Synthesis of galacto-oligosaccharides by β-galactosidase from Aspergillus oryzae using partially dissolved and supersaturated solution of lactose

The effect of enzyme to substrate ratio, initial lactose concentration and temperature has been studied for the kinetically controlled reaction of lactose transgalactosylation with Aspergillus oryzae β-galactosidase, to produce prebiotic galacto-oligosaccharides (GOS). Enzyme to substrate ratio had no significant effect on maximum yield and specific productivity. Galacto-oligosaccharide syntheses at very high lactose concentrations (40, 50 and 60%, w/w, lactose monohydrate) were evaluated at different temperatures (40, 47.5 and 55°C). Within these ranges, lactose could be found as a supersaturated solution or a heterogeneous system with precipitated lactose, resulting in significant effect on GOS synthesis. An increase in initial lactose concentration produced a slight increase in maximum yield as long as lactose remained dissolved. Increase in temperature produced a slight decrease in maximum yield and an increase in specific productivity when supersaturation of lactose occurred during reaction. Highest yield of 29 g GOS/100 g lactose added was obtained at a lactose monohydrate initial concentration of 50% (w/w) and 47.5°C. Highest specific productivity of 0.38 g GOSh(-1) mg enzyme(-1) was obtained at lactose monohydrate initial concentration of 40% (w/w) and 55°C, where a maximum yield of 27 g GOS/100 g lactose added was reached. This reflects the complex interplay between temperature and initial lactose concentration on the reaction of synthesis. When lactose precipitation occurred, values of yields and specific productivities lower than 22 g GOS/100 g lactose added and 0.03 gGOSh(-1) mg enzyme(-1) were obtained, respectively.     

Synthesis of propyl-β-d-galactoside with free and immobilized β-galactosidase from Aspergillus oryzae

Synthesis of propyl-β-galactoside catalyzed by Aspergillus oryzae β-galactosidase in soluble form was optimized using response surface methodology (RSM). Temperature and 1-propanol concentration were selected as explanatory variables; yield and productivity were chosen as response variables. Optimal reaction conditions were determined by weighing the responses through a desirability function. Then, synthesis of propyl-β-galactoside was evaluated at the optimal condition previously determined, with immobilized β-galactosidase in glyoxyl-agarose and amino-glyoxyl-agarose, and with cross-linked aggregates (CLAGs). Yields of propyl-β-galactoside obtained with CLAGs, amino-glyoxyl-agarose and glyoxyl-agarose enzyme derivatives were 0.75, 0.81 and 0.87 mol/mol and volumetric productivities were 5.2, 5.6 and 5.9 mM/h, respectively, being significantly higher than the corresponding values obtained with the soluble enzyme: 0.47 mol/mol and 4.4 mM/h. As reaction yield was increased twofold with the glyoxyl-agarose derivative, this catalyst was chosen for evaluating the synthesis of propyl-β-galactoside in repeated batch operations. Then, after ten sequential batches, the efficiency of catalyst use was 115% higher than obtained with the free enzyme. Enzyme immobilization also favored product recovery, allowing catalyst reuse, and avoiding browning reactions. Propyl-β-galactoside was recovery by extraction in 90%v/v acetone with a purity higher than 99% and its synthesis was confirmed by mass spectrometry.     

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.     

A comparison of the kinetic properties of free and immobilized Aspergillus oryzae β-galactosidase

The objective of this work was to compare the properties of free and immobilized β-galactosidase (Aspergillus oryzae), entrapped in alginate–gelatin beads and cross-linked with glutaraldehyde. The free and immobilized forms of the enzyme showed no decrease in enzyme activity when incubated in buffer solutions in pH ranges of 4.5–7.0. The kinetics of lactose hydrolysis by the free and immobilized enzymes were studied at maximum substrate concentrations of 90 g/L and 140 g/L, respectively, a temperature of 35 °C and a pH of 4.5. The Michaelis–Menten model with competitive inhibition by galactose fit the experimental results for both forms. The K_m and V_m values of the free enzyme were 52.13 ± 2.8 mM and 2.56 ± 0.3 g_glucose/L min mg_enzyme, respectively, and were 60.30 ± 3.3 mM and 1032.07 ± 51.6 g_lactose/min m³_catalyst, respectively, for the immobilized form. The maximum enzymatic activity of the soluble form of β-galactosidase was obtained at pH 4.5 and 55 °C. Alternatively, the immobilized form was most active at pH 5.0 at 60 °C. The free and immobilized enzymes presented activation energies of 6.90 ± 0.5 kcal/mol and 7.7 ± 0.7 kcal/mol, respectively, which suggested that the immobilized enzyme possessed a lower resistance to substrate transfer.     

Hydrolysis of lactose by β-galactosidase immobilized in polyvinylalcohol

Summary Fungal -galactosidase was immobilized in polyvinylalcohol gel formed in pores of contton material. Temperature and pH effects on the activity of free and immobilized enzymes were studied. The optimum temperatures of free and immobilized enzymes were 60° C and 55° C respectively. The pH optimum ranged from 4.5 to 5.0 for both enzymes. The thermal stability of the immobilized -galactosidase was slightly higher. The K_m values for soluble and immobilized enzymes were respectively 1.9 mM and 2.5 mM. The optimization of conditions for a highly effective hydrolysis of 4% lactose solution and reusability of the immobilized enzyme resulted in 75% hydrolysis after 5–6 h. The degree of conversion decreased to 50% after 30 repeated runs. The capacity of the immobilized enzyme to hydrolyze lactose in whey was also studied.     

Cost effective surface functionalization of silver nanoparticles for high yield immobilization of Aspergillus oryzae β-galactosidase and its application in lactose hydrolysis

The present study demonstrates synthesis, characterization and surface functionalization of silver nanoparticles (AgNPs) via glutaraldehyde for high yield immobilization of Aspergillus oryzae β-galactosidase. Soluble β-galactosidase (SβG), enzyme adsorbed on unmodified AgNPs (UβG) and surface modified AgNPs (MβG) showed same pH-optima at pH 4.5. However, it was observed that MβG exhibited enhanced pH stability toward acidic and alkaline sides, and increased temperature resistance as compared to SβG and UβG. Michaelis constant, K_m was increased nearly three-folds for MβG while V_max for soluble and MβG was 0.515 mM/min and 0.495 mM/min, respectively. Furthermore, MβG showed greater resistance to product inhibition mediated by galactose as compared to it soluble counterpart and exhibited excellent catalytic activity even after its fourth successive reuse. The remarkable bioconversion rates of lactose from milk in batch reactors further revealed an attractive catalytic efficiency of β-galactosidase adsorbed on surface functionalized AgNPs thereby promoting its use in the production of lactose free dairy products.     

Biocatalytic characterization of Aspergillus oryzae β-galactosidase immobilized on functionalized multi-walled carbon nanotubes

The objectives of this work were to immobilize commercial Aspergillus oryzae β-galactosidase on functionalized multi-walled carbon nanotubes (MWCNTs) using different treatments and to characterize the products. Treatments were performed with glutaraldehyde, ethylenediamine and a mixture of concentrated H₂SO₄:HNO₃. The MWCNTs and their derivatives were characterized by thermogravimetric analysis. The immobilized enzymes were evaluated using inactivation kinetics, operating conditions, that is pH and temperature, kinetic parameters and lactose hydrolysis reusability. Immobilization yield and efficiency were significantly higher for β-galactosidase immobilized on MWCNTs functionalized by the acid mixture (Ac-Gal-MWCNTs). These values were 97% and 82%, respectively, after 3?h of immobilization. The activity of the Ac-Gal-MWCNTs was maintained at ～51% of their initial activity after being stored for 90 days at 4?°C. The Ac-Gal-MWCNTs retained more than 90% of their initial activity up to the fourth recycle. As the acid functionalization was the most efficient method tested for immobilizing A. oryzae β-galactosidase on MWCNTs, this method shows promise for industrial applications.     

Effect of pH on transfructosylation and hydrolysis by β-fructofuranosidase from Aspergillus oryzae

 β-Fructofuranosidase was purified from commercial alkaline protease (Aspergillus oryzae origin). The optimal pH of its transfructosylating activity was more alkaline (pH 8) than that of its hydrolyzing activity (pH 5). In the case of a 24-h reaction with sucrose, the hydrolysis and transfructosylation reaction were optimal at pH 4–5 and pH 8, respectively. In the reaction at pH 8 1-kestose and nystose were the main fructooligosaccharides produced. The transfer ratio was hardly different between pH 5 and pH 8 early in the reaction, but the transfer products (1-kestose and nystose) were decreased at pH 5 as the reaction proceeded because of their hydrolysis. Received: 18 January 1995/Received last revision: 23 August 1995/Accepted: 13 September 1995     

Repeated-batch operation of immobilized β-galactosidase inclusion bodies-containing Escherichia coli cell reactor for lactose hydrolysis

In this study, we investigated the performance of an immobilized β-galactosidase inclusion bodies-containing Escherichia coli cell reactor, where the cells were immobilized in alginate beads, which were then used in repeated-batch operations for the hydrolysis of o-nitrophenyl-β-D-galactoside or lactose over the long-term. In particular, in the Tris buffer system, disintegration of the alginate beads was not observed during the operation, which was observed for the phosphate buffer system. The o-nitrophenyl-β-D-galactoside hydrolysis was operated successfully up to about 80 h, and the runs were successfully repeated at least eight times. In addition, hydrolysis of lactose was successfully carried out up to 240 h. Using Western blotting analyses, it was verified that the beta-galactosidase inclusion bodies were sustained in the alginate beads during the repeated-batch operations. Consequently, we experimentally verified that β-galactosidase inclusion bodies-containing Escherichia coli cells could be used in a repeated-batch reactor as a biocatalyst for the hydrolysis of o-nitrophenyl-β-D-galactoside or lactose. It is probable that this approach can be applied to enzymatic synthesis reactions for other biotechnology applications, particularly reactions that require long-term and stable operation.     

Purification and characterization of β-galactosidase from probiotic Pediococcus acidilactici and its use in milk lactose hydrolysis and galactooligosaccharide synthesis

β-galactosidase is a commercially important enzyme that was purified from probiotic Pediococcus acidilactici. The enzyme was extracted from cells using sonication and subsequently purified using ammonium sulphate fractionation and successive chromatographies on Sephadex G-100 and Q-Sepharose. The enzyme was purified 3.06-fold up to electrophoretic homogeneity with specific activity of 0.883 U/mg and yield of 28.26%. Molecular mass of β-galactosidase as estimated by SDS-PAGE and MALDI-TOF was 39.07 kDa. The enzyme is a heterodimer with subunit mass of 15.55 and 19.58 kDa. The purified enzyme was optimally active at pH 6.0 and stable in a pH range of 5.8–7.0 with more than 97% activity. Purified β-galactosidase was optimally active at 50 °C. Kinetic parameters K_m and V_max for purified enzyme were 400 µM and 1.22 × 10⁻¹ U respectively. Its inactivation by PMSF confirmed the presence of serine at the active site. The metal ions had different effects on enzyme. Ca²⁺, Mg²⁺ and Mn²⁺ slightly activated the enzyme whereas NH₄⁺, Co²⁺ and Fe³⁺ slightly decreased the enzyme activity. Thermodynamic parameters were calculated that suggested that β-galactosidase is less stable at higher temperature (60 °C). Purified enzyme effectively hydrolysed milk lactose with lactose hydrolysing rate of 0.047 min⁻¹ and t_1/2 of 14.74 min. This is better than other studied β-galactosidases. Both sonicated Pediococcus acidilactici cells and purified β-galactosidase synthesized galactooligosaccharides (GOSs) as studied by TLC at 30% and 50% of lactose concentration at 47.5 °C. These findings indicate the use of β-galactosidase from probiotic bacteria for producing delactosed milk for lactose intolerant population and prebiotic synthesis. pH and temperature optima and its activation by Ca²⁺ shows that it is suitable for milk processing.     

Induction of β-N-acetylhexosaminidase in Aspergillus oryzae

Summary Extracellular -N-acetylhexosaminidase in basic specific activity 1.5 U/mg protein was induced 15 – 35 times (up to 50 U/mg protein) by mixture of chitooligomers (crude chitin hydrolysate), 10 – 20 times (20 – 30 U/mg protein) by N-acetylglucosamine, and 10 times (14 U/mg protein) by chitosan in Aspergillus oryzae. Addition of NaCl (15 – 23 g/l) to the cultivation medium enhanced the induction in 10 – 20 %.     

β-Galactosidase of Aspergillus oryzae immobilized in an ion exchange resin combining the ionic-binding and crosslinking methods: Kinetics and stability during the hydrolysis of lactose

In this work, the hydrolysis kinetics of lactose by Aspergillus oryzae β-galactosidase was studied using the ionic exchange resin Duolite A568 as a carrier. The enzyme was immobilized using a β-galactosidase concentration of 16 g/L in pH 4.5 acetate buffer and an immobilization time of 12 h at 25 ± 0.5 °C. Next, the immobilized β-galactosidase was crosslinked using glutaraldehyde concentration of 3.5 g/L for 1.5 h. The influence of lactose concentration was studied for a range of 5–140 g/L, and the Michaelis–Menten model was fitted well to the experimental results with V_m and K_m values of 0.71 U and 35.30 mM, respectively. The influence of the product galactose as an inhibitor on the hydrolysis reaction was studied. The model that was best fitted to the experimental results was the competitive inhibition by galactose with V_m, K_m and K_i values of 0.77 U, 35.30 mM and 27.44 mM, respectively. The influence of temperature on the enzymatic activity of the immobilized enzyme was studied in the range of 10–80 °C, in which the temperature of the maximum activity was 60 °C, with an activation energy of 5.32 kcal/mol of lactose, using an initial concentration of lactose of 50 g/L in a pH 4.5 sodium acetate buffer solution. The thermal stability of the immobilized biocatalyst was determined to be in the range 55–65 °C. The first-order model described well the kinetics of thermal deactivation for all the temperatures studied. The activation energy of thermal deactivation from immobilized biocatalyst was 66.48 kcal/mol with a half-life of 8.9 h at 55 °C.     

Production of trisaccharide from lactose using β-galactosidase from Bacillus circulans modified by glutaraldehyde

Summary Free amino groups of -galactosidase-1-from Bacillus circulans were partially modified using different glutaraldehyde concentrations to increase trisaccharide production from lactose. Glutaraldehyde of 0.01%–0.03% modified 15%–40% of the free amino groups of the enzyme. The maximum yield of trisaccharide increased from 6% to 12% depending upon the degree of modification with 25% conversion of 127 mM lactose. Modification of 50% of the free amino groups of the enzyme using 0.05% glutaraldehyde produced a considerable amount of tetrasaccharide along with trisaccharide even at the initial stage of the reaction.     

Continuous production of galacto-oligosaccharides from lactose by Bullera singularis β-galactosidase immobilized in chitosan beads

Galacto-oligosaccharides (GalOS) were continuously produced using lactose and immobilized β-galactosidase from Bullera singularis ATCC 24193 in a packed bed reactor. Partially purified β-galactosidase was immobilized in Chitopearl BCW 3510 bead (970 GU/g resin) by simple adsorption. 55% (w/w) oligosaccharides was obtained continuously with a productivity of 4·4 g/(litre-h) from 100 g/litre lactose solution during a 15-day operation. Batch productivity was 6·5 g GalOS/(litre-h) from 300 g/litre lactose.     

Reduction of galactose inhibition via the mutation of β-galactosidase from Caldicellulosiruptor saccharolyticus for lactose hydrolysis

For the removal of galactose inhibition, the predicted galactose binding residues, which were determined by sequence alignment, were replaced separately with Ala. The activities of the Ala-substituted mutant enzymes were assessed with the addition of galactose. As a consequence, amino acid at position 349 was correlated with the reduction in galactose inhibition. The F349S mutant exhibited the highest activity in the presence of galactose relative to the activity measured in the absence of galactose among the tested mutant enzymes at position 349. The K _i of the F349S mutant (160 mM), which was 13-fold that of the wild-type enzyme, was the highest among the reported values of β-galactosidase. The wild-type enzyme hydrolyzed 62% of 100 g lactose/l with the addition of 30 g galactose/l, whereas the F349S mutant hydrolyzed more than 99%.     

Immobilization of Aspergillus oryzae β-galactosidase in ion exchange resins by combined ionic-binding method and cross-linking

The main objective of the present work is to study the immobilization process of Aspergillus oryzae β-galactosidase using the ionic exchange resin Duolite A568 as carrier. Initially, the immobilization process by ionic binding was studied through a central composite design (CCD), by analyzing the simultaneous influences of the enzyme concentration and pH on the immobilization medium. The results indicate that the retention of enzymatic activity during the immobilization process was strongly dependant of those variables, being maximized at pH 4.5 and enzyme concentration of 16 g/L. The immobilized enzyme obtained under the previous conditions was subjected to a cross-linking process with glutaraldehyde and the conditions that maximized the activity were a glutaraldehyde concentration of 3.83 g/L and cross-linking time of 1.87 h. The residual activity of the immobilized enzyme without glutaraldehyde cross-linking was 51% of the initial activity after 30 uses, while the enzyme with cross-linking immobilization was retained 90% of its initial activity. The simultaneous influence of pH and temperature on the immobilized β-galactosidase activity was also studied through a central composite design (CCD). The results indicate a greater stability on pH variations when using the cross-linking process.     

Optimization of β-glucosidase production from Aspergillus niger

本研究对Aspergillus niger Glu05生产β-葡萄糖苷酶的培养基组分及培养条件进行了优化.优化后的培养基组成和培养条件分别为:麸皮4％,tryptone 4％,1μmol MnSO4,1μmol NaCl,KH2PO40.2％,oH自然,摇床转速250 r/min,培养温度30℃,培养周期5d.优化后发酵液中酶活力达到44.11 IU/mL,与初始的产酶水平32.87 IU/mL相比,提高了36％.     

Purification of α-galactosidase and invertase by three-phase partitioning from crude extract of Aspergillus oryzae

alpha-Galactosidase and invertase were accumulated in a coherent middle phase in a three-phase partitioning system under different conditions (ammonium sulphate, ratio of tert-butanol to crude extract, temperature and pH). alpha-Galactosidase and invertase were purified 15- and 12-fold with 50 and 54% activity recovery, respectively. The fractions of interfacial precipitate arising from the three-phase partitioning were analyzed by SDS-PAGE. Both purified preparations showed electrophoretic homogeneity on SDS-PAGE.