An approach for the improved immobilization of penicillin G acylase onto macroporous poly(glycidyl methacrylate‐co‐ethylene glycol dimethacrylate) as a potential industrial biocatalyst

The use of penicillin G acylase (PGA) covalently linked to insoluble carrier is expected to produce major advances in pharmaceutical processing industry and the enzyme stability enhancement is still a significant challenge. The objective of this study was to improve catalytic performance of the covalently immobilized PGA on a potential industrial carrier, macroporous poly(glycidyl methacrylate‐co‐ethylene glycol dimethacrylate) [poly(GMA‐co‐EGDMA)], by optimizing the copolymerization process and the enzyme attachment procedure. This synthetic copolymer could be a very promising alternative for the development of low‐cost, easy‐to‐prepare, and stable biocatalyst compared to expensive commercially available epoxy carriers such as Eupergit or Sepabeads. The PGA immobilized on poly(GMA‐co‐EGDMA) in the shape of microbeads obtained by suspension copolymerization appeared to have higher activity yield compared to copolymerization in a cast. Optimal conditions for the immobilization of PGA on poly(GMA‐co‐EGDMA) microbeads were 1 mg/mL of PGA in 0.75 mol/L phosphate buffer pH 6.0 at 25°C for 24 h, leading to the active biocatalyst with the specific activity of 252.7 U/g dry beads. Chemical amination of the immobilized PGA could contribute to the enhanced stability of the biocatalyst by inducing secondary interactions between the enzyme and the carrier, ensuring multipoint attachment. The best balance between the activity yield (51.5%), enzyme loading (25.6 mg/g), and stability (stabilization factor 22.2) was achieved for the partially modified PGA. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:43–53, 2016     

Biospecific immobilization of mannan-penicillin G acylase neoglycoenzyme on Concanavalin A-bead cellulose

The matter of this work was to evaluate possibilities of biospecific immobilization of synthetic mannan-penicillin G acylase neoglycoconjugate on Concanavalin A support. The conjugate containing 37% (w/w) of yeast mannan was prepared. Significant biospecific interaction of this neoglycoenzyme with Con A was confirmed by precipitation method. The biospecific sorption of conjugate was investigated using Concanavalin A-triazine bead celluloses MT-100 with different content of Con A (from 1.4 to 9.8 mgCon A/gwet support). The results obtained under optimal conditions were compared with those from covalent immobilization of PGA. The sorbent capacity was observed higher for covalent binding of enzyme. On the other hand, the biospecifically immobilized neoglycoenzyme retained a greater amount of initial activity. The maximum amount of 6.6mgimmobilizedneoglycoenzyme/gwet Con A-sorbent (18.1 U/g) was achieved. The amount as well as activity of immobilized mannan-penicillin G acylase was increased by its two multiple layering on surface of sorbent (10.1mg, respectively, 23.5 U/gwet sorbent). Determined storage and operational (using flow calorimetric method) stabilities of biospecifically immobilized enzyme, were similar, possibly somewhat higher that those of covalent bound penicillin G acylase.     

Highly efficient "tight fit" immobilization of alpha-chymotrypsin in mesoporous MCM-41: a novel approach using precursor immobilization and activation

The zymogen alpha-chymotrypsinogen A is bound to mesoporous silica MCM-41 with a protein loading of 170 mg/g solid (MCM-Z) by a simple stirring in aqueous tris-HCl buffer (pH 7.2). The bound zymogen is then activated with trypsin to obtain alpha-chymotrypsin immobilized on MCM-41 (MCM-E.I) that displays an effective enzyme activity corresponding to 65 mg protein/g of solid support (3250 BTEE units/g). A direct immobilization of commercially available alpha-chymotrypsin (MCM-E.II) gives lower loading (1250 BTEE units/g). Protein content of the solid support after immobilization is confirmed by thermogravimetric analysis (TGA). The enzyme is tightly bound to the support and can be used over 100 recycles over 1 week in aqueous as well as reverse micellar media. The immobilized enzyme (MCM-E.I) has been used for resolution of N-acetyl-dl-amino acid esters and racemic trans-4-methoxy-3-phenylglycidic acid (PGA) methyl ester.     

Improvement of the catalytic properties of penicillin G acylase from Escherichia coli ATCC 11105 by selection of a new substrate specificity

Cloned penicillin G acylase (PGA) from Escherichia coli ATCC 11105 was mutagenized in vivo using N-methyl-N-nitrosoguanidine. Mutants of PGA were selected by their ability to allow growth of the host strain E. coli M8820 with the new substrates phenylacetyl--alanyl-l-proline (PhAc-Ala-Pro) phthalyl-l-leucine (Pht-Leu) or phthalylglycyl-l-proline (Pht-Gly-Pro) as sole source of proline and leucine respectively. PGA mutants were purified and immobilized onto spherical methacrylate (G-gel). The immobilized form of mutant PGA selected with (PhAc-gbAla-Pro) hydrolyzed 95% of 9 mmol penicillin G 30% faster than wild-type PGA using the same specific activities. The specific activity of the soluble enzyme was 2.7-fold, and inhibition by phenylacetic acid was halved. Immobilized PGA mutant selected with Pht-Gly-Pro hydrolyzed penicillin G 20% faster than wild-type PGA. The K _m of the soluble enzyme was increased 1.7-fold. Furthermore, the latter two mutants were also 3.6-fold more stable at 45° C than wild-type PGA. The specific activity of the mutant selected with Pht-Leu was 6.3-fold lower, and inhibition by phenylacetic acid was increased 13-fold.     

Hydrogel coated monoliths for enzymatic hydrolysis of penicillin G

The objective of this work was to develop a hydrogel-coated monolith for the entrapment of penicillin G acylase (E. coli, PGA). After screening of different hydrogels, chitosan was chosen as the carrier material for the preparation of monolithic biocatalysts. This protocol leads to active immobilized biocatalysts for the enzymatic hydrolysis of penicillin G (PenG). The monolithic biocatalyst was tested in a monolith loop reactor (MLR) and compared with conventional reactor systems using free PGA, and a commercially available immobilized PGA. The optimal immobilization protocol was found to be 5 g l(-1) PGA, 1% chitosan, 1.1% glutaraldehyde and pH 7. Final PGA loading on glass plates was 29 mg ml(-1) gel. For 400 cpsi monoliths, the final PGA loading on functionalized monoliths was 36 mg ml(-1) gel. The observed volumetric reaction rate in the MLR was 0.79 mol s(-1) m(-3) (monolith). Apart from an initial drop in activity due to wash out of PGA at higher ionic strength, no decrease in activity was observed after five subsequent activity test runs. The storage stability of the biocatalysts is at least a month without loss of activity. Although the monolithic biocatalyst as used in the MLR is still outperformed by the current industrial catalyst (immobilized preparation of PGA, 4.5 mol s(-1) m(-3) (catalyst)), the rate per gel volume is slightly higher for monolithic catalysts. Good activity and improved mechanical strength make the monolithic bioreactor an interesting alternative that deserves further investigation for this application. Although moderate internal diffusion limitations have been observed inside the gel beads and in the gel layer on the monolith channel, this is not the main reason for the large differences in reactor performance that were observed. The pH drop over the reactor as a result of the chosen method for pH control results in a decreased performance of both the MLR and the packed bed reactor compared to the batch system. A different reactor configuration including an optimal pH profile is required to increase the reactor performance. The monolithic stirrer reactor would be an interesting alternative to improve the performance of the monolith-PGA combination.     

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.     

Simple and efficient immobilization of lipase B from Candida antarctica on porous styrene-divinylbenzene beads

Two commercial porous styrene-divinylbenzene beads (Diaion HP20LX and MCI GEL CHP20P) have been evaluated as supports to immobilize lipase B from Candida antarctica (CALB). MCI GEL CHP20P rapidly immobilized the enzyme, permitting a very high loading capacity: around 110 mg CALB/wet g of support compared to the 50 mg obtained using decaoctyl Sepabeads. Although enzyme specificity of the enzyme immobilized on different supports was quite altered by the support used in the immobilization, specific activity of the enzyme immobilized on MCI GEL CHP20P was always higher than those found using decaoctyl Sepabeads for all assayed substrates. Thus, a CALB biocatalyst having 3-8 folds (depending on the substrate) higher activity/wet gram of support than the commercial Novozym 435 was obtained. Half-live of CAL-Diaion HP20LX at 60 °C was 2-3 higher than the one of Novozym 435, it was 30-40 higher in the presence of 50% acetonitrile and it was around 100 folds greater in the presence of 10 M hydrogen peroxide.Results indicate that styrene-divinylbenzene supports may be promising alternatives as supports to immobilize CALB.     

A new biocatalyst: Penicillin G acylase immobilized in sol-gel micro-particles with magnetic properties

The present work focuses on the development and basic characterization of a new magnetic biocatalyst, namely penicillin G acylase (PGA), immobilized in sol-gel matrices with magnetic properties, ultimately aimed for application in cephalexin (CEX) synthesis. A mechanically stable carrier, based on porous xerogels silica matrixes starting from tetramethoxysilane (TMOS), was prepared leading to micro-carriers with medium sized particles of 30 μm, as determined by scanning electron microscopy. An immobilization yield of 95–100% and a recovered activity of 50–65% at 37°C, as determined by penicillin G (PG) hydrolysis (pH STAT method), were observed. These results clearly exceed those reported in a previous work on PGA immobilization in sol-gel, where only 10% of activity was recovered. The values of activity were kept constant for 6 months. Immobilized PGA (682 U/g_{dry weight}) retained high specific activity throughout ten consecutive runs for PG hydrolysis, suggesting adequate biocatalyst stability. The CEX synthesis was performed at 14°C, using the free and immobilized PGA in aqueous medium. Phenylglycine methyl ester was used as acyl donor at 90 mM and 7-aminodeacetoxycephalosporanic acid was the limiting substrate at 30 mM. The CEX stoichiometric yield after 1-h reaction was close to 68% (23 mM CEX/h) and 65% (19 mM CEX/h), respectively.     

以聚丙烯腈纤维为载体制备固定化青霉素G酰化酶的研究

以酸部分水解聚丙烯腈纤维为载体 ,以戊二醛为交联剂 ,共价键结合制备了固定化胞外青霉素G酰化酶。当水解后的载体中 NH2 基含量为 690 μmol g和含水量为 64%时 ,对酶蛋白的固定量达 1 0 0mg g以上 ,固定化酶的活力达 2 30 0IU g ,酶活力总产率为 30 % ,固定化效率为 56%。酶活力的总产率和固定化率随加酶量的增加而降低。该酶可以将浓度为 2 5%～1 2 5%的青霉素G钾盐水解 98%以上。批投青霉素G钾盐为 1 0g,酶负荷为 1 50IU g(PGK) ,经2 0批水解反应后 ,剩余酶活力为 80 %。用二硫基苏醣醇处理固定化酶 ,对水解青霉素G钾盐的操作稳定性有促进作用。固定化酶的室温保存半衰期为 1 30d。用戊二醛和硼氢化钠溶液处理固定化酶后 ,酶活力的室温保存稳定性有所降低。     

Promotion of multipoint covalent immobilization through different regions of genetically modified penicillin G acylase from E. coli

A novel approach is proposed to prepare a set of immobilized derivatives of a enzyme covalently rigidified through different regions of its surface. Six different variants of penicillin G acylase (PGA) from Escherichia coli (which lacks Cys) were prepared by introducing a unique Cys residue via site-directed mutagenesis in six different enzyme regions which were rich in Lys residues. All variants exhibited a similar activity and stability compared to those of the native enzyme. Each variant was immobilized on supports having a low concentration of reactive disulfide moieties and a high concentration of poorly reactive epoxy groups. After immobilization at pH 7.0 by site-directed thiol-disulfide intermolecular exchange, derivatives were further incubated at pH 10.0 for 48 h to promote an additional intramolecular reaction between Lys residues of enzyme and epoxy groups of the support. The establishment of at least three covalent attachments per PGA molecule was determined for all immobilized enzyme variants. The different derivatives exhibited diverse stability against several distorting agents and different selectivity in two interesting reactions. The derivative of the PGA variant obtained by replacement of GlnB380 by Cys was the most stable against heat and organic cosolvents: it preserved 90% of the initial activity and was 30-fold more stable than soluble PGA. This derivative also exhibited an improved enantioselectivity in the hydrolysis of chiral esters (E was improved from 8 to 16) and in kinetically controlled synthesis of amides (synthetic yields were increased from 31 to 49%).     

Preparation of high-capacity supports containing protein G immobilized to porous silica

This study examined the preparation of high-capacity silica supports containing immobilized protein G. A maximum content of 39 mg protein G/g silica was obtained when using 100 Å pore size silica, followed by 33 mg/g for 50 Å silica and 9.3-24 mg/g for 300-4000 Å silica. The surface coverage of protein G increased with pore size, with a maximum level of 0.037 μmol/m² being obtained for 4000 Å silica. These supports gave comparable apparent activities (i.e., 30-47% binding to rabbit immunoglobulin G [IgG]), with the highest binding capacities (71-77 mg IgG/g silica) being obtained for 50-100 Å silica.     

聚丙烯腈纤维固定化青霉素酰化酶性质的研究

将巨大芽孢杆菌（Bacillusmegaterium）青霉素酞化酶连接到聚丙烯腈纤维载体上,制成固定化青霉素酰化酶。其表现活力约为2000u／g。水解青霉素G的最适温度为50℃;最适PH为9．0;在PHS．5～10．3、温度50℃以下酶的活力稳定;表观米氏常数Ka为1．33×10-8mol／L;最大反应速度Vm为2．564mmol·min-1;苯乙酸为竞争性抑制剂,抑制常数为0．16mol／L。水解10％的青霉素G钾盐溶液,使用20批,保留酶活力80％。     

Properties and application of immobilized beta-D-glucosidase coentrapped with Zymomonas mobilis in calcium alginate

The enzyme beta-D-glucosidase has been immobilized on concanavalin A-Sepharose to give a maximum loading of 2050 units/g dry weight of support material. The immobilized beta-D-glucosidase was also entrapped within calcium alginate gel spheres with apparently only 35% retention of activity when assayed with 10mM cellobiose. However, it was discovered that, unlike the immobilized enzyme, the entrapped immobilized enzyme was not subject to substrate inhibition up to 100mM cellobiose, suggesting that a concentration gradient of cellobiose existed between the bulk solution and the interior of the gel sphere. Thus, the activity of the entrapped immobilized enzyme was almost twice as high as that of the immobilized enzyme when assayed with 100mM cellobiose. Concanavalin A-Sepharose-immobilized beta-D-glucosidase and the bacterium Zymomonas mobilis coimmobilized in calcium alginate gel spheres converted cellobiose to ethanol in both batch and continuous-flow fermentation systems.     

Biodiesel production from pomace oil by using lipase immobilized onto olive pomace

In the present work, microbial lipase from Thermomyces lanuginosus was immobilized by covalent binding onto olive pomace. Immobilized support material used to produce biodiesel with pomace oil and methanol. The properties of the support and immobilized derivative were evaluated by scanning electron microscopy (SEM). The maximum immobilization of T. lanuginosus was obtained as 18.67 mg/g support and the highest specific activity was 10.31 U/mg protein. The properties of immobilized lipase were studied. The effects of protein concentration, pH and buffer concentration on the immobilization and lipase activity were investigated. Biodiesel production using the immobilized lipase was realized by a three-step addition of methanol to avoid strong substrate inhibition. Under the optimized conditions, the maximum biodiesel yield was 93% at 25 °C in 24 h reaction. The immobilized enzyme retained its activity during the 10 repeated batch reactions.     

Additional stabilization of penicillin G acylase-agarose derivatives by controlled chemical modification with formaldehyde.

We have tested the effect of chemical modifications with formaldehyde on the activity/stability of immobilized derivatives of the enzyme penicillin G acylase (PGA). These derivatives were previously stabilized through enzyme-support multipoint covalent attachment. We carried out very different chemical treatments of our derivatives by testing the effect of different variables which control the intensity and the nature of these amine-formaldehyde reactions. The variables tested were: formaldehyde concentration, pH, time, and temperature. We also developed a colorimetric titration of the free amine groups on immobilized PGA in order to evaluate the extension of the reaction between formaldehyde and the amine groups of the enzyme. As a consequence of these studies, we have been able to get additional stabilizations of our previously stabilized-immobilized derivatives: e.g. a factor of 24-fold was achieved in terms of stabilization against irreversible thermal inactivation. The integrated effect of additional chemical modification plus previous multipoint covalent attachment has allowed us to prepare PGA derivatives which are 50,000 more thermostable than native PGA as well as most of the commercial PGA derivatives.     

Immobilization of cellulase onto electrospun polyacrylonitrile (PAN) nanofibrous membranes and its application to the reducing sugar production from microalgae

This study demonstrates a method to prepare an immobilized cellulase by using an electrospun polyacrylonitrile (PAN) nanofibrous membrane as the support. To obtain an immobilized cellulase with high hydrolytic activity, the immobilization conditions including activation time, enzyme concentration, immobilization time, and temperature were optimized. Under those conditions, the immobilized cellulase possessed a protein loading of 30 mg/g-support and a specific activity of 3.2 U/mg-protein. After immobilization, the enzymatic stability of cellulase against pH and thermal stresses was improved. Fourier transform infrared spectroscopy (FTIR) measurements also revealed that the cellulase was covalently bonded to the supports. The immobilized cellulase was then used to hydrolyze cell wall of microalgae for the production of reducing sugars. Analyses using response surface methodology (RSM) show that the hydrolysis yield was affected by the reaction temperature, pH, and substrate/cellulase mass ratio, and a hydrolysis yield of 60.86% could be obtained at 47.85 °C, pH 5.82, and a substrate/cellulase mass ratio of 40 g-substrate/g-cellulase. This result suggests that the proposed scheme for the cellulase immobilization has great potential for the application to the reducing sugar production.     

Sanitization of immobilized biocatalysts for the production of 6‐aminopenicillanic acid

Five different chemical reagents and γ‐rays were tested for the sanitization of immobilized biocatalysts with high penicillin G acylase (PGA) activity. The most effective chemical reagents were N‐cetyl‐N,N,N‐trimethylammonium bromide (CTAB) and 2‐isopropyl‐5‐methylphenol (thymol). The optimum concentration of CTAB for the treatment of the immobilized enzyme was 0.25% [w/v] and 1 h, for immobilized cells 0. [w/v] and 3 h. The optimum concentration of thymol for the immobilized enzyme was found to be 0.1% [w/v] and 1 h, for immobilized cells 0.27% [w/v] and 2 h. The optimum dose of γ‐rays for the sanitization of the immobilized enzyme was established as 3.2 kGy, for immobilized cells as 4.5 kGy.     

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%。     

Epoxy sepabeads: a novel epoxy support for stabilization of industrial enzymes via very intense multipoint covalent attachment

Sepabeads-EP (a new epoxy support) has been utilized to immobilize-stabilize the enzyme penicillin G acylase (PGA) via multipoint covalent attachment. These supports are very robust and suitable for industrial purposes. Also, the internal geometry of the support is composed by cylindrical pores surrounded by the convex surfaces (this offers a good geometrical congruence for reaction with the enzyme), and it has a very high superficial density of epoxy groups (around 100 micromol/mL). These features should permit a very intense enzyme-support interaction. However, the final stability of the immobilized enzyme is strictly dependent on the immobilization protocol. By using conventional immobilization protocols (neutral pH values, nonblockage of the support) the stability of the immobilized enzyme was quite similar to that achieved using Eupergit C to immobilize the PGA. However, when using a more sophisticated three-step immobilization/stabilization/blockage procedure, the Sepabeads derivative was hundreds-fold more stable than Eupergit C derivatives. The protocol used was as follows: (i) the enzyme was first covalently immobilized under very mild experimental conditions (e.g., pH 7.0 and 20 degrees C); (ii) the already immobilized enzyme was further incubated under more drastic conditions (higher pH values, long incubation periods, etc.) in order to "facilitate" the formation of new covalent linkages between the immobilized enzyme molecule and the support; (iii) the remaining epoxy groups of the support were blocked with very hydrophilic compounds to stop any additional interaction between the enzyme and the support. This third point was found to be critical for obtaining very stable enzymes: derivatives blocked with mercaptoethanol were much less stable than derivatives blocked with glycine or other amino acids. This was attributed to the better masking of the hydrophobicity of the support by the amino acids (having two charges).     

以环氧乙烷为活性基的多孔颗粒状固定化青霉素酰化酶的制备

报道了用以环氧乙烷为活性基的多孔颗粒状载体（Eupergit-C）制备固定由巨大芽孢杆菌（B．megaterium）产生的青霉素酰化酶的研究。用已二胺,赖氨酸对载体进行化学修饰后制备固定化酶,获得了较好的固定结果。用未修饰的载体制备固化酶,经24h固定反应,酶活力达176．5IU／g（wet）,酶活力总叫率达53．7％,酶蛋白的固定量为19＝7mg/g（dr）,酶蛋白的固定效率达87．5％。游离酶的酶浓度对制备固定化酶的活力无显影响。当加酶量从312IU/g（dry）上升到6250IU／g（dry）时,固定化酶活力从89IU／g(wet）上升到475IU／g（wet）,总收率和固定化效率分别从99％和99％下降到26．5％和32．5％,酶蛋白的固定量从6．9mg/g（dry）上升到112mg/g（dry）,酶蛋白的固定效率从99％下降至80．5％。以酶活力为155IU/g(wet）,酶蛋白固定量为22mg/g(dry）的固定化酶水解青霉素G钾盐,经过20批循环水解后,剩余酶活力为92．5％。