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.     

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.     

Development of an ultra-high-temperature process for the enzymatic hydrolysis of lactose: II. Oligosaccharide formation by two thermostable beta-glycosidases

During lactose conversion at 70 degrees C, when catalyzed by beta-glycosidases from the archea Sulfolobus solfataricus (SsbetaGly) and Pyrococcus furiosus (CelB), galactosyl transfer to acceptors other than water competes efficiently with complete hydrolysis of substrate. This process leads to transient formation of a range of new products, mainly disaccharides and trisaccharides, and shows a marked dependence on initial substrate concentration and lactose conversion. Oligosaccharides have been analyzed quantitatively by using capillary electrophoresis and high performance anion-exchange chromatography. At 270 g/L initial lactose, they accumulate at a maximum concentration of 86 g/L at 80% lactose conversion. With both enzymes, the molar ratio of trisaccharides to disaccharides is maximal at an early stage of reaction and decreases directly proportional to increasing substrate conversion. Overall, CelB produces about 6% more hydrolysis byproducts than SsbetaGly. However, the product spectrum of SsbetaGly is richer in trisaccharides, and this agrees with results obtained from the steady-state kinetics analyses of galactosyl transfer catalyzed by SsbetaGly and CelB. The major transgalactosylation products of SsbetaGly and CelB have been identified. They are beta-D-Galp-(1-->3)-Glc and beta-D-Galp-(1-->6)-Glc, and beta-D-Galp-(1-->3)-lactose and beta-D-Galp-(1-->6)-lactose, and their formation and degradation have been shown to be dependent upon lactose conversion. Both enzymes accumulate beta(1-->6)-linked glycosides, particularly allolactose, at a late stage of reaction. Because a high oligosaccharide concentration prevails until about 80% lactose conversion, thermostable beta-glycosidases are efficient for oligosaccharide production from lactose. Therefore, they prove to be stable and versatile catalysts for lactose utilization.     

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.     

Properties of immobilized β-d-galactosidase from Bacillus circulans

Partially purified β-d-galactosidase (β-d-galactoside galactohydrolase, EC 3.2.1.23) from Bacillus circulans showed high activity towards both pure lactose and lactose in skim milk, and a better thermal stability than the enzyme from yeast or Escherichia coli. During the course of hydrolysis of lactose catalysed by the enzyme, considerable amounts of oligosaccharides were produced. β-d-Galactosidase from B. circulans was immobilized onto Duolite ES-762, Dowex MWA-1 and sintered alumina by adsorption with glutaraldehyde treatment. The highest activity for hydrolysis of lactose was obtained with immobilization onto Duolite ES-762. During a continuous hydrolysis of lactose, the immobilized enzyme was reversibly inactivated, probably due to oligosaccharides accumulating in the gel. The inactivation was reduced when a continuous reaction was operated at a high percent conversion of lactose in a continuous stirred tank reactor (CSTR). The half-life of the immobilized enzyme was estimated to be 50 and 15 days at 50 and 55°C, respectively, when the reaction was carried out in a CSTR with a percent conversion of lactose >70%.     

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.     

Coated-wall microreactor for continuous biocatalytic transformations using immobilized enzymes

Microstructured flow reactors are emerging tools for biocatalytic process development. A compelling design is that of the coated-wall reactor where enzyme is present as a surface layer attached to microchannel walls. However, preparation of a highly active wall biocatalyst remains a problem. Here, a stainless steel microreactor was developed where covalent immobilization of the enzyme in multiple linear flow channels of the reaction plate was supported by a macroporous wash-coat layer of gamma-aluminum oxide. Using surface functionalization with aminopropyl triethoxysilane followed by activation with glutardialdehyde, the thermophilic beta-glycosidase CelB from Pyrococcus furiosus was bound with retention of half of the specific activity of the free enzyme (800 U/mg), yielding a high catalyst loading of about 500 U/mL. This microreactor was employed for the continuous hydrolysis of lactose (100 mM) at 80 degrees C, providing a space-time yield of 500 mg glucose/(mL h) at a stable conversion of > or =70%. The immobilized enzyme displayed a half-life of 15 days under the operational conditions. Due to the absence of hydrophobic solute-material interactions, which limit the scope of microstructures fabricated from poly(dimethylsiloxane) for biocatalytic applications, the new microreactor was fully compatible with the alternate enzyme substrate 2-nitro-phenyl-beta-D-galactoside and the 2-nitro-phenol product resulting from its hydrolysis catalyzed by CelB.     

Evaluation of half-life of immobilized enzyme during continuous reaction in bioreactors: A theoretical study

A theoretical study has been carried out on the evaluation of the apparent half-life of immobilized enzyme activity during continuous reaction both in a plug-flow reactor (PFR) and in a continuous-flow stirred-tank reactor (CSTR). Two apparent half-lives have been defined: the elapsed time at which the feedrate becomes half of the initial one when the feedrate of the substrate solution is lowered to keep the conversion fixed (constant-conversion policy), and the elapsed time at which the conversion becomes half of the initial one when the feedrate (or space velocity) is kept constant (constant-feedrate policy or constant-space-velocity policy). Under no intraparticle diffusional limitation, the constant-conversion policy of operation in the PFR and CSTR gives the same half-life as that of the enzyme inactivation regardless of the formula of the reaction rate, and the constant-feedrate policy of operation in the PFR and CSTR offers the same half-life as that of the enzyme inactivation only when the reaction is zero-order. Under intra-particle diffusional limitation, apparent half-lives are always greater than that of enzyme denaturation, depending on many factors such as order of reaction, feeding policy (constant-conversion and constant-feedrate policies), initial conversion, and bioreactor configuration. It is suggested to perform the continuous operation with changing feedrate to keep the conversion (or outlet substrate concentration) fixed under the domain of zero-order kinetics so as to obtain an apparent half-life as close to the real one in industrial operation.     

β-Galactosidase from Talaromyces thermophilus immobilized on to Eupergit C for production of galacto-oligosaccharides during lactose hydrolysis in batch and packed-bed reactor

The β-galactosidase from Talaromyces thermophilus CBS 236.58 immobilized onto Eupergit C produced galacto-oligosaccharides (GalOS) in batchwise and continuous packed-bed mode of operation. A maximum yield of GalOS of 12, 39 and 80 g l⁻¹ was obtained for initial lactose concentrations of 50, 100 and 200 g l⁻¹, respectively, for batch conversion experiments. The immobilized enzyme could be re-used for several cycles for lactose hydrolysis and transformation. The maximum GalOS concentration of approximately 50 g l⁻¹ was obtained with the dilution rate of 0.375 h⁻¹ in a packed-bed reactor, when using an initial lactose concentration of 200 g l⁻¹. Continuous conversion of lactose in the packed-bed reactor resulted in the formation of relatively more trisaccharides than when employing the immobilized enzyme in discontinuous mode of operation.     

A CSTR-hollow fiber system for continuous hydrolysis of proteins. Performance and kinetics

The effect of four operating variables (enzyme concentration, substrate concentration, flow rate, and reaction volume) on the performance of CSTR-hollow fiber membrane reactor was studied for the continuous hydrolysis of a soy protein isolate using Pronase. Based on a residence time distribution study, the reactor system was modeled as an ideal CSTR in combination with the Michaelis-Menten equation of enzyme kinetics. This kinetic model correlated conversion with a space-time parameter modified to include all four independent variables. An empirical model based on curvilinear regression analysis was also developed. Both models predicted conversion fairly well, although the kinetic model slightly underpredicts at high conversion.     

Comparative study of reactor performance for the resolution of d,l-amino acids

The racemic resolution of l-valine and l-serine by fungal aminoacylase has been evaluated by comparing the performance of various reactor configurations including an anion exchange nylon tangential flow membrane reactor, a tubular reactor with aminoacylase adsorbed onto DEAE-Sephadex as support and a continuous stirred tank reactor with enzyme recycling using a flat ultrafiltration module (CSTR/UF). Among the substrates tested, the N-chloroacetyl-d,l-amino acids were the preferred substrates, showing the highest catalytic efficiency (V_m/K_m).Optimum reactor operational conditions obtained in discontinuous assays were selected to study the behaviour of the reactors in a continuous mode. DEAE-Sephadex loaded six-fold more enzyme than anion exchange nylon (60 and 10 gE/litre, respectively, related to reactor volume), whereas enzyme concentration within the CSTR/UF reactor was limited only by enzyme solubility.The tangential flow membrane reactor configuration with a 10 g/litre enzyme concentration produced higher productivity values (0·35 kg l-valine/litre per day, and 80% conversion degree) and operational stability (t = 161 days) than the CSTR/UF reactor (0·24 kg l-valine/litre per day, and 80% conversion degree) performing with the same enzyme concentration. The tubular reactor with the enzyme adsorbed onto DEAE-Sephadex (60 g/litre enzyme load) showed higher productivity values (1·9 kg l-valine/litre per day, and 80% conversion degree) and operational stability (t = 70 days) than the CSTR/UF reactor (1·05 kg l-valine/litre per day, and 80% conversion degree). However, the CSTR/UF reactor was the preferred configuration, as it had the highest enzyme load and productivity (1·95 kg l-valine/litre per day of reactor volume, and 80% conversion degree), a half-life of 55 days at 50°C, and the possibility of easy continuous enzyme addition.     

Production of galacto-oligosaccharides from lactose by Aspergillus oryzae beta-galactosidase immobilized on cotton cloth.

The production of galacto-oligosaccharides (GOS) from lactose by A. oryzae beta-galactosidase immobilized on cotton cloth was studied. The total amounts and types of GOS produced were mainly affected by the initial lactose concentration in the reaction media. In general, more and larger GOS can be produced with higher initial lactose concentrations. A maximum GOS production of 27% (w/w) of initial lactose was achieved at 50% lactose conversion with 500 g/L of initial lactose concentration. Tri-saccharides were the major types of GOS formed, accounting for more than 70% of the total GOS produced in the reactions. Temperature and pH affected the reaction rate, but did not result in any changes in GOS formation. The presence of galactose and glucose at the concentrations encountered near maximum GOS greatly inhibited the reactions and reduced GOS yield by as much as 15%. The cotton cloth as the support matrix for enzyme immobilization did not affect the GOS formation characteristics of the enzyme, suggesting no diffusion limitation in the enzyme carrier. The thermal stability of the enzyme increased approximately 25-fold upon immobilization on cotton cloth. The half-life for the immobilized enzyme on cotton cloth was more than 1 year at 40 degrees C and 48 days at 50 degrees C. Stable, continuous operation in a plugflow reactor was demonstrated for 2 weeks without any apparent problem. A maximum GOS production of 21 and 26% (w/w) of total sugars was attained with a feed solution containing 200 and 400 g/L of lactose, respectively, at pH 4.5 and 40 degrees C. The corresponding reactor productivities were 80 and 106 g/L/h, respectively, which are at least several-fold higher than those previously reported.     

Improved oligosaccharide synthesis by protein engineering of beta-glucosidase CelB from hyperthermophilic Pyrococcus furiosus

Enzymatic transglycosylation of lactose into oligosaccharides was studied using wild-type beta-glucosidase (CelB) and active site mutants thereof (M424K, F426Y, M424K/F426Y) and wild-type beta-mannosidase (BmnA) of the hyperthermophilic Pyrococcus furiosus. The effects of the mutations on kinetics, enzyme activity, and substrate specificity were determined. The oligosaccharide synthesis was carried out in aqueous solution at 95 degrees C at different lactose concentrations and pH values. The results showed enhanced synthetic properties of the CelB mutant enzymes. An exchange of one phenylalanine to tyrosine (F426Y) increased the oligosaccharide yield (45%) compared with the wild-type CelB (40%). Incorporation of a positively charged group in the active site (M424K) increased the pH optimum of transglycosylation reaction of CelB. The double mutant, M424K/F426Y, showed much better transglycosylation properties at low (10-20%) lactose concentrations compared to the wild-type. At a lactose concentration of 10%, the oligosaccharide yield for the mutant was 40% compared to 18% for the wild-type. At optimal reaction conditions, a higher ratio of tetrasaccharides to trisaccharides was obtained with the double mutant (0.42, 10% lactose) compared to the wild-type (0.19, 70% lactose). At a lactose concentration as low as 10%, only trisaccharides were synthesized by CelB wild-type. The beta-mannosidase BmnA from P. furiosus showed both beta-glucosidase and beta-galactosidase activity and in the transglycosylation of lactose the maximal oligosaccharide yield of BmnA was 44%. The oligosaccharide yields obtained in this study are high compared to those reported with other transglycosylating beta-glycosidases in oligosaccharide synthesis from lactose.     

Repeated batch and continuous operations for phosphatidylglycerol synthesis from phosphatidylcholine with immobilized phospholipase D

Summary The repeated batch and continuous operations for transphosphatidylation reaction were carried out for phosphatidylglycerol (PG) synthesis from phosphatidylcholine (PC) with the help of immobilized cabbage phospholipase D (PLD) in the presence of glycerol. The biphasic reaction system was used which included the aqueous phase containing immobilized PLD along with high concentrations of glycerol (30%–50%) and buffer, whereas the main part of substrate (PC) and products (mainly PG) formed were in the organic phase (diethyl ether).Octyl-Sepharose CL-4B having a hydrophobic octyl group was chosen for the PLD immobilization. Both immobilization yield and activity yield of immobilized enzyme were 100%. The effects of solvents, temperature and glycerol concentrations on the immobilized PLD were examined. Repeated batch conversion of PC (15 g/l) to PG was examined with the immobilized PLD in 30% glycerol. In all five batch cycles examined, 100% selectivity was obtained and there was no significant decrease in the fractional conversion of PC to PG (98%–99%) in the first three batch cycles. In the cases of a packed-bed reactor (PBR) and a continuous stirred-tank reactor (CSTR) used for continuous synthesis of PG with the immobilized PLD, the operational stabilities of the immobilized enzyme were almost the same (half life=14 h at 30°C) when purified PC was used, while in the case of partially purified PC in CSTR the half life increased more than five times.Abbreviations used PC phosphatidylcholine - PG phosphatidylglycerol - PA phosphatidic acid - PLD phospholipase D - PBR packed bed reactor - CSTR continuous stirred tank reactor Studies on enzymatic conversion of phospholipids (III)     

A comparative study of immobilized amyloglucosidase in a packed bed reactor and a continuous feed stirred tank reactor

The catalytic activity of amyloglucosidase covalently attached to DEAE-cellulose was studied in a packed bed reactor and a continuous feed stirred tank reactor (CSTR) for the reaction maltose → glucose. At low flow rates mass-transfer limitations in the bed reactor lead to lower conversions for this reactor compared to the CSTR. Simple theoretical expressions for these reactors were compared with the experimental results. There are significant differences between the kinetic parameters and pH profile of the immobilized and free enzyme. The immobilized enzyme also showed greater stability at 50°C than did free amyloglucosidase. The temperature dependence of the reaction rate was the same for immobilized and free enzyme.     

Enzymatic Synthesis of Hexyl Glycosides from Lactose At Low Water Activity and High Temperature Using Hyperthermostable β-glycosidases

Optimization of hexyl-g-glycoside synthesis from lactose in hexanol at low water activity and high temperature was investigated using g-glycosidases from hyperthermophilic organisms: Sulfolobus solfataricus (LacS) and Pyrococcus furiosus (CelB). The method for water activity adjustment by equilibration with saturated salt solutions was adapted for use at high temperature. The influence of enzyme immobilization (on XAD-4, XAD-16, or Celite), addition of surfactants (AOT or SDS), substrate concentration, water activity, and temperature (60-90°C) on enzymatic activity and hexyl-g-glycoside yield were examined. Compared to other g-glycosidases in lactose conversion into alkyl glycoside, these enzymes showed high activity in a hexanol one-phase system and synthesized high yields of both hexyl-g-galactoside and hexyl-g-glucoside. Using 32 λg/l lactose (93 λmM), LacS synthesized yields of 41% galactoside (38.1 λmM) and 29% glucoside (27.0 λmM), and CelB synthesized yields of 63% galactoside (58.6 λmM) and 28% glucoside (26.1 λmM). With the addition of SDS to the reaction it was possible to increase the initial reaction rate of LacS and hexyl-g-galactoside yield (from 41 to 51%). The activity of the lyophilized enzyme was more influenced by the water content in the reaction than the enzyme on solid support. In addition, it was concluded that for the lyophilized enzyme preparation the enzymatic activity was much more influenced by the temperature when the water activity was increased. A variety of different glycosides were prepared using different alcohols as acceptors.     

Hydrolysis of liquefied corn starch in a membrane reactor

The objective of this study was to develop a continuous hydrolysis process for the enzymatic saccharification of liquefied corn starch using a membrane reactor. A residence time distribution study confirmed that the membrane reactor could be modeled as a simple continuous stirred tank reactor (CSTR). Kinetic studies indicated that the continuous reactor operated in the first-order region with respect to substrate concentration at substrate concentrations greater than 200 g/L. At a residence time of 1 h and an enzyme concentration of 1 g/L, the maximum reaction velocity (V(m)) was 3.86 g glucose/L min and the apparent Michaelis constant (K(m) (')) was 562 g/L. The K(m) (') value for the continuous reactor was 2-7 times greater than that obtained in a batch reactor.Kinetic data were fit to a model based on the Michaelis-Menten rate expression and the design equation for a CSTR. Application of the model at low reactor space times was successful. At space times of 6 min or less, the model predicted the reactor's performance reasonably well. Additional work on the detection and quantitation of reversion products formed by glucoamylase is required. Isolation, detection, and quantitation of reversion products by HPLC was difficult. Detailed analysis on the formation of these reversion products could lead to better reactor designs in the future.     

Galactosyl transfer catalyzed by thermostable beta-glycosidases from Sulfolobus solfataricus and Pyrococcus furiosus: kinetic studies of the reactions of galactosylated enzyme intermediates with a range of nucleophiles

The transfer of a galactosyl group from an enzyme to a number of neutral primary alcohols, phenol and azide has been studied during the reactions at 80 degrees C of thermostable beta-glycosidases from Sulfolobus solfataricus (Ss beta Gly) and Pyrococcus furiosus (CelB) with 2-nitrophenyl beta-D-galactopyranoside or lactose (4-O-beta-D-galactopyranosyl D-glucopyranose) as substrates. The rate constant ratios, k(Nu)/k(water), for partitioning of the galactosylated enzyme intermediates between reaction with nucleophiles (k(Nu), M(-1) s(-1)) and water (k(water), s(-1)) have been determined from the difference in the initial velocities of the formation of 2-nitrophenol or D-glucose, and D-galactose. The results show that hydrophobic bonding interactions contribute approximately 8 kJ mol(-1) to the stabilization of the transition state for the reaction of galactosylated enzyme intermediates of Ss beta Gly and CelB with 1-butanol, compared to the transition state for the enzymatic reaction with methanol. The leaving group/nucleophile binding sites of Ss beta Gly and CelB appear about 0.8 times as hydrophobic as n-octanol. Values of k(Nu)/k(water) for reactions of galactosylated Ss beta Gly with ethanol and substituted derivatives of ethanol show no clear dependence on the pK(a) of the primary hydroxy group of these nucleophiles in the pK(a) range 12.4-16.0. The binding of phenol with the galactosylated enzyme intermediates of Ss beta Gly and CelB occurs in a form that is mainly nonproductive pertaining to beta-galactoside synthesis. Neither enzyme catalyzes galactosyl transfer to azide ion. A model is proposed for the interaction of neutral nucleophiles at an extended acceptor site of the galactosylated enzymes.     

Application of immobilized chymotrypsin in a multistage fluidized-bed reactor

The stereospecific hydrolysis of D ,L -phenylalanine methylester with immobilized α-chymotrypsin was carried out as a model reaction for the racemate resolution of aromatic amino acids in a five staged fluidized-bed reactor (FBR). Owing to ester hydrolysis, a pH shift occurred along the reactor. Because of the pH-dependent enzyme activity a particular longitudinal pH profile had to be enforced by a proper entrance pH in order to gain an optimum conversion. In the FBR with optimum pH profile, higher conversions were achieved than in a continuous stirred tank reactor (CSTR) at the pH optimum and at the same contact time. By the application of a proton balance and the results of kinetic measurements a model was developed for the prediction of the optimum longitudinal pH profile with regard to the maximum conversion.     

Use of an enzyme thermistor in continuous measurements and enzyme reactor control.

The enzyme thermistor measures the heat produced by the action of an immobilized enzyme on a substrate present in the sample. Its application in analysis of discrete samples, e.g., in clinical chemistry, is well documented, but it has not been used so far for continuous measurements. We decribe here the application of the enzyme thermistor for continuous monitoring and control of enzyme reactors. An enzyme thermistor filled with coimmobilized glucose oxidase and catalase was used to measure the amount of glucose in the outflow from a column reactor containing immobilized lactase acting on a lactose solution pumped through the reactor. The lactose conversion was kept on a constant level, irrespective of the actual enzymatic activity in the reactor, by regulating the flow through the reactor. The experiments were carried out with aqueous solutions of lactose as well as with whey from cow's milk.