路易斯酸
异构化
产量(工程)
化学
材料科学
布朗斯特德-洛瑞酸碱理论
果糖
选择性
吸附
催化作用
D-葡萄糖
解吸
酸强度
核化学
无机化学
有机化学
沸石
冶金
作者
Yuan Zhang,Jiangang Wang,Jinghua Wang,Yong Wang,Ming Wang,Hongyou Cui,Feng Song,Xiuyu Sun,Yujiao Xie,Weiming Yi
标识
DOI:10.1002/slct.201901084
摘要
Abstract Sulfonated carbons with hierarchically ordered pores (SCHOP) are not effective catalysts for glucose to 5‐hydroxymethylfurfural (5‐HMF) although they are very effective for fructose conversion due to insufficient and unsuitable Lewis acid sites in SCHOP unfavorable for isomerization of glucose to fructose. This paper attempts to intensify the Lewis acid sites on the surface of SCHOP by doping Al 2 O 3 and TiO 2 (Al−Ti@SCHOP) so as to promote glucose conversion to 5‐HMF. Characterizations by SEM, TEM, BET and N 2 adsorption‐desorption showed that the well‐ordered hierarchical pore structure of SCHOP was preserved after doping the metal oxides. EDS and XRD analyses confirmed that Al 2 O 3 and TiO 2 were well‐dispersed on the surface. FTIR, Py‐FTIR and NH 3 ‐TPD proved that not only sulfonic acid groups were introduced successfully but also very strong acid sites were formed. Furthermore, the strength of Lewis and Brönsted acid sites on the surface of Al−Ti@SCHOP were tailored by adjusting the mass ratio of Al 2 O 3 to TiO 2 . Al−Ti@SCHOP with an Al 2 O 3 /TiO 2 mass ratio of 2:1 demonstrated the highest catalytic activity for glucose dehydration to 5‐HMF. As high as above 96% of 5‐HMF selectivity could be obtained within the initial reaction time of 3.0 h, and a maximum 5‐HMF yield of 57.36% occurred at the reaction time of 5.0 h when reacting at 130 °C. Besides, the catalyst has its good stability.
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