Kai Huang , Taoli Huhe , Haichao Liu , Da-Ming Gao , Yao Zhai
{"title":"Synthesis of hierarchically porous tantalum phosphate catalysts by a sol–gel method for transformation of glucose to 5-hydroxymethylfurfural","authors":"Kai Huang , Taoli Huhe , Haichao Liu , Da-Ming Gao , Yao Zhai","doi":"10.1039/d4cy01112k","DOIUrl":null,"url":null,"abstract":"<div><div>A hierarchically porous and highly effective tantalum phosphate (TaP) solid acidic catalyst was synthesized using a sol–gel method accompanied by phase separation for converting glucose to 5-hydroxymethylfurfural (HMF). The TaP sample formed the TaPO<sub>5</sub> phase after calcining at 600 °C (TaP-600) for 4 hours with a surface area of <em>ca.</em> 103 m<sup>2</sup> g<sup>−1</sup> and an acidity of <em>ca.</em> 0.18 mmol<sub>NH<sub>3</sub></sub> g<sup>−1</sup>. The TaP-600 sample had a co-continuous macroporous structure with a regular and orderly pore arrangement, which was conducive to the diffusion of reactants and products, thereby reducing side reactions. The TaP-600 sample can afford an HMF yield of 25.6% by treating with 1.0 wt% glucose at 170 °C in pure water. Using a water–DMSO homogeneous system or a water/MIBK biphasic reaction system can protect HMF from further decomposition, obtaining a HMF yield of 63.8% and 67.1% (mol mol<sup>−1</sup>), respectively. The TaP-600 sample also showed high catalytic performance at high glucose concentration in the water/MIBK system, <em>e.g.</em> the HMF yields reached 27.5% and 23.7% at glucose concentrations of 15.0 wt% and 20.0 wt%, respectively. The productivity of HMF reached 6.6 × 10<sup>−2</sup> mol h<sup>−1</sup> kg<sub>solution</sub><sup>−1</sup> at an initial glucose concentration of 20.0 wt% in the water/MIBK biphasic system with a catalyst loading (weight ratio of catalyst to glucose) of 10.0 wt%. The TaP-600 sample can retain most of its activity after three catalytic cycles giving an HMF yield of 17.9%. These results demonstrate the significant potential of TaP for industrial-scale HMF production.</div></div>","PeriodicalId":66,"journal":{"name":"Catalysis Science & Technology","volume":"15 5","pages":"Pages 1567-1580"},"PeriodicalIF":4.4000,"publicationDate":"2025-01-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Catalysis Science & Technology","FirstCategoryId":"92","ListUrlMain":"https://www.sciencedirect.com/org/science/article/pii/S2044475325000450","RegionNum":3,"RegionCategory":"化学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"CHEMISTRY, PHYSICAL","Score":null,"Total":0}
引用次数: 0
Abstract
A hierarchically porous and highly effective tantalum phosphate (TaP) solid acidic catalyst was synthesized using a sol–gel method accompanied by phase separation for converting glucose to 5-hydroxymethylfurfural (HMF). The TaP sample formed the TaPO5 phase after calcining at 600 °C (TaP-600) for 4 hours with a surface area of ca. 103 m2 g−1 and an acidity of ca. 0.18 mmolNH3 g−1. The TaP-600 sample had a co-continuous macroporous structure with a regular and orderly pore arrangement, which was conducive to the diffusion of reactants and products, thereby reducing side reactions. The TaP-600 sample can afford an HMF yield of 25.6% by treating with 1.0 wt% glucose at 170 °C in pure water. Using a water–DMSO homogeneous system or a water/MIBK biphasic reaction system can protect HMF from further decomposition, obtaining a HMF yield of 63.8% and 67.1% (mol mol−1), respectively. The TaP-600 sample also showed high catalytic performance at high glucose concentration in the water/MIBK system, e.g. the HMF yields reached 27.5% and 23.7% at glucose concentrations of 15.0 wt% and 20.0 wt%, respectively. The productivity of HMF reached 6.6 × 10−2 mol h−1 kgsolution−1 at an initial glucose concentration of 20.0 wt% in the water/MIBK biphasic system with a catalyst loading (weight ratio of catalyst to glucose) of 10.0 wt%. The TaP-600 sample can retain most of its activity after three catalytic cycles giving an HMF yield of 17.9%. These results demonstrate the significant potential of TaP for industrial-scale HMF production.
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