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.     

Comparison of covalent immobilization of amylase on polystyrene pellets with pentaethylenehexamine and pentaethylene glycol spacers

α-Amylase from Aspergillus oryzae was covalently immobilized onto polystyrene pellets with pentaethylenehexamine (PS-PEHA-Ald) and pentaethylene glycol (PS-PG-Ald) carrying a terminal aldehyde group. Optimum immobilization occured at pH 8.0 and 25 °C, and at pH 7.0 and 35 °C for PS-PEHA-Ald and PS-PG-Ald, respectively. PS-PEHA-Ald immobilized enzyme retained approximately 75% of the initial activity over 45 days of storage, 70% of the initial activity after nine runs of recycling and displayed the better resistance to detrimental metal ions. PS-PG-Ald immobilized enzyme retained approximately 50% of the initial activity in 8h at 70 °C. The catalytic efficiencies of PS-PEHA-Ald immobilized and PS-PG-Ald immobilized amylase were 1.42 and 1.29 times higher than that of native enzyme. The activation energy of the reaction mediated by the amylase was reduced by 58.1% and 57.3% when PS-PEHA-Ald and PS-PG-Ald used as support respectively.     

Immobilization of invertase onto poly(3-methylthienyl methacrylate)/poly(3-thiopheneacetic acid) matrix

A novel immobilization matrix, poly(3-methylthienyl methacrylate)–poly(3-thiopheneacetic acid) (PMTM–PTAA), was synthesized and used for the covalent immobilization of Saccharomyces cerevisiae invertase to produce invert sugar. The immobilization resulted in 87% immobilization efficiency. Optimum conditions for activity were not affected by immobilization and the optimum pH and temperature for both free and immobilized enzyme were found to be 4.5 and 55 °C, respectively. However, immobilized invertase was more stable at high pH and temperatures. The kinetic parameters for free and immobilized invertase were also determined using the Lineweaver–Burk plot. The K_m values were 35 and 38 mM for free and immobilized enzyme, respectively. The V_max values were 29 and 24 mg glucose/mg enzyme min for free and immobilized enzyme, respectively. Immobilized enzyme could be used for the production of glucose and fructose from sucrose since it retained almost all the initial activity for a month in storage and retained the whole activity in repeated 50 batch reactions.     

Immobilization of polyphenol oxidase on chitosan–SiO<Subscript>2</Subscript> gel for removal of aqueous phenol

A partially purified potato polyphenol oxidase (PPO) was immobilized in a cross-linked chitosan–SiO₂ gel and used to treat phenol solutions. Under optimized conditions (formaldehyde 20 mg/ml, PPO 4 mg/ml and pH 7.0), the activity of immobilized PPO was 1370 U/g and its K _m value for catechol was 12 mm at 25°C. The highest activity of immobilized enzyme was at pH 7.4. Immobilization stabilized the enzyme with 73 and 58% retention of activity after 10 and 20 days, respectively, at 30°C whereas most of the free enzyme was inactive after 7 days. The efficiency of removing phenol (10 mg phenol/l) by the immobilized PPO was 86%, and about 60% removal efficiency was retained after five recycles. The immobilized PPO may thus be a useful for removing phenolic compounds from industrial waste-waters.     

Binary immobilization of tyrosinase by using alginate gel beads and poly(acrylamide-co-acrylic acid) hydrogels

The use of the immobilized and the stable enzymes has immense potential in the enzymatic analysis of clinical, industrial and environmental samples. However, their widespread uses are limited due to the high cost of their production. In this study, binary immobilization of tyrosinase by using Ca-alginate and poly(acrylamide-co-acrylic acid) [P(AAm-co-AA)] was investigated. Maximum reaction rate (Vmax) and Michaelis-Menten constant (Km) were determined for the free and binary immobilized enzymes. The effects of pH, temperature, storage stability, reuse number and thermal stability on the free and immobilized tyrosinase were also examined. For the free and binary immobilized enzymes on Ca-alginate and P(AAm-co-AA), optimum pH was found to be 7 and 5, respectively. Optimum temperature of the free and immobilized enzymes was observed to be 30 and 35 degrees C, respectively. Reuse number, storage and thermal stability of the free tyrosinase were increased by a result of binary immobilization.     

Covalent immobilization of ω-transaminase from Vibrio fluvialis JS17 on chitosan beads

Chitosan beads were prepared by emulsion method and used for the immobilization of ω-transaminase of Vibrio fluvialis. The yield of enzyme immobilization (54.3%) and its residual activity (17.8%) were higher than those obtained with other commercial beads. ω-Transaminase was effectively immobilized on the chitosan beads at pH 6.0. The optimal pH of the immobilized enzyme was pH 9.0, which is the same as that of the free enzyme. The immobilized enzyme on chitosan beads retained ca. 77% of its conversion after five consecutive reactions with the 25 mM substrate, while the immobilized enzyme on Eupergit^® C retained 12%. Also, the immobilized ω-transaminase on chitosan bead retained 70% of initial activity when it's stored at 4 °C for 3.5 weeks. Addition of the co-factor, pyridoxal 5-phosphate (PLP), was needed to maintain the stability of the immobilized ω-transaminase.     

Comparison of some properties of free and immobilized alpha-amylase by Aspergillus sclerotiorum in calcium alginate gel beads

Some properties of immobilized alpha-amylase by Aspergillus sclerotiorum within calcium alginate gel beads were investigated and compared with soluble enzyme. Optimum pH and temperature were found to be 5.0 and 40 degrees C, respectively, for both soluble and immobilized enzymes. The immobilized enzyme had a better Km value, but kcat/Km values were the same for both enzymes. Entrapment within calcium alginate gel beads improved, remarkably, the thermal and storage stability of alpha-amylase. The half life values of immobilized enzyme and soluble enzyme at 60 degrees C were 164.2, and 26.2 min, respectively. The midpoint of thermal inactivation (Tm) shifted from 56 degrees C (for soluble enzyme) to 65.4 degrees C for immobilized enzyme. The percentages of soluble starch hydrolysis for soluble and immobilized alpha-amylase were determined to be 97.5 and 92.2% for 60 min, respectively.     

Bioconversion of D-galactose to D-tagatose: continuous packed bed reaction with an immobilized thermostable L-arabinose isomerase and efficient purification by selective microbial degradation

The continuous enzymatic conversion of D-galactose to D-tagatose with an immobilized thermostable L-arabinose isomerase in packed-bed reactor and a novel method for D-tagatose purification were studied. L-arabinose isomerase from Thermoanaerobacter mathranii (TMAI) was recombinantly overexpressed and immobilized in calcium alginate. The effects of pH and temperature on D-tagatose production reaction catalyzed by free and immobilized TMAI were investigated. The optimal condition for free enzyme was pH 8.0, 60°C, 5 mM MnCl(2). However, that for immobilized enzyme was pH 7.5, 75°C, 5 mM MnCl(2). In addition, the catalytic activity of immobilized enzyme at high temperature and low pH was significantly improved compared with free enzyme. The optimum reaction yield with immobilized TMAI increased by four percentage points to 43.9% compared with that of free TMAI. The highest productivity of 10 g/L h was achieved with the yield of 23.3%. Continuous production was performed at 70°C; after 168 h, the reaction yield was still above 30%. The resultant syrup was then incubated with Saccharomyces cerevisiae L1 cells. The selective degradation of D-galactose was achieved, obtaining D-tagatose with the purity above 95%. The established production and separation methods further potentiate the industrial production of D-tagatose via bioconversion and biopurification processes.     

Immobilization of α-galactosidase on galactose-containing polymeric beads

Industrial application of α-galactosidase requires efficient methods to immobilize the enzyme, yielding a biocatalyst with high activity and stability compared to free enzyme. An α-galactosidase from tomato fruit was immobilized on galactose-containing polymeric beads. The immobilized enzyme exhibited an activity of 0.62 U/g of support and activity yield of 46%. The optimum pH and temperature for the activity of both free and immobilized enzymes were found as pH 4.0 and 37 °C, respectively. Immobilized α-galactosidase was more stable than free enzyme in the range of pH 4.0–6.0 and more than 85% of the initial activity was recovered. The decrease in reaction rate of the immobilized enzyme at temperatures above 37 °C was much slower than that of the free counterpart. The immobilized enzyme shows 53% activity at 60 °C while free enzyme decreases 33% at the same temperature. The immobilized enzyme retained 50% of its initial activity after 17 cycles of reuse at 37 °C. Under same storage conditions, the free enzyme lost about 71% of its initial activity over a period of 7 months, whereas the immobilized enzyme lost about only 47% of its initial activity over the same period. Operational stability of the immobilized enzyme was also studied and the operational half-life (t_1/2 was determined as 6.72 h for p-nitrophenyl α-d-galactopyranoside (PNPG) as substrate. The kinetic parameters were determined by using PNPG as substrate. The K_m and V_max values were measured as 1.07 mM and 0.01 U/mg for free enzyme and 0.89 mM and 0.1 U/mg for immobilized enzyme, respectively. The synthesis of the galactose-containing polymeric beads and the enzyme immobilization procedure are very simple and also easy to carry out.     

Water purification through bioconversion of phenol compounds by tyrosinase and chemical adsorption by chitosan beads

Enzymatic removal of various phenol compounds from artificial wastewater was undertaken by the combined use of mushroom tyrosinase (EC 1.14.18.1) and chitosan beads as function of pH value, temperature, tyrosinase dose, and hydrogen peroxide-to-substrate ratio. Chitosan film incubated in a p-crersol+tyrosinase mixture had the main peaks at 400-470 nm assigned to chemically adsorbed quinone derivatives, which increased over the immersion time. These results indicate that removal of phenol compounds is caused by their tyrosinase-catalyzed oxidation to the corresponding quinone derivatives and the subsequent chemical adsorption on the chitosan film. The optimum conditions for quinone adsorption were determined to be pH 7 and 45 degrees C for p-cresol. Some alkyl-substituted phenol compounds were removed by adsorption of quinone derivatives enzymatically generated on the chitosan beads, and the % removal for p-cresol, 4-ethylphenol, 4-n-propylphenol, 4-n-butylphenol, and p-chlorophenol went up to 93%. In addition, 4-tert-butylphenol underwent tyrosinase-catalyzed oxidation in the presence of hydrogen peroxide. This procedure was applicable to removal of chlorophenols and alkyl-substituted phenols.     

l-Dopa synthesis using tyrosinase immobilized on magnetic beads

Magnetic beads were prepared via suspension polymerization of glycidyl methacrylate (GMA) and methyl methacrylate (MMA) in the presence of ferric ions. Following polymerization, thermal co-precipitation of the Fe(III) ions in the beads with Fe(II) ions under alkaline condition resulted in encapsulation of Fe₃O₄ nano-crystals within the polymer matrix. The magnetic beads were activated with glutaraldehyde, and tyrosinase enzyme was covalently immobilized on the support via reaction of amino groups under mild conditions. The immobilized enzyme was used for the synthesis of l-Dopa (1-3,4-dihydroxy phenylalanine) which is a precursor of dopamine. The immobilized enzyme was characterized by temperature, pH, operational and storage stability experiments. Kinetic parameters, maximum velocity of the enzyme (V_max) and Michaelis–Menten constant (K_m) values were determined as 1.05 U/mg protein and 1.0 mM for 50–75 μm and 2.00 U/mg protein and 4.0 mM for 75–150 μm beads fractions, respectively. Efficiency factor and catalytic efficiency were found to be 1.39 and 0.91 for 75–150 μm beads and 0.73 and 0.75 for 50–75 μm beads fractions, respectively. The catalytic efficiency of the soluble tyrosinase was 0.37. The amounts of immobilized protein were on the 50–75 μm and 75–150 μm fractions were 2.7 and 2.8 mg protein/g magnetic beads, respectively.     

Kinetic properties and storage stability of catalase immobilized on to florisil

The covalent immobilization of bovine liver catalase (CAT) on to florisil via glutaraldehyde was investigated. Optimum immobilization pH and temperature were determined as pH 6.0, 10 degrees C respectively, while the amount of initial CAT per g of carrier and immobilization time was determined as 5 mg g(-1) and 120 min, respectively. The Vmax values for free and immobilized CAT were found to be 1.7 x 10(5) and 2.0 x 10(4) micromol H2O2 min(-1) mg protein(-1), respectively, whereas KM values were 33.3 mM and 1722.0 mM respectively. Operational stability was determined by using a stirred batch-type column reactor. Immobilized CAT retained about 40% of its initial activity after 50 uses. It showed higher storage stability than free CAT at 4 degrees C and 25 degrees C. Its storage stability increased with increasing relative humidity (RH) from 0 to 20% of the medium. The highest storage stability was obtained in 20% RH, however, further increase in RH from 40 to 100% significantly decreased the storage stability.     

Immobilization of β-d-galactosidase from Kluyveromyces lactis on functionalized silicon dioxide nanoparticles: characterization and lactose hydrolysis

β-D-Galactosidase (BGAL) from Kluyveromyces lactis was covalently immobilized to functionalized silicon dioxide nanoparticles (10-20 nm). The binding of the enzyme to the nanoparticles was confirmed by Fourier transform-infrared spectroscopy (FTIR) and scanning electron microscopy (SEM). Functionalized nanoparticles showed 87% immobilization yield. Soluble and immobilized enzyme preparation exhibited pH-optima at pH 6.5 and 7.0, respectively, with temperature optima at 35 and 40°C, respectively. Michaelis constant (K(m)) was 4.77 and 8.4mM for free and immobilized BGAL, respectively. V(max) for the soluble and immobilized enzyme was 12.25 and 13.51 U/ml, respectively. Nanoparticle immobilized BGAL demonstrated improved stability after favoring multipoint covalent attachment. Thermal stability of the immobilized enzyme was enhanced at 40, 50 and 65°C. Immobilized nanoparticle-enzyme conjugate retained more than 50% enzyme activity up to the eleventh cycle. Maximum lactose hydrolysis by immobilized BGAL was achieved at 8h.     

Direct immobilization of tyrosinase enzyme from natural mushrooms (Agaricus bisporus) on D-sorbitol cinnamic ester

Mushroom tyrosinase was immobilized from an extract onto the totally cinnamoylated derivative of D-sorbitol by direct adsorption as a result of the intense hydrophobic interactions that took place. The immobilization pH value and mass of lyophilized mushrooms were important parameters that affected the immobilization efficiency, while the immobilization time and immobilization support concentration were not important in this respect. The extracted/immobilized enzyme could best be measured above pH 3.5 and the optimum measuring temperature was 55 degrees C. The apparent Michaelis constant using 4-tert-butylcatechol as substrate was 0.38+/-0.02 mM, which was lower than for the soluble enzyme from Sigma (1.41+/-0.20 mM). Immobilization stabilized the extracted enzyme against thermal inactivation and made it less susceptible to activity loss during storage. The operational stability was higher than in the case of the tyrosinase supplied by Sigma and immobilized on the same support. The results show that the use of p-nitrophenol as enzyme-inhibiting substrate during enzyme extraction and immobilization made the use of ascorbic acid unnecessary and is a suitable method for extracting and immobilizing the tyrosinase enzyme, providing good enzymatic activity and stability.     

Production and immobilization of a novel thermoalkalophilic extracellular amylase from bacilli isolate

A Thermoalkalophilic amylase was produced from an environmental bacterial isolate. The enzyme was then immobilized through its amino groups onto the epoxy rings of magnetic poly glycidyl methacrylate [m-poly (GMA)] beads. The free enzyme was active within a large pH range, between 7 and 12 and displayed the optimum activity at 95°C and pH 10. The immobilization appeared to increase the stability of the enzyme as its bound form showed optimum activity at 105°C and pH 11.0. Kinetic studies demonstrated that immobilized enzyme had higher K(m) and lower V(max) values. The activity of the free and bound enzyme was determined, at 37°C and pH 10.0 and pH 11.0, respectively, in the presence of various organic solvents and detergents (5%, v/v). Results obtained indicated that detergents, sodium dodecyl sulfate (SDS) and TritonX-100, caused six fold increase and that various organic solvents also increased the activity of the amylase.     

Production of lipase in a fermentor using a mutant strain of Corynebacterium species: its partial purification and immobilization

Extracellular Corynebacterium lipase was produced using a 2.5 L Chemap fermentor using 1300 ml fermentation medium at temperature 33 degrees C, agitator speed 50 rpm, aeration rate 1 VVM having KLa 16.21 hr(-1). Crude lipase was purified by salting out method followed by dialysis and immobilized using calcium alginate gel matrix followed by glutaraldehyde cross linking Purification process increased specific activity of enzyme from 2.76 to 114.7 IU/mg. Activity of immobilized enzyme was 107.31 IU/mg. Optimum temperature for purified and immobilized enzyme activity were 65 degrees and 50 degrees C respectively. Optimum pH was 8.0 in both the cases, Km and Vmax value for purified lipase were 111.1 micromol/min and 14.7% respectively. Ca2+ (5 mM) was found to be stimulator for enzyme activity. Immobilized lipase retained 68.18% of the original activity when stored for 40 days.     

Immobilization and characterization of lipase from an indigenous Bacillus aryabhattai SE3-PB isolated from lipid-rich wastewater

Abstract

Extracellular lipase from an indigenous Bacillus aryabhattai SE3-PB was immobilized in alginate beads by entrapment method. After optimization of immobilization conditions, maximum immobilization efficiencies of 77%?±?1.53% and 75.99%?±?3.49% were recorded at optimum concentrations of 2% (w/v) sodium alginate and 0.2?M calcium chloride, respectively, for the entrapped enzyme. Biochemical properties of both free and immobilized lipase revealed no change in the optimum temperature and pH of both enzyme preparations, with maximum activity attained at 60?°C and 9.5, respectively. In comparison to free lipase, the immobilized enzyme exhibited improved stability over the studied pH range (8.5–9.5) and temperature (55–65?°C) when incubated for 3?h. Furthermore, the immobilized lipase showed enhanced enzyme-substrate affinity and higher catalytic efficiency when compared to soluble enzyme. The entrapped enzyme was also found to be more stable, retaining 61.51% and 49.44% of its original activity after being stored for 30 days at 4?°C and 25?°C, respectively. In addition, the insolubilized enzyme exhibited good reusability with 18.46% relative activity after being repeatedly used for six times. These findings suggest the efficient and sustainable use of the developed immobilized lipase for various biotechnological applications.     

Immobilization of cellulase from newly isolated strain Bacillus subtilis TD6 using calcium alginate as a support material

Bacillus subtilis TD6 was isolated from Takifugu rubripes, also known as puffer fish. Cellulase from this strain was partially purified by ammonium sulphate precipitation up to 80% saturation, entrapped in calcium alginate beads, and finally characterized using CMC as the substrate. For optimization, various parameters were observed, including pH maximum, temperature maximum, sodium alginate, and calcium chloride concentration. pH maximum of the enzyme showed no changes before and after immobilization and remained stable at 6.0. The temperature maximum showed a slight increase to 60 °C. Two percent sodium alginate and a 0.15 M calcium chloride solution were the optimum conditions for acquisition of enzyme with greater stability. K (m) and V (max) values for the immobilized enzyme were slightly increased, compared with those of free enzyme, 2.9 mg/ml and 32.1 μmol/min/mL, respectively. As the purpose of immobilization, reusability and storage stability of the enzyme were also observed. Immobilized enzyme retained its activity for a longer period of time and can be reused up to four times. The storage stability of entrapped cellulase at 4 °C was found to be up to 12 days, while at 30 °C, the enzyme lost its activity within 3 days.     

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.     

Repeated batch production of agar-oligosaccharides from agarose by an amberlite IRA-900 immobilized agarase system

The production of agar-oligosaccharides from agarose by free and immobilized agarase, obtained from a Pseudomonas aeruginosa AG LSL-11 was investigated and the activity, longevity and the operational stability of immobilized enzyme was compared with that of the free enzyme. The agar hydrolyzed products of free enzyme and immobilized enzyme were neoagarobiose, neoagarotetraose and neoagarohexaose as evidenced by LC-MS analysis. The immobilization of agarase was confirmed by SEM and also by the enzymatic transformation of agarose into agaroligosaccharides. The free agarase showed maximum activity at 40°C, whereas it’s immobilized counterpart showed maximum activity at 45oC, however, the optimum pH for both systems remained unchanged (pH 8.0). The relative activities of free agarase at pH 9.0 and 10.0 were 90 and 74%, respectively, whereas, the corresponding activities of the immobilized system were determined to be 97 and 90%. The stabilities of free agarase at pH 9.0 and 10.0 were 80 and 60% respectively, but for the immobilized system the respective residual activities were estimated to be 97 and 85%. Immobilized agarase appears to be more tolerant to high temperatures in terms of its activity and stability as it is compared to that of the free enzyme which retained 74 and 50.84% of relative activity at 55 and 60°C while, free agarase retained only 40 and 16.79% of its original activity. Furthermore, the immobilized agarase could be reused in batches efficiently for eight cycles, and could be stored for 3 months at 4°C as wet beads and for more than 6 months as dry beads.