Continuous production of maltotetraose using a dual immobilized enzyme system of maltotetraose-forming amylase and pullulanase

In order to produce a product with a high content of maltotetraose, dual-enzyme systems composed of immobilized maltotetraose-forming amylase (G(4)-forming amylase) and pullulanase were studied. The thermostability of individually immobilized enzymes was examined in continuous operation; studies revealed that the enzyme immobilized on "Chitopearl" was much more stable than that immobilized on Diaion HP-50. The effects of operating conditions on the stability of G(4) forming amylase immobilized on "Chitopearl" were examined to confirm that the apparent half-life data could be arranged using the immobilized enzyme stability factor, f(s). As for the dual immobilized enzyme system, six methods of usage were considered, with five yielding a 7-10% (w/w) higher content of maltotetraose product than the single-enzyme system. The effects of operating conditions on the maltotetraose production reaction were examined to confirm that the maltotetraose content of the products could be analyzed using the specific space velocity,SSV. In dual immobilized enzyme systems, pullulanase immobilized on the same carrier as the G(4)-forming amylase was found to be more stable than pullulanase immobilized on separate carriers. The effectiveness of using immobilized pullulanase along with the G(4)-forming amylase was confirmed from constant-conversion operations in which the maltotetraose content in the product was kept at 50% (w/w) in laboratory-scale experimentation.     

Some factors affecting the stability of glucoamylase immobilized on hornblende and on other inorganic supports

Glucoamylase from four different companies was studied: three had similar stability (half-life at 50°C about 140 hr); the fourth was less stable (half-life at 50°C about 20 hr). The immobilized enzymes were all less stable than their soluble counterparts: immobilized enzyme stability depended on the soluble enzyme used, the support, and method of immobilization. Thus enzyme bound to Enzacryl-TIO was less stable than enzyme bound to hornblende (metal-link method); this, in turn, was less stable than enzyme bound to hornblende by a silane–glutaraldehyde process. Bound enzyme stability was also improved by the presence of substrate or product (starch maltose or glucose). After 110 hr at 50°C in the presence of maltose (10% (w/v)) one preparation (a more stable soluble enzyme boul1d to hornblende by a silane–glutaraldehyde process) retained over 95% of its activity: activity loss was too low to permit the estimation of a half-life.     

Continuous production of maltotetraose using immobilized Pseudomonas stutzeri amylase

A continuous production process of maltotetraose was investigated by using immobilized maltotetraose (G(4))- forming amylase (1,4-alpha-D-glucan maltotetraohydrolase, EC3.2.1.60) from Pseudomonas stutzeri adsorbed on a macroporous hydrophobic resin. The maximum reaction rate was obtained at 55 degrees C and the activation energy of hydrolysis by immobilized G(4)-forming amylase was calculated to be 8.45 kcal/mol. The maltotetraose yield was greatly influenced by the flow rate of substrate solution, its concentration, and the immobilized enzyme activity. The newly defined factor "specific space velocity" was successfully introduced to normalize the operating parameters. Using this factor, the immobilized enzyme reactor then can be simulated and the operating dynamics can be determined.     

Kinetics and stability of immobilized chicken liver xanthine dehydrogenase.

Xanthine dehydrogenase (EC 1.2.1.37) was isolated from chicken livers and immobilized by adsorption to a Sepharose derivative, prepared by reaction of n-octylamine with CNBr-activated Sepharose 4B. Using a crude preparation of enzyme for immobilization it was observed that relatively more activity was adsorbed than protein, but the yield of immobilized activity increased as a purer enzyme preparation was used. As more activity and protein were bound, relatively less immobilized activity was recovered. This effect was probably due to blocking of active xanthine dehydrogenase by protein impurities. The kinetics of free and immobilized xanthine dehydrogenase were studied in the pH range 7.5-9.1. The Km and V values estimated for free xanthine dehydrogenase increase as the pH increase; the K'm and V values for the immobilized enzyme go through a minimum at pH 8.1. By varying the amount of enzyme activity bound per unit volume of gel, it was shown that K'm is larger than Km are result of substrate diffusion limitation in the pores of the support material. Both free and immobilized xanthine dehydrogenase showed substrate activation at low concentrations (up to 2 microM xanthine). Immobilized xanthine dehydrogenase was more stable than the free enzyme during storage in the temperature range of 4-50 degrees C. The operational stability of immobilized xanthine dehydrogenase at 30 degrees C was two orders of magnitude smaller than the storage stability, t 1/2 was 9 and 800 hr, respectively. The operational stability was, however, better than than of immobilized milk xanthine oxidase (t 1/2 = 1 hr). In addition, the amount of product formed per unit initial activity in one half-life, was higher for immobilized xanthine dehydrogenase than for immobilized xanthine oxidase. Unless immobilized milk xanthine oxidase can be considerable stabilized, immobilized chicken liver xanthine dehydrogenase is more promising for application in organic synthesis.     

Immobilization of lipase on chitin and its use in nonconventional biocatalysis

Chitin was functionalized with hexamethylenediamine followed by glutaraldehyde activation, and its capacity to bind Candida rugosa lipase was investigated. The loading of 250 units g(-1) support showed to be effective, resulting in a uniform enzyme fixation with high catalytic activity. Both free and immobilized lipases were characterized by determining the activity profile as a function of pH, temperature, and thermal stability. For the immobilized lipase, the influence of the reaction temperature and substrate polarity in nonconventional biocatalysis was also analyzed. Production of butyl esters was found to be dependent on the substrate partition coefficient, which accounts the greatest value for the system butanol and butyric acid. The highest enzyme activity was found for the system butanol and caprylic acid at a reaction temperature of 40 degrees C. Under such conditions, the operational stability tests indicated that a small enzyme deactivation occurs after 12 batches, revealing a biocatalyst half-life of 426.7 h.     

Synthesis of aspartame precursor with an immobilized thermolysin in tert-amyl alcohol

N-(Benzyloxycarbonyl)-L-aspartyl-L-phenylalanine methyl ester (Z-AspPheOMe), a precursor of the synthetic sweetner asparatame, was synthesized from N-(benzyloxycarbolyl)-L-aspartic acid (Z-Asp) and L-phenylalanine methyl ester (PheOMe) with an immobilized thermolysin in various organic solvents. We found that in tert-amyl alcohol containing a small amount of water the immobilized enzyme showed a high activity comparble to that in ethyl acetate with quite a high stability. The immobilized enzyme was fully stable up to 70 degrees C in tert-amyl alcohol in the absence of the subatrate, and up to 50 degrees C in the presence of the substrate. The high stability in the presence of the substrate was found due to the fact that the release of calcium ions, the stabilizing factor of thermolysin, is suppressed.The substrate concentration dependence of the initial synthetic rate with the immobilized enzyme was quite different from that with the free enzyme in the biphasic system, in contrast to that in ethyl acetate. Finally, Z-AspPheOMe was continuously synthesized in a column reactor using 200 mM PheOMe and 120 mM Z-Asp as the substrate for over 300 h at 45 degrees C and a space velocity of 1 h(-1) without any loss of acivity. (c) 1994 John Wiley & Sons, Inc.     

Thermal inactivation of immobilized penicillin acylase in the presence of substrate and products

Inactivation of immobilized penicillin acylase has been studied in the presence of substrate (penicillin G) and products (phenylacetic acid and 6-aminopenicillanic acid), under the hypothesis that substances which interact with the enzyme molecule during catalysis will have an effect on enzyme stability. The kinetics of immobilized penicillin acylase inactivation was a multistage process, decay constants being evaluated for the free-enzyme and enzyme complexes, from whose values modulation factors were determined for the effectors in each enzyme complex at each stage. 6-Aminopenicillanic acid and penicillin G stabilized the enzyme in the first stage of decay. Modulation factors in that stage were 0.96 for penicillin G and 0.98 for 6-aminopenicillanic acid. Phenylacetic acid increased the rate of inactivation in both stages, modulating factors being -2.31 and -2.23, respectively. Modulation factors influence enzyme performance in a reactor and are useful parameters for a proper evaluation. (c) 1996 John Wiley & Sons, Inc.     

Covalent binding of a nerve agent hydrolyzing enzyme within polyurethane foams

A phosphotriesterase preparation, extracted from Escherichia coli DH5alpha cells, was immobilized within a polyurethane foam matrix during polymer synthesis. The enzyme-foam interaction was shown to be covalent and analysis of the hydrolysis of paraoxon in aqueous solution demonstrated that more than 50% of the initial enzyme specific activity was retained after immobilization in the foam. Factors affecting the rate of paraoxon degradation include foam hydrophobicity, the degree of mixing applied to initiate polymerization, and foam pretreatment prior to use in substrate hydrolysis. The storage stability of the foam is significant, with phosphotriesterase-foam activity profiles exhibiting a three month half-life. Foams are currently being developed for biocatalytic air filtering, in which gaseous substrates will be simultaneously adsorbed and degraded by the immobilized enzyme system. (c) 1996 John Wiley & Sons, Inc.     

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。     

Immobilization of enzymes with polyaziridine: II. D-amino acid oxidase

Summary A novel method of enzyme immobilization using a tri-functional aziridine to immobilize enzymes was used to immobilize D-amino acid oxidase (DAAO) with good retention of enzymatic activity (62%–89%). The stability of the immobilized DAAO in a fixed bed reactor with continuous operation using D-phenylalanine as substrate yielded a projected half-life of 69 days which is far superior to other methods of immobilization of DAAO.     

Immobilized enzymes: Pectin esterase covalently coupled to dorous glass particles

Pectin esterase (E.C. 3.1.1.11) was covalently immobilized to porous glass particles by reaction of the native protein with pendant, benzoyl azide groups of the carrier. Enzyme loading on the carrier was 0.5 unit per ml as measured by pH stat, assay. Decreasing the size of the immobilized enzyme particles by grinding produced a 12-fold increase in activity suggesting severe internal mass transport restrictions on turnover kinetics, Gross fractionation of the citrus pectin substrate into high and low molecular weight categories and their subsequent use in kinetic characterization shows no effect of molecular weight upon the kinetic behavior of the native enzyme. In contrast the immobilized enzyme displayed a 5-fold increase in the apparent. K_m for the high molecular weight fraction relative to that of the low molecular weight fraction. A striking difference exists in the low pH profile of immobilized pectin esterase relative to the native enzyme. Carrier matrix interactions with the polyelectrolyte substrate are invoked to explain this difference. The thermal stability of the immobilized enzyme is relatively low and displays a half-life of approximately 2 weeks at 25°C.     

Continuous hydrolysis of olive oil by immobilized lipase in organic solvent

Lipase (EC 3.1.1.3) from Candida rugosa was immobilized with DEAE-Sephadex A50, Sephadex G50, Sephadex LH-20, Amberlite IRA94, and Amberlite XAD-7. The enzye immobilized with DEAE-Sephadex A50 was found to be most effective for continuous hydrolysis of olive oil in isooctane. For the continuous reaction, 0.2 g of dry immobilized enzyme was swollen with predetermined amount of water, and packed in a glass column reactor. When the organic solvent (Isooctane) containing olive oil substrate was cocurrently fed with aqueous buffer, the two phases were evenly distributed throughout the packed bed without surfactant supplement or prior mixing of the two phases. A small amount of the surfactant (AOT) was used only in packing procedure, and no additional surfactant was necessary thereafter. Effects of initial water content of the swollen gel, buffer types, and strength were examined in the continuous reaction. Our results suggest that the operational half-life was affected by desorption of the bound enzyme. Under the conditions of 20% olive oil in isooctane and 25 mM triethanolamine buffer (pH 7.0), operational half life was 220 h at 30 degrees C. The reactor was also operable with n-hexane, but the operational stability of the immobilized enzyme in n-hexane was only half of that in isooctane. Our results indicate that various enzyme carrier having hydrophilic or amphiphilic properties could be used for two-phase continuous reaction in packed-bed column, reactor without any surfactant supply or prior dispersion of the two immiscible phases. (c) 1992 John Wiley & Sons, Inc.     

Inversion of sucrose in a continuous process with β-d-fructofuranosidase (invertase) immobilized on bead DEAHP-cellulose

Inversion of sucrose with β-d-fructofuranosidase (EC 3.2.1.26) immobilized by the ionic bond on bead DEAHP-cellulose has been studied under flow conditions. Under these conditions, the inversion of sucrose is affected by the concentration and flow rate of the substrate and by the reaction temperature. The effect of substrate concentration on the reaction was investigated in the range 19.5–64.2 wt %; the effect of flow rate was examined in the range 0.25–5.57 g solution per min, and the temperature range used was 25–50°C. It was found that the activities of immobilized β-d-fructofuranosidase in stirred and flow reactors were the same. The lower activities of β-d-fructofuranosidase in the case of concentrated solutions, and of immobilized β-d-fructofuranosidase compared with the native enzyme are attributed to more difficult diffusion through the beads of the ion exchanger, especially of the strongly viscous substrate. A long-term investigation of the enzyme activity over a period of three months demonstrated the stability of the β-d-fructofuranosidase immobilized by the ionic bond on bead DEAHP-cellulose; the half-life of the enzyme was 215 days. It was also found that the immobilization of the enzyme on a carrier was more effective under flow conditions, i.e. through an ion exchanger in the column, than under the equilibrium conditions of a stirred reactor.     

Two-phase system membrane reactor with cofactor recycling.

For the purpose of constructing a two-phase system reactor the enzymatic process of l-menthol production with cofactor recycling was studied as a model. The half-life of the menthone reductase immobilized onto activated carbon was 4 times as high as that of the free enzyme. The enzyme was capable of regenerating NADH when methyl isobutyl carbinol was used as a second substrate. Continuous production of l-menthol was achieved by using a reactor equipped with a hydrophobic microfiltration membrane. It was found that both NAD(H) and the enzyme could be retained in the reactor and the products, l-methanol and methyl isobutyl ketone, passed through the membrane. The production of l-methanol was maintained for 270 h at a rate of 46.1 g l-1 d-1, and had decreased by one-half at 607 h. The recycling number of NAD(H) was 2500 (max. 3020) during the operation. The number of theoretical plates was calculated to be 40 for the separation of l-menthol from other reactants.     

Studies on the stability of immobilized xanthine oxidase and urate oxidase.

The stability of immobilized preparations of xanthine oxidase and urate oxidase was studied, and optimized, because of the potential joint use of both enzymes in clinical analysis. Xanthine oxidase was immobilized on cellulose, Sepharose, hornblende, Enzacryl-TIO, and porous glass. Thehalf-lives of these preparations at 30 degree C ranged from 40 min to 5.0 hr. In this respect immobilized enzyme resembled soluble enzyme in dilute solution (0.11 mg/ml), when the half-live was about 3.5 hr. More concentrated enzyme solution (1 mg/ml) had a half-life of 64 hr, and was, therefore, considerably more stable than the untreated immobilized xanthine oxidase preparations. Inclusion of albumen in storage and assay buffer increased the half-life of bound xanthine oxidase. So also did treatment with glutaraldehyde: in the case of xanthine oxidase bound to Enzarcyl-TIO such treatment increased the half-life at 30 degree C from 3 hr to about 100 hr. Immobilized xanthine dehydrogenase was more stable than immobilized xanthine oxidase: the dehydrogenase lost no activity during continuous assay for 5 hr at 30 degree C. The stability of immobilized urate oxidase depended on the quantity of enzyme used and on the time of stirring during immobilization: thus a preparation was made (by stirring urate oxidase (48 mg/g support) with Enzacryl-TIO for 24 hr) which lost no activity during 350 hr at 30 degree C.     

Immobilized Clostridium perfringens neuraminidase. Substrate cleavage and enzyme release during incubation.

Pure Clostridium perfringens neuraminidase was immobilized on Sepharose 4 B, azido-Sepharose 4 B and controlled pore glass (CPG)- glycophase using different coupling procedures. The immobilized enzyme showed increased stability under various conditions relative to the soluble enzyme. The low release of active enzyme from the supports under incubation conditions was quantitated using a highly sensitive radioactive assay. The activity of the immobilized enzyme was dependent on the nature of the support and the substrate. Activity decreased with increasing substrate molecular weight, but the enzyme showed improved cleavage with GD1a micelles and human erythrocytes, substrates having ordered surface properties. Uses of immobilized neuraminidase in biochemistry and cell biology are considered and evaluated relative to the measured release of enzyme from the supports reported and to the molecular size and organization of possible substrates.     

交联葡聚糖结合无花果蛋白酶的制备与性质

本文报道了将Sephadgx G-200与对β-硫酸酯乙砜基苯胺(SESA)首先醚化制备对氨基苯砜乙基交联葡聚糖(ABSE-Sephadex G-200),然后经重氮化固定无花果蛋白酶。固定化酶的活力回收达69％。BANA对该酶固定化过程中的活性变化有保护作用。天然酶与固定化酶都具有良好的耐热性,在69°～70℃,80min固定化酶较天然酶稳定。 用苯甲酰-DL-精氨酰-β-荼胺(BANA)为底物,在半胱氨酸存在下,测定了两种形式酶的动力学性质。在pH7.7的磷酸盐缓冲系统中,37℃,天然无花果蛋白酶的K_m=0.32mol/L;在间歇振摇下固定化酶的表观K′m=1.02mmol/L。最适pH无明显改变,均为pH7.7。     

Immobilization of functionally unstable catechol-2,3-dioxygenase greatly improves operational stability

Thermophilic catechol 2,3-dioxygenase (EC 1.13.11.2) from Bacillus stearothermophilus has been immobilized on highly activated glyoxyl agarose beads. The enzyme could be fully immobilized at 4 degrees C and pH 10.05 with a high retention of activity (around 80%). Enzyme immobilized under these conditions showed little increase in thermostability compared with the soluble enzyme, but further incubation of immobilized enzyme at 25 degrees C and pH 10.05 for 3 h before borohydride reduction resulted in conjugates exhibiting a 100-fold increase in stability (c.f. the free enzyme). The stability of catechol 2,3-dioxygenase immobilized under these conditions was essentially independent of protein concentration whereas free enzyme was rapidly inactivated at low protein concentrations. An apparent stabilization factor of over 700-fold was recorded in the comparison of free and immobilized catechol 2,3-dioxygenases at protein concentrations of 10 μg/ml. Immobilization increased the 'optimum temperature' for activity by 20 degrees C, retained activity at substrate concentrations where the soluble enzyme was fully inactivated and enhanced the resistance to inactivation during catalysis. These results suggest that the immobilization of the enzyme under controlled conditions with the generation of multiple covalent links between the enzyme and matrix both stabilized the quaternary structure of the protein and increased the rigidity of the subunit structures.     

Continuous D-tagatose production by immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

D-Tagatose was continuously produced using thermostable L-arabinose isomerase immobilized in alginate with D-galactose solution in a packed-bed bioreactor. Bead size, L/D (length/diameter) of reactor, dilution rate, total loaded enzyme amount, and substrate concentration were found to be optimal at 0.8 mm, 520/7 mm, 0.375 h(-1), 5.65 units, and 300 g/L, respectively. Under these conditions, the bioreactor produced about 145 g/L tagatose with an average productivity of 54 g tagatose/L x h and an average conversion yield of 48% (w/w). Operational stability of the immobilized enzyme was demonstrated, with a tagatose production half-life of 24 days.     

Immobilization of glucoamylase by adsorption on carbon supports and its application for heterogeneous hydrolysis of dextrin

Glucoamylase (GA) was immobilized by adsorption on carbon support: on Sibunit, on bulk catalytic filamentous carbon (bulk CFC) and on activated carbon (AC). This was used to prepare heterogeneous biocatalysts for the hydrolysis of starch dextrin. The effect of the texture characteristics and chemical properties of the support surface on the enhancement of the thermal stability of the immobilized enzyme was studied, and the rates of the biocatalyst's thermal inactivation at 65-80 degrees C were determined. The thermal stability of glucoamylase immobilized on different carbon supports was found to increase by 2-3 orders of magnitude in comparison with the soluble enzyme, and decrease in the following order: GA on Sibunit>GA on bulk CFC>GA on AC. The presence of the substrate (dextrin) was found to have a significant stabilizing effect. The thermal stability of the immobilized enzyme was found to increase linearly when the concentration of dextrin was increased from 10 wt/vol % to 50 wt/vol %. The total stabilization effect for glucoamylase immobilized on Sibunit in concentrated dextrin solutions was about 10(5) in comparison with the enzyme in a buffer solution. The developed biocatalyst, 'Glucoamylase on Sibunit' was found to have high operational stability during the continuous hydrolysis of 30-35 wt/vol % dextrin at 60 degrees C, its inactivation half-time (t1/2) exceeding 350 h. To improve the starch saccharification productivity, an immersed vortex reactor (IVR) was designed and tested in the heterogeneous process with the biocatalyst 'Glucoamylase on Sibunit'. The dextrin hydrolysis rate, as well as the process productivity in the vortex reactor, was found to increase by a factor of 1.2-1.5 in comparison with the packed-bed reactor.