Improving reuse cycles of Thermomyces lanuginosus lipase (NS-40116) by immobilization in flexible polyurethane

Enzyme immobilization using a low-cost support that allows increasing operational stability and reutilization arise as a great economic advantage for the industry. In this work, it was explored different methods of Thermomyces lanuginosus lipase (NS-40116) immobilization in flexible polyurethane foam (PU). PU polymer was synthesized using polyether and toluene diisocyanate as monomers. PU-NS-40116 immobilized was evaluated in terms of stability in a range of pH (7.0 and 9.0), temperature (24, 50 and 60?°C) for 24?h, and storage stability (room temperature and 4?°C) for 30?days. The results showed that after 30?days of storage immobilized enzyme kept 80% of initial enzyme activity. PU support before and after immobilization process was characterized by scanning electron microscopy and Fourier transform infrared spectroscopy. Free and immobilized enzymes were compared in terms of hydrolysis of soybean oil. Immobilized enzyme by entrapment was evaluated in successive cycles of reuse showing catalytic activity above 50% even after 5 successive cycles of reuse, confirming the efficiency of immobilization process.     

Biotransformation of 3-cyanopyridine to nicotinic acid by free and immobilized cells of recombinant Escherichia coli

An efficient biocatalytic process for the production of nicotinic acid (niacin) from 3-cyanopyridine was developed using cells of recombinant Escherichia coli JM109 harboring the nitrilase gene from Alcaligenes faecalis MTCC 126. The freely suspended cells of the biocatalyst were found to withstand higher concentrations of the substrate and the product without any signs of substrate inhibition. Immobilization of the cells further enhanced their substrate tolerance, stability and reusability in repetitive cycles of nicotinic acid production. Under optimized conditions (37 °C, 100 mM Tris buffer, pH 7.5) for the immobilized cells, the recombinant biocatalyst achieved a 100% conversion of 1 M 3-cyanopyridine to nicotinic acid within 5 h at a cell mass concentration (fresh weight) of 500 mg/mL. The high substrate/product tolerance and stability of the immobilized whole cell biocatalyst confers its potential industrial use.     

Immobilization of acetylcholinesterase in nanofibrous PVA/BSA membranes by electrospinning

Electrospinning, a simple and versatile method to fabricate nanofibrous supports, has attracted continuous attention in the field of enzyme immobilization. In this study, acetylcholinesterase (AChE) has been successfully immobilized in PVA nanofibers via electrospinning of a mixture of AChE, BSA as an enzyme stabilizing additive and PVA. The maximum activity recovery of immobilized AChE was about 40%. In comparison with free enzyme, the immobilized AChE showed improved stability while retaining a considerable amount of activity at lower pH values. Moreover, the immobilized AChE retained >34% of its initial activity when stored at 30°C for 100 days and retained 70% of its initial activity after ten consecutive reactor batch cycles.     

Effect of calcium on immobilization of rice (<Emphasis Type="Italic">Oryza sativa</Emphasis> L.) peroxidase for bioassays in sodium alginate and Agarose gel

The direct immobilization of soluble peroxidase isolated and partially purified from shoots of rice seedlings in calcium alginate beads and in calcium agarose gel was carried out. Peroxidase was assayed for guaiacol oxidation products in presence of hydrogen peroxide. The maximum specific activity and immobilization yield of the calcium agarose immobilized peroxidase reached 2,200 U mg⁻¹ protein (540 mU cm⁻³ gel) and 82%, respectively. In calcium alginate the maximum activity of peroxidase upon immobilization was 210 mU g⁻¹ bead with 46% yield. The optimal pH for agarose immobilized peroxidase was 7.0 which differed from the pH 6.0 for soluble peroxidase. The optimum temperature for the agarose immobilized peroxidase however was 30°C, which was similar to that of soluble peroxidase. The thermal stability of calcium agarose immobilized peroxidase significantly enhanced over a temperature range of 30∼60°C upon immobilization. The operational stability of peroxidase was examined with repeated hydrogen peroxide oxidation at varying time intervals. Based on 50% conversion of hydrogen peroxide and four times reuse of immobilized gel, the specific degradation of guaiacol for the agarose immobilized peroxidase increased three folds compared to that of soluble peroxidase. Nearly 165% increase in the enzyme protein binding to agarose in presence of calcium was noted. The results suggest that the presence of calcium, ions help in the immobilization process of peroxidase from rice shoots and mediates the direct binding of the enzyme to the agarose gel and that agarose seems to be a better immobilization matrix for peroxidase compared to sodium alginate.     

Design of β‐galactosidase/silica biocatalysts: Impact of the enzyme properties and immobilization pathways on their catalytic performance

The use of heterogeneous biocatalysis in industrial applications is advantageous and the enzyme stability improvement is a continuous challenge. Therefore, we designed β‐galactosidase heterogeneous biocatalysts by immobilization, involving the support synthesis and enzyme selection (from Bacillus circulans, Kluyveromyces lactis, and Aspergillus oryzae). The underivatized, tailored, macro‐mesoporous silica exhibited high surface area, offered high enzyme immobilization yields and activity. Its chemical activation with glyoxyl groups bound the enzyme covalently, which suppressed lixiviation and conferred higher pH and thermal stability (120‐fold than for the soluble enzyme), without observable reduction of activity/stability due to the presence of silica. The best balance between the immobilization yield (68%), activity (48%), and stability was achieved for Bacillus circulans β‐galactosidase immobilized on glyoxyl‐activated silica, without using stabilizing agents or modifying the enzyme. The enzyme stabilization after immobilization in glyoxyl‐activated silica was similar to that observed in macroporous agarose‐glyoxyl support, with the reported microbiological and mechanical advantages of inorganic supports. The whey lactolysis at pH 6.0 and 25°C by using this catalyst (1 mg ml^?1, 290 UI g^?1) was still 90%, even after 10 cycles of 10 min, in batch process but it could be also implemented on continuous processes at industrial level with similar results.     

Bacterial cellulose as carrier for immobilization of laccase: Optimization and characterization

Bacterial cellulose (BC) has attracted attention as a new functional material due to its excellent mechanical strength, tridimensional nanostructure, high purity, and increased water absorption, compared to plant cellulose. In this work, commercial laccase was immobilized on BC and the influence of enzyme concentration, contact time, and pH was optimized toward the recovery activity of immobilized laccase. This optimization was carried out using a 3³ experimental design and response surface methodology. Enzyme concentration played a critical role in laccase immobilization. Under optimized conditions (0.15 μL L^?1 of enzyme concentration, 4.8 h of contact time, pH 5.4), the predicted and experimental response were equal to 47.88 and 49.30%, respectively. The thermal stability of the immobilized laccase was found to increase notably at 60 and 70°C presenting stabilization factor equal to 1.79 and 2.11, respectively. The immobilized laccase showed high operational stability, since it retained 86% of its initial activity after seven consecutive biocatalytic cycles of reaction with 2,2′‐azinobis‐(3‐ethylbenzothiazoline‐6‐sulfonic acid). Kinetic studies showed that the values of Michaelis–Menten constant and maximum reaction rate decreased upon immobilization (9.9‐ and 1.6‐fold, respectively). Globally, the use of immobilized laccase on BC offers an interesting tool for industrial biocatalytic applications.     

Continuous production of inulo-oligosaccharides from chicory juice by immobilized endoinulinase

Several carrier materials were examined for endoinulinase immobilization. A polystyrene carrier material (UF93^®) gave the best immobilization capacity (217 units/g carrier) and operational stability. Carbohydrate compositions in the reaction product were quite similar irrespective of the support materials even though each carrier material has different pore structure associated with diffusional restriction. After immobilization the optimal pH for enzyme activity was shifted from 5.0 to 4.5, whereas optimal temperature (55v°C) was unaltered. Continuous production of inulo-oligosaccharides from chicory juice was carried out using the polystyrene-bound endoinulinase. The recommended operating conditions of the enzyme reactor for maximizing productivity were as follows: feed concentration, 100 g/l chicory juice; flow rate, as superficial space velocity 2.0 h^у; temperature, 55v°C. The enzyme reactor was run for 28 days at 55v°C achieving an oligosaccharide yield of 82% without any significant loss of initial enzyme activity, where the volumetric productivity was 200 g/l · h. Furthermore, there was no marked difference in operational stability between the two reactors fed with pure inulin solution and with chicory juice as a substrate even though chicory juice contains a lot of impurities.     

Immobilization of cyclodextrin glucanotransferase on amberlite IRA-900 for biosynthesis of transglycosylated xylitol

Cyclodextrin glucanotransferase (CGTase) fromThermoanaerobacter sp. was adsorbed on the ion exchange resin Amberlite IRA-900. The optimum conditions for the immobilization of the CGTase were pH 6.0 and 600 U CGTase/g resin, and the maximum yield of immobilization was around 63% on the basis of the amount ratio of the adsorbed enzyme to the initial amount in the solution. Immobilization of CGTase shifted the optimum temperature for the enzyme to produce transglycosylated xylitol from 70°C to 90°C and improved the thermal stability of immobilized CGTase, especially after the addition of soluble starch and calcium ions. Transglycosylated xylitol was continuously produced using immobilized CGTase in the column type packed bed reactor, and the operating conditions for maximum yield were 10% (w/v) dextrin (13 of the dextrose equivalent) as the glycosyl donor, 10% (w/v) xylitol as the glycosyl acceptor, 20 mL/h of medium flow rate, and 60°C. The maximum yield of transglycosylated xylitol and productivity were 25% and 7.82 g·L⁻¹·h⁻¹, respectively. The half-life of the immobilized CGTase in a column type packed bed reactor was longer than 30 days.     

Immobilization and characterization of cellulase on concanavalin A (Con A)-layered calcium alginate beads

Cellulase has been immobilized on hybrid concanavalin A (Con A)-layered calcium alginate–starch beads. Immobilized cellulase retained about 82% of its activity. Con A was extracted from jack bean and the obtained crude protein was characterized by sodium dodecyl sulfate-polyacrylamide gel electrophoresis analysis. The immobilized beads showed high mechanical and storage stability; immobilized cellulase retained 100% and 85% activity at 4°C and 30°C, respectively, over one month. The immobilized cellulase retained about 70% of its activity after five cycles of use. The immobilized cellulase retained 70% activity after 120-min exposure to 60°C, whereas the soluble form only retained about 20%, showing that immobilization improved thermal stability. Surface morphology and elemental analysis of immobilized cellulase were examined using scanning electron microscope equipped with energy-dispersive X-ray. Based on the enzyme stability and reuse, this method of immobilization is both convenient and cheap.     

Repeated batch and continuous operations for phosphatidylglycerol synthesis from phosphatidylcholine with immobilized phospholipase D

Summary The repeated batch and continuous operations for transphosphatidylation reaction were carried out for phosphatidylglycerol (PG) synthesis from phosphatidylcholine (PC) with the help of immobilized cabbage phospholipase D (PLD) in the presence of glycerol. The biphasic reaction system was used which included the aqueous phase containing immobilized PLD along with high concentrations of glycerol (30%–50%) and buffer, whereas the main part of substrate (PC) and products (mainly PG) formed were in the organic phase (diethyl ether).Octyl-Sepharose CL-4B having a hydrophobic octyl group was chosen for the PLD immobilization. Both immobilization yield and activity yield of immobilized enzyme were 100%. The effects of solvents, temperature and glycerol concentrations on the immobilized PLD were examined. Repeated batch conversion of PC (15 g/l) to PG was examined with the immobilized PLD in 30% glycerol. In all five batch cycles examined, 100% selectivity was obtained and there was no significant decrease in the fractional conversion of PC to PG (98%–99%) in the first three batch cycles. In the cases of a packed-bed reactor (PBR) and a continuous stirred-tank reactor (CSTR) used for continuous synthesis of PG with the immobilized PLD, the operational stabilities of the immobilized enzyme were almost the same (half life=14 h at 30°C) when purified PC was used, while in the case of partially purified PC in CSTR the half life increased more than five times.Abbreviations used PC phosphatidylcholine - PG phosphatidylglycerol - PA phosphatidic acid - PLD phospholipase D - PBR packed bed reactor - CSTR continuous stirred tank reactor Studies on enzymatic conversion of phospholipids (III)     

Enhanced bioconversion of colchicine to regiospecific 3-demethylated colchicine (3-DMC) by whole cell immobilization of recombinant E. coli harboring P450 BM-3 gene

Biotransformation of colchicine into regiospecific 3-demethylated colchicine (3-DMC) which is pharmacologically active and a potent anti-cancer drug, mediated by immobilization of recombinant microbial monooxygenases is a novel and promising strategy for its production. In the present study, recombinant Escherichia coli expressing P450 BM-3 was immobilized in calcium-alginate beads and its ability to catalyze colchicine into 3-DMC was investigated. Characteristics of immobilized system showed that optimum conditions for activity of microbial cells were not affected due to immobilization. The optimum pH and temperature for both free and immobilized cells were found to be 7.5 and 37.5 °C, respectively. Experimental variables under consideration such as Ca²⁺ concentration, alginate concentration, P450 BM-3 enzyme activity and colchicine concentration were optimized using response surface methodology. The immobilized cells exhibited a markedly improved thermal stability as compared to free cells. The yield of 3-DMC with immobilized microbial cells was found to be an average of 69%, with 82, 73 and 52% across three independent batches in succession as against bioconversion by free cells, which indicated improved operational stability and reusability of immobilized cells in batch processes. Additionally, a packed bed reactor has been proposed for the immobilized biocatalytic system for bioconversion of colchicine and other biochemicals.     

Immobilization of glucoamylase on DEAE-cellulose activated with chloride compounds

Partially purified glucoamylase (1,4-α-d-glucan glucohydrolase, EC 3.2.1.3) from Aspergillus niger NRRL 330 has been immobilized on DEAE-cellulose activated with cyanuric chloride in 0.2 m acetate buffer, pH 4.2. In the matrix-bound glucoamylase, enzyme yield was 20 mg g^?1 of support, corresponding to 40 200 units g^?1 of DEAE support. Binding of the enzyme narrows the pH optimum from 3.8–5.2 to 3.6. Thermal stability of the bound glucoamylase enzyme was decreased although it showed a higher temperature optimum (70°C) than the free form (55°C). The rate of reaction of glucoamylase was also changed after immobilization. V_max values for free and bound enzyme were 36.6 and 22.6 μmol d-glucose ml^?1 min^?1 and corresponding K_m values were 3.73 and 4.8 g l^?1 respectively. Free and immobilized enzyme when used in the saccharification process gave 84 and 56% conversion of starch to d-glucose, respectively. The bound enzyme was quite stable and in the batch process it was able to operate for about five cycles without any loss of activity.     

Development of Bed Reactor Using Brick Dust Immobilized CIVI-Cellulase from Seeds of Cowpea (Vigna sinensis L)

Cellulase extracted from seeds of Cowpea (Vigna sinensis L var VITA-4) was partially purified and immobilized on brick dust as solid support via glutaraldehyde. The percentage retention of the enzyme activity on brick dust was nearly 85%. After immobilization specific activity of the enzyme increased from 0.275 to 0.557 U mg^?1 protein with about 2 fold enrichment. The optimum pH and temperature of soluble enzyme were determined as pH 4.6 and WC, respectively whereas immobilized enzyme showed at pH 5.0 and 37°C, respectively. The V_max values for soluble and immobilized enzyme were determined as 6.67 and 1.25 mg min^?1, respectively whereas K_m values were 4.35 and 4.76 mg ml^?1, respectively. The immobilized enzyme displayed higher thermal stability than soluble enzyme and retained about 50% of its initial activity after 12 reuses. Immobilized enzyme was packed in an indigenously designed double walled glass bed reactor for continuous production of reducing sugars.     

Stabilization of immobilized l-arabinose isomerase for the production of d-tagatose from d-galactose

The aim of this work was to develop a stable immobilized enzyme biocatalyst for the isomerization of d -galactose to d -tagatose at high temperature. l -Arabinose isomerase from the hyperthermophilic bacterium Thermotoga maritima (TMAI) was produced as a (His)₆-tagged protein, immobilized on a copper–chelate epoxy support and subjected to several postimmobilization treatments aimed at increasing its operational and structural stability. Treatment with glutaraldehyde and ethylenediamine resulted in a more than twofold increase in the operational stability and in all enzyme subunits linked, directly or indirectly, to the support via covalent bonds. A postimmobilization treatment of the immobilized derivatives with mercaptoethanol for the removal of any remaining copper ions, determined a further increase of the operational biocatalytic activity. Immobilized derivatives subjected to both treatments were used for the bioconversion of 18 g/L d -galactose to d -tagatose at 80°C in a packed bed reactor in three repeated cycles and showed a better operational stability compared with the literature data. This study shows that a postimmobilization stabilization treatment with glutaraldehyde and ethylenediamine can stabilize the multi-subunit structure of an enzyme immobilized on a metal-chelate epoxy support with an increase of its operational stability, results that are not easily achievable with the sole immobilization on epoxy or metal chelate-epoxy supports in the case of complex multimeric enzymes with geometric incongruence with the support.     

Continuous production of fructooligosaccharides using fructosyltransferase immobilized on ion exchange resin

A continuous production of fructooligosaccharides from sucrose was investigated by fructosyltransferase immobilized on a high porous resin, Diaion HPA 25. The optimum pH (5.5) and temperature (55°C) of the enzyme for activity was unaltered by immobilization, and the immobilized enzyme became less sensitive to the pH change. The optimal operation conditions of the immobilized enzyme column for maximizing the productivity were as follows: 600 g/L of sucrose feed concentration, flow rate of superficial space velocity 2.7 h^?1. When the enzyme column was run at 50°C, about 8% loss of the initial activity of immobilized enzyme was observed after 30 days of continuous operation, during which high productivity of 1174 g/L·h was achieved. The kinds of products obtained using the immobilized enzyme were almost the same as those using soluble enzymes or free cells.     

Immobilization of <Emphasis Type="Italic">Aspergillus oryzae</Emphasis> β-galactosidase on low-pressure plasma-modified cellulose acetate membrane using polyethyleneimine for production of galactooligosaccharide

The aim of this study was to produce galactooligosaccharides (GOS) from lactose using β-galactosidase from Aspergillus oryzae immobilized on a low-pressure plasma-modified cellulose acetate (CA) membrane. Specifically, a novel method was developed for multilayer enzyme immobilization involving polyethyleneimine (PEI)-enzyme aggregate formation and growth on a CA membrane. A large amount of enzyme (997 μg/cm² membrane) was immobilized with 66% efficiency. The K _m value for the immobilized enzyme was estimated to be 48 mM, which indicates decreased affinity for the substrate, whereas the Vmax value was smaller. The immobilized enzyme showed good storage and operational stability. The half-life of the immobilized enzyme on the membrane was about 1 month at 30°C and ∼ 60 h at 60°C. Maximum GOS production of 27% (w/w) was achieved with 70% lactose conversion from 320 g/L of lactose at pH 4.5 and 60°C. Trisaccharides were the major types of GOS formed and accounted for about 75% of the total GOS produced. Based on these results, immobilized enzyme technology could be applied to GOS production from lactose.     

Encapsulation in a sol–gel matrix of lipase from Aspergillus niger obtained by bioconversion of a novel agricultural residue

Lipase from Aspergillus niger was obtained from the solid-state fermentation of a novel agroindustrial residue, pumpkin seed flour. The partially purified enzyme was encapsulated in a sol–gel matrix, resulting in an immobilization yield of 71.4 %. The optimum pH levels of the free and encapsulated enzymes were 4.0 and 3.0, respectively. The encapsulated enzyme showed greater thermal stability at temperatures of 45 and 60 °C than the free enzyme. The positive influence of the encapsulation process was observed on the thermal stability of the enzyme, since a longer half-life t _1/2 and lower deactivation constant were obtained with the encapsulated lipase when compared with the free lipase. Kinetic parameters were found to follow the Michaelis–Menten equation. The K _m values indicated that the encapsulation process reduced enzyme–substrate affinity and the V _max was about 31.3 % lower than that obtained with the free lipase. The operational stability was investigated, showing 50 % relative activity up to six cycles of reuse at pH 3.0 at 37 °C. Nevertheless, the production of lipase from agroindustrial residue associated with an efficient immobilization method, which promotes good catalytic properties of the enzyme, makes the process economically viable for future industrial applications.     

Development of an ultrahigh-temperature process for the enzymatic hydrolysis of lactose. IV. Immobilization of two thermostable beta-glycosidases and optimization of a packed-bed reactor for lactose conversion.

Recombinant hyperthermostable beta-glycosidases from the archaea Sulfolobus solfataricus (Ss beta Gly) and Pyrococcus furiosus (CelB) were covalently attached onto the insoluble carriers chitosan, controlled pore glass (CPG), and Eupergit C. For each enzyme/carrier pair, the protein-binding capacity, the immobilization yield, the pH profiles for activity and stability, the activity/temperature profile, and the kinetic constants for lactose hydrolysis at 70 degrees C were determined. Eupergit C was best among the carriers in regard to retention of native-like activity and stability of Ss beta Gly and CelB over the pH range 3.0-7.5. Its protein binding capacity of approximately 0.003 (on a mass basis) was one-third times that of CPG, while immobilization yields were typically 80% in each case. Activation energies for lactose conversion by the immobilized enzymes at pH 5.5 were in the range 50-60 kJ/mol. This is compared to values of approximately 75 kJ/mol for the free enzymes. Immobilization expands the useful pH range for CelB and Ss beta Gly by approximately 1.5 pH units toward pH 3.5 and pH 4.5, respectively. A packed-bed enzyme reactor was developed for the continuous conversion of lactose in different media, including whey and milk, and operated over extended reaction times of up to 14 days. The productivities of the Eupergit C-immobilized enzyme reactor were determined at dilution rates between 1 and 12 h(-1), and using 45 and 170 g/L initial lactose. Results of kinetic modeling for the same reactor, assuming plug flow and steady state, suggest the presence of mass-transfer limitation of the reaction rate under the conditions used. Formation of galacto-oligosaccharides in the continuous packed-bed reactor and in the batch reactor using free enzyme was closely similar in regard to yield and individual saccharide components produced.     

Cyanide hydratase from Aspergillus niger K10: Overproduction in Escherichia coli,purification, characterization and use in continuous cyanide degradation

A cyanide hydratase from Aspergillus niger K10 was expressed in Escherichia coli and purified. Apart from HCN, it transformed some nitriles, preferentially 2-cyanopyridine and fumaronitrile. V_max and K_m for HCN were ca. 6.8 mmol min⁻¹ mg⁻¹ protein and 109 mM, respectively. V_max for fumaronitrile and 2-cyanopyridine was two to three orders of magnitude lower than for HCN (ca. 18.8 and 10.3 μmol min⁻¹ mg⁻¹, respectively) but K_m was also lower (ca. 14.7 and 3.7 mM, respectively). Both cyanide hydratase and nitrilase activities were abolished in truncated enzyme variants missing 18–34 C-terminal aa residues. The enzyme exhibited the highest activity at 45 °C and pH 8–9; it was unstable at over 35 °C and at below pH 5.5. The operational stability of the whole-cell catalyst was examined in continuous stirred membrane reactors with 70-mL working volume. The catalyst exhibited a half-life of 5.6 h at 28 °C. A reactor loaded with an excess of the catalyst was used to degrade 25 mM KCN. A conversion rate of over 80% was maintained for 3 days.     

Purification and characterization of a nitrilase from Aspergillus niger K10

Aspergillus niger K10 cultivated on 2-cyanopyridine produced high levels of an intracellular nitrilase, which was partially purified (18.6-fold) with a 24% yield. The N-terminal amino acid sequence of the enzyme was highly homologous with that of a putative nitrilase from Aspergillus fumigatus Af293. The enzyme was copurified with two proteins, the N-terminal amino acid sequences of which revealed high homology with those of hsp60 and an ubiquitin-conjugating enzyme. The nitrilase exhibited maximum activity (91.6 U mg^-1) at 45°C and pH 8.0. Its preferred substrates, in the descending order, were 4-cyanopyridine, benzonitrile, 1,4-dicyanobenzene, thiophen-2-acetonitrile, 3-chlorobenzonitrile, 3-cyanopyridine, and 4-chlorobenzonitrile. Formation of amides as by-products was most intensive, in the descending order, for 2-cyanopyridine, 4-chlorobenzonitrile, 4-cyanopyridine, and 1,4-dicyanobenzene. The enzyme stability was markedly improved in the presence of d-sorbitol or xylitol (20% w/v each). p-Hydroxymercuribenzoate and heavy metal ions were the most powerful inhibitors of the enzyme.