Immobilization of α-amylase and amyloglucosidase onto ion-exchange resin beads and hydrolysis of natural starch at high concentration

α-Amylase was immobilized on Dowex MAC-3 with 88 % yield and amyloglucosidase on Amberlite IRA-400 ion-exchange resin beads with 54 % yield by adsorption process. Immobilized enzymes were characterized to measure the kinetic parameters and optimal operational parameters. Optimum substrate concentration and temperature were higher for immobilized enzymes. The thermal stability of the enzymes enhanced after the immobilization. Immobilized enzymes were used in the hydrolysis of the natural starch at high concentration (35 % w/v). The time required for liquefaction of starch to 10 dextrose equivalent (DE) and saccharification of liquefied starch to 96 DE increased. Immobilized enzymes showed the potential for use in starch hydrolysis as done in industry.     

Co-immobilization of amyloglucosidase and pullulanase for enhanced starch hydrolysis

Summary Amyloglucosidase and pullulanase were co-immobilized using a hydrophilic polyurethane foam (Hypol^® 2002). The combined amyloglucosidase and pullulanase activity of the immobilized enzyme was 32.2% ± 1.7% relative to the non-immobilized enzyme. The co-immobilized enzymes were capable of using a variety of glycogen and starch substrates. Co-immobilization of amyloglucosidase and pullulanase increased the glucose yield 1.6-fold over immobilized amyloglucosidase alone. No decrease in activity was observed after 4 months storage for the co-immobilized enzymes. The results suggest that co-immobilization of amyloglucosidase and pullulanase in polyurethane foams is a potentially useful approach for commercial starch hydrolysis. Offprint requests to: K. B. Storey     

High throughput covalent immobilization process for improvement of shelf-life,operational cycles,relative activity in organic media and enzymatic kinetics of urease and its application for urea removal from water samples

High throughput covalent urease immobilization was performed through the amide bond formation between the urease and the amino-functional MNPs. The enzyme’s performances, including shelf-life, reusability, enzymatic kinetics, and the enzyme relative activity in organic media was improved. At optimal conditions, the immobilization efficiency was calculated about 95.0% with keeping 94.7% of the urease initial specific activity. The optimal pH for maximum activity of the free and immobilized urease was calculated as 7.0 at 37.0 °C and 8.0 at 60.0 °C, respectively. The kinetics studies showed the K_m of 26.0 mM and 8.0 mM and the V_max of 5.31 μmol mg⁻¹ min⁻¹ and 3.93 μmol mg⁻¹ min⁻¹ for the free and immobilized urease, respectively. The ratio K_cat/K_m as a measure of catalytic efficiency and enzyme specificity was calculated as 0.09 mg mL⁻¹ min⁻¹ and 0.22 mg mL⁻¹ min⁻¹ for the free and immobilized urease, respectively, indicating an improvement in the enzymatic kinetics. The shelf-life and operational studies of immobilized urease indicated that approximately 97.7% and 88.5% of its initial activity was retained after 40 days and 17 operational cycles, respectively. The immobilized urease was utilized to urea removal from water samples with an efficiency between 91.5–95.0%.     

Preparation and some properties of immobilized Penicillium funiculosum 258 dextranase

The production of dextranase was investigated in static cultures of Penicillium funiculosum 258. Maximal enzyme productivity was attained at pH 8.0, with 3.5% (w/v) dextran (MW, 260 000) as carbon source, NaNO₃ (1%, w/v) and yeast extract (0.2%, w/v) as nitrogen source, 0.4% (w/v) K₂HPO₄ and 0.06% (w/v) MgSO₄. It was possible to increase the productivity of dextranase to 41.8 units ml⁻¹ in the modified medium. The enzyme was immobilized on different carriers by different techniques of immobilization. The enzyme prepared by covalent binding on chitosan using glutaraldehyde had the highest activity, the immobilized enzyme retaining 63% of its original specific activity. Compared with the free dextranase, the immobilized enzyme exhibited: a higher pH optimum, a higher optimal reaction temperature and energy of activation, a higher Michaelis constant, improved thermal stability and higher values of deactivation rate constant. The immobilized enzyme retained about 80% of the initial catalytic activity even after being used for 12 cycles.     

A novel maltohexaose-forming α-amylase from Bacillus caldovelox: patterns and mechanisms of action

Summary The acidophilic, thermostable -amylase of Bacillus caldovelox displays a unique end-product profile and action pattern on starch. Maltohexaose is preferentially produced, with a maximum yield of 40–44% (w/w) from 35% (w/v) starch and dextrins (DE 9 and DE 18). Maltohexaose, the initial product of 1% (w/v) starch and 35% (w/v) dextrin (DE 42) hydrolysis, is subsequently converted into maltopentaose with a maximum yield of 30% (w/w). This reaction does not involve glucose production. Substrates were hydrolysed from the non-reducing end by either a uni- or multimolecular mechanism, with no hydrolysis of maltohexaose or smaller sugars. The K _m values for soluble starch and maltoheptaose were 4.68 mg/ml and 2.13 × 10^–2 M, respectively. Offprint requests to: C. T. Kelly     

Enzymatic production of glucose from different qualities of grain sorghum and application of ultrasound to enhance the yield

The objective of the present work was to add value to three different qualities of grain sorghum namely normal healthy, germinated, and blackened through production of glucose, and to intensify glucose production (yield) by means of ultrasound treatment. Liquefaction (using Bacillus licheniformis α-amylase) and saccharification (using amyloglucosidase) processes were optimized with use of normal sorghum flour as a starting material for the production of glucose. The effect of ultrasound treatment on the sorghum slurry prior to liquefaction was studied on the processes of liquefaction and saccharification under optimized conditions. Due to ultrasound treatment, liquefact DE increased by 10-25% depending upon sonication time and the intensity. Ultrasound treatment of 1 min at 100% amplitude was found to decrease the average particle size of the slurry from 302 μm to 115 μm, which resulted in an increased percentage of saccharification by about 8%. The reason for the increase in the percentage of saccharification was attributed to the availability of additional starch for hydrolysis due to ultrasound-assisted disruption of the protein matrix (surrounding starch granules) and the amylose-lipid complex. Integration of ultrasound treatment in the state of art of the production of glucose from dry-milled sorghum and its possible subsequent use in the bioethanol production may improve the overall economics of the process.     

Starch hydrolysis modeling: application to fuel ethanol production

Efficiency of the starch hydrolysis in the dry grind corn process is a determining factor for overall conversion of starch to ethanol. A model, based on a molecular approach, was developed to simulate structure and hydrolysis of starch. Starch structure was modeled based on a cluster model of amylopectin. Enzymatic hydrolysis of amylose and amylopectin was modeled using a Monte Carlo simulation method. The model included the effects of process variables such as temperature, pH, enzyme activity and enzyme dose. Pure starches from wet milled waxy and high-amylose corn hybrids and ground yellow dent corn were hydrolyzed to validate the model. Standard deviations in the model predictions for glucose concentration and DE values after saccharification were less than ±0.15% (w/v) and ±0.35%, respectively. Correlation coefficients for model predictions and experimental values were 0.60 and 0.91 for liquefaction and 0.84 and 0.71 for saccharification of amylose and amylopectin, respectively. Model predictions for glucose (R ² = 0.69–0.79) and DP4⁺ (R ² = 0.8–0.68) were more accurate than the maltotriose and maltose for hydrolysis of high-amylose and waxy corn starch. For yellow dent corn, simulation predictions for glucose were accurate (R ² > 0.73) indicating that the model can be used to predict the glucose concentrations during starch hydrolysis.     

Optimization of α‐Amylase Immobilization in Calcium Alginate Beads

Abstract

α‐Amylase enzyme was produced by Aspergillus sclerotiorum under SSF conditions, and immobilized in calcium alginate beads. Effects of immobilization conditions, such as alginate concentration, CaCl₂ concentration, amount of loading enzyme, bead size, and amount of beads, on enzymatic activity were investigated. Optimum alginate and CaCl₂ concentration were found to be 3% (w/v). Using a loading enzyme concentration of 140 U mL^?1, and bead (diameter 3 mm) amount of 0.5 g, maximum enzyme activity was observed. Beads prepared at optimum immobilization conditions were suitable for up to 7 repeated uses, losing only 35% of their initial activity. Among the various starches tested, the highest enzyme activity (96.2%) was determined in soluble potato starch hydrolysis for 120 min at 40°C.     

Degradation of starchy substrates by a crude enzyme preparation and utilization of the hydrolysates for lactic fermentation

An enzyme preparation obtained from Aspergillus ustus, possessing cellulase, α-amylase, amyloglucosidase, proteinase and d-xylanase activities, was used along with commercial bacterial α-amylase and amyloglucosidase for the degradation of ragi (Eleusine coracana) flour and wheat (Triticum vulgare) bran. Lactic acid yield from ragi hydrolysate, adjusted to 5% reducing sugars (w/v), was 25% when fermented with Lactobacillus plantarum. The yields increased to 78% and 94% when the ragi hydrolysate was fortified with 20% and 60% (v/v) wheat bran hydrolysate, respectively. When commercial α-amylase and amyloglucosidase were used for the hydrolysis of ragi and wheat bran and L. plantarum was employed to ferment the hydrolysates containing 5% reducing sugars (w/v), lactic acid yields were 10% in ragi hydrolysate and 57% and 90% when the ragi hydrolysate was fortified with 20% and 60% (v/v) of wheat bran hydrolysate, respectively. α-Amylase and amyloglucosidase hydrolysed wheat bran added at 20% (v/v) as the sole source of nutrient to soluble starch hydrolysate (5% reducing sugars) gave 22% yield of lactic acid. The yield increased to 55% by the utilization of A. ustus enzyme preparation in addition to α-amylase and amyloglucosidase for wheat bran hydrolysis.     

Starch conversion by amylases fromAureobasidium pullulans

Summary A color variant strain (NRRL Y-12974) ofAureobasidium pullulans produced a saccharifying -amylase and two forms of glucoamylase extracellularly when grown on starch at 28°C for 4 days. A sugar syrup containing DP1 (degree of polymerization) and DP2 (31) was made from maltodextrin DE (dextrose equivalent) 10 (35%, w/w) at 55°C and pH 4.5 using the amylase preparation (40 U g^–1 DS (dry substance). The syrup composition was highly dependent upon substrate concentration but nearly independent of enzyme dose. Glucose syrup containing 93% glucose was made from maltodextrin DE 10 (35%, w/w) at 65°C and pH 4.5 using the same enzyme preparation at 100 U g^–1 DS. The enzyme preparation (100 U g^–1 DS) produced 98–100% glucose from raw corn starch at pH 4.5 and 50°C.The mention of firm names or trade products does not imply that they are endorsed or recommended by the US Department of Agriculture over other firms or similar products not mentioned. Abbreviations: DE, dextrose equivalent (an indication of polymerization; reducing sugars as percentage glucose); DP, degree of polymerization; DP1, glucose; DP2, disaccharide; DP3, trisaccharide; DP4, tetrasaccharide; DS, dry substance.     

Process optimization for the production of sugar for the bioethanol industry from sorghum,a non-conventional source of starch

A commercial preparation of -amylase, Biotempase, obtained from Biocon India Pvt. Ltd., and crude glucoamylase produced from Aspergillus sp. NA21 were used to hydrolyse sorghum powder, a non-conventional starchy substrate. Among various concentrations of starch (15–35%, dry weight/volume) tried for maximum liquefaction; slurry made with 25% substrate concentration proved optimal. An economical process of liquefaction was carried out using steam under pressure (0.2–0.3 bar, 104–105 °C) to liquefy a 25% slurry in just 45 min, contrary to a slower process carried out at 95 °C in a water bath. For liquefaction of starch a pH of 5.0 proved to be optimum. The dose of Biotempase as prescribed by the supplier could be reduced by 33% achieving the same degree of liquefaction, by addition of CaCl₂ to the starch slurry at the concentration of 200 mg/l. The conditions for the saccharification of liquefied starch were optimized to be 45 °C and pH 5.0, producing 90% saccharification in 24 h. Supplementation of divalent ions Ca²⁺, Mg²⁺ and Zn²⁺ in the process of saccharification showed no effect. Finally glucose was found to be the main hydrolysis product in the saccharification of sorghum starch.     

Forming nanoparticles of α-amylase and embedding them into solid surfaces

In the current work nanoparticles (NPs) of α-amylase were generated in an aqueous solution using high-intensity ultrasound, and were subsequently immobilized on polyethylene (PE) films, or polycarbonate (PC) plates, or on microscope glass slides. The α-amylase NPs coated on the solid surfaces have been characterized by ESEM, TEM, FTIR, XPS and AFM. The substrates immobilized with α-amylase were used for hydrolyzing soluble potato starch to maltose. The amount of enzyme introduced in the substrates, leaching properties, and the catalytic activity of the immobilized enzyme were compared. The catalytic activity of the amylase deposited on the three solid surfaces was compared to that of the same amount of free enzyme at different pHs and temperatures. α-Amylase coated on PE showed the best catalytic activity in all the examined parameters when compared to native amylase, especially at high temperatures. When immobilized on glass, α-amylase showed better activity than the native enzyme over all pH and temperature values studied. However, the immobilization on PC did not improve the enzyme activity at any pH and any temperature compared to the free amylase. The kinetic parameters, K_m and V_max were also calculated. The amylase coated PE showed the most favorable kinetic parameters (K_m = 5 g L⁻¹ and V_max = 5E−07 mol mL⁻¹ min⁻¹). In contrast, the anchored enzyme-PC exhibited unfavorable kinetic parameters (K_m = 16 g L⁻¹, V_max = 4.2E−07 mol mL⁻¹ min⁻¹). The corresponding values for amylase-glass were K_m = 7 g L⁻¹, V_max = 1.8E−07 mol mL⁻¹ min⁻¹, relative to those obtained for the free enzyme (K_m = 6.6 g L⁻¹, V_max = 3.3E−07 mol mL⁻¹ min⁻¹).     

Immobilization of a thermostable α‐amylase by covalent binding to an alginate matrix increases high temperature usability

Thermostable α‐amylase was covalently bound to calcium alginate matrix to be used for starch hydrolysis at liquefaction temperature of 95°C. 1‐ethyl‐3‐(3‐dimethylamino‐propyl) carbodiimide hydrochloride (EDAC) was used as crosslinker. EDAC reacts with the carboxylate groups on the calcium alginate matrix and the amine groups of the enzyme. Ethylenediamine tetraacetic acid (EDTA) treatment was applied to increase the number of available carboxylate groups on the calcium alginate matrix for EDAC binding. After the immobilization was completed, the beads were treated with 0.1 M calcium chloride solution to reinstate the bead mechanical strength. Enzyme loading efficiency, activity, and reusability of the immobilized α‐amylase were investigated. Covalently bound thermostable α‐amylase to calcium alginate produced a total of 53 g of starch degradation/mg of bound protein after seven consecutive starch hydrolysis cycles of 10 min each at 95°C in a stirred batch reactor. The free and covalently bound α‐amylase had maximum activity at pH 5.5 and 6.0, respectively. The Michaelis‐Menten constant (K_m) of the immobilized enzyme (0.98 mg/mL) was 2.5 times greater than that of the free enzyme (0.40 mg/mL). The maximum reaction rate (V_max) of immobilized and free enzyme were determined to be 10.4‐mg starch degraded/mL min mg bound protein and 25.7‐mg starch degraded/mL min mg protein, respectively. The high cumulative activity and seven successive reuses obtained at liquefaction temperature make the covalently bound thermostable α‐amylase to calcium alginate matrix, a promising candidate for use in industrial starch hydrolysis process. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Characterization of microbial endo-β-glucanase immobilized in alginate beads

Endo-β-glucanase (endo-β-1,4-glucano-glucanase EC 3.2.1.4), isolated from Trichoderma reesei, was immobilized in calcium alginate beads, retaining 75% of its original activity. The polyanionic moiety surrounding the immobilized enzyme displaced the pH-activity profile to alkaline regions with respect to that of the free enzyme. The enzyme was inhibited by carboxymethylcellulose, but this inhibition appeared to be decreased by immobilizatíon. The enzyme immobilized in alginate beads showed a K_m value (1.02% w/v) lower than that of the enzyme (1.31%). The apparent V_max of immobilized cellulase preparations (238.3 μmol glucose/ml × h) decreased by a factor of 0.59 with respect to that of the soluble enzyme. The optimum temperature (60°C) of the free and entrapped enzymes remained unaltered. In contrast, the half-life of the endoglucanase immobilized in calciumalginate beads was 4.6 h at 55°C and 5.4 h at 60°C, while that of the free enzyme was 3.0 h at 55°C and 1.2 h at 60°C. A technological application of the immobilized enzymes was tested using wheat straw as a source of fermentable sugars. The hydrolytic degradation of straw, by means of a crude extract of free and immobilized cellulases and β-glucosidase, released a large amount of reducing sugars from wheat straw after 48 h (between 250–720 mg glucose/g straw), carrying out more than a 90% saccharification. A mixture of immobilized β-glucosidase and free cellulases maintained 80% of the activity of the soluble counterparts, and the co-immobilization of both types of enzymes reduced by hydrolytic efficiency to half.     

Immobilized glucose oxidase on different supports for biotransformation removal of glucose from oligosaccharide mixtures

Four immobilized forms of glucose oxidase (GOD) were used for biotransformation removal of glucose from its mixture with dextran oligosaccharides. GOD was biospecifically bound to Concanavalin A-bead cellulose (GOD-ConA-TBC) and covalently to triazine-bead cellulose (GOD-TBC). Eupergit C and Eupergit CM were used for preparation of other two forms of immobilized GOD: GOD-EupC and GOD-EupCM. GOD-ConA-TBC and GOD-EupC exhibited the best operational and storage stabilities. pH and temperature optima of these two immobilized enzyme forms were broadened and shifted to higher values (pH 7 and 35 °C) in comparison with those of free GOD. The decrease of V_max values after immobilization was observed, from 256.8 ± 7.0 μmol min⁻¹ mg_GOD⁻¹ for free enzyme to 63.8 ± 4.2 μmol min⁻¹ mg_GOD⁻¹ for GOD-ConA-TBC and 45 ± 2.7 μmol min⁻¹ mg_GOD⁻¹ for GOD-EupC, respectively. Depending on the immobilization mode, the immobilized GODs were able to decrease the glucose content in solution to 3.8–15.6% of its initial amount The best glucose conversion, was achieved by an action of GOD-EupCM on a mixture of 100 g dextran with 9 g of glucose (i.e. 98.7% removal of glucose).     

A Shinella β-N-acetylglucosaminidase of glycoside hydrolase family 20 displays novel biochemical and molecular characteristics

β-N-Acetylglucosaminidases (GlcNAcases) are important for many biological functions and industrial applications. In this study, a glycoside hydrolase family 20 GlcNAcase from Shinella sp. JB10 was expressed in Escherichia coli BL21 (DE3). Compared to many GlcNAcases, the purified recombinant enzyme (rJB10Nag) exhibited a higher specificity activity (538.8 µmol min⁻¹ mg⁻¹) or V _max (1030.0 ± 82.1 µmol min⁻¹ mg⁻¹) toward p-nitrophenyl β-N-acetylglucosaminide and N,N′-diacetylchitobiose (specificity activity of 35.4 µmol min⁻¹ mg⁻¹) and a higher N-acetylglucosaminide tolerance (approximately 50% activity in 70.0 mM N-acetylglucosaminide). The degree of synergy on enzymatic degradation of chitin by a commercial chitinase and rJB10Nag was as high as 2.35. The enzyme was tolerant to most salts, especially 3.0–15.0% (w/v) NaCl and KCl. These biochemical characteristics make the JB10 GlcNAcase a candidate for use in many potential applications, including processing marine materials and the bioconversion of chitin waste. Furthermore, the enzyme has the highest proportions of alanine (16.5%), glycine (10.5%), and random coils (48.8%) with the lowest proportion of α-helices (24.9%) among experimentally characterized GH 20 GlcNAcases from other organisms.

     

High synergistic antibacterial,antibiofilm, antidiabetic and antimetabolic activity of Withania somnifera leaf extract-assisted zinc oxide nanoparticle

Nanotechnology is currently gaining immense attention to combat food borne bacteria, and biofilm. Diabetes is a common metabolic disease affecting majority of people. A better therapy relies on phytomediated nanoparticle synthesis. In this study, W. somnifera leaf extract-assisted ZnO NPs (Ws-ZnO NPs) was synthesized and characterized. From HR-TEM analysis, it has been found that the hexagonal wurtzite particle is 15.6 nm in size and − 12.14 mV of zeta potential. A greater antibacterial effect of Ws-ZnO NPs was noticed against E. faecalis and S. aureus at 100 µg mL⁻¹. Also, the biofilm of E. faecalis and S. aureus was greatly inhibited at 100 µg mL⁻¹ compared to E. coli and P. aeruginosa. The activity of α-amylase and α-glucosidase enzyme was inhibited at 100 µg mL⁻¹ demonstrating its antidiabetic potential. The larval and pupal development was delayed at 25 µg mL⁻¹ of Ws-ZnO NPs. A complete mortality (100%) was recorded at 25 µg mL⁻¹. Ws-ZnO NPs showed least LC₅₀ value (9.65 µg mL⁻¹) compared to the uncoated ZnO NPs (38.8 µg mL⁻¹) and leaf extract (13.06 µg mL⁻¹). Therefore, it is concluded that Ws-ZnO NPs are promising to be used as effective antimicrobials, antidiabetic and insecticides to combat storage pests.

     

Purification and characterization of a thermostable pullulanase fromThermoactinomyces thalpophilus

Summary Thermoactinomyces thalpophilus No. 15 produced an extracellular pullulanase in an aerobic fermentation with soluble starch, salts, and complex nitrogen sources. Acetone fractionation, ion-exchange chromatography, and gel filtration purified the enzyme from cell-free broth 16-fold to an electrophoretically homogeneous state (specific activity, 1352 U/mg protein; yield, 4%). The purified enzyme (estimated MW 79 000) was optimally active at pH 7.0 and 70°C and retained 90% relative activity at 80°C (30 min) in the absence of substrate. The enzyme was activated by Co²⁺, inhibited by Hg²⁺, and exhibited enhanced stability in the presence of Ca²⁺. The enzyme hydrolyzed pullulan (K _m 0.32%, w/v) forming maltotriose, and hydrolyzed amylopectin (K _m 0.36%, w/v), amylopectin beta-limit dextrin (K _m 0.45%, w/v) and glycogen beta-limit dextrin (K _m 1.11%, w/v) forming maltotriose and maltose.     

Production of gluconic acid by immobilized in pumice stones mycelium of Aspergillus niger using unconventional oxygenation of culture

Gluconic acid was produced in repeated batch processes with Aspergillus niger AM-11, immobilized in pumice stone particles using an unconventional oxygenation of culture media based on the addition of H₂O₂, decomposed by catalase to O₂ and water. The highest gluconic acid productivity of 8.2 g l^–1 h^–1 was reached with 30 g immobilized mycelium per 150 ml, 10% (w/v) glucose, at 24 °C and pH 6.5, with O₂ at 100% saturation. The immobilized mycelium was successfully reused up to 8 times in 1-h batches with only a slight loss (11%) of gluconic acid productivity.     

Continuous conversion of starch to glucose with immobilized glucoamylase

Partially purified glucoamylase from Aspergillus awamori NRRL 3112 was immobilized on diethylaminoethyl cellulose in the presence of low ionic-strength acetate buffers at pH 4.2. The active enzyme–cellulose complex was used to convert starch substrates continuously to glucose in stirred reactors. Substrate concentrations as high as 30% could be quantitatively converted to glucose at a rate of more than 25 mg/min/liter at 55°C for periods of 3 to 4 weeks in a 4-liter reactor. Shutdowns were due to mechanical problems and not to loss of enzymes, which could be recovered with no appreciable loss of specific activity. Transfer products, such as isomaltose and panose, were present in immobilized enzyme-produced syrups but to no greater degree than in soluble glucoamylase digests of starch.