Immobilization of the hydantoin cleaving enzymes from Arthrobacter aurescens DSM 3747.

The immobilization procedure of the two industrially important hydantoin cleaving enzymes--hydantoinase and L-N-carbamoylase from Arthrobacter aurescens DSM 3747--was optimized. Using different methods (carbodiimide, epoxy activated carriers) it was possible to immobilize the crude hydantoinase from A. aurescens DSM 3747 to supports containing primary amino groups with a yield of up to 60%. Immobilization on more hydrophobic supports such as Eupergit C and C 250 L resulted in lower yields of activity, whereas the total protein coupled remained constant. All attempts to immobilize the crude L-N-carbamoylase resulted in only low activity yields. Therefore, the enzyme was highly purified and used in immobilization experiments. The pure enzyme could easily be obtained in large amounts by cultivation of a recombinant Escherichia coli strain following a three step purification protocol consisting of cell disruption, chromatography on Streamline diethylaminoethyl and Mono Q. The immobilization of the L-N-carbamoylase was optimized with respect to the coupling yield by varying the coupling method as well as the concentrations of protein, carrier and carbodiimide. Using 60 mM of water-soluble carbodiimide, nearly 100% of the enzyme activity and protein could be immobilized to EAH Sepharose 4B.     

Immobilization of dextransucrase from Leuconostoc mesenteroides NRRL B-512F on Eupergit C supports

Dextransucrase from Leuconostoc mesenteroides B-512F was immobilized on epoxy-activated acrylic polymers with different textural properties (Eupergit C and Eupergit C 250L). Prior to immobilization, dextransucrase was treated with dextranase to remove the dextran layer covering the enzyme surface, thus increasing the accessibility of its reactive groups to the epoxide centers of the support. Elimination of 99% of the initial carbohydrate content was determined by the anthrone method. To prevent enzyme inactivation, the immobilization was carried out at pH 5.4, at which the coupling to the support took place through the carboxylic groups of the enzyme. The effects of the amount (mg) of dextransucrase added per gram of support (from 0.2:1 to 30:1), temperature and contact time were studied. Maximum activity recovery of 22% was achieved using Eupergit C 250L. Using this macroporous support, the maximum specific activity (710 U/g biocatalyst) was significantly higher than that obtained with the less porous Eupergit C (226 U/g biocatalyst). The dextransucrase immobilized on Eupergit C 250L showed similar optimal temperature (30 degrees C) and pH (5-6) compared with the native enzyme. In contrast, a notable stabilization effect at 30 degrees C was observed as a consequence of immobilization. After a fast partial inactivation, the dextransucrase immobilized on Eupergit C 250L maintained more than 40% of the initial activity over the following 2 days. The features of this immobilized system are very attractive for its application in batch and fixed-bed bioreactors.     

Immobilization and biocatalysis of chlorophyllase in selected organic solvent systems

Chlorophyllase extract from Phaeodactylum tricornutum was immobilized by physical adsorption on DEAE-cellulose and silica gel as well as by covalent binding on Eupergit C, Eupergit C250L, Eupergit C/ethylenediamine (EDA) and Eupergit C250L/EDA. Although the highest immobilization yield (83-93%) and efficiency (51-53%) were obtained when chlorophyllase extract was immobilized on DEAE-cellulose and silica gel, there was no improvement in the thermal stability of chlorophyllase as compared to that of the free one. The immobilization of chlorophyllase extract on Eupergit C250L/EDA resulted by a high recovery of enzymatic activity, with an immobilization efficiency of 44%, and promoted a higher stabilization of chlorophyllase (four times) in the aqueous/miscible organic solvent medium. On the other hand, the inhibitory effect of refined bleached deodorized (RBD) canola oil was reduced by immobilization of chlorophyllase extract onto silica gel as compared to those obtained with other enzyme preparations. However, the re-cycled chlorophyllase extract immobilized on Eupergit C250L/EDA retained more than 75% of its initial enzyme activity after 6 cycles, whereas that immobilized on silica gel was completely inactivated. The highest catalytic efficiency, for both free and immobilized chlorophyllase on Eupergit C250L/EDA, was obtained in the ternary micellar system as compared to the aqueous/miscible organic solvent and biphasic media.     

Development of an ultrahigh-temperature process for the enzymatic hydrolysis of lactose. IV. Immobilization of two thermostable beta-glycosidases and optimization of a packed-bed reactor for lactose conversion.

Recombinant hyperthermostable beta-glycosidases from the archaea Sulfolobus solfataricus (Ss beta Gly) and Pyrococcus furiosus (CelB) were covalently attached onto the insoluble carriers chitosan, controlled pore glass (CPG), and Eupergit C. For each enzyme/carrier pair, the protein-binding capacity, the immobilization yield, the pH profiles for activity and stability, the activity/temperature profile, and the kinetic constants for lactose hydrolysis at 70 degrees C were determined. Eupergit C was best among the carriers in regard to retention of native-like activity and stability of Ss beta Gly and CelB over the pH range 3.0-7.5. Its protein binding capacity of approximately 0.003 (on a mass basis) was one-third times that of CPG, while immobilization yields were typically 80% in each case. Activation energies for lactose conversion by the immobilized enzymes at pH 5.5 were in the range 50-60 kJ/mol. This is compared to values of approximately 75 kJ/mol for the free enzymes. Immobilization expands the useful pH range for CelB and Ss beta Gly by approximately 1.5 pH units toward pH 3.5 and pH 4.5, respectively. A packed-bed enzyme reactor was developed for the continuous conversion of lactose in different media, including whey and milk, and operated over extended reaction times of up to 14 days. The productivities of the Eupergit C-immobilized enzyme reactor were determined at dilution rates between 1 and 12 h(-1), and using 45 and 170 g/L initial lactose. Results of kinetic modeling for the same reactor, assuming plug flow and steady state, suggest the presence of mass-transfer limitation of the reaction rate under the conditions used. Formation of galacto-oligosaccharides in the continuous packed-bed reactor and in the batch reactor using free enzyme was closely similar in regard to yield and individual saccharide components produced.     

Production of L-tryptophan from D,L-5-indolylmethylhydantoin by resting cells of a mutant of Arthrobacter species (DSM 3747).

The reaction parameters and the stereospecificity of the enzymatic cleavage of D,L-5-indolylmethylhydantoin in producing L-tryptophan with resting cells of Arthrobacter sp. DSM 3747 were studied. When intact cells were tested, the optimal pH was between 8.5 and 9.0 and the optimal temperature was 50 degrees C. Both, L-N-carbamoylase and hydantoinase could be stabilized over 24 h at 30 and 40 degrees C by the addition of D,L-5-indolylmethylhydantoin. Furthermore, the hydantoinase was stable over 24 h at 50 degrees C by the addition of 0.5 mM Mn2+ ions. The treatment with sodium desoxycholate turned out to be successful in overcoming the poor availability of D,L-5-indolylmethylhydantoin for the cells. The optimal temperature with permeabilized cells decreased to 30 degrees C and therefore ensured a good enzyme stability. While the L-N-carbamoylase proved to be absolutely L-specific, the hydantoinase led to a mixture of enantiomers of N-carbamoyltryptophan. The produced D-N-carbamoyl-tryptophan caused an inhibition of the L-N-carbamoylase. The transformation yield from D,L-5-indolylmethylhydantoin always reached 100%.     

Preparative-scale kinetic resolution of racemic styrene oxide by immobilized epoxide hydrolase

Epoxide hydrolase from Aspergillus niger was immobilized onto the modified Eupergit C 250 L through a Schiff base formation. Eupergit C 250 L was treated with ethylenediamine to introduce primary amine groups which were subsequently activated with glutaraldehyde. The amount of introduced primary amine groups was 220 μmol/g of the support after ethylenediamine treatment, and 90% of these groups were activated with glutaraldehyde. Maximum immobilization of 80% was obtained with modified Eupergit C 250 L under the optimized conditions. The optimum pH was 7.0 for the free epoxide hydrolase and 6.5 for the immobilized epoxide hydrolase. The optimum temperature for both free and immobilized epoxide hydrolase was 40 °C. The free epoxide hydrolase retained 52 and 33% of its maximum activity at 40 and 60 °C, respectively after 24h preincubation time whereas the retained activities of immobilized epoxide hydrolase at the same conditions were 90 and 75%, respectively. Immobilized epoxide hydrolase showed about 2.5-fold higher enantioselectivity than that of free epoxide hydrolase. A preparative-scale (120 g/L) kinetic resolution of racemic styrene oxide using immobilized preparation was performed in a batch reactor and (S)-styrene oxide and (R)-1-phenyl-1,2-ethanediol were both obtained with about 50% yield and 99% enantiomeric excess. The immobilized epoxide hydrolase was retained 90% of its initial activity after 5 reuses.     

Immobilization of pycnoporus coccineus laccase on Eupergit C: Stabilization and treatment of olive oil mill wastewaters

The use of olive oil mill wastewaters (OMW) as an organic fertilizer is limited by their phytotoxic effect, due to the high concentration of phenolic compounds. As an alternative to physico-chemical methods for OMW detoxification, the laccase from Pycnoporus coccineus, a white-rot fungus with the ability to decrease the chemical oxygen demand (COD) and color of the industrial effluent, is being studied. In this work, the P. coccineus laccase was immobilized on two acrylic epoxy-activated resins, Eupergit C and Eupergit C 250L. The highest activity was obtained with the macroporous Eupergit C 250L, reaching 110 U g^?1 biocatalyst. A substantial stabilization effect against pH and temperature was obtained upon immobilization. The soluble enzyme maintained ≥80% of its initial activity after 24 h at pH 7.0–10.0, whereas the immobilized laccase kept the activity in the pH range 3.0–10.0. The free enzyme was quickly inactivated at temperatures >50°C, whereas the immobilized enzyme was very stable up to 70°C. Gel filtration profiles of the OMW treated with the immobilized enzyme (for 8 h at room temperature) showed both degradation and polymerization of the phenolic compounds.     

Preparation and application of poly(N,N-dimethylacrylamide-co-acrylamide) and poly(N-isopropylacrylamide-co-acrylamide)/kappa-Carrageenan hydrogels for immobilization of lipase

In the present of this study, two novel polymeric matrixes that are poly(N,N-dimethylacrylamide-co-acrylamide) and poly(N-isopropylacrylamide-co-acrylamide)/kappa-Carrageenan was synthesized and applied for immobilization of lipase. For the immobilization of enzyme, two different immobilization procedures have been carried out via covalently binding and entrapment methods. On the free and immobilized enzymes activities, optimum pH, temperature, storage and thermal stability was investigated. The optimum temperature for free, covalently immobilized and entrapped enzymes was found to be 30, 35 and 30 degrees C, respectively. Optimum pH for both free and immobilized enzymes was also observed at pH 8. Maximum reaction rate (Vmax) and Michaelis-Menten constant (Km) were determined for free and immobilized lipases. Furthermore, the reuse numbers of immobilized enzymes also studied. It was observed that after 40th use in 5 days, the retained activities for covalently immobilized and entrapped lipases were found as 39% and 22%, respectively. Storage and thermal stability of enzyme was also increased by as a result of immobilization procedures.     

Preparation and properties of immobilized papain and lipase.

Papain and lipase were immobilized on derivatized Sepharose 4-B. The activated agarose had a binding capacity of 1.2 micronmol amino groups/ml packed agarose or 17 mg proteins/g dry agarose. The immobilized enzyme preparations were tested for the effects of pH of assay, temperature of assay, and substrate concentrations. The effect of 6M urea on the activity of papain was also determined. Soluble forms of the enzymes were used for comparison. Immobilization of the enzymes resulted in slightly different pH and temperature optima for activities. For immobilized papain Km(app) was similar to the one observed with soluble papain. Immobilization of lipase, however, cause a decrease in Km values. The immobilized enzyme preparations were stable when stored at 4 degrees C and pH 7.5 for periods up to eight months. The soluble enzymes lost their activity within 96 hr under similar storage conditions. Immobilized papain did not lose any activity after treatment with 6M urea for 270 min, whereas soluble papain lost 81% of its activity after the urea treatment, indicating that the immobilization of papain imparted structural and conformational stability to this enzyme.     

Preparative-scale kinetic resolution of racemic styrene oxide by immobilized epoxide hydrolase

Epoxide hydrolase from Aspergillus niger was immobilized onto the modified Eupergit C 250 L through a Schiff base formation. Eupergit C 250 L was treated with ethylenediamine to introduce primary amine groups which were subsequently activated with glutaraldehyde. The amount of introduced primary amine groups was 220 μmol/g of the support after ethylenediamine treatment, and 90% of these groups were activated with glutaraldehyde. Maximum immobilization of 80% was obtained with modified Eupergit C 250 L under the optimized conditions. The optimum pH was 7.0 for the free epoxide hydrolase and 6.5 for the immobilized epoxide hydrolase. The optimum temperature for both free and immobilized epoxide hydrolase was 40 °C. The free epoxide hydrolase retained 52 and 33% of its maximum activity at 40 and 60 °C, respectively after 24 h preincubation time whereas the retained activities of immobilized epoxide hydrolase at the same conditions were 90 and 75%, respectively. Immobilized epoxide hydrolase showed about 2.5-fold higher enantioselectivity than that of free epoxide hydrolase. A preparative-scale (120 g/L) kinetic resolution of racemic styrene oxide using immobilized preparation was performed in a batch reactor and (S)-styrene oxide and (R)-1-phenyl-1,2-ethanediol were both obtained with about 50% yield and 99% enantiomeric excess. The immobilized epoxide hydrolase was retained 90% of its initial activity after 5 reuses.     

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).     

Immobilization on Eupergit C of cyclodextrin glucosyltransferase (CGTase) and properties of the immobilized biocatalyst

The extreme thermophilic cyclodextrin glucanotransferase (CGTase) from Thermoanaerobacter sp. was covalently attached to Eupergit C. Different immobilization parameters (incubation time, ionic strength, pH, ratio enzyme/support, etc.) were optimized. The maximum yield of bound protein was around 80% (8.1 mg/g support), although the recovery of β-cyclodextrin cyclization activity was not higher than 11%. The catalytic efficiency was lower than 15%. Results were compared with previous studies on covalent immobilization of CGTase.

The enzymatic properties of immobilized CGTase were investigated and compared with those of the soluble enzyme. Soluble and immobilized CGTases showed similar optimum temperature (80–85 °C) and pH (5.5) values, but the pH profile of the immobilized CGTase was broader at higher pH values. The thermoinactivation of the CGTase coupled to Eupergit C was slower than the observed with the native enzyme. The half-life of the immobilized enzyme at 95 °C was five times higher than that of the soluble enzyme. The immobilized CGTase maintained 40% of its initial activity after 10 cycles of 24 h each. After immobilization, the selectivity of CGTase (determined by the ratio CDs/oligosaccharides) was notably shifted towards oligosaccharide production.     

氨基化二氧化硅颗粒固定木瓜蛋白酶研究

采用正硅酸乙酯与N-(β-氨乙基)氨丙基三乙氧基硅烷在油包水形成的微胶囊中同步水解的方法,一步法制备了氨基化的二氧化硅颗粒,得到的颗粒粒径在0.3～0.5μm之间,平均大小为0.37μm, 氨基含量和颗粒大小可控,氨基含量高达56mmol/g。此颗粒经戊二醛处理后,采用共价法固定木瓜蛋白酶,固定化最适pH6.5,最佳给酶量为15mg/g载体,固定化酶的最适反应温度为70℃,最适反应pH为6.5,固定化酶热稳定性,pH耐受性,贮存稳定性都明显高于游离酶,表明此颗粒可作为一种优良的酶固定化载体。     

Increase in conformational stability of enzymes immobilized on epoxy-activated supports by favoring additional multipoint covalent attachment*

Epoxy supports (Eupergit C) may be very suitable to achieve the multipoint covalent attachment of proteins and enzymes, therefore, to stabilize their three-dimensional structure. To achieve a significant multipoint covalent attachment, the control of the experimental conditions was found to be critical. A three-step immobilization/stabilization procedure is here proposed: 1) the enzyme is firstly covalently immobilized under very mild experimental conditions (e.g. pH 7.0 and 20 degrees C); 2) the already immobilized enzyme is further incubated under more drastic conditions (higher pH values, longer incubation periods, etc.) to "facilitate" the formation of new covalent linkages between the immobilized enzyme molecule and the support; 3) the remaining groups of the support are blocked to stop any additional interaction between the enzyme and the support. Progressive establishment of new enzyme-support attachments was showed by the progressive irreversible covalent immobilization of several subunits of multi-subunits proteins (all non-covalent structures contained in crude extracts of different microorganism, penicillin G acylase and chymotrypsin). This multipoint covalent attachment enabled the significant thermostabilization of two relevant enzymes, (compared with the just immobilized derivatives): chymotrypsin (5-fold factor) and penicillin G acylase (18-fold factor). Bearing in mind that this stabilization was additive to that achieved by conventional immobilization, the final stabilization factor become 100-fold comparing soluble penicillin G acylase and optimal derivative. These stabilizations were observed also when the inactivations were promoted by the enzyme exposure to drastic pH values or the presence of cosolvents.     

酶的定向固定化方法及其对酶生物活性的影响

固定化酶可以提高酶的稳定性,但通常酶通过酶分子上的多个赖氨酸残基随意固定在载体上,这样会使酶的活性显著下降,采用定向固定化酶不仅可以提高酶的稳定性,而且可以保存它的活性。综述了定向固定化酶的几种方法,比较了定向固定化和随意固定化对酶活性的影响。另外,还叙述了酶的活性位点结构变化的自旋共振波谱(EPR)检测。     

Methods for the immobilization of lipases and their use for ester synthesis

The lipase from Pseudomonas fluorescens was immobilized onto five different carriers: celite, octyl-silica, aminopropyl-silica, gluterdialdehyde-activated silica and Eupergit C250L. Activities and operational stabilities of the prepared catalysts were compared using the enantioselective acylation of (R,S)-1-phenylethanol by vinyl acetate as acyl donor and t-butylmethyl ether with variable water content (0.038-0.97% v/v) as reaction medium. The above carriers provide catalysts with widely different specific activities ranging from excellent 25 mmol/h mg protein (celite) to 0.07 mmol/h mg protein (glutardialdehyde-activated silica) on the lower end. The lipase immobilized onto Eupergit C250L exhibited the best operational stability among the catalysts studied. It retained 30% of its initial activity after 11 cycles of application, each with a duration between 2 and 6 h.     

Immobilization of <Emphasis Type="Italic">Alcaligenes faecalis</Emphasis> penicillin G acylase on epoxy-type supports

Alcaligenes faecalis penicillin G acylase has several desired features over other penicillin G acylases and its use in industry requires immobilization. In this work, two novel supports ZH-EP (epoxy type) and ZH-HA (epoxy-amino type) were used to immobilize Alcaligenes faecalis penicillin G acylase (AfPGA) with Eupergit C as reference. The saturation of immobilized protein on ZH-EP (269 mg/g, 116 h) and ZH-HA (296 mg/g, 15 h) was obtained more rapidly than Eupergit C (197 mg/g, 260 h). And the activity of immobilized AfPGA on ZH-EP (520 U/g) and ZH-HA (2200 U/g) was higher than that on Eupergit C (310 U/g). The properties of three immobilized enzymes were compared and no obvious difference was observed, which indicated that ZH-EP and ZH-HA were promised in industry.     

Immobilization of oxalate decarboxylase to Eupergit and properties of the immobilized enzyme

Oxalate decarboxylase, an oxalate degradation enzyme used for medical diagnosis and decreasing the oxalate level in the food or paper industry, was covalently immobilized to Eupergit C. Different immobilization parameters, including ratio of enzyme to support, ammonia sulfate concentration, pH, and incubation time, were optimized. Under the condition of enzyme/support ratio at 1:20, pH 9, with 1.5?mol/L (NH(4))(2)SO(4), room temperature, and shaking at 30?rpm for 24?hr, activity recovery of immobilized Oxdc reached 90% with an apparent specific activity of 0.44?U/mg support. The enzymatic properties of immobilized Oxdc were investigated and compared with those of the soluble enzyme. Both shared a similar profile of optimum conditions; the optimum pH and temperature for soluble and immobilized Oxdc were 3.5 and 50°C, respectively. The immobilized enzyme was more stable at lower pH and higher temperatures. The kinetic parameters for soluble and immobilized enzyme were also determined.     

Immobilization of Bacillus licheniformis L-Arabinose Isomerase for Semi-Continuous L-Ribulose Production

Bacillus licheniformis L-arabinose isomerase (BLAI) with a broad pH range, high substrate specificity, and high catalytic efficiency for L-arabinose was immobilized on various supports. Eupergit C, activated-carboxymethylcellulose, CNBr-activated agarose, chitosan, and alginate were tested as supports, and Eupergit C was selected as the most effective. After determination of the optimum enzyme concentration, the effects of pH and temperature were investigated using a response surface methodology. The immobilized BLAI enzyme retained 86.4% of the activity of the free enzyme. The optimal pH for the immobilized BLAI was 8.0, and immobilization improved the optimal temperature from 50 °C (free enzyme) to a range between 55 and 65 °C. The half life improved from 2 at 50 °C to 212 h at 55 °C following immobilization. The immobilized BLAI was used for semi-continuous production of L-ribulose. After 8 batch cycles, 95.1% of the BLAI activity was retained. This simple immobilization procedure and the high stability of the final immobilized BLAI on Eupergit C provide a promising solution for large-scale production of L-ribulose from an inexpensive L-arabinose precursor.     

Immobilization of pancreatic lipase on chitin and chitosan

In this study, porcine pancreatic lipase (EC 3.1.1.3) was immobilized on chitin and chitosan by adsorption and subsequent crosslinking with glutaraldehyde, which was added before (conjugation) or after (crosslinking) washing unbound proteins. Conjugation proved to be the better method for both supports. The properties of free and immobilized enzymes were also investigated and compared. The results showed that the pH optimum was shifted from 8.5 to 9.0 for both the immobilized enzymes. Also, the optimum temperature was shifted from 30 to 40 degrees C for chitin-enzyme and to 45 degrees C for chitosan-enzyme conjugates. The immobilization efficiency is low, but the immobilized enzymes have good reusability and stability (storage and operational). Besides these properties, the immobilized lipases were also suitable for catalyzing esterification reactions of fatty acids and fatty alcohols, both with a medium chain length. According to our results, esterification activities of immobilized lipases were two- and four-fold higher for chitosan- and chitin-enzyme, than for the free enzyme, respectively. The immobilization procedure shows a great potential for commercial applications of the immobilized lipase, a relatively low cost commercial enzyme.