Combined product and substrate inhibition equation for cellobiase

Cellobiase (CE 3.2.1.21) is a β-glucosidase which hydrolyzes cellobiose to glucose and is known to be subject to both product and substrate inhibition. This work report a model which combines both product and substrate inhibition effects for cellobiase isolated from a commercial preparation of Trichoderma viride from Miles Laboratories (Elkhart, IN). An integrated rate equation is presented which predicts the trends of time courses for hydrolyses of cellobiose a t concentrations ranging from 14.6–1416mM cellobiose. The constants used in the model (determined from initial rate data) are compared to those reported for cellobiase obtained from other sources of T. Viride. Most notable in this comparison is the apparently higher activity and reduced inhibition of this enzyme compared to other sources of cellobiase.     

An amperometric enzyme biosensor for real‐time measurements of cellobiohydrolase activity on insoluble cellulose

An amperometric enzyme biosensor for continuous detection of cellobiose has been implemented as an enzyme assay for cellulases. We show that the initial kinetics for cellobiohydrolase I, Cel7A from Trichoderma reesei, acting on different types of cellulose substrates, semi‐crystalline and amorphous, can be monitored directly and in real‐time by an enzyme‐modified electrode based on cellobiose dehydrogenase (CDH) from Phanerochaete chrysosporium (Pc). PcCDH was cross‐linked and immobilized on the surface of a carbon paste electrode which contained a mediator, benzoquinone. An oxidation current of the reduced mediator, hydroquinone, produced by the CDH‐catalyzed reaction with cellobiose, was recorded under constant‐potential amperometry at +0.5 V (vs. Ag/AgCl). The CDH‐biosensors showed high sensitivity (87.7 µA mM^?1 cm^?2), low detection limit (25 nM), and fast response time (t_95% ～ 3 s) and this provided experimental access to the transient kinetics of cellobiohydrolases acting on insoluble cellulose. The response from the CDH‐biosensor during enzymatic hydrolysis was corrected for the specificity of PcCDH for the β‐anomer of cello‐oligosaccharides and the approach were validated against HPLC. It is suggested that quantitative, real‐time data on pure insoluble cellulose substrates will be useful in attempts to probe the molecular mechanism underlying enzymatic hydrolysis of cellulose. Biotechnol. Bioeng. 2012; 109: 3199–3204. © 2012 Wiley Periodicals, Inc.     

Kinetics of solka floc cellulose hydrolysis by trichoderma viride cellulase

A product inhibition model is developed to describe the hydrolysis of cellulose by the Trichoderma viride enzyme system. It is assumed that noncompetitive inhibition by cellobiose dominates the reaction kinetics. Experiments show that this is indeed a reasonable assumption for initial cellulose concentrations of up to 15 g/liter and at hydrolysis extents up to 65′. Kinetic parameters were determined for the noncompetitive inhibitionmodel in batch experiments with durations of up to 1.5 hr. These parameterswere then used in predicting reaction progress for up to 10 hr. Cellobiose was added to the reaction mixture at the onset of some runs and againreliable predictions were obtained for up to 8 hr of hydrolysis. Finally reaction was carried out in a membrane reactor whereby the product cellobiose was being continuously removed and again reasonable predictability was obtained with a higher net reaction rate.     

Cellobiase from Trichoderma viride: purification, properties, kinetics, and mechanism

Three distinct cellobiase components were isolated from a commercial Trichoderma viride cellulase preparation by repeated chromatography on DEAE cellulose eluting by a salt gradient. The purified cellobiase preparations were evaluated for physical properties, kinetics, and mechanism. Results from this work include: 1) development of one step enzyme purification procedure using DEAE-cellulose; 2) isolation of three chromatographically distinct, yet kinetically similar, cellobiase fractions of molecular weight of approximately 76,000; 3) determination of kinetics which shows that cellobiase hydrolyzes cellobiose by a noncompetitive mechanism and that the product, glucose, inhibits the enzyme, and 4) development of an equation, based on the mechanism of cellobiase action, which accurately predicts the time course of cellobiose hydrolysis over an eightfold range of substrate concentration and conversions of up to 90%. Based on the data presented in the paper, it is shown that product inhibition of cellobiase significantly retards the rate of cellobiose hydrolysis.     

Hydrolysis of cellobiose using β-glucosidase from Penicillium funiculosum. Kinetic analysis

The kinetics of cellobiose hydrolysis was studied using β-glucosidase from Penicillium funiculosum, both free and immobilized on nylon powder, at different temperatures, pH values, enzymatic activities and initial cellobiose and glucose concentrations. The experimental results were fitted to a kinetic model by considering the substrate and product inhibitions as well as the thermal deactivation of β-glucosidase with a mean deviation of less than 10%. The immobilization of β-glucosidase led to an increase in the stability of the enzyme against changes in the pH value.     

Electrochemical oxidation of water by a cellobiose dehydrogenase from <Emphasis Type="BoldItalic">Phanerochaete chrysosporium</Emphasis>

Cellobiose dehydrogenase (CDH) is a redox protein containing two electron transfer centers; a flavin coenzyme performing a two-electron transfer reaction and an iron-heme coenzyme facilitating single-electron transfer. Purified CDH from Phanerochaete chrysosporium was immobilized on a pyrolytic graphite electrode and electron transfer from cellobiose to the electrode was generated. With cellobiose present during cyclic voltammetry, this novel enzyme/electrode system exhibited sharp, stable oxidation peaks with slower, though equivalent, reduction peaks. During cyclic voltammetry without substrate, the enzyme was rapidly oxidized during the initial scan, with no corresponding enzyme reduction during the reducing half of the cycle. After resting for several hours in aqueous buffer, the full oxidation current appeared again. These results suggest that the CDH is reduced by water splitting, albeit at a slow rate.     

Product inhibition of the recombinant CelS,an exoglucanase component of the Clostridium thermocellum cellulosome

CelS is the most abundant subunit and an exoglucanase component of the Clostridium thermocellum cellulosome, multicomponent cellulase complex. The product inhibition pattern of CelS was examined using purified recombinant CelS (rCelS) produced in Escherichia coli. The rCelS activity on cellopentaose was strongly inhibited by cellobiose. The rCelS activity was also inhibited by lactose. Glucose was only marginally inhibitory. Cellobiose appeared to inhibit the rCelS activity through a competitive mechanism. The inhibition was relieved when -glucosidase was added, presumably because of the conversion of cellobiose into glucose. These hydrolysis product inhibition patterns are consistent with those of the crude enzyme (cellulosome), suggesting that CelS is a rate-limiting factor in the activity of the cellulosome.     

Modelling of the enzymatic hydrolysis of cellobiose and cellulose by a complex enzyme mixture of Trichoderma reesei QM 9414

Summary The enzymatic hydrolysis of cellobiose and cellulose by the cell-free culture filtrate of Trichoderma reesei QM 9414 was investigated. The concentrations of cellobiose and glucose were measured as a function of time for different initial concentrations of cellobiose. It was not possible to describe these concentration variations by a model which considers only the cellobiase hydrolysis with competitive and noncompetitive substrate and product inhibition; it is necessary that the endo--1.4-glucanase with competitive product inhibition is also taken into account.The enzymatic hydrolysis of cellulose (Avicel) was described with a mathematical model by using the results of the decomposition of cellobiose by the same enzyme mixture.the identified model parameters are presented. A sensitivity analysis of the parameter was carried out also.     

Cellulase enzyme production during continuous culture growth of Sporotrichum (Chrysosporium) thermophile

Summary The cellulolytic fungus Sporotrichum (Chrysosporium) thermophile produces an extracellular cellobiose dehydrogenase during batch culture on cellulose or cellobiose. In chemostat culture at pH 5.6 on cellobiose this enzyme was produced in parallel with endo-cellulase. At pH 5.0 in continuous or fed-batch culture such a pattern was not evident. At constant growth rate in a chemostat with varying pH, activity of these enzymes was found to be poorly correlated. Thus the induction of cellobiose dehydrogenase shows a dependence on pH and cellobiose concentration which is different to that for endo-cellulase. The natural inducer of these enzymes and the role of cellobiose dehydrogenase remain to be elucidated.     

A product inhibition study of cellulases from Trichoderma longibrachiatum using dyed cellulose

Amorphous acid-swollen cellulose dyed with Reactive Orange was used to determine the relevant inhibition constants of cellulases from Trichoderma longibrachiatum by cellulose hydrolysis products (glucose and cellobiose). The method is based on the initial rate of increasing the hydrolysate absorbance (A_490mn) in the presence of added product. On adding glucose, the initial rate of glucose formation from cellulose and the rate of dye release were lower than the relevant rates in the absence of added product; however, the rate of cellobiose formation did not change. On the other hand, added cellobiose inhibited the rate of cellobiose formation from dyed cellulose and the rate of increase of the hydrolysate absorbance but did not affect the glucose formation. The constants of competitive inhibition of cellulases by glucose and cellobiose were 0.072 and 0.012 M, respectively. These inhibition parameters differed from those obtained from the analysis of the progress kinetics for extended reaction times.     

The inhibition of β-glucosidase activity in Trichoderma reesei C30 cellulase by derivatives and isomers of glucose

The inhibition of β-glucosidase in Trichoderma reesei C30 cellulase by D -glucose, its isomers, and derivatives was studied using cellobiose and ρ-nitrophenyl-β-glucoside (PNPG) as substrates for determining enzyme activity. The enzymatic hydrolysis of both substrates was inhibited competitively by glucose with approximate K_i values of 0.5mM and 8.7mM for cellobiose and PNPG as substrate, respectively. This inhibition by glucose was maximal at pH 4.8, and no inhibition was observed at pH 6.5 and above. The α anomer of glucose inhibited β-glucosidase to a greater extent than did the β form. Compared with D -glucose, L -glucose, D -glucose-6-phosphate, and D -glucose-1-phosphate inhibited the enzyme to a much lesser extent, unlike D -glucose-L -cysteine which was almost as inhibitory as glucose itself when cellobiose was used as substrate. Fructose (2?100mM) was found to be a poor inhibitor of the enzyme. It is suggested that high rates of cellobiose hydrolysis catalyzed by β-glucosidase may be prolonged by converting the reaction product glucose to fructose using a suitable preparation of glucose isomerase.     

Alleviating product inhibition in cellulase enzyme Cel7A

Enzymes that degrade cellulose into glucose are one of the most expensive components of processes for converting cellulosic biomass to fuels and chemicals. Cellulase enzyme Cel7A is the most abundant enzyme naturally employed by fungi to depolymerize cellulose, and like other cellulases is inhibited by its product, cellobiose. There is thus great economic incentive for minimizing the detrimental effects of product inhibition on Cel7A. In this work, we experimentally generated 10 previously proposed site‐directed mutant Cel7A enzymes expected to have reduced cellobiose binding energies (the majority of mutations were to alanine). We then tested their resilience to cellobiose as well as their hydrolytic activities on microcrystalline cellulose. Although every mutation tested conferred reduced product inhibition (and abolished it for some), our results confirm a trade‐off between Cel7A tolerance to cellobiose and enzymatic activity: Reduced product inhibition was accompanied by lower overall enzymatic activity on crystalline cellulose for the mutants tested. The tempering effect of mutations on inhibition was nearly constant despite relatively large differences in activities of the mutants. Our work identifies an amino acid in the Cel7A product binding site of interest for further mutational studies, and highlights both the challenge and the opportunity of enzyme engineering toward improving product tolerance in Cel7A. Biotechnol. Bioeng. 2016;113: 330–338. © 2015 The Authors. Biotechnology and Bioengineering Published by Wiley Periodicals, Inc.     

Enzymatic hydrolysis of cellulose to glucose lung immobilized β-glucosidase

The production of sugars by enzymatic hydrolysis of cellulose is a multistep process which includes conversion of the intermediate cellobiose to glucose by β-glucosidase. Aside from its role as an intermediate, cellobiose inhibits the endoglucanase components of typical cellulase enzyme systems. Because these enzyme systems often contain insufficient concentrations of β-glucosidase to prevent accumulation of inhibitory cellobiose, this research investigated the use of supplemental immobilized β-glucosidase to increase yield of glucose. Immobilized β-glucosidase from Aspergillus phoenicis was produced by sorption at controlled-pore alumina with about 90% activity retention. The product lost only about 10% of the original activity during an on-stream reaction period of 500 hr with cellobiose as substrate; maximum activity occurred near pH 3.5 and the apparent activation energy was about 11 kcal/mol. The immobilized β-glucosidase was used together with Trichoderma reesei cellulase to hydrolyze cellulosic materials, such as Solka Floc, corn stove and exploded wood. Increased yields of glucose and greater conversions of cellobiose of glucose were observed when the reaction systems contained supplemental immobilized β-glucosidase.     

A mutant β-glucosidase increases the rate of the cellulose enzymatic hydrolysis

The enzymatic hydrolysis of cellulose and lignocellulosic materials is marked by a rate decrease along the reaction time. Cellobiohydrolase slow dissociation from the substrate and its inhibition by the cellobiose produced are relevant factors associated to the rate decrease. In that sense, addition of β-glucosidases to the enzyme cocktails employed in cellulose enzymatic hydrolysis not only produces glucose as final product but also reduces the cellobiohydrolase inhibition by cellobiose. The digestive β-glucosidase GH1 from the fall armyworm Spodoptera frugiperda, hereafter called Sfβgly, containing the mutation L428V showed an increased k_cat for cellobiose hydrolysis. In comparison to assays conducted with the wild-type Sfβgly and cellobiohydrolase TrCel7A, the presence of the mutant L428V increased in 5 fold the initial rate of crystalline cellulose hydrolysis and reduced to one quarter the time needed to TrCel7A produce the maximum glucose yield. As our results show that mutant L428V complement the action of TrCel7A, the introduction of the equivalent replacement in β-glucosidases is a promising strategy to reduce costs in the enzymatic hydrolysis of lignocellulosic materials.     

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.     

Cellotriose Synthesis Using d-Glucose as a Starting Material by Two Step Reactions of Immobilized β-Glucosidases

We tried to polymerize d-glucose to cellotriose, the smallest substrate for β-1,4-glucan synthesis by the β-transglycosylase of Trichoderma longibrachiatum, without participation of high energy compounds such as nucleotide sugars. A commercial β-glucosidase (sweet almond) showed a typical condensation reaction of d-glucose, producing cellobiose when it was entrapped in a visking tube and incubated in 30% d-glucose solution. The reaction was done with immobilized enzyme covalently bound to Polyacrylamide beads, and entrapped enzyme. Cellobiose (21.0 mg) was obtained from 30 g of d-glucose in a 3-day reaction, where 0.29 unit of the entrapped enzyme preparation was incubated with 100 ml of 30% d-glucose at pH 6.0 and 41°C. Gentiobiose was also produced in the mixture as a minor product. The immobilized β-glucosidase (Sumizyme C) preparation covalently bound to Polyacrylamide beads could catalyze a transglucosylation reaction to produce cellotriose from cellobiose in a good yield without production of gentiobiose. The transfer reaction was optimal at pH 4.8 and 30°C. Cellotriose (11.2 mg) was produced from the reaction mixture containing 68 mg of cellobiose and the enzyme preparation (0.1 unit) after 24-hr of incubation at the optimal conditions. Both immobilized β-glucosidases, sweet almond and Sumizyme C, may be used repeatedly without any loss of the initial activity.     

Kinetics and mathematical model of hydrolysis and transglycosylation catalysed by cellobiase

The kinetics of hydrolysis and transglycosylation reactions catalysed by cellobiase (β-d-glucoside glucohydrolase, EC 3.2.1.21) from Aspergillus foetidus in the cellobiose-d-glucose reaction system have been studied. The formation of transglycosylation products was observed at cellobiose concentrations $\text{>10}{}^{\mathrm{?2}}\text{m}$, whereas at lower substrate concentrations the only reaction product was d-glucose. In the cellobiase-catalysed transglycosylation a (1→6)-β-linkage was formed after the transfer of a d-glucose residue to acceptor molecule. The basic transglycosylation products were isocellotriose and gentiobiose. A small amount of oligosaccharides with a higher degree of polymerization was also formed. The maximum content of transglycosylation products amounted to 25–30% of the total saccharide content in the system at the initial cellobiose concentration (0.1–0.3 m). The processes in the reaction system were inhibited by the substrate and product (d-glucose). A general scheme for cellobiose hydrolysis has been proposed and validated, allowing for the inhibition and transglycosylation effects. Based on this scheme, a mathematical model for cellobiose hydrolysis has been suggested to describe the kinetics of substrate consumption and product (d-glucose) accumulation, as well as the kinetics of formation and consumption of transglycosylation products throughout the course of enzymatic reaction with various initial amounts of cellobiose, starting from low concentrations up to 0.2–0.3 m (7–11% bv weight).     

Sophorose induction of an intracellular b-glucosidase in Trichoderma

The disaccharide sophorose induces Trichoderma to increase a solube intracellular b-glucosidase that hydrolyses cellobiose, sophorose, and p-nitrophenyl-b-D-glucopyranoside. Simultaneously, it depresses the activity of a similar insoluble enzyme that is associated with the mycelium. Gel electrophoresis indicates that a single enzyme is responsible for all the soluble intracellular b-glucosidase activity. Cycloheximide severely inhibits sophorose induction of this enzyme indicating that the increase in activity normally obtained with sophorose is due to the de novo formation of the enzyme. The same sugars that promote the formation and release of cellulase by Trichoderma induce an increase in the soluble intracellular b-glucosidase. A function of the soluble intracellular enzyme appears to be the hydrolysis of cellobiose, which would otherwise accumulate during cellulose degradation, and thus to prevent cellobiose inhibition of cellulase.     

Relationship Between Substrate Concentration and Fermentation Product Ratios in Clostridium thermocellum Cultures

Growth of Clostridium thermocellum in batch cultures was studied over a broad range of cellobiose concentrations. Cultures displayed important differences in their substrate metabolism as determined by the end product yields. Bacterial growth was severely limited when the initial cellobiose concentration was 0.2 (wt/vol), was maximal at substrate concentrations between 0.5 and 2.0%, and did not occur at 5.0% cellobiose. Ethanol accumulated maximally (38.3 μmol/10⁹ cells) in cultures with an initial cellobiose concentration of 0.8%, whereas cultures in 2.0% cellobiose accumulated only 17.3 μmol, and substrate-limited cultures (0.2% cellobiose) accumulated little, if any, ethanol beyond that initially detected (8.3 μmol/10⁹ cells). In a medium with 0.8% cellobiose, ethanol was produced at a constant rate of approximately 1.1 μmol/10⁹ cells per h from late-logarithmic phase (16 h) of growth well into stationary phase (44 h). When ethanol was added exogenously at levels more than twice the maximum produced by the cultures themselves (0.5% [vol/vol]), neither the extent of growth (maximum Klett units, 150) nor the amounts of ethanol produced (~0.17%) by the culture was affected. The ratio of ethanol to acetate was highest (2.8) when cells were grown in 0.8% cellobiose and lowest (1.2) when cells were grown in 0.2% cellobiose.