Leigh Murphy

A kinetic model for the burst phase of processive cellulases

Cellobiohydrolases (exocellulases) hydrolyze cellulose processively, i.e. by sequential cleaving of soluble sugars from one end of a cellulose strand. Their activity generally shows an initial burst, followed by a pronounced slowdown, even when substrate is abundant and product accumulation is negligible. Here, we propose an explicit kinetic model for this behavior, which uses classical burst phase theory as the starting point. The model is tested against calorimetric measurements of the activity of the cellobiohydrolase Cel7A from Trichodermau2003reesei on amorphous cellulose. A simple version of the model, which can be solved analytically, shows that the burst and slowdown can be explained by the relative rates of the sequential reactions in the hydrolysis process and the occurrence of obstacles for the processive movement along the cellulose strand. More specifically, the maximum enzyme activity reflects a balance between a rapid processive movement, on the one hand, and a slow release of enzyme which is stalled by obstacles, on the other. This model only partially accounts for the experimental data, and we therefore also test a modified version that takes into account random enzyme inactivation. This approach generally accounts well for the initial time course (approximately 1u2003h) of the hydrolysis. We suggest that the models will be useful in attempts to rationalize the initial kinetics of processive cellulases, and demonstrate their application to some open questions, including the effect of repeated enzyme dosages and the ‘double exponential decay’ in the rate of cellulolysis.

Product inhibition of five Hypocrea jecorina cellulases.

Product inhibition of cellulolytic enzymes has been deemed a critical factor in the industrial saccharification of cellulosic biomass. Several investigations have addressed this problem using crude enzyme preparations or commercial (mixed) cellulase products, but quantitative information on individual cellulases hydrolyzing insoluble cellulose remains insufficient. Such knowledge is necessary to pinpoint and quantify inhibitory weak-links in cellulose hydrolysis, but has proven challenging to come by. Here we show that product inhibition of mono-component cellulases hydrolyzing unmodified cellulose may be monitored by calorimetry. The key advantage of this approach is that it directly measures the rate of hydrolysis while being essentially blind to the background of added product. We investigated the five major cellulases from Hypocrea jecorina (anamorph: Tricoderma reesei), Cel7A (formerly CBH1), Cel6A (CBH2), Cel7B (EG1), Cel5A (EG2) and Cel12A (EG3), for their sensitivity to the products glucose and cellobiose. The strongest inhibition was found for Cel7A, which showed a 50% activity-loss in 19 mM cellobiose (IC(50)=19 mM). The other exoglucanase, Cel6A, was much less inhibited by cellobiose, but showed the highest sensitivity to glucose among all investigated enzymes. The endoglucanases Cel12A and Cel7B were moderately inhibited by cellobiose (IC(50)=60-80 mM), and weakly inhibited by glucose (IC(50)=350-380 mM). The highest resistance to both products was found for Cel5A, which retained about 75% of its activity at the highest investigated concentrations (respectively 65 mM cellobiose and 1000 mM glucose).

An enzymatic signal amplification system for calorimetric studies of cellobiohydrolases

The study of cellulolytic enzymes has traditionally been carried out using endpoint measurements by quantitation of reaction products using high-performance liquid chromatography (HPLC) or overall determination of produced reducing ends. To measure catalytic activity, model substrates such as solubilized cellulose derivates, soluble chromogenic, and fluorogenic oligomeric substrates are often employed even though they do not reflect the natural insoluble substrate hydrolysis. Thermochemical methods using, for example, isothermal titration calorimetry (ITC) yield data where the primary observable is heat production. This can be converted to the rate of reaction and allows direct and continuous monitoring of the hydrolysis of complex substrates. To overcome the low molar enthalpy of the hydrolysis of the glycosidic bond, which is typically on the order of -2.5 kJ mol(-1), an enzymatic signal amplification method has been developed to measure even slow hydrolytically active enzymes such as cellobiohydrolases. This method is explained in detail for the amplification of the heat signal by more than 130 times by using glucose oxidase and catalase. The kinetics of this complex coupled reaction system is thoroughly investigated, and the potential use to generate kinetic models of enzymatic hydrolysis of unmodified cellulosic substrates is demonstrated.

Effects of non-ionic surfactants on the interactions between cellulases and tannic acid: A model system for cellulase–poly-phenol interactions

Addition of non-ionic surfactants (NIS) is known to accelerate enzymatic lignocellulose hydrolysis. The mechanism behind this accelerating effect is still not elucidated but has been hypothesized to originate from favorable NIS-lignin interactions which alleviate non-productive adsorption of cellulases to lignin. In the current work we address this hypothesis using tannic acid (TAN) as a general poly-phenolic model compound (for lignin and soluble phenolics) and measure the mutual interactions of cellulases (CBHI, CBHII, EGI, EGII and BG), TAN and NIS (Triton X-100) using isothermal titration calorimetry (ITC). The experimental results suggest rather strong enzyme-specific interactions with TAN in reasonable agreement with enzyme specific lignin inhibition found in the literature. Enzyme-TAN interactions were disrupted by the presence of NIS by a mechanism of strong TAN-NIS interaction. The presence of NIS also alleviated the inhibitory effect of TAN on cellulase activity. All together the current work provides strong indications that favorable NIS-poly-phenol interactions alleviate non-productive cellulase-poly-phenol interactions and hence may provide a mechanism for the accelerating effect of NIS on lignocellulose hydrolysis.

Advantages of isothermal titration calorimetry for xylanase kinetics in comparison to chemical-reducing-end assays

In lignocellulosic raw materials for biomass conversion, hemicelluloses constitute a substantial fraction, with xylan being the primary part. Although many pretreatments reduce the amount or change the distribution of xylan, it is important to degrade residual xylan so as to improve the overall yield. Typically, xylanase reaction rates are measured in stopped assays by chemical quantification of the reducing ends. With isothermal titration calorimetry (ITC), the heat flow of the hydrolysis can be measured in continuous fashion, with the reaction rate being directly proportional to the heat flow. Reaction enthalpies for carbohydrate hydrolysis are typically below 5kJ/mol, which is the limiting factor for straight forward calorimetric quantification of enzymatic reaction rates using current ITC technology. To increase the apparent reaction enthalpy, we employed a subsequent oxidation of hydrolysis products by carbohydrate oxidase and catalase. Here we show that the coupled assay with carbohydrate oxidase and catalase can be used to measure enzyme kinetics of a GH10 xylanase from Aspergillus aculeatus on birch xylan and wheat arabinoxylan. Results are discussed in the light of a critical analysis of the sensitivity of four chemical-reducing-end quantification methods using well-characterized substrates.