Design and characterization of a prototype enzyme microreactor: Quantification of immobilized transketolase kinetics

In this work, we describe the design of an immobilized enzyme microreactor (IEMR) for use in transketolase (TK) bioconversion process characterization. The prototype microreactor is based on a 200‐μm ID fused silica capillary for quantitative kinetic analysis. The concept is based on the reversible immobilization of His₆‐tagged enzymes via Ni‐NTA linkage to surface derivatized silica. For the initial microreactor design, the mode of operation is a stop‐flow analysis which promotes higher degrees of conversion. Kinetics for the immobilized TK‐catalysed synthesis of L ‐erythrulose from substrates glycolaldehyde (GA) and hydroxypyruvate (HPA) were evaluated based on a Michaelis–Menten model. Results show that the TK kinetic parameters in the IEMR (V_max(app) = 0.1 ± 0.02 mmol min^–1, K_m(app) = 26 ± 4 mM) are comparable with those measured in free solution. Furthermore, the k_cat for the microreactor of 4.1 × 10⁵ s^?1 was close to the value for the bioconversion in free solution. This is attributed to the controlled orientation and monolayer surface coverage of the His₆‐immobilized TK. Furthermore, we show quantitative elution of the immobilized TK and the regeneration and reuse of the derivatized capillary over five cycles. The ability to quantify kinetic parameters of engineered enzymes at this scale has benefits for the rapid and parallel evaluation of evolved enzyme libraries for synthetic biology applications and for the generation of kinetic models to aid bioconversion process design and bioreactor selection as a more efficient alternative to previously established microwell‐based systems for TK bioprocess characterization. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010     

Production of Ricinoleic Acid from Castor Oil by Immobilised Lipases

Abstract

Porcine pancreatic lipase (PPL), Candida rugosa lipase (CRL), and Castor bean lipase (CBL) were immobilized on celite by deposition from aqueous solution by the addition of hexane. Lipolytic performance of free and immobilized lipases were compared and optimizations of lipolytic enzymatic reactions conditions were performed by free and immobilized derivatives using olive oil as substrate. Afterwards, the influence on lipolysis of castor oil of free lipases and immobilized lipase derivatives have been studied in the case of production of ricinoleic acid. All of the lipases performances were compared and enzyme derivative was selected to be very effective on the production of ricinoleic acid by lipolysis reaction. Various reaction parameters affecting the production of ricinoleic acid were investigated with selected the enzyme derivative.

The maximum ricinoleic acid yield was observed at pH 7–8, 50°C, for 3 hours of reaction period with immobilized 1,3-specific PPL on celite. The kinetic constants K_m and V_max were calculated as 1.6 × 10^?4 mM and 22.2 mM from a Lineweaver–Burk plot with the same enzyme derivative. To investigate the operational stability of the lipase, the three step lipolysis process was repeated by transferring the immobilized lipase to a substrate mixture. As a result, the percentange of conversion after usage decreased markedly.     

Reversible immobilization of cephalosporin C acylase on epoxy supports coated with polyethyleneimine

In this study, a recombinant cephalosporin C acylase (CCA) was covalently or physically immobilized on an epoxy-activated support LX1000-EPC4 (EP) or its derivatives, EP-polyethyleneimine (EP-PEI) and EP-ethylenediamine (EP-EDA) with cationic groups on the surface. Zeta potential was used as a tool for activated carrier analysis and immobilization analysis. The EP-PEI (the cationic polymer PEI grafted support) showed higher zeta potential than EP-EDA (the small diamine EDA modified support) and EP support. Among these three supports, immobilization of CCA on EP-PEI had the highest specific activity according to the range of enzyme loadings. Michaelis constant K_m values of EP-PEI-CCA and EP-EDA-CCA were 22?mM and 30?mM, respectively, which were lower than that of the free enzyme (43?mM), suggesting that the support’s zeta potential is related to the affinity of the enzyme for the substrate. The enzyme immobilized on EP-PEI showed a much higher thermal stability (stabilization factor of 32-fold compared with the free enzyme) than that on the EP-EDA (stabilization factor of 5.5-fold) and EP supports (stabilization factor of 1.7-fold). The adsorption of CCA on EP-PEI support was very strong and reversible. The CCA could be thoroughly desorbed using a high concentration of NaCl (e.g., 2 M) at low pH value (pH 3.0). The regenerated EP-PEI support could then be reused for enzyme immobilization.     

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

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

Covalent immobilization of acetylcholinesterase on a novel polyacrylic acid‐based nanofiber membrane

In this study, polyacrylic acid‐based nanofiber (NF) membrane was prepared via electrospinning method. Acetylcholinesterase (AChE) from Electrophorus electricus was covalently immobilized onto polyacrylic acid‐based NF membrane by demonstrating efficient enzyme immobilization, and immobilization capacity of polymer membranes was found to be 0.4 mg/g. The novel NF membrane was synthesized via thermally activated surface reconstruction, and activation with carbonyldiimidazole upon electrospinning. The morphology of the polyacrylic acid‐based membrane was investigated by scanning electron microscopy, Fourier Transform Infrared Spectroscopy, and thermogravimetric analysis. The effect of temperature and pH on enzyme activity was investigated and maxima activities for free and immobilized enzyme were observed at 30 and 35°C, and pH 7.4 and 8.0, respectively. The effect of 1 mM Mn²⁺, Ni²⁺, Cu²⁺, Zn²⁺, Mg²⁺, Ca²⁺ ions on the stability of the immobilized AChE was also investigated. According to the Michaelis–Menten plot, AChE possessed a lower affinity to acetylthiocholine iodide after immobilization, and the Michaelis–Menten constant of immobilized and free AChE were found to be 0.5008 and 0.4733 mM, respectively. The immobilized AChE demonstrated satisfactory reusability, and even after 10 consecutive activity assay runs, AChE maintained ca. 87% of its initial activity. Free enzyme lost its activity completely within 60 days, while the immobilized enzyme retained approximately 70% of the initial activity under the same storage time. The favorable reusability of immobilized AChE enables the support to be employable to develop the AChE‐based biosensors.     

Immobilization and characterisation of a lipase from a new source, Bacillus sp. ITP-001

A new source of lipase from Bacillus sp. ITP-001 was immobilized by physical adsorption on the polymer poly(3-hydroxybutyrate-co-hydroxyvalerate) (PHBV) in aqueous solution. The support and immobilized lipase were characterised, compared to the lyophilised lipase, with regard to the specific surface area, adsorption–desorption isotherms, pore volume (Vp) and size (dp) by nitrogen adsorption, differential scanning calorimetry, thermogravimetric analysis, chemical composition analysis, Fourier transform infrared spectroscopy and biochemical properties. The immobilized enzyme displayed a shift in optimum pH towards the acidic side with an optimum at pH 4.0, whereas the optimum pH for the free enzyme was at pH 7.0; the optimum temperature of activity was 80 and 37 °C for the free and immobilized enzyme, respectively. The inactivation rate constant for the immobilized enzyme at 37 °C was 0.0038 h^?1 and the half-life was 182.41 h. The kinetic parameters obtained for the immobilized enzyme gave a Michaelis–Menten constant (K _m) of 49.10 mM and a maximum reaction velocity (V _max) of 205.03 U/g. Furthermore, the reuse of the lipase immobilized by adsorption allowed us to observe that it could be reused for 10 successive cycles, duration of each cycle (1 h), maintaining 33 % of the initial activity.     

Competitive substrate inhibition of amyloglucosidase from Rhizopus sp. by vanillin and curcumin

Kinetic studies of two glucosylation reactions catalyzed by an amyloglucosidase from Rhizopus sp. leading to the synthesis of vanillin-α/β-D-glucoside from D-glucose and vanillin and curcumin-bis-α-D-glucoside from D-glucose and curcumin were investigated in detail. Initial reaction rates were determined from kinetic runs involving different concentrations of D-glucose and vanillin (5?mM to 0.1?M) or D-glucose and curcumin (5?mM to 0.1?M). Graphical double reciprocal plots showed that the kinetics of the two enzyme catalyzed reactions exhibited Ping-Pong Bi-Bi mechanism where competitive substrate inhibition by vanillin/curcumin led to dead-end amyloglucosidase–vanillin/curcumin complexes at higher concentrations of vanillin/curcumin. An attempt to obtain the best fit of this kinetic model through computer simulation yielded in good approximation, the values of four important kinetic parameters, vanillin-α/β-D-glucoside: k_cat=35.0±3.2 10^?5M?h^?1·mg, K_i=10.5±1.1?mM, K_mD-glucose=60.0±6.2?mM, K_mvanillin=50.0±4.8?mM; curcumin-bis-α-D-glucoside: k_cat=6.07±0.58 10^?5M?h^?1·mg, K_i=3.0±0.28?mM, K_mD-glucose=10.0±0.9?mM, K_mcurcumin=4.6±0.5?mM.     

Characterization of cross‐linked immobilized arylesterase from Gluconobacter oxydans 621H with activity toward cephalosporin C and 7‐aminocephalosporanic acid

Cross‐linked enzyme aggregates (CLEAs) were prepared from several precipitant agents using glutaraldehyde as a cross‐linking agent with and without BSA, finally choosing a 40% saturation of ammonium sulfate and 25 mM of glutaraldehyde. The CLEAs obtained under optimum conditions were biochemically characterized. The immobilized enzyme showed higher thermal activity and a broader range of pH and organic solvent tolerance than the free enzyme. Arylesterase from Gluconobacter oxydans showed activity toward cephalosporin C and 7‐aminocephalosporanic acid. The CLEAs had a Kcat/K_M of 0.9 M^?1/S^?1 for 7‐ACA (7‐aminocephalosporanic acid) and 0.1 M^?1/S^?1 for CPC (cephalosporin c), whereas free enzyme did not show a typical Michaelis–Menten kinetics. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 32:36–42, 2016     

Enhanced activity and stability of <Emphasis Type="SmallCaps">l</Emphasis>-arabinose isomerase by immobilization on aminopropyl glass

Immobilization of Bacillus licheniformis l-arabinose isomerase (BLAI) on aminopropyl glass modified with glutaraldehyde (4 mg protein g support⁻¹) was found to enhance the enzyme activity. The immobilization yield of BLAI was proportional to the quantity of amino groups on the surface of support. Reducing particle size increased the adsorption capacity (q _m) and affinity (k _a). The pH and temperature for immobilization were optimized to be pH 7.1 and 33°C using response surface methodology (RSM). The immobilized enzyme was characterized and compared to the free enzyme. There is no change in optimal pH and temperature before and after immobilization. However, the immobilized BLAI enzyme achieved 145% of the activity of the free enzyme. Correspondingly, the catalytic efficiency (k _cat/K _m) was improved 1.47-fold after immobilization compared to the free enzyme. The thermal stability was improved 138-fold (t _1/2 increased from 2 to 275 h) at 50°C following immobilization.     

Immobilization of Bacillus licheniformis 5A1 milk-clotting enzyme and characterization of its enzyme properties

Milk-clotting enzyme from Bacillus licheniformis 5A1 was immobilized on Amberlite IR-120 by ionic binding. Almost all the enzyme activity was retained on the support. The immobilized milk-clotting enzyme was repeatedly used to produce cheese in a batch reactor. The production of cheese was repeated 5 times with no loss of activity. The specific activity calculated on a bound-protein basis was slightly higher than that of free enzyme. The free and immobilized enzyme were highly tolerant to repeated freezing and thawing. The optimum temperature for milk-clotting activity was 70 °C with the free enzyme whereas, it was ranged from 70 to 80 °C with the immobilized milk-clotting enzyme. The activation energy (E _A) of the immobilized milk-clotting enzyme was lower than the free enzyme (E _A = 1.59 and 1.99 Kcal mol⁻¹ respectively). The immobilized milk-clotting enzyme exhibited great thermal stability. The milk-clotting optimum pH was 7.0 for both free and immobilized enzyme. The Michaelis constant K _m of the immobilized milk-clotting enzyme was slightly lower than the free enzyme.     

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

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

Pseudomonas fluorescens lipase immobilization on polysiloxane–polyvinyl alcohol composite chemically modified with epichlorohydrin

The technique based on sol–gel approach was used to generate silica matrices derivatives by hydrolysis of silane compounds. The present work evaluates a hybrid matrix obtained with tetraethoxysilane (TEOS) and polyvinyl alcohol (PVA) on the immobilization yield of lipase from Pseudomonas fluorescens. The resulting polysiloxane–polyvinyl alcohol (POS–PVA) matrix combines the property of PVA as a suitable polymer to retain proteins with an excellent optical, thermal and chemical stability of the host silicon oxide matrix. Aiming to render adequate functional groups to the covalent binding with the enzyme the POS–PVA matrix was chemically modified using epichlorohydrin. The results were compared with immobilized derivative on POS–PVA activated with glutaraldehyde. Immobilization yield based on the recovered lipase activity depended on the activating agent and the highest efficiency (32%) was attained when lipase was immobilized on POS–PVA activated with epichlorohydrin, which, probably, provided more linkage points for the covalent bind of the enzyme on the support. This was confirmed by determining the morphological properties using different techniques as X-ray diffraction and scanning electron microscopy (SEM). Comparative studies were carried out to attain optimal activities for free lipase and immobilized systems. For this purpose, a central composite experimental design with different combinations of pH and temperature was performed. Enzymatic hydrolysis with the immobilized enzyme in the framework of the Michaelis–Menten mechanism was also reported. Under optimum conditions, the immobilized derivative on POS–PVA activated with epichlorohydrin showed to have more affinity for the substrate in the hydrolysis of olive oil, with a Michaelis–Menten constant value (K_m) of 293 mM, compared to the value of 401 mM obtained for the immobilized lipase on support activated with glutaraldehyde. Data generated by DSC showed that both immobilized derivatives have similar thermal stabilities.     

Aryl acylamidase activity of human serum albumin with o-nitrotrifluoroacetanilide as the substrate

Albumin is generally regarded as an inert protein with no enzyme activity. However, albumin has esterase activity as well as aryl acylamidase activity. A new acetanilide substrate, o-nitrotrifluoroacetanilide (o-NTFNAC), which is more reactive than the classical o-nitroacetanilide, made it possible to determine the catalytic parameters for hydrolysis by fatty-acid free human serum albumin. Owing to the low enzymatic activity of albumin, kinetic studies were performed at high albumin concentration (0.075 mM). The albumin behavior with this substrate was Michaelis-Menten like. Kinetic analysis was performed according to the formalism used for catalysis at high enzyme concentration. This approach provided values for the turnover and dissociation constant of the albumin-substrate complex: k_cat = 0.13 ± 0.02 min ? ¹ and K_s = 0.67 ± 0.04 mM. MALDI-TOF experiments showed that unlike the ester substrate p-nitrophenyl acetate, o-NTFNAC does not form a stable adduct (acetylated enzyme). Kinetic analysis and MALDI-TOF experiments demonstrated that hydrolysis of o-NTFNAC by albumin is fully rate-limited by the acylation step (k_cat = k₂). Though the aryl acylamidase activity of albumin is low (k_cat/K_s = 195 M^{? 1}min^{? 1}), because of its high concentration in human plasma (0.6–1 mM), albumin may participate in hydrolysis of aryl acylamides through second-order kinetics. This suggests that albumin may have a role in the metabolism of endogenous and exogenous aromatic amides, including drugs and xenobiotics.     

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.     

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.     

Catalytic properties of the immobilized Aspergillus tamarii xylanase

Xylanase from Aspergillus tamarii was covalently immobilized on Duolite A147 pretreated with the bifunctional agent glutaraldehyde. The bound enzyme retained 54.2% of the original specific activity exhibited by the free enzyme (120 U/mg protein). Compared to the free enzyme, the immobilized enzyme exhibited lower optimum pH, higher optimum reaction temperature, lower energy of activation, higher K_m (Michaelis constant), lower V_max (maximal reaction rate). The half-life for the free enzyme was 186.0, 93.0, and 50.0 min for 40, 50, and 60°C, respectively, whereas the immobilized form at the same temperatures had half-life of 320, 136, and 65 min. The deactivation rate constant at 60°C for the immobilized enzyme is about 6.0 × 10⁻³, which is lower than that of the free enzyme (7.77 × 10⁻³ min). The energy of thermal deactivation was 15.22 and 20.72 kcal/mol, respectively for the free and immobilized enzyme, confirming stabilization by immobilization. An external mass transfer resistance was identified with the immobilization carrier (Duolite A147). The effect of some metal ions on the activity of the free and immobilized xylanase has been investigated. The immobilized enzyme retained about 73.0% of the initial catalytic activity even after being used 8 cycles.     

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

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

Fibrous polymer-grafted chitosan/clay composite beads as a carrier for immobilization of papain and its usability for mercury elimination

Papain, which is an industrially important enzyme, has been immobilized on fibrous polymer-modified composite beads, namely poly(methacrylic acid)-grafted chitosan/clay. Characterization studies have been done using FTIR and SEM analysis. Operating parameters such as pH and initial concentration of papain have been varied to obtain the finest papain immobilized polymer-modified composite beads. The immobilization capacity of composite beads has been determined as 34.47 ± 1.18 (n = 3) mg/g. The proteolytic activity of immobilized papain was operated using bovine serum albumin (BSA) and maximum velocity (V _max) and Michaelis–Menten constant (K_m) values of the free and immobilized enzymes were determined using Lineweaver–Burk and Eadie–Hofstee equations. Usability of papain immobilized polymer-modified composite beads as adsorbents for the elimination of mercury was investigated. The maximum removal capacity of PIPMC beads has been found to be 4.88 ± 0.21 mg Hg/g when the initial metal concentration and weight of polymer-modified composite beads were 50 mg/L and 0.04 g at pH 7, respectively. Mercury removal performance of the papain immobilized polymer-modified composite beads was investigated in conjunction with Cu (II), Zn (II) and Cd (II) ions. The mercury adsorption capacity of papain immobilized polymer-modified composite beads was a slight reduction from 1.15 to 0.89 mg/g in presence of multiple metal salts.     

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.     

α-<Emphasis Type="SmallCaps">l</Emphasis>-Rhamnosidase of <Emphasis Type="Italic">Aspergillus terreus</Emphasis> immobilized on ferromagnetic supports

α-l-Rhamnosidase from Aspergillus terreus was covalently immobilized on the following ferromagnetic supports: polyethylene terephthalate (Dacron-hydrazide), polysiloxane/polyvinyl alcohol (POS/PVA), and chitosan. The powdered supports were magnetized by thermal coprecipitation method using ferric and ferrous chlorides, and the immobilization was carried out via glutaraldehyde. The activity of the Dacron-hydrazide (0.53 nkat/μg of protein) and POS/PVA (0.59 nkat/μg of protein) immobilized enzyme was significantly higher than that found for the chitosan derivative (0.06 nkat/μg of protein). The activity–pH and activity–temperature profiles for all immobilized enzymes did not show difference compared to the free enzyme, except the chitosan derivative that presented higher maximum temperature at 65 °C. The Dacron-hydrazide derivative thermal stability showed a similar behavior of the free enzyme in the temperature range of 40–70 °C. The POS/PVA and chitosan derivatives were stable up to 60 °C, but were completely inactivated at 70 °C. The activity of the preparations did not appreciably decrease after ten successive reuses. Apparent K _m of α-l-rhamnosidase immobilized on magnetized Dacron-hydrazide (1.05 ± 0.22 mM), POS/PVA (0.57 ± 0.09 mM), and chitosan (1.78 ± 0.24 mM) were higher than that estimated for the soluble enzyme (0.30 ± 0.03 mM). The Dacron-hydrazide enzyme derivative showed better performance than the free enzyme to hydrolyze 0.3% narigin (91% and 73% after 1 h, respectively) and synthesize rhamnosides (0.116 and 0.014 mg narirutin after 1 h, respectively).