxyphenylglycine methyl ester and 6-aminopenicillanic acid, catalyzed by penicillin G acylase immobilized on agarose, at 25°C. Michaelis-Menten kinetic parameters (with and without inhibition) were obtained from initial velocity data (pH 7.5 and 6.5). Amoxicillin synthesis reactions were used to validate the kinetic model after checking mass transport effects. A reasonable representation of this system was achieved under some operational conditions, but the model failed under others. Nevertheless, it will be useful whenever a simplified model is required, e.g., in model-based control algorithms for the enzymatic reactor.     

Strategies for Enhancing the Production of Penicillin G Acylase from Bacillus badius: Influence of Phenyl Acetic Acid Dosage

Bacillus badius isolated from soil has been identified as potential producer of penicillin G acylase (PGA). In the present study, batch experiments performed at optimized inoculum size, temperature, pH, and agitation yielded a maximum PGA of 9.5 U/ml in shake flask. The experiments conducted in bioreactor with different oxygen flow rates revealed that 0.66 vvm oxygen flow rate could be sufficient for the maximum PGA activity of 12.7 U/ml. From a detailed investigation on the strategies of the addition of phenyl acetic acid (PAA) for increasing the production of PGA, it was found that the controlled addition of 10 ml of 0.1 % (w/v) PAA once in every 2 h from 6th hour of growth showed the maximum PGA activity of 32 U/ml. Thus, our studies for the first time showed that at concentration above 0.1 % (w/v) PAA, the PGA production decreased. This selective condition paves the way for less costly bioprocess for the production of PGA.     

青霉素酰化酶在含铁MCM-41介孔分子筛上的固定化研究

制备了具有长程有序结构、孔径分布狭窄的含铁MCM-41介孔分子筛，利用直接法和共价结合法将青霉素酰化酶固定在分子筛表面。结果表明，两种方法制备的固定化酶对青霉素G水解反应的表观活性分别为782U/g和256U／g；经6次连续操作使用，二者保持初始活性的49．4％和81．2％，后者的操作稳定性好于前者。共价结合法制备的固定化酶活性较低，是由于Fe—MCM-41表面修饰后比表面积和孔径明显减小所致。     

含环氧基亲水性固定化青霉素酰化酶共聚载体的合成与性能研究

环氧基团可以在温和条件下与酶分子的氨基反应使其固定于载体表面.选用含有活性环氧基团的甲基丙烯酸缩水甘油酯(GMA)和亲水性的N-乙烯吡咯烷酮(NVP)两种单体,以N,N′-亚甲基双丙烯酰胺(MBAA)为交联剂,甲醇水溶液作致孔剂,液体石蜡为主介质,通过反相悬浮聚合技术成功地合成了亲水性大孔GMA-NVP-MBAA三元共聚物载体(GNM).通过调节交联剂的用量和单体NVP与GMA的比例,可以调节载体的孔径、比表面积及在水中的溶胀性能.将巨大芽孢杆菌青霉素酰化酶共价偶联于平均孔径为16.5nm、表面环氧基含量为0.906mmol/g的GNM共聚物载体,制成固定化酰化酶,其表观活性高达625U/g,水解青霉素G钾盐的最适宜温度为50℃,pH值为8.0.固定化酶在4℃保存40d,活性保持不变.经3次使用后,活性达到稳定值(601U/g左右),再经12次使用,活性几乎保持不变.     

Enzymatic Hydrolysis of N-Acylated 1-Aminophosphonic Acids

Abstract

Penicillin acylase from E. coli (FC 3.5.1.11) was found to hydrolyse N-phenylacetylated 1-aminoalkylphosphonic acids and their esters. Enzyme preferentially converts the R-form of the substrates: the ratios of the bimolecular rate constants of penicillin acylase-catalysed hydrolysis of R-and S- forms of 1-(N-phenylacetaminol-ethylphosphonic acid and its dimethyl- and diisopropyl- esters are 58000, 2600, 1800; these derivatives were shown to have the greatest values of the catalytic constants for enzymatic hydrolysis of all known substrates of penicillin acylase: 237, 148, and 134 s; corresponding values of Michaelis constants are 3.7×10^?5, 6.8×10^?4, and 6.2×10^?4 M. The kinetics of the enzymatic hydrolysis of 1-(N-phenylacetaminol-ethylphosphonic acid was investigated up to high degrees of conversion. The inhibition of penicillin acylase by high concentrations of the R-form of the substrate (with substrate inhibition constant 0.07 Ml and competitive inhibition by the reaction product phenylacetic acid (K_i=3.5×10_?5 M) was observed. Penicillin acylase was shown to possess quite broad substrate specificity among N-acylated 1-aminoalkylphosphonic acids and was found to be capable of hydrolysing 1-(N-phenylacetaminol-substituted 2-phenylethyl-, 1-phenylmethyl- and 3-methylbutylphosphonic acids with high efficiency and enantioselectivity.     

含氨基和环氧基双功能基的聚合物刷磁性微球的制备及对青霉素G酰化酶的固定化

在内部分散超顺磁性Fe3O4纳米粒子的二乙烯苯交联聚丙烯酸微球表面引入原子转移自由基聚合(ATRP)引发剂,引发聚合向微球表面分别引入P(GMMA-r-DMAEMA-r-GMA)、P(GMMA-r-DMAEMA)和P(GMMA-r-GMA)无规共聚物刷(GMMA为甲基丙烯酸甘油单酯,DMAEMA为甲基丙烯酸-N,N-二甲氨基乙酯,GMA为甲基丙烯酸缩水甘油酯),聚合物刷中GMMA链节的作用是使聚合物刷具有亲水性,DMAEMA引入氨基,GMA引入环氧基.研究了青霉素G酰化酶在这些载体上的固定化和其酶活性.结果表明,同时引入环氧基和氨基的P(GMMA-r-DMAEMA-r-GMA)刷磁性微球固定化青霉素G酰化酶的活性和活性收率都最高,其固定化动力学比只含环氧基P(GMMA-r-GMA)刷磁性微球的好.固定化酶比自由酶更耐热,固定化酶的最佳pH值比自由酶的略高,固定化酶重复使用10次后其活性保留70%.     

Immobilization of Penicillin G Acylase on Calcined Layered Double Hydroxides

A hydrotalcite-like Mg2 /Al3 layered double hydroxide (LDH) material was prepared by means of amodified coprecipitation method involving a rapid mixing step followed by a separate aging process. LDH calcined at 500℃ , denoted as CLDH, was characterized by XRD, IR and BET surface area measurements.CLDH has a poor crystalline MgO-like structure with a high surface area and porosity. CLDH was used as asupport for the immobilization of penicillin G acylase(PGA). The effect of varying the immobilization conditions, such as pH, contact time and the ratio of enzyme to support, on the activity of the immobilized enzymein the hydrolysis of penicillin G has been studied. It was found that the activity of the immobilized enzyme decreased slightly with decreasing pH and reached a maximum after a contact time of 24 h. The activity of theimmobilized enzyme increased with increasing the ratio of enzyme to support. It was found that the adsorption of PGA inhibited the expected reaction of CLDH with an aqueous medium to regenerate a LDH phase. Itsoriginal activity(36%) after 15 cycles of reuse of the immobilized enzyme was retained, but no further loss in the activity was observed.     

含环氧基团的聚合物载体合成方法的改进及其固定化青霉素酰化酶

 以 Span-60 和 Tween-20 为复合分散剂, 以 N,N′-亚甲基双丙烯酰胺为交联剂, 以甲基丙烯酸缩水甘油酯和烯丙基缩水甘油醚为功能性单体, 用反相悬浮聚合技术成功制备了含环氧基团的聚合物载体, 并用红外光谱和低温氮吸附对聚合物载体进行了表征. 以 Span-60 和 Tween-20 为复合分散剂, 替代原有的 Span-60 和硬脂酸钙复合分散剂, 大幅度减少了后处理过程中所需的时间和溶剂用量, 使固定化青霉素酰化酶的活性从 215 U/g 提高到 320 U/g. 与游离酶相比, 该固定化酶具有较好的操作稳定性, 在 pH = 5~11 和不高于 50 oC 的环境中具有较好的稳定性. 固定化酶的水解反应动力学过程与游离酶相同, 均遵循米氏反应动力学, 而且活性与底物浓度密切相关. 当底物浓度为 6.5% 时, 固定化酶的活性最高, 达到 353 U/g.