A new method for immobilization of acetylcholinesterase

A new method for immobilization of acetylcholinesterase (AChE) to alginate gel beads by activating the carbonyl groups of alginate using carbodiimide coupling agent has been successfully developed. Maximum reaction rate (V _max) and Michaelis–Menten constant (K _m) were determined for the free and binary immobilized enzyme. The effects of pH, temperature, storage stability, reuse number and thermal stability on the free and immobilized AChE were also investigated. For the free and binary immobilized enzyme on the Ca–alginate gel beads, optimum pH values were found to be 7 and 8, respectively. Optimum temperatures for the free and immobilized enzyme were observed to be 30 and 35 °C, respectively. Upon 60 days of storage the preserved activity of free and immobilized enzyme were found as 4 and 68%, respectively. In addition, reuse number, and thermal stability of the free AChE were increased by as a result of binary immobilization.     

Immobilization and properties of β-D-galactosidase fromLactobacillus bulgaricus

β-D-galactosidase (EC 3.2.1.23) fromLactobacillus bulgaricus (1373) was immobilized by entrapment in a Polyacrylamide gel lattice. The enzymatic properties of the immobilized β-galactosidase were compared with those of the native enzyme. The temperature and pH optima were not affected by the immobilization. After entrapment of the enzyme no significant change was observed in its thermostability. The pH stability of the immobilized enzyme was higher than that of the native enzyme on the acidic side. TheK _m values for the immobilized and native β-galactosidase with both lactose ando-nitrophenyl-β-D-galactoside as substrates were comparable. The immobilized enzyme could be repeatedly used 12 times without any loss of activity. No loss in the activity of the immobilized β-galactosidase was found after its storage for 30 days at 4°C and for 20 days at 25°C.     

Continuous production ofL-malic acid by immobilizedBrevibacterium ammoniagenes cells

Summary Continuous production ofL-malic acid from fumaric acid using immobilized microbial cells was investigated. Several microorganisms having fumarase activity were immobilized into a polyacrylamide gel lattice. Among the microorganisms tested, immobilizedBrevibacterium ammoniagenes IAM 1645 showed the highest enzyme activity, but produced an unwanted by-product, succinic acid. Conditions for suppression of this side reaction were investigated, and bile extract treatment of immobilized cells was found to be effective.The bile extract treatment of immobilized cells also resulted in a marked increase of reaction rate forL-malic acid formation.No difference was observed between the native enzyme and immobilized cells in optimal pH and temperature of the enzyme reaction.The effect of temperature on the reaction rate and the stability of fumarase activity of an immobilized cell column were investigated under conditions of continuous enzyme reaction. The decay of enzyme activity during continuous enzyme reaction was expressed by an exponential relationship. Half-life of the fumarase activity of the immobilized cell column at 37°C was calculated to be 52.5 days.Presented at the Annual Meeting of the Society of Fermentation Technology, Japan, Osaka, Japan, October 30, 1975.     

Transformation of rifamycin B with immobilized rifamycin oxidase of Curvularia lunata

Rifamycin oxidase of Curvularia lunata was immobilized on polyacrylamide gel. The optimum pH and temperature for immobilized enzyme reaction were 6.5 and 50 °C, respectively. Enzyme stability increased on immobilization and the half lives of immobilized enzyme preparations at 30 and 40 °C were 30 and 11.5 d, respectively. With 2.5 mm beads diffusional resistances were observed. Reusability studies showed that 1 mm size beads gave a higher rate of transformation in comparison with 2 or 2.5 mm beads.     

Improved immobilized enzyme systems using spherical micro silica sol-gel enzyme beads

Spherical micro silica sol-gel immobilized enzyme beads were prepared in an emulsion system using cyclohexanone and Triton-X 114. The beads were used for thein situ immobilization of transaminase, trypsin, and lipase. Immobilization during the sol to gel phase transition was investigated to determine the effect of the emulsifying solvents, surfactants, and mixing process on the formation of spherical micro sol-gel enzyme beads and their catalytic activity. The different combinations of sol-gel precursors affected both activity and the stability of the enzymes, which suggests that each enzyme has a unique preference for the silica gel matrix dependent upon the characteristics of the precursors. The resulting enzyme-entrapped micronsized beads were characterized and utilized for several enzyme reaction cycles. These results indicated improved stability compared to the conventional crushed form silica sol-gel immobilized enzyme systems.     

Efficient immobilization technique for enhancement of cellobiose dehydrogenase activity on silica gel

In this study, cellobiose dehydrogenase (CDH) of Phanerochaete chrysosporium ATCC 32629 was immobilized on silica gel for the further application of CDH in the saccharification process of biomass. To prevent the loss of enzyme activity during enzyme immobilization, the pretreatment of CDH was performed by various pretreatment materials before immobilization. When pretreated enzymes were used in immobilization, the activities of immobilized CDH were higher than non-pretreated CDH even in same amounts of immobilized protein. The specific activity of pretreated immobilized CDH with lactose was about two times higher than that of non-pretreated immobilized CDH. Moreover, the pretreated immobilized CDH showed better reusability than non-pretreated immobilized CDH, with 67.3% of its original activity being retained after 9 reuses.     

Novel sol-gel immobilization of horseradish peroxidase employing a detergentless micro-emulsion system

A novel sol-gel immobilization method employing a detergentless micro-emulsion system that consisted ofn-hexane/iso-propanol/water was developed and used to immobilize a horseradish peroxidase (HRP). Micro-sized gel powder containing enzymes was generated in the ternary solution without drying and grinding steps or the addition of detergent, therefore, the method described in this study is a simple and straightforward process for the manufacture of gel powder. The gel powder made in this study was able to retain 84% of its initial enzyme activity, which is higher than gel powders produced through other immobilization methods. Furthermore, the HRP immobilized using this method, was able to maintain its activity at or above 95% of its initial activity for 48h, whereas the enzyme activities of free HRP and HRP that was immobilized using the other sol-gel method decreased dramatically. In addition, even when in the presence of excess hydrogen peroxide, the enzyme immobilized using the novel sol-gel method described here was more stable than enzymes immobilized using the other method.     

Immobilization of endo-polygalacturonase from Aspergillus ustus on silica gel

Endo-polygalacturonase from Aspergillus ustus when immobilized on to modified silica gel retained 28% of its original activity. The immobilized enzyme could be re-used through 10 cycles of reaction with almost 90% retention of its original activity. It had increased thermostability over its soluble form: the half-life of the soluble enzyme at 40 °C was less than 10 h whereas the immobilized enzyme retained 82% of its activity after 10 h at 40 °C. Similarly, at 50 °C the half-life of the soluble enzyme was 30 min whereas that of the immobilized enzyme was 5 h.     

Application of enzyme flow microcalorimetry to the study of microkinetic properties of immobilized biocatalyst

Summary Flow microcalorimeter was used for the study of microkinetic properties of Escherichia coli cells enriched with the penicillin G acylase activity immobilized in calcium pectate gel. The experimental kinetic data were obtained by measurement of the thermometric signal in the microcalorimetric column with immobilized enzyme and described by the introduced mathematical model involving the mass transfer and reaction kinetic phenomena.     

Purification, immobilization and characterization of linoleic acid isomerase on modified palygorskite

Linoleic acid isomerase from Lactobacillus delbrueckii subsp. bulgaricus 1.1480 was purified by DEAE ion-exchange chromatography and gel filtration chromatography. An overall 5.1% yield and purification of 93-fold were obtained. The molecular weight of the purified protein was ~41 kDa which was analyzed by SDS-PAGE. The purified enzyme was immobilized on palygorskite modified with 3-aminopropyltriethoxysilane. The immobilized enzyme showed an activity of 82 U/g. The optimal temperature and pH for the activity of the free enzyme were 30 °C and pH 6.5, respectively; whereas those for the immobilized enzyme were 35 °C and pH 7.0, respectively. The immobilized enzyme was more stable than the free enzyme at 30–60 °C, and the operational stability result showed that more than 85% of its initial activity was retained after incubation for 3 h. The K _m and V _max values of the immobilized enzyme were found to be 0.0619 mmol l⁻¹ and 0.147 mmol h⁻¹ mg⁻¹, respectively. The immobilized enzyme had high operational stability and retained high enzymatic activity after seven cycles of reuse at 37 °C.     

Immobilization of horseradish peroxidase on β-cyclodextrin-capped silver nanoparticles: Its future aspects in biosensor application

This study aimed to work out a simple and high-yield procedure for the immobilization of horseradish peroxidase on silver nanoparticle. Ultraviolet–visible (UV-vis) and Fourier-transform infrared spectroscopy and transmission electron microscopy were used to characterize silver nanoparticles. Horseradish peroxidase was immobilized on β-cyclodextrin-capped silver nanoparticles via glutaraldehyde cross-linking. Single-cell gel electrophoresis (Comet assay) was also performed to confirm the genotoxicity of silver nanoparticles. To decrease toxicity, silver nanoparticles were capped with β-cyclodextrin. A comparative stability study of soluble and immobilized enzyme preparations was investigated against pH, temperature, and chaotropic agent, urea. The results showed that the cross-linked peroxidase was significantly more stable as compared to the soluble counterpart. The immobilized enzyme exhibited stable enzyme activities after repeated uses.     

L-Lactic acid production from raw cassava starch in a circulating loop bioreactor with cells immobilized in loofa (Luffa cylindrica)

l-Lactic acid was produced from raw cassava starch, by simultaneous enzyme production, starch saccharification and fermentation in a circulating loop bioreactor with Aspergillus awamori and Lactococcus lactis spp. lactis immobilized in loofa sponge. A. awamori was immobilized directly in cylindrical loofa sponge while the L. lactis was immobilized in a loofa sponge alginate gel cube. In the loofa sponge alginate gel cube, the sponge serves as skeletal support for the gel with the cells. The alginate gel formed a hard outer layer covering the soft porous gel inside. By controlling the rate and frequency of broth circulation between the riser and downcomer columns, the riser could be maintained under aerobic condition while the downcomer was under anaerobic condition. Repeated fed-batch l-lactic acid production was performed for more than 400 h and the average lactic acid yield and productivity from raw cassava starch were 0.76 g lactic acid g^–1 starch and 1.6 g lactic acid l^–1 h^–1, respectively.     

Acid proteinases production by humicola lutea cells immobilized in polyhydroxyethylmethacrylate gel

The spores of Humicola lutea entrapped in polyhydroxyethylmethacrylate gel were precultivated in production medium for mycelial formation. The immobilized mycelium was reused in batch mode for acid proteinases production. The influence of precultivation time, initial inoculum gel volume, and gel particle size on the enzyme activity and proteinases production half-life were studied. After 70 h precultivation of the entrapped spores (10 ml initial inoculum volume, 12–27 mm³ gel particle size) maximum proteinases activity of 100–140% (compared with free cells) was registered in 15 reaction cycles. Under the same condition the half-life time was 18 cycles, while for the free cells it was 5 cycles. The main advantage of the polyhydroxyethylmethacylate immobilized H. lutea was the long acid proteinases production half-life at a low concentration of outgrowing cells in the medium.     

Glucoamylase and α-amylase production by immobilized Aspergillus niger

Summary Aspergillus niger mycelia or spores were immobilized in calcium alginate gel beads and employed for production of glucoamylase and -amylase by repeated batch process. The immobilized mycelium produced lower enzyme activities than immobilized spores germinated in a growth medium and subsequently cultured in an enzyme production medium. In repeated batch experiments, free cells could be used for only 4 4-day batches, whereas with immobilized spores at least 11 4-day batches with a gradual increase in enzyme activities in each successive batch were possible. The activity ratio of glucoamylase and -amylase produced was altered by immobilization.     

Mechanism for reversible inactivation of immobilized β-galactosidase from Bacillus circulans during continuous production of galacto-oligosaccharides

Summary The specific activity-dependent stability of the immobilized -galactosidase-2 (-d-galactoside galactohydrolase, EC 3.2.1.23) from Bacillus circulans during the continuous production of galactooligosaccharides from lactose was studied. This was done by measuring the elution pattern of saccharides from the various immobilized Merckogel (controlled pore silica gel) columns and the amount of saccharides remaining in the gel. It was suggested that oligosaccharides produced were trapped inside the three dimensional enzyme aggregate with the immobilized enzyme having a specific activity of 240 units/g of wet gel, causing gradual inactivation, while the immobilized enzyme with 15 units/g of wet gel was stable since the oligosaccharides were not accumulated.Free -galactosidase-2 was stable during continuous reaction in a membrane reactor.     

Chainia Penicillin V Acylase: Strain Characteristics, Enzyme Immobilization, and Kinetic Studies

Aerobic cultures of an actinomycete were found to produce penicillin V acylase (PVA) (PA, EC-3.5.1.11) extracellularly. The presence of L-2-3 diamino-propionic acid in cell wall and formation of sclerotia on culture media led to its identification as Chainia, a sclerotial Streptomyces. Partially purified acylase was adsorbed on kieselguhr and entrapped in polyacrylamide gel. The immobilized preparation proved effective with respect to retention of enzyme and enzyme activity even after 15 successful cycles. The pH optimum for crude enzyme was in the range of pH 7.5–8.0, and for the (NH4)₂ SO₄ fraction it was pH 8.5. The immobilized enzyme showed maximal activity at pH 9.5. The optimum temperature for acylase activity was at 55°C. The crude enzyme, ammonium sulfate fraction, and immobilized enzyme showed K _m value for penicillin V of 6.13 mM, 14.3 mM, and 17.1 mM, respectively. Received: 11 December 1997 / Accepted: 9 April 1998     

Purification of malic enzyme from bovine heart mitochondria by affinity chromatography

A simple two-step method for the purification of malic enzyme from bovine heart mitochondria in high yield is described. It consists of successive affinity chromatography steps on immobilized C⁸-(aminohexyl)-NADP and N⁶-(aminohexyl)-ADP. The molecular weight estimated by gel filtration of the homogeneous enzyme is 250,000 and the subunit molecular weight by SDS-polyacrylamide gel electrophoresis is 59,000.     

A new method of whole microbial cell immobilization

Summary A simple method for producing gelatin-immobilized microbial cells is described. The microorganism used as an example was baker's yeast (Saccharomyces cerevisiae). The gel particles containing these cells were utilized as an immobilized enzyme (invertase) both in stirred batch and packed bed systems.     

Continuous production of galacto-oligosaccharides from lactose using immobilized β-galactosidase from Bacillus circulans

Summary -Galactosidase-2 (-d-galactoside galactohydrolase, EC 3.2.1.23) from Bacillus circulans was purified using hydroxyapatite gel chromatography and immobilized onto Duolite ES-762 (phenolformaldehyde resin) and Merckogel (controlled pore silica gel) for continuous production of galacto-oligosaccharides using lactose as the substrate. The maximum amount of ologosaccharides produced by the immobilized enzyme was 35–40% of the total sugar during hydrolysis of 4.56% lactose. Partially purified -galactosidase from B. circulans was also immobilized onto various supports for the same purpose. The stability of the immobilized -galactosidase-2 or partially purified enzyme during a continuous reaction depended on their supports and specific activity. Of the supports tested, Merckogel was best for operational stability. With this support, the enzyme was quite stable with specific activity up to 15 units/g of wet gel; it was reversibly inactivated with more.     

Enhancement and stabilization of the production of glucoamylase by immobilized cells of Aureobasidium pullulans in a fluidized-bed reactor

Summary Glucoamylase production by Aureobasidium pollulans A-124 was compared in free-living cells, cells immobilized in calcium alginate gel beads aerated on a rotary shaker (agitation rate 150 rpm), and immobilized cells aerated in an air bubble column reactor. Fermentation conditions in the bioreactor were established for bead concentration, substrate (starch) concentration, calcium chloride addition to the fermentation medium, and rate of aeration. Production of glucoamylase was optimized at approximately 1.5 units of enzyme activity/ml medium in the bioreactor under the following conditions: aeration rate, 2.0 vol air per working volume of the bioreactor (280 ml) per minute; gel bead concentration, 30% of the working volume; substrate (starch) concentration, at 0.3% (w/v); addition of calcium chloride to the medium at a final concentration of 0.01 M. Productivity levels were stabilized through the equivalent of ten batches of medium with the original inoculum of immobilized beads. Offprint requests to: M. Petruccioli