Hen egg white as a feeder protein for lipase immobilization

Enzyme stabilization via immobilization is one of the preferred processes as it provides the advantages of recovery and reusability. In this study, Thermomyces lanuginosus lipase has been immobilized through crosslinking using 2% glutaraldehyde and hen egg white, as an approach towards CLEA preparation. The immobilization efficiency and the properties of the immobilized enzyme in terms of stability to pH, temperature, and denaturants was studied and compared with the free enzyme. Immobilization efficiency of 56% was achieved with hen egg white. The immobilized enzyme displayed a shift in optimum pH towards the acidic side with an optimum at pH 4.0 whereas the pH optimum for free enzyme was at pH 6.0. The immobilized enzyme was stable at higher temperature retaining about 83% of its maximum activity as compared to the free enzyme retaining only 41% activity at 70 °C. The denaturation of lipase in free form was rapid with a half-life of 2 h at 60 °C and 58 min at 70 °C as compared to 12 h at 60 °C and 2 h at 70 °C for the immobilized enzyme. The effect of denaturants, urea and guanidine hydrochloride on the free and immobilized enzyme was studied and the immobilized enzyme was found to be more stable towards denaturants retaining 74% activity in 8 M urea and 98% in 6 M GndHCl as compared to 42% and 33% respectively in the case of free enzyme. The apparent K_m (2.08 mM) and apparent V_max (0.95 μmol/min) of immobilized enzyme was lower as compared to free enzyme; K_m (8.0 mM) and V_max (2.857 μmol/min). The immobilized enzyme was reused several times for the hydrolysis of olive oil.     

Semi-interpenetrating polymer networks (semi-IPNs) for entrapment of laccase and their use in Acid Orange 52 decolorization

Laccase enzyme (L) from Trametes versicolor was entrapped in three hydrogel structures namely poly(acrylamide-N-isopropylacrylamide), P(AAm-NIPA), and semi-interpenetrating networks of poly(acrylamide)/alginate, P(AAm)/Alg, and poly(acrylamide-N-isopropylacrylamide)/alginate, P(AAm-NIPA)/Alg. The optimum temperatures for free and all immobilized systems were found to be 40 °C. For free and immobilized laccase systems of P(AAm-NIPA)-L, P(AAm)/Alg-L and P(AAm-NIPA)/Alg-L, K_m values were found to be 6.7 × 10^?3, 8.8 × 10^?2, 5.5 × 10^?2 and 1.8 × 10^?2 mM; V_max values were calculated as 1.8 × 10^?3, 2.5 × 10^?2, 1.5 × 10^?2 and 6.1 × 10^?3 mM min^?1, respectively. For free and the same immobilized systems, the enzymes retained 42%, 91%, 79% and 86% of their initial activities at the end of 56 days of storage. After using the mentioned immobilized systems repeatedly 10 times, they retained 77%, 71% and 84% of their original activities, respectively. For free and the same immobilized systems, decolorization of Acid Orange 52 (AO52) in 6 h were found to be 63%, 50%, 48% and 66%, respectively. Addition of 2,2′-azino-bis-(3-ethylbenzothiazoline-6-sulfonic acid), ABTS, into the assay medium increased these values up to 73%, 73%, 74% and 75%, respectively.     

Immobilization of urease on vapour phase stain etched porous silicon

Porous silicon layers fabricated by the reaction-induced vapor phase stain etch method were coated with 5% polyethylenimine. Urease from Canavalia brasiliensis beans was immobilized on this support through covalent linking with 2.5% glutaraldehyde. The pH and temperature profile of the immobilized and free urease exhibited higher activity at pH 6.5 and 37 °C. After being stored for 30 days at 4 °C, the immobilized enzyme had 75% of the initial activity. The maximum apparent Michaelis constant for free urease (K_m) was 94.33 mM whereas for immobilized urease was 53.04 mM. The maximum reaction velocity (V_max) for free urease was 3.51 mmol/min and for immobilized urease was 1.57 mmol/min.     

Effects of aqueous ozone on Pseudomonas syringae viability and ice nucleating activity

This study reports the impact of different ozone treatments on a Pseudomonas syringae strain known for its ice nucleation activity (INA). Ozone is a very powerful germicidal agent used for water treatment. The effect of ozone on viability and on cultivability of P. syringae was determined by flow cytometry analysis and by plate counting respectively. The impact of ozone on the outer membrane using the INA as marker was investigated by the drop freezing technique.The destruction curve followed a shoulder pattern with a slight reduction in population with CT values between 0 and 8 min. For an initial population of 9.3 log CFU mL^?1, the cultivability was lost starting at 14 min and a loss of viability was observed after 16 min of ozone treatment at 0.45 mg L^?1. Microscopic observations at this point revealed whole but aggregated bacilli. INA decreased after 8 min of ozone treatment but did not disappear. This decrease could be due to the progressive disruption of ice nucleating sites in the outer membrane. It was however partially restored after long storage at 4 °C of dead cells treated for 16 min.     

The effect of PI3 kinase inhibitor LY294002 on voltage-dependent K+ channels in rabbit coronary arterial smooth muscle cells

AimsWe examined the effect of LY294002, a phosphatidylinositol 3-kinase (PI3K) inhibitor, on voltage-dependent K⁺ (Kv) channels.Main methodsElectrophysiological recordings were performed in freshly isolated rabbit coronary arterial smooth muscle cells.Key findingsThe Kv current amplitude was inhibited by LY294002 in a dose-dependent manner, with a K_d value of 1.48 μM. Without alteration of the kinetics of activation, LY294002 accelerated the decay rate of Kv channel inactivation. The rate constants of association and dissociation for LY294002 were 1.83 ± 0.01 μM^? 1 s^? 1 and 2.59 ± 0.14 s^? 1, respectively. Application of LY294002 had no significant impact on the steady-state activation or inactivation curves. In the presence of LY294002, the recovery time constant from inactivation was increased, and Kv channel inhibition increased under train pulses (1 or 2 Hz). This indicates that LY294002-induced Kv channel inhibition is use-dependent. Furthermore, pretreatment with another PI3K inhibitor, wortmannin (10 μM), did not affect the Kv current, and did not change the inhibitory effect of LY294002.SignificanceBased on these results, we suggest that LY294002 directly blocks Kv current irrespective of PI3K inhibition.     

Optimization and immobilization of amylase obtained from halotolerant bacteria isolated from solar salterns

The objective of the present study was to isolate halotolerant bacteria from the sediment sample collected from Marakanam Solar Salterns, Tamil Nadu, India using NaCl supplemented media and screened for amylase production. Among the 22 isolates recovered, two strains that had immense potential were selected for amylase production and designated as P1 and P2. The phylogenetic analysis revealed that P1 and P2 have highest homology with Pontibacillus chungwhensis (99%) and Bacillus barbaricus (100%). Their amylase activity was optimized to obtain high yield under various temperature, pH and NaCl concentration. P1 and P2 strain showed respective, amylase activity maximum at 35 °C and 40 °C; pH 7.0 and 8.0; 1.5 M and 1.0 M NaCl concentration. Further under optimized conditions, the amylase activity of P1 strain (49.6 U mL^?1) was higher than P2 strain. Therefore, the amylase enzyme isolated from P. chungwhensis P1 was immobilized in sodium alginate beads. Compared to the free enzyme form (49.6 U mL^?1), the immobilized enzyme showed higher amylase activity as 90.3 U mL^?1. The enzyme was further purified partially and the molecular mass was determined as 40 kDa by SDS–PAGE. Thus, high activity of amylase even under increased NaCl concentration would render immense benefits in food processing industries.     

Determination of seed viability of eight wild Saudi Arabian species by germination and X-ray tests

Our purpose was to evaluate the usefulness of the germination vs. the X-ray test in determining the initial viability of seeds of eight wild species (Salvia spinosa, Salvia aegyptiaca, Ochradenus baccatus, Ochradenus arabicus, Suaeda aegyptiaca, Suaeda vermiculata, Prosopisfarcta and Panicumturgidum) from Saudi Arabia. Several days were required to determine viability of all eight species via germination tests, while immediate results on filled/viable seeds were obtained with the X-ray test. Seeds of all the species, except Sa.aegyptiaca, showed high viability in both the germination (98–70% at 25/15 °C, 93–66% at 35/25 °C) and X-ray (100–75%) test. Furthermore, there was general agreement between the germination (10% at 25/15 °C and 8% at 35/25 °C) and X-ray (5%) tests that seed viability of Sa.aegyptiaca was very low, and X-ray analysis revealed that this was due to poor embryo development. Seeds of P.farcta have physical dormancy, which was broken by scarification in concentrated sulfuric acid (10 min), and they exhibited high viability in both the germination (98% at 25/15 °C and 93% at 35/25 °C) and X-ray (98%) test. Most of the nongerminated seeds of the eight species except those of Sa.aegyptiaca were alive as judged by the tetrazolium test (TZ). Thus, for the eight species examined, the X-ray test was a good and rapid predictor of seed viability.     

Comparative biochemical characterization of soluble and chitosan immobilized β-galactosidase from Kluyveromyces lactis NRRL Y1564

An investigation was conducted on the production of β-galactosidase (β-gal) by different strains of Kluyveromyces, using lactose as a carbon source. The maximum enzymatic activity of 3.8 ± 0.2 U/mL was achieved by using Kluyveromyces lactis strain NRRL Y1564 after 28 h of fermentation at 180 rpm and 30 °C. β-gal was then immobilized onto chitosan and characterized based on its optimal operation pH and temperature, its thermal stability and its kinetic parameters (K_m and V_max) using o-nitrophenyl β-d-galactopyranoside as substrate. The optimal pH for soluble β-gal activity was found to be 6.5 while the optimal pH for immobilized β-gal activity was found to be 7.0, while the optimal operating temperatures were 50 °C and 37 °C, respectively. At 50 °C, the immobilized enzyme showed an increased thermal stability, being 8 times more stable than the soluble enzyme. The immobilized enzyme was reused for 10 cycles, showing stability since it retained more than 70% of its initial activity. The immobilized enzyme retained 100% of its initial activity when it was stored at 4 °C and pH 7.0 for 93 days. The soluble β-gal lost 9.4% of its initial activity when it was stored at the same conditions.     

Electrospinning of chitosan nanofibers: Processing optimization

In this study, the electrospinning of chitosan has been investigated. The problem of chitosan high viscosity, which limits its spinability, is resolved through the application of an alkali treatment which hydrolyzes chitosan chains and so decreases its their molecular weight. Solutions of the treated chitosan in aqueous 70–90% acetic acid produce nanofibers with appropriate quality and processing stability. Decreasing the acetic acid concentration in the solvent increases the mean diameter of the nanofibers. Optimum nanofibers are achieved with chitosan which is hydrolyzed for 48 h. Such nanofibers result in a moisture regain which is 74% greater than that of treated and untreated chitosan powder. The diameter of this nanofiber, 140 nm, is strongly affected by the electrospinning conditions as well as by the concentration of the solvent. FTIR investigations prove that neither the alkali treatment nor the electrospinning process change the chemical nature of the polymer.     

Influence of whole microalgal cell immobilization and organic solvent on the bioconversion of androst-4-en-3,17-dione to testosterone by Nostoc muscorum

The use of free, immobilized and reused immobilized cells of the microalga Nostoc muscorum was studied for bioconversion of androst-4-en-3,17-dione (AD) to testosterone in hexadecane. Among polymers such as agar, agarose, κ-carrageenan, polyacrylamide, polyvinyl alcohol, and sodium alginate that were examined for cell entrapment, sodium alginate with a concentration of 2% (w/v) proved to be the proper matrix for N. muscorum cells immobilization. The bioconversion characteristics of immobilized whole algal cells at ranges of temperatures, substrate concentrations, and shaking speeds were studied followed by a comparison with those of free cells. The conditions were 30 °C, 0.5 g/L, and 100 rpm, respectively. The immobilized N. muscorum showed higher yield (72 ± 2.3%) than the free form (24 ± 1.3%) at the mentioned conditions. The bioconversion yield did not decrease during reuse of immobilized cells and remained high even after 5 batches of bioreactions while Na-alginate 3% was used; however, reuse of alginate 2% beads did not give a satisfactory result.     

Immobilization of α-galactosidase on galactose-containing polymeric beads

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

Immobilization of fungal (Trametes versicolor) laccase onto Amberlite IR-120 H beads: Optimization and characterization

Laccase from Trametes versicolor was immobilized on Amberlite IR-120 H beads. Maximum immobilization obtained was 78.7% at pH = 4.5 and temperature T = 45 °C. Kinetic parameters, K_m and V_max values, were determined respectively as 0.051 mM and 2.77 × 10^?2 mM/s for free and 4.70 mM and 5.27 × 10^?3 mM/s for immobilized laccase. The Amberlite–laccase system showed a 30% residual activity after 7 cycles. On the other hand, the loss of activity for free laccase after 7 days of storage at 4 °C was 18.5% in comparison to Amberlite–laccase system with a loss of 1.4%, during the same period. Improved operational, thermal and storage stabilities of the immobilized laccase were obtained compared to the free counterpart. Therefore, the use of low-cost matrices, like Amberlite for enzyme immobilization represents a promising product for enzymatic industrial applications.     

Immobilization of Candida rugosa lipase on electrospun cellulose nanofiber membrane

A biocatalyst with high activity retention of lipase was fabricated by the covalent immobilization of Candida rugosa lipase on a cellulose nanofiber membrane. This nanofiber membrane was composed of nonwoven fibers with 200 nm nominal fiber diameter. It was prepared by electrospinning of cellulose acetate (CA) and then modified with alkaline hydrolysis to convert the nanofiber surface into regenerated cellulose (RC). The nanofiber membrane was further oxidized by NaIO₄. Aldehyde groups were simultaneously generated on the nanofiber surface for coupling with lipase. Response surface methodology (RSM) was applied to model and optimize the modification conditions, namely NaIO₄ content (2–10 mg/mL), reaction time (2–10 h), reaction temperature (25–35 °C) and reaction pH (5.5–6.5). Well-correlating models were established for the residual activity of the immobilized enzyme (R² = 0.9228 and 0.8950). We found an enzymatic activity of 29.6 U/g of the biocatalyst was obtained with optimum operational conditions. The immobilized lipase exhibited significantly higher thermal stability and durability than equivalent free enzyme.     

Immobilization of catalase onto Eupergit C and its characterization

Bovine liver catalase was covalently immobilized onto Eupergit C. Optimum conditions of immobilization: pH, buffer concentration, temperature, coupling time and initial catalase amount per gram of carrier were determined as 7.5, 1.0 M, 25 °C, 24 h and 4.0 mg/g, respectively. V_max and K_m were determined as 1.4(±0.2) × 10⁵ U/mg protein and 28.6 ± 3.6 mM, respectively, for free catalase, and as 3.7(±0.4) × 10³ U/mg protein and 95.9 ± 0.6 mM, respectively, for immobilized catalase. The thermal stability of the immobilized catalase in terms of half-life time (29.1 h) was comparably higher than that of the free catalase (9.0 h) at 40 °C. Comparison of storage stabilities showed that the free catalase completely lost its activity at the end of 11 days both at room temperature and 5 °C. However, immobilized catalase retained 68% of its initial activity when stored at room temperature and 79% of its initial activity when stored at 5 °C at the end of 28 days. The highest reuse number of immobilized catalase was 22 cycles of batch operation when 40 mg of immobilized catalase loaded into the reactor retaining about 50% of its original activity. In the plug flow type reactor, the longest operation time was found as 82 min at a substrate flow rate of 2.3 mL/min when the remaining activity of 40 mg immobilized catalase was about 50% of its original activity. The resulting immobilized catalase onto Eupergit C has good reusability, thermal stability and long-term storage stability.     

Immobilization of phytase on epoxy-activated Sepabead EC-EP for the hydrolysis of soymilk phytate

In this work, an active phytase concentrated extract from soybean sprout was immobilized on a polymethacrylate-based polymer Sepabead EC-EP which is activated with epoxy groups. The immobilized enzyme exhibited an activity of 0.1 U/g of carrier and activity yield of 64.7%. The optimum temperature and pH for the activity of both free and immobilized enzymes were found as 60 °C and pH 5.0, respectively. The immobilized enzyme was more stable than free enzyme in the range of pH 3.0–8.0 and more than 70% of the original activity was recovered. Both the enzymes completely retained nearly about 84% of their original activity at 65 °C. The K_m and V_max values were measured as 5 mM and 0.63 U/mg for free enzyme and 12.5 mM and 0.71 U/mg for immobilized enzyme, respectively. Free and immobilized soybean sprout phytase enzymes were also used in the biodegradation of soymilk phytate. The immobilized enzyme hydrolysed 92.5% of soymilk phytate in 7 h at 60 °C, as compared with 98% hydrolysis observed for the native enzyme over the same period of time. The immobilization procedure on Sepabead EC-EP is very cheap and also easy to carry out, and the features of the immobilized enzyme are very attractive that the potential for practical application is considerable.     

Characterization of the lipase immobilized on Mg–Al hydrotalcite for biodiesel

Immobilization of Saccharomyces cerevisiae lipase by physical adsorption on Mg–Al hydrotalcite with a Mg/Al molar ratio of 4.0 led to a markedly improved performance of the enzyme. The immobilized lipase retained activity over wider ranges of temperature and pH than those of the free lipase. The immobilized lipase retained more than 95% relative activity at 50 °C, while the free lipase retained about 88%. The kinetic constants of the immobilized and free lipases were also determined. The apparent activation energies (E_a) of the free and immobilized lipases were estimated to be 6.96 and 2.42 kJ mol^?1, while the apparent inactivation energies (E_d) of free and immobilized lipases were 6.51 and 6.27 kJ mol^?1, respectively. So the stability of the immobilized lipase was higher than that of free lipase. The water content of the oil must be kept below 2.0 wt% and free fatty acid content of the oil must be kept below 3.5 mg KOH g [oil]^?1 in order to get the best conversion. This immobilization method was found to be satisfactory to produce a stable and functioning biocatalyst which could maintain high reactivity for repeating 10 batches with ester conversion above 81.3%.     

Immobilization of alkaline serine endopeptidase from Bacillus licheniformis on SBA-15 and MCF by surface covalent binding

An industrial enzyme, alkaline serine endopeptidase, was immobilized on surface modified SBA-15 and MCF materials by amide bond formation using carbodiimide as a coupling agent. The specific activities of free enzyme and enzyme immobilized on SBA-15 and MCF were studied using casein (soluble milk protein) as a substrate. The highest activity of free enzyme was obtained at pH 9.5 while this value shifted to pH 10 for SBA-15 and MCF immobilized enzyme. The highest activity of immobilized enzymes was obtained at higher temperature (60 °C) than that of the free enzyme (55 °C). Kinetic parameters, Michaelis–Menten constant (K_m) and maximum reaction velocity (V_max), were calculated as K_m = 13.375, 11.956, and 8.698 × 10^?4 mg/ml and V_max = 0.156, 0.163 and 0.17 × 10^?3 U/mg for the free enzyme and enzyme immobilized on SBA-15 and MCF, respectively. The reusability of immobilized enzyme showed 80% of the activity retained even after 15 cycles. Large pore sized MCF immobilized enzyme was found to be more promising than the SBA-15 immobilized enzyme due to the availability of larger pores of MCF, which offer facile diffusion of substrate and product molecules.     

Decolorization of azo dye by immobilized Pseudomonas luteola entrapped in alginate–silicate sol–gel beads

Pseudomonas luteola was immobilized by entrapment in alginate–silicate sol–gel beads for decolorization of the azo dye, Reactive Red 22. The influences of biomass loading and operating conditions on specific decolorization rate and dye removal efficiency were studied in details. The immobilized cells were found to be less sensitive to changes in agitation rates (dissolved oxygen levels) and pH values. Michaelis–Menten kinetics could be used to describe the decolorization kinetics with the kinetic parameters being 36.5 mg g⁻¹ h⁻¹, 300.1 mg l⁻¹ and 18.2 mg g⁻¹ h⁻¹, 449.8 mg l⁻¹ for free and immobilized cells, respectively. After five repeated batch cycles, the decolorization rate of the free cells decreased by nearly 54%, while immobilized cells still retained 82% of their original activity. The immobilized cells exhibited better thermal stability during storage and reaction when compared with free cells. From SEM observation, a dense silicate gel layer was found to surround the macroporous alginate–silicate core, which resulted in much improved mechanical stability over that of alginate beads when tested under shaking conditions. Alginate–silicate matrices appeared to be the best matrix for immobilization of P. luteola in decolorization of Reactive Red 22 when compared with previous results using synthetic or natural polymer matrices.     

Treatment of dye-rich wastewater by an immobilized thermophilic cyanobacterial strain: Phormidium sp.

The removal of Remazol Blue and Reactive Black B by the immobilized thermophilic cyanobacterial strain Phormidium sp. was investigated under thermophilic conditions in a batch system, in order to determine the optimal conditions required for the highest dye removal. In the experiments, performed at pH 8.5, with different initial dye concentrations between 9.1 mg l⁻¹ and 82.1 mg l⁻¹ and at 45 °C, calcium alginate immobilized Phormidium sp. showed high dye decolorization, with maximum uptake yields ranging from 50% to 88% at all dye concentrations tested. When the effects of high dye concentrations on dye removal were investigated, the highest uptake yield in the beads was 50.3% for 82.1 mg l⁻¹ Remazol Blue and 60.0% for 79.5 mg l⁻¹ Reactive Black B. The highest color removal was detected at 45 °C and 50 °C incubation temperatures for all dye concentrations. As the temperature decreased, the removal yield of immobilized Phormidium sp. also decreased. At about 75 mg l⁻¹ initial dye concentrations, the highest specific dye uptake measured was 41.29–41.17 mg g⁻¹ for Remazol Blue and 47.69–43.82 mg g⁻¹ for Reactive Black B at 45 °C and 50 °C incubation temperatures, respectively, after 8 days incubation.     

Application of chitosan beads immobilized Rhodococcus sp. NCIM 2891 cholesterol oxidase for cholestenone production

The cell-bound cholesterol oxidase from the Rhodococcus sp. NCIM 2891 was purified three fold by diethylaminoethyl–sepharose chromatography. The estimated molecular mass (SDS-PAGE) and K_m of the enzyme were ∼55.0 kDa and 151 μM, respectively. The purified cholesterol oxidase was immobilized on chitosan beads by glutaraldehyde cross-linking reaction and immobilization was confirmed by Fourier transform infrared spectroscopy, scanning electron microscopy and energy dispersive X-ray analysis. The optimum temperature (45 °C, 5 min) for activity of the enzyme was increased by 5 °C after immobilization. Both the free and immobilized cholesterol oxidases were found to be stable in many organic solvents except for acetone. Fe²⁺ and Pb²⁺ at 0.1 mM of each acted as inhibitors, while Ag⁺, Ca²⁺, Ni²⁺ and Zn²⁺ activated the enzyme at similar concentration. The biotransformation of cholesterol (3.75 mM) with the cholesterol oxidase immobilized beads (3.50 U) leads to ∼88% millimolar yield of cholestenone in a reaction time of 9 h at 25 °C. The immobilized enzyme retains ∼67% activity even after 12 successive batches of operation. The biotransformation method thus, shows a great promise for the production of pharmaceutically important cholestenone.