The continuous hydrolysis of geniposide to genipin using immobilized β-glucosidase on calcium alginate gel

Summary The reaction velocity of immobilized -glucosidase was approximated by the first-order reaction kinetics. A plug flow reactor was used for continuous hydrolysis of geniposide with this immobilized enzyme. The activity of this immobilized enzyme was retained 100% for 600 h. The amount of genipin formed by using the immobilized enzyme was 17 fold that formed using the native enzyme without reuse. Using immobilized enzyme, purity and yield of genipin, which is a hydrolyzate of geniposide, was improved comparing with the native enzyme.     

The effect of soluble alginate and calcium on β-galactosidase activity produced by the thermotolerant, ethanol-producing yeast strain Kluyveromyces marxianus imb3

Since it has previously been demonstrated that ethanol production by the thermotolerant yeast strain, Kluyveromyces marxianus IMB3 is more efficient in calcium alginate-based immobilization systems during growth on lactose-containing media, it was decided to examine the separate effects of soluble alginate and free calcium on the β-galactosidase activity produced by that organism. It was found that the presence of Ca²⁺ significantly increased the thermal stability of the activity at 45?°C, although the pH?and temperature optima remained the same in the presence and absence of that cation. It was also found that the presence of 2% (w/v) sodium alginate (soluble) had a very limited positive effect on the thermal stability of the enzyme at 45?°C, although it was found that activity was very significantly stimulated at that temperature. The activity was found to have an enhanced thermal stability at 30?°C in the presence of sodium alginate. The presence of sodium alginate in assay mixtures had no significant effect on the Km of the activity for the substrate o-nitrophenyl-β-D-galactoside. The results observed in the presence of either free calcium or soluble alginate may at least partially explain enhanced ethanol production by this microorganism in alginate-based immobilization systems.     

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.     

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.     

Immobilization of β-galactosidase on modified polypropilene membranes

A new immobilized system: β-galactosidase-modified polypropylene membrane was created. It was obtained 13 different carriers by chemical modification of polypropylene membranes by two stages. The first stage is treatment with K(2)Cr(2)O(7) to receive carboxylic groups on membrane surface. The second stage is treatment with different modified agents ethylendiamine, hexamethylenediamine, hydrazine dihydrochloride, hydroxylamine, o-phenylenediamine, p-phenylenediamine, N,N'-dibenzyl ethylenediamine diacetate to receive amino groups. The quantity of the amino groups, carboxylic groups and the degree of hydrophilicity of unmodified and modified polypropilene membranes were determined. β-Galactosidase was chemically immobilized on the obtained carries by glutaraldehyde. The highest relative activity of immobilized enzyme was recorded at membrane modified with 10% hexamethylenediamine (Membrane 5) - 92.77%. The properties of immobilized β-galactosidase on different modified membranes - pH optimum, temperature optimum, pH stability and thermal stability were investigated and compared with those of free enzyme. The storage stability of all immobilized systems was studied. It was found that the most stable system is immobilized enzyme on Membrane 5. The system has kept 90% of its initial activity at 300th day (pH=6.8; 4°C). The stability of the free and immobilized β-galactosidase on the modified membrane 5 with 10% HMDA in aqueous solutions of alcohols - mono-, diol and triol was studied. The kinetics of enzymatic reaction of free and immobilized β-galactosidase on the modified membrane 5 at 20°C and 40°C and at the optimal pH for both forms of the enzyme were investigated. It was concluded that the modified agent - hexamethylenediamine, with long aliphatic chain ensures the best immobilized β-galactosidase system.     

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.     

Lactose hydrolysis by immobilized β-galactosidase on nylon-6: A novel spin-basket reactor

Summary -D-galactosidase from Kluyveromyces lactis immobilized on nylon-6 microbeads was used to hydrolyze lactose in skim milk (containing 28.6% total solids), using a novel spin-basket reactor. More than 75% of lactose was hydrolyzed at 34°C within a short space-time (<7 min) without experiencing any plugging such as typically seen in packed columns.     

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.     

Production of ethanol from molasses at 45 °C using Kluyveromyces marxianus IMB3 immobilized in calcium alginate gels and poly(vinyl alcohol) cryogel

The thermotolerant, ethanol-producing yeast strain Kluyveromyces marxianus IMB3 has been immobilized in calcium alginate gel and poly(vinyl alcohol) cryogel (PVAC) beads. The immobilized preparations were used as biocatalyst in fed-batch reactor systems for prolonged periods. The substrate utilized in each case consisted of sugar cane molasses diluted to yield a sugar load of 140?g/l. During the first cycle the maximum ethanol concentration produced by the alginate system was 57?g/l, representing 80% of the maximum theoretical yield. In the system employing the PVAC-immobilized biocatalyst, ethanol production increased to a maximum of 52–53?g/l, representing 73% of the maximum theoretical yield. In both cases, maximum ethanol concentration was achieved within a 72-hour period. When each system was operated on a fed-batch basis for a prolonged period of time the average ethanol concentrations produced in the alginate- and the PVAC-immobilized systems were 21 and 45?g/l, respectively. The results suggest that the PVAC-based immobilization system may provide a more practical alternative to alginate for the production of ethanol by K. marxianus IMB3 in continuous or semi-continuous fermentation systems.     

Effects of the Bgs locus on mouse β-galactosidase

The Bgs locus determines tissue levels of β-galactosidase in the mouse, so that enzyme levels are twice as high in mice carrying the Bgs ^hallele as in mice carrying the Bgs ^dallele (Felton et al., 1974). By immunotitration with antiserum to purified β-galactosidase, we have found that the Bgs locus influences the amount of enzyme protein present in the tissues. We have utilized recombinant inbred lines derived from a cross between C57BL/6J and DBA/2J mice to confirm the location of the Bgs locus on chromosome 9. The inhibition of mouse β-galactosidase by the active-site-directed reagent N-bromoacetyl-β-d-galactosylamine has been investigated. β-Galactosidase from the high and low Bgs strains has identical affinity for this inhibitor.     

Preparation of active corn peptides from zein through double enzymes immobilized with calcium alginate–chitosan beads

Double enzymes (alcalase and trypsin) were effectively immobilized in a composite carrier (calcium alginate–chitosan) to produce immobilized enzyme beads referred to as ATCC. The immobilization conditions for ATCC were optimized, and the immobilized enzyme beads were characterized. The optimal immobilization conditions were 2.5% of sodium alginate, 10:4 sodium alginate to the double enzymes, 3:7 chitosan solution to CaCl₂ and 2.5 h immobilization time. The ATCC beads had greatly enhanced stability and good usability compared with the free form. The ATCC residual activity was retained at 88.9% of DH (degree of hydrolysis) after 35 days of storage, and 36.0% of residual activity was retained after three cycles of use. The beads showed a higher zein DH (65.8%) compared with a single enzyme immobilized in the calcium alginate beads (45.5%) or free enzyme (49.3%). The ATCC kinetic parameters V_max and apparent K_m were 32.3 mL/min and 456.62 g⁻¹, respectively. Active corn peptides (CPs) with good antioxidant activity were obtained from zein in the ethanol phase. The ATCC might be valuable for preparing CPs and industrial applications.     

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.     

A new bioprocess for the production of prebiotic lactosucrose by an immobilized β-galactosidase

A new bioprocess for the synthesis of lactosucrose was studied using a covalently immobilized β-galactosidase on macrospheres of chitosan. The effects of temperature and pH on the production of lactosucrose and other oligosaccharides were evaluated. At 30 °C and pH 7.0, the maximum concentration of lactosucrose reached to 79 g L⁻¹. The change of the reaction conditions allowed to modify the qualitative profile of the final products without quantitative change in the total of oligosaccharides produced. At pH 7 and 30 °C, products profile was 79 g L⁻¹ of lactosucrose, 37 g L⁻¹ of galactooligosaccharides and 250 g L⁻¹ of total oligosaccharides, while at pH 5 and 64 °C the concentrations for the same compounds were 40, 62 and 250 g L⁻¹, respectively. The immobilization increased the thermal stability up to 260-fold. Using 300 g L⁻¹ of sucrose and 300 g L⁻¹ of lactose, and 8.5 mg of chitosan mL⁻¹, 30 cycles of reuse were performed and the biocatalyst kept the maximal lactosucrose synthesis. These results fulfill some important aspects for the enzyme immobilization and oligosaccharides synthesis: the simplicity of the protocols, the high operational stability of the enzyme and the possibility of driving the final products.     

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.     

Effect of ethionine on the synthesis of β-galactosidase inEscherichia coli

Ethionine at concentrations of 10⁻³M, 5×10⁻³M and 10⁻²M inhibits growth, both of β-galactosidase inducible ML-30 and constitutive ML-308Escherichia coli strains. The protein synthesis (measured by the incorporation of l-leucine-¹⁴C and l-aspartic-¹⁴C acid into proteins) of these strains is inhibited to the same extent as their growth. The synthesis of inducible and constitutive β-galactosidase produced by the strains ML-30 and ML-308, respectively, is considerably inhibited by ethionine.     

Properties of Aspergillus japonicus β-fructofuranosidase immobilized on porous silica

-Fructofuranosidase from Aspergillus japonicus MU-2, which produces fructo-oligosaccharides (1-kestose: O--D-fructofuranosyl-(2 1)--D-fructofuranosyl -D-glucopyranoside); and nystose: O--D-fructofuranosyl-(2 1)--D-fructofuranosyl-(2 1)--D-fructofuranosyl -D-glucopyranoside) from sucrose, was immobilized, covalently with glutaraldehyde onto alkylamine porous silica, at high efficiency (64%). Optimum pore diameter of porous silica for immobilization of the enzyme was 91.7 nm. After immobilization, the enzyme's stabilities to temperature, metal ions and proteolysis were improved, while its optimum pH and temperature were unchanged. The highest efficiency of continuous production of fructo-oligosaccharides (more than 60%), using a column packed with the immobilized enzyme, was obtained at 40% to 50% (w/v) sucrose. The half-life of the column during long-term continuous operation at 55°C was 29 days.     

Heterologous β-phellandrene production by alginate immobilized Synechocystis sp. PCC 6803

Journal of Applied Phycology - The aim of the present work was the investigation of various cultivation conditions in order to provide a foundation for a sustainable, financially viable, and...     

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.     

Influence of novobiocin on the induction kinetics of β-galactosidase in Escherichiacoli

Novobiocin (0.05 μg/ml) reduced the growth rate of cultures of $\text{Escherichia}$$\text{coli}$ strain DK6 by about a factor of 2. The lag in appearance of β-galactosidase-forming capacity was extended from 50 sec to 85 sec by the drug. This appeared to be the result of a reduced rate of nascent mRNA elongation.