Immobilization of Candida antarctica lipase B (CALB) on surface-modified rice husk ashes (RHA) via physical adsorption and cross-linking methods

In the present study, the recovery of activity of Candida antarctica lipase B (CALB) immobilized onto surface-modified rice husk ash (RHA) was 90% for both cross-linking and adsorption methods. Both cross-linked and adsorbed immobilized preparations were very stable, retaining more than 48% of their activity over the range of temperatures studied. The optimum temperature and optimum pH values were 37?°C and 7.0, respectively for both immobilized preparations, while the relative activities after storage at 4.0?°C for 60 days were 55% and 65% using cross-linking and adsorption methods, respectively. Also, the activity of the immobilized lipase began to decrease after 10 cycles, more than 58% of the initial activities were still retained after 10 cycles for both immobilization methods. These results indicated that lipase immobilized by cross-linking and adsorption not only effected activity recovery, but also remarkably effected stability, reusability and application adaptability. It can be concluded that, surface-modified RHA can be used as alternative supports for immobilization of CALB for polymerization reactions.     

Polyvinylamine‐coated polyester fibers as a carrier matrix for the immobilization of peroxidases

Biocatalytic transformations that employ immobilized enzymes become increasingly important for industrial applications. Synthetic or natural textile fiber materials such as polyester, polyamide or viscose are support materials that are comparatively inexpensive. Contrary to traditional support materials, their flexibility enables their use in reactors of any geometry and a fast and residue‐free removal from batch reactors. In this study a permanently immobilized peroxidase (Baylase®) has been investigated on polyester felt as a solid support as a new heterogeneous catalyst system. The polyester felt was functionalized by coating with polyvinylamine and subsequent activation with glutaraldehyde as a crosslinking agent. The enzyme load on the textile surface, the activity of the immobilized protein after repeated use as well as the storage stability was evaluated. Scanning electron micrographs and UV Vis spectroscopy made it possible to verify the enzyme immobilization on the textile surface. Furthermore, the load of immobilized peroxidase was determined by ICP OE spectrometry to be 9–12 mg per gram of textile. The activity of immobilized Baylase® remained high over 35 reaction cycles and a storage period of 8 weeks.     

Decolorization of Kraft effluent by free and immobilized lignin peroxidases and horseradish peroxidase

Color removal from Kraft effluent by lignin peroxidase and horseradish peroxidase was compared. Free lignin peroxidase and horseradish peroxidase removed color from kraft effluent. Immobilization of lignin peroxidase type III, lyophilized fungal culture and horseradish peroxidase on CNBr-Sepharose 4B improved the decolorization by factor of 2.9, 4.5 and 2.6, respectively in 48 h. Lignin peroxidase type I was effective only in the immobilized form in decolorization. In general, the immobilized form all the studied systems exhibited an average value around of 30% polymer consumption and very little of depolymerization. Lignin peroxidases and lyophilized fungal culture were shown to have considerable potential for treating Kraft effluents.     

Nutrient removal from slaughterhouse wastewater in an intermittently aerated sequencing batch reactor

The performance of a 10 L sequencing batch reactor (SBR) treating slaughterhouse wastewater was examined at ambient temperature. The influent wastewater comprised 4672+/-952 mg chemical oxygen demand (COD)/L, 356+/-46 mg total nitrogen (TN)/L and 29+/-10 mg total phosphorus (TP)/L. The duration of a complete cycle was 8 h and comprised four phases: fill (7 min), react (393 min), settle (30 min) and draw/idle (50 min). During the react phase, the reactor was intermittently aerated with an air supply of 0.8L/min four times at 50-min intervals, 50 min each time. At an influent organic loading rate of 1.2g COD/(Ld), average effluent concentrations of COD, TN and TP were 150 mg/L, 15 mg/L and 0.8 mg/L, respectively. This represented COD, TN and TP removals of 96%, 96% and 99%, respectively. Phase studies show that biological phosphorus uptake occurred in the first aeration period and nitrogen removal took place in the following reaction time by means of partial nitrification and denitrification. The nitrogen balance analysis indicates that denitrification and biomass synthesis contributed to 66% and 34% of TN removed, respectively.     

Removal of phenols from mixtures by co-immobilized laccase/tyrosinase and Polyclar adsorption

An enzymatic method for removal of phenols from their mixtures was investigated. Phenols in an aqueous solution were removed after a two-step treatment with co-immobilized laccase and tyrosinase and Polyclar (polyvinylpolypyrrolidone). A laccase from Pyricularia oryzae and mushroom tyrosinase were co-immobilized on Mikroperl in a fixed-bed tubular bioreactor by a rapid and simple method. The support immobilized 95% of the total laccase units and 35% of the total tyrosinase units. Different mixtures of phenols were passed through the column with co-immobilized laccase and tyrosinase. This method removed 42–90% of different phenolic substances by a single passage through the bioreactor. The second step employed Polyclar for additional removal of phenolic substances from mixtures. The degree of removal depends on the nature of the phenols. Complete removal was achieved for a-naphthol, 2,4-dichlorophenol, 4-methoxyphenol, b-naphthol, 4-chloro-3-methylphenol and catehin. The operational stability of the immobilized system was 10–90 h depending on the substrate. The biocatalyst was capable of continuous transformation of different phenols in mixtures. Journal of Industrial Microbiology & Biotechnology (2000) 24, 383–388. Received 12 August 1999/ Accepted in revised form 18 February 2000     

Immobilisation of soybean seed coat peroxidase on its natural support for phenol removal from wastewater

Soybean seed coat peroxidase (SBP; EC 1.11.1.7) was immobilised on its natural support, soybean seed coats, anticipating its use in phenol removal. Periodate and glutaraldehyde chemistries were assayed. Periodate failed to immobilise any SBP, whereas glutaraldehyde was effective. The optimum concentration of glutaraldehyde was found to be 1%. Immobilisation shifted the optimum pH for phenol removal from 4.0 to 6.0. Treated seed coat retained its activity over a 4-week period, and reusability assays showed that treated seed coats could be reused once for phenol removal. Polyethylene glycol (PEG) increased the stability of phenol degradation activity. In addition, the phenolic polymer was adsorbed on to seed coats, thus making removal of the polymeric product easier.     

Immobilisation of soybean seed coat peroxidase on its natural support for phenol removal from wastewater

Soybean seed coat peroxidase (SBP; EC 1.11.1.7) was immobilised on its natural support, soybean seed coats, anticipating its use in phenol removal. Periodate and glutaraldehyde chemistries were assayed. Periodate failed to immobilise any SBP, whereas glutaraldehyde was effective. The optimum concentration of glutaraldehyde was found to be 1%. Immobilisation shifted the optimum pH for phenol removal from 4.0 to 6.0. Treated seed coat retained its activity over a 4-week period, and reusability assays showed that treated seed coats could be reused once for phenol removal. Polyethylene glycol (PEG) increased the stability of phenol degradation activity. In addition, the phenolic polymer was adsorbed on to seed coats, thus making removal of the polymeric product easier.     

树脂载体固定S-腺苷甲硫氨酸合成酶的研究

目的:筛选一种适合S-腺苷甲硫氨酸合成酶固定化的树脂载体,进行固定化工艺优化及固定化酶性质研究。方法:以固定化率和表观酶活回收率为指标,筛选固定化效果最佳的一种树脂,采用单因素实验对固定化条件进行优化。结果:阴离子交换树脂载体ESR-2表现出最优的固定化率(94.03%)和酶活回收率(47.45%);最佳固定化条件为加酶量4U/g、pH 8.0、15℃吸附10h,最佳条件下固定化酶表观酶活为2.1U/g,表观酶活回收率达51.6%。固定化酶的最适pH为8.5,最适温度为35℃,连续反应10批次后酶活剩余77.92%。结论:树脂载体ESR-2固定化S-腺苷甲硫氨酸合成酶酶活及稳定性较好,能够用于S-腺苷甲硫氨酸的工业化大规模生产。     

Comparison of two continuous fungal bioreactors for posttreatment of anaerobically pretreated weak black liquor from kraft pulp mills

The purpose of this work was to evaluate and compare two continuous systems of posttreatment of anaerobically pretreated weak black liquor (WBL). The first system consisted of a packed bed reactor (PBR) with Trametes versicolor (Tv) immobilized on wood cubes of holm oak (biocubes). The second system was a fluidized bed reactor (FBR) with Lentinus edodes (Le) immobilized on wood cubes of holm oak. The reactors operated for 65 days at a hydraulic retention time (HRT) of 5 days, at 28 degrees C, with continuous aeration. Response variables monitored were conventional and specific, unit, net removal efficiency (eta and eta(sun), respectively) of chemical oxygen demand (COD), color, and ligninoids, and enzymatic activities of manganese peroxidase (MnP), lignin peroxidase (LiP), laccase (Lac) and proteases. The PBR showed an average color eta superior to that of the FBR (52.42 +/- 21.78% and 25.34 +/- 14.38% for PBR and FBR, respectively); removals of COD and ligninoids presented a similar pattern to that of color. Lac activity was significantly larger in PBR than in FBR. Activity of MnP in PBR was higher than that of the FBR (0.004 and 0.002 U MnP/mL, respectively). This difference could be ascribed to the different fungi present in each bioreactor. LiP activity was very low in both reactors. Average value of proteases was almost double in the FBR as compared with PBR (0.472 and 0.209 U Proteases/mL, respectively). During the last 2 weeks of operation, biocubes in the FBR experienced a significant loss of the attached Le biomass, probably by attrition. This and higher protease activity in the FBR could explain the lower pollutant removals achieved in the FBR. Overall, PBR with immobilized Tv showed a better performance than the FBR with Le for the posttreatment of the recalcitrant anaerobic effluent. Extended and sustained pollutant removal (65 days) was achieved in the PBR, although more research is needed to evaluate bioreactor performance at shorter hydraulic retention times.     

Preparation of a stable biocatalyst of bovine liver catalase using immobilization and postimmobilization techniques

Bovine liver catalase was immobilized on different supports. The tetrameric nature of this enzyme was found to cause its rapid inactivation in diluted conditions due to subunit dissociation, a fact that may rule out its industrial use. Multi-subunit immobilization using highly activated glyoxyl agarose was not enough to involve all enzyme subunits. In fact, washing the derivative produced a strong decrease in the enzyme activity. Further cross-linking of previously immobilized enzyme with tailor-made dextran-aldehyde permitted the multimeric structure to be fully stabilized using either multisubunit preparations immobilized onto highly activated glyoxyl-agarose support or one subunit enzymes immobilized onto poorly activated glyoxyl-agarose. The highest stability of the final biocatalyst was observed using the multisubunit immobilized derivative cross-linked with dextran-aldehyde. The optimal derivative retained around 60% of the immobilized activity, did not release any enzyme subunits after boiling in the presence of SDS, and did not lose activity during washing, and its stability did not depend on the dilution. This derivative was used for 10 cycles in the destruction of 10 mM hydrogen peroxide without any decrease in the enzyme activity.     

Immobilization and kinetics of catalase onto magnesium silicate

Bovine liver catalase was immobilized covalently with glutaraldehyde, or glutaraldehyde+3-aminopropionic acid as a spacer, onto magnesium silicate. The coupling time was determined as 2 h for immobilization. The pH and temperature optima as well as the changes in the kinetics (K_m, V_max, E_a) of the immobilized catalase was observed and discussed. Immobilized catalase preparations showed higher storage stabilities than free catalase. The half-life of free catalase, catalase immobilized via glutaraldehyde and catalase immobilized via glutaraldehyde+spacer were calculated as 2, 55 and 10 days at room temperature and 4, 85 and 107 days at 5 °C, respectively. The operational stability of the catalase immobilized via glutaraldehyde was higher than the catalase immobilized via glutaraldehyde+spacer. The remaining activity of the catalase immobilized via glutaraldehyde was about 90% and that of the catalase immobilized via glutaraldeyde+spacer was about 30% after 20 cycles of batch operation.     

Immobilization of pectawamorine G10x by gel entrapment

Polyacrylamide gel immobilization of pectawamorine G10x was investigated. Its pectinesterase and polygalacturonase activity and stability in storage were measured. The degree of pectawamorine binding during gel immobilization was 80--90%, 55% of initial activity being retained. Thermal stability of the immobilized and native preparations was equal. Pectinesterase activity of the gel immobilized enzyme increased during storage.     

Kraft mill anaerobic effluent color enhancement by a fixed-bed adsorption system

An anaerobic reactor and a fixed-bed adsorption sequential system (FBAS) were applied to remove color from kraft mill effluent. Under anaerobic conditions, Biological Oxygen Demand (BOD₅) removal was between 84 to 90% w/w, while Chemical Oxygen Demand (COD) removal ranged between 46 to 55% w/w. Total phenolic compounds were poorly removed (8 to 15% w/w) whereas the color was not removed by anaerobic digestion. For the FBAS system, three different columns were packed with natural and activated (calcinated and acidified) allophanic soil and fed with kraft mill anaerobic effluent. In activated soil columns, color and total phenolic compounds removal were around 95% w/w, whereas in the natural soil column the values were 87% w/w and 81% w/w, respectively.     

2,4-Dichlorophenol (DCP) containing wastewater treatment using a hybrid-loop bioreactor

Synthetic wastewater containing 2,4-dichlorophenol (DCP) was biologically treated using a hybrid-loop bioreactor system consisting of a packed column biofilm reactor (PCBR) and an aerated tank with effluent recycle. Effects of the feed DCP concentration on COD, DCP and toxicity removals were investigated. Biomass concentration in the packed column and in the aeration tank decreased with increasing feed DCP content due to toxic effects of DCP on the microorganisms. Low biomass concentrations at high DCP contents resulted in low COD, DCP and toxicity removals. Therefore, percent DCP, COD and toxicity removals decreased with increasing feed DCP content. Nearly 70% COD removal was achieved with a feed DCP content of 380 mg L(-1). The system should be operated with the feed DCP lower than 100 mg L(-1) in order to obtain DCP, COD and toxicity removals above 90%.     

Calcium alginate–starch hybrid support for both surface immobilization and entrapment of bitter gourd (Momordica charantia) peroxidase

Calcium alginate–starch hybrid gel was employed as an enzyme carrier both for surface immobilization and entrapment of bitter gourd peroxidase. Entrapped crosslinked concanavalin A–bitter gourd peroxidase retained 52% of the initial activity while surface immobilized and glutaraldehyde crosslinked enzyme showed 63% activity. A comparative stability of both forms of immobilized bitter gourd peroxidase was investigated against pH, temperature and chaotropic agent; like urea, heavy metals, water-miscible organic solvents, detergent and inhibitors. Entrapped peroxidase was significantly more stable as compared to surface immobilized form of enzyme. The pH and temperature-optima for both immobilized preparations were the same as for soluble bitter gourd peroxidase. Entrapped crosslinked concanavalin A–bitter gourd peroxidase showed 75% of the initial activity while the surface immobilized and crosslinked bitter gourd peroxidase retained 69% of the original activity after its seventh repeated use.     

Immobilized laccase for decolourization of Reactive Black 5 dyeing effluent

Reactive Black 5 industrial dyeing effluent was decolourized by free and immobilized laccase. The stability of the enzyme (194 h free and 79 h immobilized) depended on the dyeing liquor composition and the chemical structure of the dye. In the decolourization experiments with immobilized laccase, two phenomenons were observed – decolourization due to adsorption on the support (79%) and dye degradation due to the enzyme action (4%). Dyeing in the enzymatically recycled effluent provided consistency of the colour with both bright and dark dyes.     

Immobilization of Rhizopus oryzae lipase on magnetic Fe3O4-chitosan beads and its potential in phenolic acids ester synthesis

A novel and simple method was developed for the preparation of magnetic Fe₃O₄ nanoparticles by chemical co-precipitation method and subsequent coating with 3-aminopropyltrimethoxysilane (APTMS) through silanization process. Magnetic Fe₃O₄-chitosan particles were prepared by the suspension cross-linking and covalent technique to be used in the application of magnetic carrier technology. The synthesized immobilization supports were characterized by scanning electron microscopy (SEM), thermogravimetric analysis (TGA) and X-ray diffraction (XRD). Using glutaraldehyde as the coupling agent, the lipase from R. oryzae was successfully immobilized onto the functionalized magnetic Fe₃O₄-chitosan beads. The results showed that 86.60% of R. oryzae lipase was bound on the synthesized immobilization support. This immobilized lipase was successfully used for the esterification of phenolic acid which resulted in esterification of phenolic acid in isooctane solvent reaction system for 8 consecutive cycles (totally 384 h), 72.6% of its initial activity was retained, indicating a high stability in pharmaceutical and industrial applications.     

Preparation of immobilized/stabilized biocatalysts of β-glucosidases from different sources: Importance of the support active groups and the immobilization protocol

β-Glucosidases from two different commercial preparations, Pectinex Ultra SP-L and Celluclast® 1.5L, were immobilized on divinylsulfone (DVS) supports at pH 5.0, 7.0, 9.0, and 10. In addition, the biocatalysts were also immobilized in agarose beads activated by glyoxyl, and epoxide as reagent groups. The best immobilization results were observed using higher pH values on DVS-agarose, and for Celluclast® 1.5L, good results were also obtained using the glyoxil-agarose immobilization. The biocatalyst obtained using Pectinex Ultra SP-L showed the highest thermal stability, at 65°C, and an operational stability of 67% of activity after 10 reuses cycles when immobilized on DVS-agarose immobilized at pH 10 and blocked with ethylenediamine. The β-glucosidase from Celluclast® 1.5L produced best results when immobilized on DVS-agarose immobilized at pH 9 and blocked with glycine, reaching 7.76-fold higher thermal stability compared to its free form and maintaining 76% of its activity after 10 successive cycles. The new biocatalysts obtained by these protocols showed reduction of glucose inhibition of enzymes, demonstrating the influence of immobilization protocols, pH, and blocking agent.     

An enzymatic method for removal of phenol from industrial effluent

Phenols in an aqueous solution were removed after treatment with peroxidase in the presence of hydrogen peroxide. Phenols occur in wastewater of a number of industries, such as high temperature coal conversion, petroleum refining, resin and plastic, wood and dye industries, etc. It can be toxic when present at elevated levels and is known to be carcinogeneous. Thus, removal of such compound from these industrial effluents is of great importance. An enzymatic method for removal of phenols from industrial wastewater, using turnip peroxidase, has been developed. Phenol-containing industrial wastewater was treated with immobilized turnip peroxidase in the presence of hydrogen peroxide. In the reaction, a number of phenols are oxidized to form the corresponding free radicals in the presence of hydrogen peroxide as an oxidant. Free radicals polymerize to form substances that are less soluble in water than the original substances. The precipitates were removed by conventional methods and residual phenol was estimated. The present report describes the immobilization of turnip peroxidase on silica via covalent coupling, and its utility in phenol removal. A comparative study was also carried out with other immobilization techniques, viz., calcium alginate entrapment, polyacrylamide gel entrapment, etc. Peroxidase, covalently bound to silica, showed 95% removal of phenol, whereas naphthol was removed up to 99%.     

煤渣-草炭基质垂直流人工湿地系统对城市污水的净化效果

垂直流人工湿地系统不但具有较高的水力负荷率(54—64cm.^-1),而且对有机物和N、P都具有较高的去除效果．其对化粪池出水中的COD、BOD5、NIA4^+-N和总P的去除率分别为76％--87％,88％--92％,75％--85％和77％--91％．处理出水中COD、BOD5、NH4^+-N和总P的平均浓度分别小于60、20、25和2．0mg.L^-1.植物种植试验结果表明,种植风车草可提高氨氮、总N和总P的去除率,分别为2％--3％、4％--6％、10％--14％．