Membrane reactor for enzymatic hydrolysis of cellobiose

A pressurized, stirred vessel attached with an ultrafiltration membrane was used as a membrane reactor, Cellobiose hydrolysis by cellobiase was carried out and theoretically analyzed in terms of steady-state conversion and flow rate through the membrane. When the flow rate exceeds a critical value, a significant fraction of the enzyme inside the reactor is localized in the concentration polarization layer where shear from stirring is high. Consequently, enzyme deactivation inside the concentration polarization layer is accelerated and the conversion decreases due to an exchange of active enzyme in bulk with deactivated enzyme in the polarization layer via convection and back diffusion. Successful operation can be obtained at flow rates lower than the critical point to avoid the polarization and thus the deactivation. It is shown that 6.5 L of 2 mg/mL of cellobiose solution is hydrolyzed to glucose with a conversion of 91% in 20 h with 1.617 mg of cellobiase enzyme, in a reactor attached with a PM 10 membrane of an effective surface area of 39.2 cm².     

Immobilised enzyme microreactor for screening of multi-step bioconversions: characterisation of a de novo transketolase-ω-transaminase pathway to synthesise chiral amino alcohols

Complex molecules are synthesised via a number of multi-step reactions in living cells. In this work, we describe the development of a continuous flow immobilized enzyme microreactor platform for use in evaluation of multi-step bioconversion pathways demonstrating a de novo transketolase/ω-transaminase-linked asymmetric amino alcohol synthesis. The prototype dual microreactor is based on the reversible attachment of His₆-tagged enzymes via Ni-NTA linkage to two surface derivatised capillaries connected in series. Kinetic parameters established for the model transketolase (TK)-catalysed conversion of lithium-hydroxypyruvate (Li-HPA) and glycolaldehyde (GA) to l-erythrulose using a continuous flow system with online monitoring of reaction output was in good agreement with kinetic parameters determined for TK in stop-flow mode. By coupling the transketolase catalysed chiral ketone forming reaction with the biocatalytic addition of an amine to the TK product using a transaminase (ω-TAm) it is possible to generate chiral amino alcohols from achiral starting compounds. We demonstrated this in a two-step configuration, where the TK reaction was followed by the ω-TAm-catalysed amination of l-erythrulose to synthesise 2-amino-1,3,4-butanetriol (ABT). Synthesis of the ABT product via the dual reaction and the on-line monitoring of each component provided a full profile of the de novo two-step bioconversion and demonstrated the utility of this microreactor system to provide in vitro multi-step pathway evaluation.     

Enzymatic synthesis of chiral amino‐alcohols by coupling transketolase and transaminase‐catalyzed reactions in a cascading continuous‐flow microreactor system

Rapid biocatalytic process development and intensification continues to be challenging with currently available methods. Chiral amino‐alcohols are of particular interest as they represent key industrial synthons for the production of complex molecules and optically pure pharmaceuticals. (2S,3R)‐2‐amino‐1,3,4‐butanetriol (ABT), a building block for the synthesis of protease inhibitors and detoxifying agents, can be synthesized from simple, non‐chiral starting materials, by coupling a transketolase‐ and a transaminase‐catalyzed reaction. However, until today, full conversion has not been shown and, typically, long reaction times are reported, making process modifications and improvement challenging. In this contribution, we present a novel microreactor‐based approach based on free enzymes, and we report for the first time full conversion of ABT in a coupled enzyme cascade for both batch and continuous‐flow systems. Using the compartmentalization of the reactions afforded by the microreactor cascade, we overcame inhibitory effects, increased the activity per unit volume, and optimized individual reaction conditions. The transketolase‐catalyzed reaction was completed in under 10 min with a volumetric activity of 3.25 U ml^?1. Following optimization of the transaminase‐catalyzed reaction, a volumetric activity of 10.8 U ml^?1 was attained which led to full conversion of the coupled reaction in 2 hr. The presented approach illustrates how continuous‐flow microreactors can be applied for the design and optimization of biocatalytic processes.

     

Enhanced transglucosylation/hydrolysis ratio of mutants of Pyrococcus furiosus beta-glucosidase: effects of donor concentration, water content, and temperature on activity and selectivity in hexanol.

The transglucosylation reaction catalyzed by wild-type beta-glucosidase CelB from hyperthermophilic Pyrococcus furiosus and active site mutants (M424K, F426Y, M424K/F426Y) was studied. The conversion of pentyl-beta-glucoside to hexyl-beta-glucoside in hexanol was used as a model transglucosylation reaction. Hydrolysis to glucose was a side reaction. The selectivity towards transglucosylation was quantified by the S value defined as follows: S = r(S) x a(W)/r(H) x a(hex) where r(S) and r(H) are the initial rates of transglucosylation and hydrolysis and a(w) and a(hex) are the thermodynamic activities of water and hexanol. The activity (rates of hydrolysis and transglucosylation) and the selectivity (S value) were measured as a function of pentyl-beta-glucoside concentration (5-240 mM), water content (1-100% v/v), and temperature (50-95 degrees C). All mutants had lower activity than the wild-type enzyme, but they had higher selectivity, which means that they provided a higher ratio of transglucosylation product to hydrolysis product. The largest increase in S-value (2.6 fold) was obtained by the F426Y mutant, which resulted in increased hexyl-beta-glucoside yield from 56% to 69%. In addition, the F426Y enzyme had higher selectivity over the wide range of temperatures tested. The activity of CelB wild-type and CelB F426Y increased as a function of water activity (a(w)), and complete activation by the water was obtained in a two-phase system with 20% water phase. In contrast to CelB wild-type, the F426Y mutant had transferase activity as low as a(w) = 0.29. Surprisingly, the S value increased with increasing water activity up to a(w) = 0.92. At still higher water content the S value decreased.     

Entrapment in E. coli improves the operational stability of recombinant beta-glycosidase CelB from Pyrococcus furiosus and facilitates biocatalyst recovery

beta-Glycosidase CelB from the hyperthermophilic archaeon Pyrococcus furiosus is a versatile biocatalyst that has been used for the hydrolysis and synthesis of beta-d-glycosidic compounds at high temperatures and in non-conventional solvents. In spite of its outstanding thermal stability, CelB is prone to inactivation in the presence of reducing sugars and through recirculation in loop enzyme reactors. Entrapment into E. coli cells was used here to improve the stability of recombinant CelB under conditions promoting strong inactivation. Glutardialdehyde-mediated protein cross-linking or rigidification of the cell membrane by adding magnesium ions was required to prevent release of CelB from within the cell into the bulk solution. In the presence of 1M glucose or when applying recirculation rates of 2.6 min(-1), the entrapped enzyme was around two-fold more stable at 80 degrees C than free CelB. The significance of the stabilisation was attenuated by the decrease in CelB initial activity which was due to cross-linking and glutardialdehyde concentration-dependent. Entrapment facilitated downstream processing of CelB and biocatalyst recovery in repeated batchwise conversions of lactose at elevated temperatures.     

Purification, Characterization, and Molecular Analysis of Thermostable Cellulases CelA and CelB from Thermotoga neapolitana

Two thermostable endocellulases, CelA and CelB, were purified from Thermotoga neapolitana. CelA (molecular mass, 29 kDa; pI 4.6) is optimally active at pH 6.0 at 95°C, while CelB (molecular mass, 30 kDa; pI 4.1) has a broader optimal pH range (pH 6.0 to 6.6) at 106°C. Both enzymes are characterized by a high level of activity (high V_max value and low apparent K_m value) with carboxymethyl cellulose; the specific activities of CelA and CelB are 1,219 and 1,536 U/mg, respectively. With p-nitrophenyl cellobioside the V_max values of CelA and CelB are 69.2 and 18.4 U/mg, respectively, while the K_m values are 0.97 and 0.3 mM, respectively. The major end products of cellulose hydrolysis, glucose and cellobiose, competitively inhibit CelA, and CelB. The K_i values for CelA are 0.44 M for glucose and 2.5 mM for cellobiose; the K_i values for CelB are 0.2 M for glucose and 1.16 mM for cellobiose. CelB preferentially cleaves larger cellooligomers, producing cellobiose as the end product; it also exhibits significant transglycosylation activity. This enzyme is highly thermostable and has half-lives of 130 min at 106°C and 26 min at 110°C. A single clone encoding the celA and celB genes was identified by screening a T. neapolitana genomic library in Escherichia coli. The celA gene encodes a 257-amino-acid protein, while celB encodes a 274-amino-acid protein. Both proteins belong to family 12 of the glycosyl hydrolases, and the two proteins are 60% similar to each other. Northern blots of T. neapolitana mRNA revealed that celA and celB are monocistronic messages, and both genes are inducible by cellobiose and are repressed by glucose.     

Improving low-temperature catalysis in the hyperthermostable Pyrococcus furiosus beta-glucosidase CelB by directed evolution

The beta-glucosidase from the hyperthermophilic archaeon Pyrococcus furiosus (CelB) is the most thermostable and thermoactive family 1 glycosylhydrolase described to date. To obtain more insight in the molecular determinants of adaptations to high temperatures and study the possibility of optimizing low-temperature activity of a hyperthermostable enzyme, we generated a library of random CelB mutants in Escherichia coli. This library was screened for increased activity on p-nitrophenyl-beta-D-glucopyranoside at room temperature. Multiple CelB variants were identified with up to 3-fold increased rates of hydrolysis of this aryl glucoside, and 10 of them were characterized in detail. Amino acid substitutions were identified in the active-site region, at subunit interfaces, at the enzyme surface, and buried in the interior of the monomers. Characterization of the mutants revealed that the increase in low-temperature activity was achieved in different ways, including altered substrate specificity and increased flexibility by an apparent overall destabilization of the enzyme. Kinetic characterization of the active-site mutants showed that in all cases the catalytic efficiency at 20 degrees C on p-nitrophenyl-beta-D-glucose, as well as on the disaccharide cellobiose, was increased up to 2-fold. In most cases, this was achieved at the expense of beta-galactosidase activity at 20 degrees C and total catalytic efficiency at 90 degrees C. Substrate specificity was found to be affected by many of the observed amino acid substitutions, of which only some are located in the vicinity of the active site. The largest effect on substrate specificity was observed with the CelB variant N415S that showed a 7.5-fold increase in the ratio of p-nitrophenyl-beta-D-glucopyranoside/p-nitrophenyl-beta-D-galactopyra noside hydrolysis. This asparagine at position 415 is predicted to interact with active-site residues that stabilize the hydroxyl group at the C4 position of the substrate, the conformation of which is equatorial in glucose-containing substrates and axial in galactose-containing substrates.     

Lipase immobilized microstructured fiber based flow-through microreactor for facile lipid transformations

A facile continuous flow-through Candida antarctica lipase B immobilized silica microstructured optical fiber (SMOF) microreactor for application in lipid transformations has been demonstrated herewith. The lipase was immobilized on the amino activated silica fiber using glutaraldehyde as a bifunctional reagent. The immobilized lipase activity in the SMOF was tested calorimetrically by determination of p-nitrophenyl butyrate hydrolysis products. The specific activity of the immobilized lipase was calculated to be 0.91 U/mg. The SMOF microreactor performance was evaluated by using it as a platform for synthesis of butyl laurate from lauric acid and n-butanol in n-hexane and n-heptane at 50 °C, with products identified by gas chromatography–mass spectrometry (GC–MS). Different substrate mole ratios were evaluated, with 1:3, lauric acid:n-butanol showing best performance. Remarkably, percentage yields of up to 99% were realized with less than ∼38 s microreactor residence time. In addition, the SMOF microreactor could be reused many times (at least 7 runs) with minimal reduction in the activity of the enzyme. The enzyme stability did not change even with storage of the microreactor in ambient conditions over one month.     

Development of an ultrahigh-temperature process for the enzymatic hydrolysis of lactose. III. Utilization of two thermostable beta-glycosidases in a continuous ultrafiltration membrane reactor and galacto-oligosaccharide formation under steady-state conditions.

Hydrolysis of lactose by hyperthermophilic beta-glycosidases from the archaea Sulfolobus solfataricus (SsbetaGly) and Pyrococcus furiosus (CelB) was carried out at 70 degrees C in a continuous stirred-tank reactor (CSTR) coupled to a 10-kDa cross-flow ultrafiltration module to recycle the enzyme. Recirculation rates of > or =1 min(-1), reaction of proteins with reducing sugars, and enzyme adsorption onto the membrane are major "operational" factors of enzyme inactivation in the CSTR. They cause the half-life times of SsbetaGly and CelB to be reduced two- and eight-fold, respectively, the average value for both enzymes now being approximately 5 to 7 days. Using lactose at initial concentrations of 45 and 170 g/L, the CSTR was operated at a constant conversion level of approximately 80% for more than 2 weeks without the occurrence of microbial contamination. The productivities for the SsbetaGly-catalyzed conversion of lactose were determined at different dilution rates and initial substrate concentrations, and exceed by a factor of < or =2 those observed with CelB under otherwise identical conditions. This difference reflects the approximately eight-fold stronger product inhibition of CelB by D-glucose. While the maximum total galacto-oligosaccharide production (90-100 mM) at 170 g/L lactose in the CSTR was not different from that in the batch reactor (CelB) or was greater by approximately 25% (SsbetaGly), continuous and batchwise reactions with both enzymes differed markedly with regard to relative proportions of the individual saccharide components present at 80% substrate conversion. The CSTR yielded an up to four-fold greater ratio of disaccharides to trisaccharides concomitant with a 5- to 30-fold larger relative proportion of beta-D-Galp-(1-->3)-D-Glc in the product mixture. The results show that apart from continuous hydrolysis of lactose at 70 degrees C, a CSTR charged with SsbetaGly or CelB and operated at steady-state conditions could be a useful reaction system for the production of galacto-oligosaccharides in which composition is narrower and more easily programmable, in terms of the individual components contained, as compared to the batchwise reaction.     

Transgalactosylation by thermostable beta-glycosidases from Pyrococcus furiosus and Sulfolobus solfataricus. Binding interactions of nucleophiles with the galactosylated enzyme intermediate make major contributions to the formation of new beta-glycosides during lactose conversion.

The hyperthermostable beta-glycosidases from the Archaea Sulfolobus solfataricus (SsbetaGly) and Pyrococcus furiosus (CelB) hydrolyse beta-glycosides of D-glucose or D-galactose with relaxed specificities pertaining to the nature of the leaving group and the glycosidic linkage. To determine how specificity is manifested under conditions of kinetically controlled transgalactosylation, the major transfer products formed during the hydrolysis of lactose by these enzymes have been identified, and their appearance and degradation have been determined in dependence of the degree of substrate conversion. CelB and SsbetaGly show a marked preference for making new beta(1-->3) and beta(1-->6) glycosidic bonds by intermolecular as well as intramolecular transfer reactions. The intramolecular galactosyl transfer of CelB, relative to glycosidic-bond cleavage and release of glucose, is about 2.2 times that of SsbetaGly and yields beta-D-Galp-(1-->6)-D-Glc and beta-D-Galp-(1-->3)-D-Glc in a molar ratio of approximately 1 : 2. The partitioning of galactosylated SsbetaGly between reaction with sugars [kNu (M-1. s-1)] and reaction with water [kwater (s-1)] is about twice that of CelB. It gives a mixture of linear beta-D-glycosides, chiefly trisaccharides at early reaction times, in which the prevailing new glycosidic bonds are beta(1-->6) and beta(1-->3) for the reactions catalysed by SsbetaGly and CelB, respectively. The accumulation of beta-D-Galp-(1-->6)-D-Glc at the end of lactose hydrolysis reflects a 3-10-fold specificity of both enzymes for the hydrolysis of beta(1-->3) over beta(1-->6) linked glucosides. Galactosyl transfer from SsbetaGly or CelB to D-glucose occurs with partitioning ratios, kNu/kwater, which are seven and > 170 times those for the reactions of the galactosylated enzymes with 1-propanol and 2-propanol, respectively. Therefore, the binding interactions with nucleophiles contribute chiefly to formation of new beta-glycosides during lactose conversion. Likewise, noncovalent interactions with the glucose leaving group govern the catalytic efficiencies for the hydrolysis of lactose by both enzymes. They are almost fully expressed in the rate-limiting first-order rate constant for the galactosyl transfer from the substrate to the enzyme and lead to a positive deviation by approximately 2.5 log10 units from structure-reactivity correlations based on the pKa of the leaving group.     

Membrane-bound alkaline phosphatase from ectopic mineralization and rat bone marrow cell culture

Cells from rat bone marrow exhibit the proliferation-differentiation sequence of osteoblasts, form mineralized extracellular matrix in vitro and release alkaline phosphatase into the medium. Membrane-bound alkaline phosphatase was obtained by method that is easy to reproduce, simpler and fast when compared with the method used to obtain the enzyme from rat osseous plate. The membrane-bound alkaline phosphatase from cultures of rat bone marrow cells has a MW(r) of about 120 kDa and specific PNPP activity of 1200 U/mg. The ecto-enzyme is anchored to the plasma membrane by the GPI anchor and can be released by PIPLC (selective treatment) or polidocanol (0.2 mg/mL protein and 1% (w/v) detergent). The apparent optimum pH for PNPP hydrolysis by the enzyme was pH 10. This fraction hydrolyzes ATP (240 U/mg), ADP (350 U/mg), glucose 1-phosphate (1100 U/mg), glucose 6-phosphate (340 U/mg), fructose 6-phosphate (460 U/mg), pyrophosphate (330 U/mg) and beta-glycerophosphate (600 U/mg). Cooperative effects were observed for the hydrolysis of PPi and beta-glycerophosphate. PNPPase activity was inhibited by 0.1 mM vanadate (46%), 0.1 mM ZnCl2 (68%), 1 mM levamisole (66%), 1 mM arsenate (44%), 10 mM phosphate (21%) and 1 mM theophylline (72%). We report the biochemical characterization of membrane-bound alkaline phosphatase obtained from rat bone marrow cells cultures, using a method that is simple, rapid and easy to reproduce. Its properties are compared with those of rat osseous plate enzyme and revealed that the alkaline phosphatase obtained has some kinetics and structural behaviors with higher levels of enzymatic activity, facilitating the comprehension of the mineralization process and its function.     

Polypyrrole nanotube array sensor for enhanced adsorption of glucose oxidase in glucose biosensors

A novel amperometric biosensor based on polypyrrole (PPy) nanotube array deposited on a Pt plated nano-porous alumina substrate and its performances are described. Glucose oxidase (GOx) enzyme was selected as the model enzyme in this study. Commercially available nano-porous alumina discs were used to fabricate electrodes in order to study the feasibility of enzyme entrapment by physical adsorption. A PPy/PF6- film comprising of nanotube array was synthesized using a solution containing 0.05 M Pyrrole and 0.1 M NaPF6 at a current density of 0.3 mA/cm2 for 90 s. The immobilization was done by physical adsorption of 5 microL of GOx (from a stock solution of 2 mg/mL of 210 U/mg) on each electrode. A sensitivity of 7.4 mA cm(-2) M(-1) was observed with PPy nanotube array where the maximum tube diameter was 100 nm. A linear range of 500 microM-13 mM and a response time of about 3 s were observed with a nanotube array where the maximum tube diameter was 200 nm. The synthesized nanotube arrays were characterized by galvanostatic electrochemical technique. Calculated value of apparent Michaelis-Menten constant (Km) was 7.01 mM. The use of nano-porous template electrodes leads to an efficient enzyme loading and provides an increased surface area for sensing the reaction. These factors contribute to increase the characteristic performances of the novel biosensor.     

Membrane microreactor in biocatalytic transesterification of triolein for biodiesel production

Transesterification is a principal chemical reaction that occurs in biodiesel production. We developed a novel biocatalytic membrane microreactor (BMM) for continuous transesterification by utilizing an asymmetric membrane as an enzyme-carrier for immobilization. The BMM was developed by pressure driven filtration of lipase from Pseudomonas fluorescens, which is suitable for highly efficient biocatalytic transesterification. Lipase solution was allowed to permeate through an asymmetric membrane with NMWL 300 kDa composed of polyethersulfone. The performances of BMM were studied in biodiesel synthesis via transesterification of triolein with methanol. Transesterification was carried out by passing a solution of triolein and methanol through the asymmetric membrane. The degree of triolein conversion using this microreactor was ca. 80% with a reaction time of 19 min. The BMM system displayed good stability, with no activity decay over a period of 12 day with continuous operation. Results from triolein transesterification clearly demonstrate the potential of an asymmetric membrane as an enzyme carrier material. Enzyme activity (mmol/h·g_lipase) was approximately 3 fold higher than that of native free lipase.     

Enzymatic synthesis of β‐glucosylglycerol using a continuous‐flow microreactor containing thermostable β‐glycoside hydrolase CelB immobilized on coated microchannel walls

β‐Glucosylglycerol (βGG) has potential applications as a moisturizing agent in cosmetic products. A stereochemically selective method of its synthesis is kinetically controlled enzymatic transglucosylation from a suitable donor substrate to glycerol as acceptor. Here, the thermostable β‐glycosidase CelB from Pyrococcus furiosus was used to develop a microstructured immobilized enzyme reactor for production of βGG under conditions of continuous flow at 70°C. Using CelB covalently attached onto coated microchannel walls to give an effective enzyme activity of 30 U per total reactor working volume of 25 µL, substrate conversion and formation of transglucosylation product was monitored in dependence of glucosyl donor (2‐nitrophenyl‐β‐D ‐glucoside (oNPGlc), 3.0 or 15 mM; cellobiose, 250 mM), the concentration of glycerol (0.25–1.0 M), and the average residence time (0.2–90 s). Glycerol caused a concentration‐dependent decrease in the conversion of the glucosyl donor via hydrolysis and strongly suppressed participation of the substrate in the reaction as glucosyl acceptor. The yields of βGG were ≥80% and ≈60% based on oNPGlc and cellobiose converted, respectively, and maintained up to near exhaustion of substrate (≥80%), giving about 120 mM (30 g/L) of βGG from the reaction of cellobiose and 1 M glycerol. The structure of the transglucosylation products, 1‐O‐β‐D ‐glucopyranosyl‐rac‐glycerol (79%) and 2‐O‐β‐D ‐glucopyranosyl‐sn‐glycerol (21%), was derived from NMR analysis of the product mixture of cellobiose conversion. The microstructured reactor showed conversion characteristics similar to those for a batchwise operated stirred reactor employing soluble CelB. The advantage of miniaturization to the microfluidic format lies in the fast characterization of full reaction time courses for a range of process conditions using only a minimum amount of enzyme. Biotechnol. Bioeng. 2009;103: 865–872. © 2009 Wiley Periodicals, Inc.     

Identification of tandemly repeated type VI cellulose-binding domains in an endoglucanase from the aerobic soil bacterium Cellvibrio mixtus

Cellulose-binding domains (CBD) play a pivotal role during plant cell wall hydrolysis by cellulases and xylanases from aerobic soil bacteria. Recently we␣have reported the molecular characterisation of a single-domain endoglucanase from Cellvibrio mixtus, suggesting that some cellulases produced by this aerobic bacterium preferentially hydrolyse soluble cellulosic substrates. Here we describe the complete nucleotide sequence of a second cellulase gene, celB, from the soil bacterium C. mixtus. It revealed an open reading frame of 1863 bp that encoded a polypeptide, defined as cellulase B (CelB), with a predicted M _r of 66 039. CelB contained a glycosyl hydrolase family 5 catalytic domain at its N terminus followed by two repeated domains, which exhibited sequence identity with type VI CBD previously found in xylanases. Full-length CelB bound to cellulose while catalytically active truncated cellulase derivatives were unable to bind the polysaccharide, confirming that CelB is a modular enzyme and that the type VI CBD homologues were functional. Analysis of the biochemical properties of CelB revealed that the enzyme hydrolyses a range of cellulosic substrates, although it was unable to depolymerise Avicel. We propose that type VI CBD, usually found in xylanases, provide an additional mechanism by which cellulases can accumulate on the surface of the plant cell wall, although they do not potentiate cellulase activity directly. These results demonstrate that C. mixtus, in common with other aerobic bacteria, is able to produce cellulases that are directed to the hydrolysis of cellulose in its natural environment, the plant cell wall. Received: 6 October 1997 / Received revision: 22 December 1997 / Accepted: 2 January 1998     

Development of an ultrahigh-temperature process for the enzymatic hydrolysis of lactose. IV. Immobilization of two thermostable beta-glycosidases and optimization of a packed-bed reactor for lactose conversion.

Recombinant hyperthermostable beta-glycosidases from the archaea Sulfolobus solfataricus (Ss beta Gly) and Pyrococcus furiosus (CelB) were covalently attached onto the insoluble carriers chitosan, controlled pore glass (CPG), and Eupergit C. For each enzyme/carrier pair, the protein-binding capacity, the immobilization yield, the pH profiles for activity and stability, the activity/temperature profile, and the kinetic constants for lactose hydrolysis at 70 degrees C were determined. Eupergit C was best among the carriers in regard to retention of native-like activity and stability of Ss beta Gly and CelB over the pH range 3.0-7.5. Its protein binding capacity of approximately 0.003 (on a mass basis) was one-third times that of CPG, while immobilization yields were typically 80% in each case. Activation energies for lactose conversion by the immobilized enzymes at pH 5.5 were in the range 50-60 kJ/mol. This is compared to values of approximately 75 kJ/mol for the free enzymes. Immobilization expands the useful pH range for CelB and Ss beta Gly by approximately 1.5 pH units toward pH 3.5 and pH 4.5, respectively. A packed-bed enzyme reactor was developed for the continuous conversion of lactose in different media, including whey and milk, and operated over extended reaction times of up to 14 days. The productivities of the Eupergit C-immobilized enzyme reactor were determined at dilution rates between 1 and 12 h(-1), and using 45 and 170 g/L initial lactose. Results of kinetic modeling for the same reactor, assuming plug flow and steady state, suggest the presence of mass-transfer limitation of the reaction rate under the conditions used. Formation of galacto-oligosaccharides in the continuous packed-bed reactor and in the batch reactor using free enzyme was closely similar in regard to yield and individual saccharide components produced.     

Substrate specificity engineering of beta-mannosidase and beta-glucosidase from Pyrococcus by exchange of unique active site residues

A beta-mannosidase gene (PH0501) was identified in the Pyrococcus horikoshii genome and cloned and expressed in E. coli. The purified enzyme (BglB) was most specific for the hydrolysis of p-nitrophenyl-beta-D-mannopyranoside (pNP-Man) (Km: 0.44 mM) with a low turnover rate (kcat: 4.3 s(-1)). The beta-mannosidase has been classified as a member of family 1 of glycoside hydrolases. Sequence alignments and homology modeling showed an apparent conservation of its active site region with, remarkably, two unique active site residues, Gln77 and Asp206. These residues are an arginine and asparagine residue in all other known family 1 enzymes, which interact with the catalytic nucleophile and equatorial C2-hydroxyl group of substrates, respectively. The unique residues of P. horikoshii BglB were introduced in the highly active beta-glucosidase CelB of Pyrococcus furiosus and vice versa, yielding two single and one double mutant for each enzyme. In CelB, both substitutions R77Q and N206D increased the specificity for mannosides and reduced hydrolysis rates 10-fold. In contrast, BglB D206N showed 10-fold increased hydrolysis rates and 35-fold increased affinity for the hydrolysis of glucosides. In combination with inhibitor studies, it was concluded that the substituted residues participate in the ground-state binding of substrates with an equatorial C2-hydroxyl group, but contribute most to transition-state stabilization. The unique activity profile of BglB seems to be caused by an altered interaction between the enzyme and C2-hydroxyl of the substrate and a specifically increased affinity for mannose that results from Asp206.     

Overexpression of celB gene coding for beta-glucosidase from Pyrococcus furiosus using a baculovirus expression vector system in silkworm, Bombyx mori

beta-Glucosidase is a member of the glycosyl hydrolases that specifically catalyze the hydrolysis of terminal nonreducing beta-D-glucose residues from the end of various oligosaccharides with the release of beta-D-glucose. CelB gene, encoding the thermostable beta-glucosidase, was amplified from the Pyrococcus furiosus genome and then cloned into the baculoviral transfer vector under the control of the polyhedrin gene promoter. After co-transfection with the genetically modified parental Bombyx mori nucleopolyhedrovirus (BmNPV), the recombinant virus containing celB gene was used to express beta-glucosidase in silkworm. The recombinant beta-glucosidase was purified to about 81% homogeneity in a single heat-treatment step. The optimal activity of the expressed beta-glucosidase was obtained at pH 5.0 and about 105 degrees C; divalent cations and high ionic strength did not affect the activity remarkably. This suggested that the enzymatic characteristics of recombinant beta-glucosidase were similar to the native counterpart. The expressed beta-glucosidase accounted for more than 10% of silkworm total haemolymph proteins according to the protein quantification and densimeter scanning. The expression level reached 10,199.5 U per ml haemolymph and 19,797.4 U per silkworm larva, and the specific activity of the one-step purified crude enzyme was 885 U per mg. It was demonstrated to be an attractive approach for mass production of thermostable beta-glucosidase using this system.     

Effect of growth conditions on the production of manganese peroxidase by three strains of Bjerkandera adusta

We were looking for a strain of Bjerkandera adusta that produces high titres of manganese peroxidase under optimal conditions for large-scale enzyme purification. We have chosen two strains from the University of Alberta Microfungus Collection and Herbarium, UAMH 7308 and 8258, and compared the effects of growth conditions and medium composition on enzyme production with the well-characterized strain BOS55 (ATCC 90940). Of four types of cereal bran examined, rice bran at 3% (w/v) in 60 mM phosphate buffer pH 6 supported the highest levels of enzyme production. Using 100 mL medium in 500-mL Erlenmeyer flasks, maximum enzyme levels in the culture supernatant occurred after about 10 days of growth; 5.5 U x mL(-1) for UAMH 7308, 4.4 U x mL(-1) for UAMH 8258, and 1.7 U x mL(-1) for BOS55, where units are expressed as micromoles of Mn-malonate formed per minute. Growth as submerged cultures in 10-L stirred tank reactors produced 3.5 U x mL(-1) of manganese peroxidase (MnP) by UAMH 8258 and 2.5 U x mL(-1) of MnP by 7308, while enzyme production by BOS55 was not successful in stirred tank reactors but could be scaled up in 2-L shake flasks containing 400 mL rice bran or glucose-malt-yeast extract (GMY)-Mn-glycolate medium to produce MnP levels of 1.7 U x mL(-1). These results show that the two strains of B. adusta, UAMH 7308 and 8258, can produce between two and three times the manganese peroxidase level of B. adusta BOS55, that they are good candidates for scale up of enzyme production, and that the rice bran medium supports higher levels of enzyme production than most previously described media.