Abstract

Cellulose saccharification to glucose is an operation of paramount importance in the bioenergy sector and the chemical and food industries, while glucose is a critical platform chemical in the integrated biorefinery. Among the cellulose degrading enzymes, β-glucosidases are responsible for cellobiose hydrolysis, the final step in cellulose saccharification, which is usually the critical bottleneck for the whole cellulose saccharification process. The design of very active and stable β-glucosidase-based biocatalysts is a key strategy to implement an efficient saccharification process. Enzyme immobilization and reaction engineering are two fundamental tools for its understanding and implementation. Here, we have designed an immobilized-stabilized solid-supported β-glucosidase based on the glyoxyl immobilization chemistry applied in porous solid particles. The biocatalyst was stable at operational temperature and highly active, which allowed us to implement 25 °C as working temperature with a catalyst productivity of 109 mmol/min/gsupport. Cellobiose degradation was implemented in discontinuous stirred tank reactors, following which a simplified kinetic model was applied to assess the process limitations due to substrate and product inhibition. Finally, the reactive process was driven in a continuous flow fixed-bed reactor, achieving reaction intensification under mild operation conditions, reaching full cellobiose conversion of 34 g/L in a reaction time span of 20 min.

Highlights

  • We find in nature β-glucosidases that are devoid of the classical cellulose binding domain (CBM) typical in exoglucanases for example, but others have this binding domain [7], suggesting that they can immobilized near the source of cellobiose and cellooligosaccharides of low molecular weight that are their substrates [8] while possibly benefitting from the stabilizing environment created by the confinement near the surface of the reacting solid substrate [9,10]

  • Thecharacteristic characteristicreaction reactiontime timeisis time given by the ratio of substrate concentration and Vmax and it indicates the minimum time given by the ratio of substrate concentration and Vmax and it indicates the minimum time to reach 100% of conversion if enzyme kinetic would respond to zero order of reaction to reach 100% of conversion if enzyme kinetic would respond to zero order of reaction (KM very low)

  • The methodology of multipoint covalent immobilization on glyoxyl activated supports showed a superior performance in terms of catalyst productivity and operational stability

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Summary

Introduction

While global demand for energy and material resources is increasing, the environmental impact due to the extraction, transport, transformation, and use of fossil resources poses a critical challenge to humanity, affecting our environment even at global scale. Pretreatments based on heat, mechanical forces, acid, and basis reagents and/or solvents are needed to attain the adequate accessibility and reactivity of the target solid substrate, rich in cellulose. Such cellulose will be the target for the action of depolymerising (endo- and exoglucanases and lytic polysaccharide monooxygenases -LPMOs-) and saccharifying enzymes (β-glucosidases), aided by other hydrolases acting on remaining hemicellulose and pectin, and other proteins disrupting the crystal structure of cellulose (swollenins, expansins) [5,6]

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