Dye decolorisation by laccase entrapped in copper alginate

A novel immobilisation system was developed for dye decolorisation using laccase produced by Ganoderma sp. KU-Alk4. The enzyme showed high efficiency in dye decolorisation when entrapped in Cu–Al and Cu-alginate beads. The former gave the highest activity but the enzyme activity survived longer in the latter. An experimental design of two 3 × 3 Latin Square experiments was applied to evaluate the effects of three different alginate compositions (low, intermediate and high mannuronate), concentration of alginate, (1.5, 3.0 and 4.5% w/v) and concentration of cross-linking agent, CuSO₄ (0.075, 0.15 and 0.225 M) on the decolorisation of indigo carmine dye and residual laccase activity in beads. The most significant factor for residual activity was the concentration of the cross-linking agent (P < 0.05) followed by alginate composition (P < 0.1). Increasing the alginate concentration resulted in only small increase in the dye decolorisation. However, higher laccase activity remained in 3.0% w/v alginate beads. Maximal dye decolorisation was achieved when 3.6% w/v low mannuronate alginate and 0.15 M CuSO₄ was used. Optimal conditions were confirmed in an extended experimental run. Results are presented from 9 successive batch runs over 12 days, reaching 96% removal of the dye (216 mg/l).     

Enhanced production of laccase activity by <Emphasis Type="Italic">Trametes versicolor </Emphasis>immobilized into alginate beads by the addition of different inducers

In the present paper the effect of adding veratryl alcohol and copper sulphate on laccase activity production by Trametes versicolor immobilized into alginate beads has been investigated. Employing copper sulphate as laccase inducer or supplementing the culture medium with veratryl alcohol, led to maximum values of laccase activity. However, the highest laccase activity (around 4,000 U l⁻¹) was obtained in cultures simultaneously supplemented with copper sulphate (3 mM) and veratryl alcohol (20 mM). These values implied a considerable enhancement in relation to␣control cultures without any inducer (around 200 U l⁻¹). The production of laccase by immobilized T. versicolor in a 2-l airlift bioreactor with the optimized inducer has been evaluated. Laccase activities around 1,500 U l⁻¹ were attained. The bioreactor operated for 44 days without operational problems and the bioparticles (fungus grows in alginate beads) maintained their shape throughout the fermentation. Moreover, the extracellular liquid obtained was studied in terms of pH and temperature activity and stability. On the other hand, anthracene was added in two-repeated batches in order to determine the efficiency of this process to degrade pollutants. Near complete degradation was reached in both batches. Moreover, in vitro degradation of several polycyclic aromatic hydrocarbons by crude laccase was also performed.     

Laccase-mediated Remazol Brilliant Blue R decolorization in a fixed-bed bioreactor

A crude laccase mixture preparation from Pleurotus ostreatus cultures supplemented with copper and ferulic acid was used to decolorize the anthraquinonic dye Remazol Brilliant Blue R (RBBR). Performance of this enzymatic system was tested, and a maximum of 70% decolorization was achievable under optimal conditions. The crude preparation was immobilized by entrapment in copper alginate beads attaining 65% yield of laccase activity. Stability of the immobilized laccases was remarkably increased in comparison with that of the free enzyme preparation. Efficiency of the immobilized system was evaluated during stepwise dye additions in batch operations. Under the best conditions, 70% RBBR decolorization was achieved even after 20 cycles, although decolorization time exponentially increased after the 10th cycle. Different fixed-bed bioreactors were prepared and analyzed in continuous decolorization processes. The best performance was obtained by decreasing the amount of enzyme loaded and by improving laccase retention using chitosan-coated alginate beads.     

Repeated batch production of ethanol from Jerusalem artichoke tubers using recycled immobilized cells of Kluyveromyces fragilis

Summary Recycled immobilized cells of Kluyveromyces fragilis ATCC 28244 were used for repeated batch production of ethanol from the inulin sugars derived from Jerusalem artichoke tubers. Using 10% initial sugar concentration, a maximum ethanol concentration of 48 g/l was achieved in 7 h when the immobilized cell concentration in the Ca alginate beads was 72 g dry wt. immobilized cell/l bead volume. The maximum ethanol production rate was 13.5 g ethanol/l bioreactor volume/h. The same Ca alginate beads containing the cells were used repeatedly for 11 batch runs starting with fresh medium at the beginning of each run. The ethanol yield was found to be almost constant at 96% of the theoretical for all 11 batch runs, while the maximum ethanol production rate during the last batch run was found to be 70% of the original ethanol rate obtained in the first batch run.     

Improvement of biodesulfurization activity of alginate immobilized cells in biphasic systems

The immobilization of Pseudomonas delafieldii R-8 in calcium alginate beads has been studied in order to improve biodesulfurization activity in oil/water (O/W) biphasic systems. A gas jet extrusion technique was performed to produce immobilized beads. The specific desulfurization rate of 1.5 mm diameter beads was 1.4-fold higher than that of 4.0 mm. Some nonionic surfactants can significantly increase the activity of immobilized cells. The desulfurization rate with the addition of 0.5% Span 80 increased 1.8-fold compared with that of the untreated beads. The rate of biodesulfurization was markedly enhanced by decreasing the size of alginate beads and adding the surfactant Span 80, most likely resulting from the increasing mass transfer of substrate to gel matrix.     

Decolorization of phenolic effluents by soluble and immobilized phenol oxidases

Summary Colour removal from phenplic industrial effluents by phenol oxidase enzymes and white-rot fungi was compared. Soluble laccase and horseradish peroxidase (HRP) removed colour from pulp mill (E), cotton mill hydroxide (OH) and cotton mill sulphide (S) effluents, but rapid and irreversible enzyme inactivation took place. Entrapment of laccase in alginate beads improved decolorization by factors of 3.5 (OH) and 2 (E); entrapment of HRP improved decolorization by 36 (OH), 20 (E) and 9 (S). Beads were unsuitable for continuous use because the enzymes were rapidly released into solution. Co-polymerization of laccase or HRP with L-tyrosine gave insoluble polymers with enzyme activity. Entrapment of the co-polymers in gel beads further increased the efficiency of decolorization of E by 28 (laccase) and by 132 (HRP) compared with soluble enzymes. Maximum decolorization of all three effluents by batch cultures of Coriolus versicolor (70%–80% in 8 days) was greater than the maximum enzymic decolorization (48% of OH in 3 days by entrapped laccase). Soluble laccase (222 units ml^–1) precipitated 1.2 g l^–1 phenol from artificial coal conversion effluent at pH 6.0 and the rate of precipitation and enzyme inactivation was faster at pH 6.0 than at pH 8.5.Offprint requests to: R. G. Burns     

Reactive blue 19 decolouration by laccase immobilized on silica beads

Laccase (31.5 U of activity/g or 4.39 μg of protein/m²) from Trametes versicolor was immobilized on controlled-porosity-carrier silica beads and evaluated for the decolouration of Reactive blue 19, an anthraquinone dye. Although there was an initial, rapid adsorption of the dye to the packed bed in a recirculating reactor, about 97.5% of Reactive blue 19 removal was due to enzymatic degradation. The free enzyme lost 52% of its activity in 48 h. However, the activity of the immobilized laccase was unchanged after 4 months of storage in phosphate buffer under ambient conditions followed by three successive decolourations over 120 h. Treating the laccase immobilized beads with ethanolamine reduced dye adsorption by 40%.     

Immobilization of fructosyltransferase by chitosan and alginate for efficient production of fructooligosaccharides

The effective system of reusing mycelial fructosyltransferase (FTase) immobilized with two polymers, chitosan and alginate were evaluated for continuous production of fructooligosaccharides (FOS). The alginate beads were successfully developed by maintaining spherical conformation of using 0.3% (w/v) sodium alginate with 0.1% (w/v) of CaCl₂ solution for highest transfructosylating activity. The characteristics of free and immobilized FTase were investigated and results showed that optimum pH and temperature of FTase activity were altered by immobilized materials. A successive production of FOS by FTase entrapped alginate beads was observed at an average of 62.96% (w/w) up to 7 days without much losing its activity. The data revealed by HPLC analysis culminate 67.75% (w/w) of FOS formation by FTase entrapped alginate beads and 42.79% (w/w) by chitosan beads in 36 h of enzyme substrate reaction.     

Immobilized laccase of Cerrena unicolor for elimination of endocrine disruptor micropollutants

The white-rot fungus Cerrena unicolor C-139 produced 450?000 U l⁻¹ of laccase when cultivated in submerged (50 ml) fermentation of wheat bran. Laccase (benzenediol: oxygen oxidoreductase, EC 1.10.3.2.), from C. unicolor C-139 was immobilized covalently on control porosity carrier silica beads. The activity of the immobilized laccase was approximately 15.8 units per gram of silica beads. The pH optimum was between 2.5 and 3.0 for free and immobilized laccase. The immobilization of enzyme appeared to be the main factor for retention of laccase activity at high temperature of 80 °C. The apparent K_m value (100 μmol) of immobilized laccase from C. unicolor C-139 was 6.7 times higher than free laccase (15 μmol) using 2,2-azino-bis-[3-ethylthiazoline-6-sulfonate] (ABTS) as the substrate. Immobilized laccase was able to eliminate 80 % of Bisphenol A, 40 % of Nonylphenol, and 60 % of Triclosan from solutions containing 50 μmol of each micropollutant separately. The experiments were run three times consecutively with the same immobilized laccase without loss of enzyme activity.     

Production of thermostable and neutral glucoamylase using immobilized <Emphasis Type="Italic">Thermomucor indicae-seudaticae</Emphasis>

Thermomucor indicae-seudaticae was immobilized in alginate, κ-carrageenan, agarose, agar, polyacrylamide and loofah (Luffa cylindrica) sponge (as such or coated with alginate/starch/Emerson YpSs agar), and used for the production of glucoamylase in submerged fermentation. The mycelium developed from alginate-immobilized sporangiospores secreted higher glucoamylase titres (22.7 U ml⁻¹) than those immobilized in other gel matrices and the freely growing mycelial pellets (18.5 U ml⁻¹). Loofah network provided a good support for mycelial growth, but the enzyme production was lower than that attained with alginate beads. Glucoamylase production increased with inoculum density and the optimum levels were achieved when 40 calcium alginate beads (∼5 × 10⁶ immobilized spores) were used to inoculate 50 ml production medium. The alginate bead inoculum displayed high storage stability at 4°C and produced comparable enzyme titres up to 120 days. The glucoamylase production by hyphae emerged from the immobilized sporangiospores was almost stable over eight batches of repeated fermentation. Scanning electron micrographs of alginate beads, after batch fermentation, revealed extensive mycelial growth inside and around the beads.     

Production of l (+) lactic acid by Lactobacillus delbrueckii immobilized in functionalized alginate matrices

The role of functionalized alginate gels as immobilized matrices in production of l (+) lactic acid by Lactobacillus delbrueckii was studied. L. delbrueckii cells immobilized in functionalized alginate beads showed enhanced bead stability and selectivity towards production of optically pure l (+) lactic acid in higher yields (1.74Yp/s) compared to natural alginate. Palmitoylated alginate beads revealed 99% enantiomeric selectivity (ee) in production of l (+) lactic acid. Metabolite analysis during fermentation indicated low by-product (acetic acid, propionic acid and ethanol) formation on repeated batch fermentation with functionalized immobilized microbial cells. The scanning electron microscopic studies showed dense entrapped microbial cell biomass in modified immobilized beads compared to native alginate. Thus the methodology has great importance in large-scale production of optically pure lactic acid.     

Solid matrix characterization of immobilized Pseudomonas putida MTCC 1194 used for phenol degradation

Characterization studies of calcium alginate beads with encapsulated Pseudomonas putida MTCC 1194, used for the biodegradation of phenol, were carried out to investigate the reactivity, reusability and structural strength of the solid matrix. Various techniques were employed to improve the structural stability of the immobilized solid necessary for its use in commercial reactors like packed bed flow reactor, fluidized bed and CSTR systems. Experiments were performed to establish the optimum conditions for durability, strength and steady biochemical reactivity. During a batch run of 40 h a gradual decline in the rate of phenol degradation was observed with the immobilized system. The calcium alginate beads with high structural strength yielded decreased activity. Treatment with a hardening agent like glutaraldehyde for different concentrations and treatment times led to variations in structural stability, reusability and the extent of phenol degradation. Scanning electron microscope studies of the immobilized solid indicated the internal distribution pattern of the cells encapsulated in a calcium alginate bead. Received: 13 November 1998 / Received revision: 27 January 1999 / Accepted: 31 January 1999     

Production of xylanase by immobilized Trichoderma reesei SAF3 in Ca-alginate beads

In the present study, the optimum conditions for the production of xylanase by immobilized spores of Trichoderma reesei SAF3 in calcium alginate beads were determined. The operational stability of the beads during xylanase production under semi-continuous fermentation was also studied. The influence of alginate concentration (1, 2, 3, and 4%) and initial cell loading (100, 200, 300, 400, and 500 beads per flask) on xylanase production was considered. The production of xylanase was found to increase significantly with increasing concentration of alginate and reached a maximum yield of 3.12 ± 0.18 U ml⁻¹ at 2% (w/v). The immobilized cells produced xylanase consistently up to 10 cycles and reached a maximum level at the forth cycle (3.36 ± 0.2 U ml⁻¹).     

Production of bioflavor by regeneration from protoplasts of Ulva pertusa (Ulvales,Chlorophyta)

Protoplasts were isolated from thalli of Ulva pertusa using a mixed enzyme solution of 2.0% Cellulase Onozuka R-10, 2.0% Macerozyme R-10, and 2.0% Driselase. Isolated protoplasts regenerated cell walls, developed into thalli, and propagated in large numbers under aeration in the preparative scale-culture system. Typical bioflavor compounds produced from the regenerated plants, as well as from field-collected plants, were found to be long chain aldehydes, which gave a typical seaweed odor. The long chain aldehydes were formed enzymatically from unsaturated fatty acids and released into the culture fluid. A Percoll/mannitol discontinuous density gradient separation of the heterogeneous protoplasts led to a selection of cell lines with high production of bioflavor. The cells that regenerated from protoplasts were immobilized by polymer matrices such as alginate, -carrageenan, agarose, and agar. Living cells entrapped in alginate beads in aerated cultures survived best. However, the beads started to breakdown after two months. The immobilized cells demonstrated a higher bioflavor production than did the cultured cells.     

Immobilization of soybean (Glycine max) urease on alginate and chitosan beads showing improved stability: Analytical applications

The soybean (Glycine max) urease was immobilized on alginate and chitosan beads and various parameters were optimized and compared. The best immobilization obtained were 77% and 54% for chitosan and alginate, respectively. A 2% chitosan solution (w/v) was used to form beads in 1N KOH. The beads were activated with 1% glutaraldehyde and 0.5 mg protein was immobilized per ml of chitosan gel for optimum results. The activation and coupling time were 6 h and 12 h, respectively. Further, alginate and soluble urease were mixed to form beads and final concentrations of alginate and protein in beads were 3.5% (w/v) and 0.5 mg/5 ml gel. From steady-state kinetics, the optimum temperature for urease was 65 °C (soluble), 75 °C (chitosan) and 80 °C (alginate). The activation energies were found to be 3.68 kcal mol⁻¹, 5.02 kcal mol⁻¹, 6.45 kcal mol⁻¹ for the soluble, chitosan- and alginate-immobilized ureases, respectively. With time-dependent thermal inactivation studies, the immobilized urease showed improved stability at 75 °C and the t_1/2 of decay in urease activity was 12 min, 43 min and 58 min for soluble, alginate and chitosan, respectively. The optimum pH of urease was 7, 6.2 and 7.9 for soluble, alginate and chitosan, respectively. A significant change in K_m value was noticed for alginate-immobilized urease (5.88 mM), almost twice that of soluble urease (2.70 mM), while chitosan showed little change (3.92 mM). The values of V_max for alginate-, chitosan-immobilized ureases and soluble urease were 2.82 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein, 2.65 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein and 2.85 × 10² μmol NH₃ min⁻¹ mg⁻¹ protein, respectively. By contrast, reusability studies showed that chitosan–urease beads can be used almost 14 times with only 20% loss in original activity while alginate–urease beads lost 45% of activity after same number of uses. Immobilized urease showed improved stability when stored at 4 °C and t_1/2 of urease was found to be 19 days, 80 days and 121 days, respectively for soluble, alginate and chitosan ureases. The immobilized urease was used to estimate the blood urea in clinical samples. The results obtained with the immobilized urease were quite similar to those obtained with the autoanalyzer^®. The immobilization studies have a potential role in haemodialysis machines.     

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.     

Improving of Catalase Stability Properties by Encapsulation in Alginate/Fe3O4 Magnetic Composite Beads for Enzymatic Removal of H2O2

The aim of this study was enhancing of stability properties of catalase enzyme by encapsulation in alginate/nanomagnetic beads. Amounts of carrier (10–100 mg) and enzyme concentrations (0.25–1.5 mg/mL) were analyzed to optimize immobilization conditions. Also, the optimum temperature (25–50°C), optimum pH (3.0–8.0), kinetic parameters, thermal stability (20–70°C), pH stability (4.0–9.0) operational stability (0–390 min), and reusability were investigated for characterization of the immobilized catalase system. The optimum pH levels of both free and immobilized catalase were 7.0. At the thermal stability studies, the magnetic catalase beads protected 90% activity, while free catalase maintained only 10% activity at 70°C. The thermal profile of magnetic catalase beads was spread over a large area. Similarly, this system indicated the improving of the pH stability. The reusability, which is especially important for industrial applications, was also determined. Thus, the activity analysis was done 50 times in succession. Catalase encapsulated magnetic alginate beads protected 83% activity after 50 cycles.     

Dye decolorization by <Emphasis Type="Italic">Trametes hirsuta</Emphasis> immobilized into alginate beads

Summary The present paper studies the production of laccase by Trametes hirsuta immobilized into alginate beads in an airlift bioreactor. In order to enhance laccase production fresh ammonium chloride was added, which led to the production, of high laccase activities (around 1000 U l⁻¹). The bioreactor operated for 40 days without operational problems and the bioparticles maintained their shape throughout fermentation. Dye decolorization was performed at bioreactor scale operating in the batch mode. High decolorization percentages were obtained in a short time (96% for indigo carmine and 69% for phenol red in 24 h), indicating the suitability of this process for application to synthetic dye decolorization. On the other hand, in vitro decolorization of several industrial azo dyes by crude laccase produced in the above bioreactor was also performed. It was found that some of the dyes needed the addition of 1-hydroxybenzotriazole for their decolorization.     

Preparation and characterization of epoxy-functionalized magnetic chitosan beads: laccase immobilized for degradation of reactive dyes

Cross-linked magnetic chitosan beads were prepared by phase-inversion technique in the presence of epichlorohydrin under alkaline condition, and used for covalent immobilization of laccase. The activity of the immobilized laccase on the magnetic chitosan was about 260 U (g/dry beads) with an enzyme loading of about 16.33 ± 0.39 mg [(g/dry beads) mg/g]. Kinetic parameters, V _max and K _m values were determined as 21.7 U/mg protein and 9.4 μM for free enzyme, and 15.6 U/mg protein and 19.7 μM for the immobilized laccase, respectively. The operational and thermal stabilities of the immobilized laccase were improved compared to free counterpart. The immobilized laccase was operated in a batch reactor for the decolorization of reactive dyes from aqueous solution. The laccase immobilized on magnetic chitosan beads was very effective for removal of textile dyes from aqueous solution which creates an important environmental problem in the discharged textile dying solutions.