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PubMed2006

Properties of immobilized pepsin on Modified PMMA microspheres.

In this work we use micro-size poly(methyl methacrylate)/acrylaldehyde microspheres as a support for pepsin immobilization. The aldehyde groups on the microspheres offer a very simple, mild and firm combination for enzyme immobilization. The amount of enzyme we can bind to this support reaches 82 mg/g, which is much higher than for other supports (mostly less than 10 mg/g). Compared to free enzyme, the Km of immobilized enzyme is increased, whereas the Vmax is decreased. Further, the Vmax/Km value for immobilized pepsin is about 50% of the value for free enzyme. This is better than values reported previously, generally lower than 35%. The optimum temperature shifts from 43 degrees C for free pepsin to 47 degrees C. However, the optimum pH does not change between free and immobilized enzyme. This improved resistance of the immobilized enzyme towards changes in temperature and pH also shows that the aldehyde modified poly(methyl methacrylate)/acrylaldehyde microspheres can be a valuable support for pepsin immobilization.

Coated Materials, Biocompatible↗

PubMed2006

Production of galacto-oligosaccharides by immobilized recombinant beta-galactosidase from Aspergillus candidus.

The preparation of galacto-oligosaccharides (GOSs) was studied using the immobilized recombinant beta-galactosidase from Aspergillus candidus CGMCC3.2919. The optimal pH and temperature for the immobilized enzyme were observed at pH 6.5 and 40 degrees C, respectively. Increasing the initial lactose concentration increased the yield of GOSs. The dilution rate was found to be a key factor during the continuous production of GOSs. The maximum productivity, 87 g/L.h was reached when 400 g/L lactose was fed at dilution rate of 0.8/h. The maximum GOS yield reached 37% at dilution rate of 0.5/h. Continuous operation was maintained for 20 days in a packed-bed reactor without apparent decrease in GOS production. The average yield of GOSs was 32%, corresponding to the average productivity of 64 g/L.h, which implied that the immobilized recombinant beta-galactosidase has potential application for GOS production.

Aspergillus↗

PubMed2001

Haloalkane hydrolysis with an immobilized haloalkane dehalogenase.

Haloalkane dehalogenase from Rhodococcus rhodochrous was covalently immobilized onto a polyethyleneimine impregnated gamma-alumina support. The dehalogenating enzyme was found to retain greater than 40% of its original activity after immobilization, displaying an optimal loading (max. activity/supported protein) of 70 to 75 mg/g with an apparent maximum (max. protein/support) of 156 mg/g. The substrate, 1,2,3-trichloropropane, was found to favorably partition (adsorb) onto the inorganic alumina carrier (10 to 20 mg/g), thereby increasing the local reactant concentration with respect to the catalyst's environment, whereas the product, 2,3-dichloropropan-1-ol, demonstrated no affinity. Additionally, the inorganic alumina support exhibited no adverse effects because of solvent/component incompatibilities or deterioration due to pH variance (pH 7.0 to 10.5). As a result of the large surface area to volume ratio of the support matrix and the accessibility of the bound protein, the immobilized biocatalyst was not subject to internal mass transfer limitations. External diffusional restrictions could be eliminated with simple agitation (mixing speed: 50 rpm; flux: 4.22 cm/min). The pH-dependence of the immobilized dehalogenase was essentially the same as that for the native enzyme. Finally, both the thermostability and resistance toward inactivation by organic solvent were improved by more than an order of magnitude after immobilization.

Aluminum Oxide↗

PubMed2001

Enzyme microgels in packed-bed bioreactors with downstream amperometric detection using microfabricated interdigitated microsensor electrode arrays.

In this article, we describe the use of pH- responsive hydrogels as matrices for the immobilization of two enzymes, glucose oxidase (GOx) and glutamate oxidase (GlutOx). Spherical hydrogel beads were prepared by inverse suspension polymerization and the enzymes were immobilized by either physical entrapment or covalent immobilization within or on the hydrogel surface. Packed-bed bioreactors were prepared containing the bioactive hydrogels and these incorporated into flow injection (FI) systems for the quantitation of glucose and monosodium glutamate (MSG) respectively. The FI amperometric detector comprised a microfabricated interdigitated array within a thin-layer flow cell. For the FI manifold incorporating immobilized GOx, glucose response curves were found to be linear over the concentration range 1.8-280 mg dL(-1) (0.1-15.5 mM) with a detection limit of 1.4 mg dL(-1) (0.08 mM). Up to 20 samples can be manually analyzed per hour, with the hydrogel-GOx bioreactor exhibiting good within-day (0.19%) precision. The optimized FI manifold for MSG quantitation yielded a linear response range of up to 135 mg dL(-1) (8 mM) with a detection limit of 3.38 mg dL(-1) (0.2 mM) and a throughput of 30 samples h(-1). Analysis of commercially produced soup samples gave a within-day precision of 3.6%. Bioreactors containing these two physically entrapped enzymes retained > 60% of their initial activities after a storage period of up to 1 year.

Aspergillus niger↗

PubMed2001

Thiosulphate improves yield of hydrogen production from glucose by the immobilized formate hydrogenlyase system of Escherichia coli.

Escherichia coli cells with formate hydrogenlyase activity that were immobilized in agar beads produced hydrogen from glucose at the approximate yield of 0.6 mole of hydrogen per mole. Succinate or thiosulphate added to glucose increased hydrogen production two-fold. Thiosulphate did not increase the rate of hydrogen production but reduced the consumption of glucose for the same amount of hydrogen produced compared to control. Oxaloacetate and traces of pyruvate instead of succinate accumulated at the end when thiosulphate was present.

Anaerobiosis↗

PubMed2002

Direct transesterification of gases by "dry" immobilized lipase.

Several different reactor configurations, including single pass, continuous recycle, and batch reactor modes, were used to investigate the effects of temperature and water activity, or relative humidity, on lipase-catalyzed, gas-phase transesterifications. Temperature and relative humidity were controlled both inside reactors and throughout the course of the reaction to account for and optimize their effects. Results indicated that, at low relative humidity, reaction rates increased with temperature up to 60 degrees C. However, when relative humidity was increased, a similar increase in temperature resulted in the loss of nearly all enzyme activity. These results are consistent with the idea that enzymes without free water are more thermally stable. Furthermore, at constant ambient temperatures, production increased dramatically with an increase in relative humidity, confirming the idea that an increase in water activity increases catalytic activity. A mass balance performed on reactors at higher relative humidity revealed that hydrolysis (rather than transesterification) of the ester substrate could significantly decrease product yields.

Animals↗

PubMed2002

Production of lipolyzed butteroil by a calf pregastric esterase immobilized in a hollow fiber reactor: III. Effect of glycerol.

Lipolysis of butter oil in a hollow fiber reactor containing an immobilized calf pregastric esterase was studied at 40 degrees C, a pH of 6.0, and glycerol concentrations of 0, 150, and 500 g/L in the buffer solution. The concentrations of 10 fatty acid species in the lipolyzed product were determined using high-performance liquid chromatography. The rate of loss of enzyme activity and the relative selectivities of this esterase depended on the glycerol concentration. By contrast, the overall rate of release of fatty acids was not affected by the glycerol concentration. Loss of enzyme activity was modeled using first-order kinetics. The models for deactivation and reaction kinetics were fit simultaneously to the data. The model was successful in describing the rates of release of all 10 fatty acid species for a range of space times from 0 to 25 h. The parameters of the model were tested for dependence on glycerol concentration.

Animals↗

PubMed2002

Self-activating factor X derivative fused to the C-terminus of a cellulose-binding module: Production and properties.

In this work, a new derivative of FX was engineered. It comprises a cellulose-binding module (CBM) fused to the N-terminus of the truncated light chain (E2FX) of FX and a hexahistidine tag (H6) fused to the C-terminus of the heavy chain. The sequence LTR at the site of cleavage of the activation peptide from the N-terminus of the heavy chain is changed to IEGR to render the derivative self-activating. However, N-linked glycans on the CBM of the derivative blocked its binding to cellulose and those on the activation peptide slowed its activation. Therefore, the sites of N-linked glycosylation on the CBM and on the activation peptide were eliminated by mutation. The final derivative can be produced in good yield by cultured mammalian cells. It is purified easily with Ni(2+)-agarose, it is self-activating, and it can be immobilized on cellulose. When immobilized on a column of cellulose beads, the activated derivative retains approximately 80% of its initial activity after 30 days of continuous hydrolysis of a fusion protein substrate. Under these conditions of operation, the effective substrate:enzyme ratio is >10(4).

Animals↗

PubMed2002

High-activity enzyme-polyurethane coatings.

The synthesis of water-borne polyurethane coatings in the presence of diisopropylfluorophosphatase (DFPase, E.C. 3.8.2.1) enabled the irreversible attachment of the enzyme to the polymeric matrix. The distribution of immobilized DFPase as well as activity retention are homogeneous within the coating. The resulting enzyme-containing coating (ECC) film hydrolyzes diisopropylfluorophosphate (DFP) in buffered media at high rates, retaining approximately 39% intrinsic activity. Decreasing ECC hydrophilicity, via the use of a less hydrophilic polyisocyanate during polymerization, significantly enhanced the intrinsic activity of the ECC. DFPase-ECC has biphasic deactivation kinetics, where the initial rapid deactivation of DFPase-ECC leads to the formation of a hyperstable and active form of enzyme.

Coated Materials, Biocompatible↗

PubMed2002

Enzyme recovery during gas/liquid two-phase flow microfiltration of enzyme/yeast mixtures.

The effect of a gas/liquid two-phase flow on the recovery of an enzyme was evaluated and compared with standard crossflow operation when confronted with the microfiltration of a high-fouling yeast suspension. Ceramic tubular and flat sheet membranes were used. At constant feed concentration (permeate recycling) and transmembrane pressure, the results obtained with the tubular membrane were dependent on the two-phase flow pattern. In comparison with single-phase flow performances at the same liquid velocity, the enzyme transmission was maintained at a high level with a bubble flow pattern but it decreased by 70% with a slug flow, whatever the flow rate ratio. Identical results were obtained with flat sheet membranes: for the highest flow rate ratio, the enzyme transmission was reduced by 70% even though the permeate flux was improved by 240%. During diafiltration experiments with the tubular membrane, it was found that a bubble flow pattern led to a 13% higher enzyme recovery compared to single-phase flow conditions, whereas with a slug flow the enzyme recovery was strongly reduced. With bubble flow conditions, energy consumption was minimal, confirming that this flow pattern was the most suitable for enzyme recovery.

Adsorption↗

PubMed2002

Structure-function relationships in immobilized chymotrypsin catalysis.

Specific activities and the amounts of active immobilized enzyme were determined for several different preparations of alpha-chymotrypsin immobilized on CNBr-activated Sepharose 4B. Electron paramagnetic resonance (EPR) spectroscopy of free and immobilized enzyme with a spin label coupled to the active site was used to probe the effects of different immobilization conditions on the immobilized enzyme active site configuration. Specific activity of active enzyme decreased and rotational correlation time of the spin label increased with increasing immobilized enzyme loading. Enzyme immobilized using an intermediate six-carbon spacer arm exhibited greater specific activity and spin label mobility than directly coupled enzyme. The observed activity changes due to immobilization were completely consistent with corresponding active site structure alterations revealed by EPR spectroscopy.

Animals↗

PubMed2003

Preparation and characterization of reactive and stable glucose oxidase-containing liposomes modulated with detergent.

Glucose oxidase-containing liposomes (GOL) as well as detergent-modulated glucose oxidase-containing liposomes were prepared and characterized, focusing not only on the reactivity of the liposomes upon external addition of glucose but also on the leakage of the entrapped glucose oxidase (GO) from the liposomes with the aim of developing a reactive and stable liposomal GO system. The membranes of the GOL prepared were composed of 1-palmitoyl-2-oleoyl-sn-glycero-3-phosphocholine (POPC) and modulated with either Triton X-100 or cholate. In the absence of added detergent, no GO leakage from the GOL was observed while its enzymatic activity was very low (low glucose permeability). As detergent-modulated liposomes, mixed POPC/Triton X-100 and mixed POPC/cholate liposomes (abbreviated as TL and CL, respectively) were prepared at different effective detergent/POPC molar ratios (R(e)) ranging from R(e) = 0 to R(e) = R(e) (sat) (R(e) (sat) is the critical value of R(e) at which the liposome membrane is saturated with detergent). The reactivity of GO-loaded TL (abbreviated as GOTL) or GO-loaded CL (GOCL) increased drastically with increase in the respective detergent content in the liposomes. In the case of GOTL, at R(e) (sat) = 0.40, a high reactivity was measured with a simultaneous high extent of GO leakage, suggesting that the observed enzymatic reaction was catalyzed mainly by leaked GO, caused by the interaction of Triton X-100 with the POPC membrane. On the other hand, GOCL prepared at R(e) (sat) = 0.43 showed relatively high reactivity with only a small extent of GO leakage, suggesting that most of the enzyme reaction was limited by the glucose permeation across the bilayers of GOCL. The GO leakage from GOCL was found to occur mostly during the rearrangement of the liposomal membrane during the preparation of the GOCL (mixing the GOL and cholate). Fluorescence polarization measurements of membrane-associated DPH (1,6-diphenyl-1,3,5-hexatriene) indicated that CL prepared by modifying POPC with cholate did not lead to a drastic change in membrane fluidity, indicating that the interacting cholate molecules did not penetrate deeply into the POPC bilayers. In summary, it was clearly shown that the membrane permeability of GOL can be quite simply modulated by mixing it with a certain amount of cholate to form highly reactive and stable GOCL with minimal enzyme leakage.

Cholates↗

PubMed2003

Surface functionalization of porous polypropylene membranes with polyaniline for protein immobilization.

Commercial porous polypropylene membranes were chemically modified with polyaniline (PANI) using ammonium persulfate as the oxidizer. The influence of polymerization conditions on the membrane properties was studied by adsorption analysis and membrane permeability. The PANI-coated polypropylene (PANI/PP) membranes possessed high affinity toward the proteins, which can be immobilized onto the membrane surface through physical adsorption or covalent immobilization. The quantity of immobilized horseradish peroxidase (HRP) and its activity depended on the quantity and quality (oxidation level) of PANI. The storage conditions for PANI/PP membranes containing immobilized HRP were studied. HRP immobilized on the PANI/PP membrane was shown to retain 70% of its activity after 3-month storage at +5 degrees C, suggesting that this material can be used for practical application, such as in bioreactors as enzyme membranes.

Adsorption↗

PubMed2003

Improvement of the yield of physiologically active oligosaccharides in continuous hydrolysis of chitosan using immobilized chitosanases.

The continuous production of chitosan oligosaccharides using a packed-bed enzyme reactor was investigated as to the effects of the operation conditions on the yield of pentamers and hexamers of chitosan oligosaccharides. A column reactor packed with immobilized chitosanases prepared by the multipoint attachment method was used for continuous hydrolysis of chitosan. In this reactor, the decrease of the yield of the target intermediate oligosaccharides due to axial mixing was negligible. The surface enzyme density of the support and flow rate of the substrate solution significantly affected the maximum yield of pentamers and hexamers. These effects were summarized as a correlation with the Damköhler number (Da), defined as the ratio of the maximum reaction rate to the maximum mass transfer rate. The optimum condition was determined based on Da. Under the optimized condition (Da = 0.12), pentamers and hexamers could be produced continuously for a month with a yield of over 35% (7 kg/m(3) in concentration).

Bioreactors↗

PubMed2004

Effect of immobilization support, water activity, and enzyme ionization state on cutinase activity and enantioselectivity in organic media.

We studied the reaction between vinyl butyrate and 2-phenyl-1-propanol in acetonitrile catalyzed by Fusarium solani pisi cutinase immobilized on zeolites NaA and NaY and on Accurel PA-6. The choice of 2-phenyl-1-propanol was based on modeling studies that suggested moderate cutinase enantioselectivity towards this substrate. With all the supports, initial rates of transesterification were higher at a water activity (a(w)) of 0.2 than at a(w) = 0.7, and the reverse was true for initial rates of hydrolysis. By providing acid-base control in the medium through the use of solid-state buffers that control the parameter pH-pNa, which we monitored using an organo-soluble chromoionophoric indicator, we were able, in some cases, to completely eliminate dissolved butyric acid. However, none of the buffers used were able to improve the rates of transesterification relative to the blanks (no added buffer) when the enzyme was immobilized at an optimum pH of 8.5. When the enzyme was immobilized at pH 5 and exhibited only marginal activity, however, even a relatively acidic buffer with a pK(a) of 4.3 was able to restore catalytic activity to about 20% of that displayed for a pH of immobilization of 8.5, at otherwise identical conditions. As a(w) was increased from 0.2 to 0.7, rates of transesterification first increased slightly and then decreased. Rates of hydrolysis showed a steady increase in that a(w) range, and so did total initial reaction rates. The presence or absence of the buffers did not impact on the competition between transesterification and hydrolysis, regardless of whether the butyric acid formed remained as such in the reaction medium or was eliminated from the microenvironment of the enzyme through conversion into an insoluble salt. Cutinase enantioselectivity towards 2-phenyl-1-propanol was indeed low and was not affected by differences in immobilization support, enzyme protonation state, or a(w).

Acetonitriles↗

PubMed2003

Catalytic behaviors of enzymes attached to nanoparticles: the effect of particle mobility.

Nanoparticles provide an ideal remedy to the usually contradictory issues encountered in the optimization of immobilized enzymes: minimum diffusional limitation, maximum surface area per unit mass, and high effective enzyme loading. In addition to the promising performance features, the unique solution behaviors of the nanoparticles also point to a transitional region between the heterogeneous (with immobilized enzymes) and homogeneous (with soluble free enzymes) catalysis. The particle mobility, which is related to particle size and solution viscosity through Stokes-Einstein equation, may impact the reaction kinetics according to the collision theory. The mobility-activity relationship was examined through experimental studies and theoretical modeling in the present work. Polystyrene particles with diameters ranging from 110-1000 nm were prepared. A model enzyme, alpha-chymotrypsin, was covalently attached to the nanoparticles up to 6.6 wt%. The collision theory model was found feasible in correlating the catalytic activities of particles to particle size and solution viscosity. Changes in the size of particles and the viscosity of reaction media, which all affect the mobility of the enzyme catalyst, evidently altered the intrinsic activity of the particle-attached enzyme. Compared to K(M), k(cat) appeared to be less sensitive to particle size and viscosity.

Calcium Carbonate↗

PubMed2001

Factors affecting alpha,-1,2 glucooligosaccharide synthesis by Leuconostoc mesenteroides NRRL B-1299 dextransucrase.

The optimization of alpha-1,2 glucooligosaccharide (GOS) synthesis from maltose and sucrose by Leuconostoc mesenteroides NRRL B-1299 dextransucrase was achieved using experimental design and consecutive analysis of the key parameters. An increase of the pH of the reaction from 5.4 to 6.7 and of the temperature from 25 to 40 degrees C significantly favored alpha-1,2 GOS synthesis, thanks to a significant decrease of the side reactions, i.e., dextran and leucrose synthesis. These positive effects were not sufficient to compensate for the decrease of enzyme stability caused by the use of high pH and temperature. However, the critical parameters were the sucrose to maltose concentration ratio (S/M) and the total sugar concentration (TSC). Alpha1,2 GOS synthesis was favored at high S/M ratios. But using these conditions also led to an increase of side reactions which could be modulated by choosing the appropriate TSC. Finally, with S/M = 4 and TSC = 45% w/v, dextran and leucrose productions were limited and the final alpha-1,2 GOS yield reached 56.7%, the total GOS yield being 88%.

Chromatography, High Pressure Liquid↗

PubMed2001

Sol-gel immobilization of serine proteases for application in organic solvents.

The serine proteases alpha-chymotrypsin, trypsin, and subtilisin Carlsberg were immobilized in a sol-gel matrix and the effects on the enzyme activity in organic media are evaluated. The percentage of immobilized enzyme is 90% in the case of alpha-chymotrypsin and the resulting specific enzyme activity in the transesterification of N-acetyl-L-phenylalanine ethyl ester with 1-propanol in cyclohexane is 43 times higher than that of a nonimmobilized lyophilized alpha-chymotrypsin. The activities of trypsin and subtilisin Carlsberg are enhanced with 437 and 31 times, respectively. The effect of immobilization on the enzyme activity is highest in hydrophobic solvents.

Chromatography, Gas↗