Abstract

The mechanism of glucose isomerization to fructose catalyzed by Lewis acidic Sn sites in the framework of MOR, BEA, MFI and MWW zeolites was investigated by periodic DFT calculations. The main focus was on the influence of the nature of the active site and the zeolite topology on the rate-controlling hydride shift step. A general finding is that the Sn-catalyzed isomerization of glucose is strongly promoted by proximate hydroxyl groups. These hydroxyl groups can derive from co-adsorbed water molecules or internal silanols. The cooperative action of such proton donors with the Lewis acidic Sn sites results in more effective compensation of the negative charge developing on the O1 atom of glucose during the rate-controlling hydride shift reaction step. The variation in the shape of the micropores with a zeolite topology affects the mode and strength of carbohydrate adsorption, which is dominated by van der Waals forces. Their influence on the intrinsic reactivity of intrazeolite Sn sites is small. We propose that higher glucose adsorption energy in the narrower micropores of 10-membered ring zeolites (e.g., Sn-MFI and Sn-MWW) adversely affects the intrachannel diffusion compared to that in the zeolites with larger pores. The high catalytic performance of Sn-MWW towards glucose transformation is due to the lower barrier for the hydride shift step resulting from the presence of a relatively strong acidic bridging silanol group next to the Lewis acidic Sn site.

Highlights

  • The industrial process for fructose production utilizes D-glucose/xylose isomerase enzyme for the conversion of glucose.[17]

  • Earlier mechanistic studies evidence that the rate-controlling step in the glucose to fructose isomerization reaction is the hydride shift (H-shift) between the C1 and C2 atoms of the anionic acyclic glucose (o-Glu) intermediate coordinated to a lattice Sn site.[30,38,45]

  • Assuming that the initial sugar activation step by SnOH is a facile process,[38] we focus on analysing the effect of zeolite topology and local geometry of the active site on the important H-shift step

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Summary

Introduction

The industrial process for fructose production utilizes D-glucose/xylose isomerase enzyme for the conversion of glucose.[17]. An important challenge is to develop chemocatalysts for aldose–ketose isomerization.[18] Among different homogeneous[19,20,21,22,23] and heterogeneous[24,25,26,27,28] catalysts developed so far, the Lewis acidic large-pore zeolite Sn-BEA is active in selective glucose conversion.[9,29,30,31,32,33] Sn-BEA offers the possibility of converting glucose with high selectivity to lactic acid,[32,33] while its good isomerization activity can be used in combination with mineral acids to convert glucose into HMF.[9]. They have been successfully employed to understand better the mechanisms of the

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