Aqueous phase synthesis of 5-hydroxymethylfurfural from glucose over large pore mesoporous zirconium phosphates: effect of calcination temperature

K Saravanan, KS Park, S Jeon, JW Bae - ACS omega, 2018 - ACS Publications
ACS omega, 2018ACS Publications
For a solid acid-catalyzed dehydration of biomass-derived carbohydrates into useful furan
derivatives, a suitable porous solid acid catalyst having an optimum acidic density and its
strength is required to avoid cascade reactions in biomass conversion processes. A large-
pore mesoporous zirconium phosphate (m-ZrP) was prepared hydrothermally using P123 as
a template in water solvent, which resulted in a higher pore diameter (> 9 nm) having
wormhole-like pore structures with balanced Lewis (L) to Brönsted (B) acid sites. The …
For a solid acid-catalyzed dehydration of biomass-derived carbohydrates into useful furan derivatives, a suitable porous solid acid catalyst having an optimum acidic density and its strength is required to avoid cascade reactions in biomass conversion processes. A large-pore mesoporous zirconium phosphate (m-ZrP) was prepared hydrothermally using P123 as a template in water solvent, which resulted in a higher pore diameter (>9 nm) having wormhole-like pore structures with balanced Lewis (L) to Brönsted (B) acid sites. The effects of calcination temperature (500–800 °C) on the textural, acidic/basic, and structural properties of the m-ZrP with its catalytic performance for glucose dehydration to 5-hydroxymethylfurfural (HMF) were investigated in a pure water media as a green and sustainable alternative solvent. The larger number of L and B acid sites and basic sites with their appropriate strengths were clearly related with a better catalytic performance in terms of glucose conversion and HMF yield. The strong L acid and basic sites in the m-ZrP efficiently promoted the glucose isomerization to fructose, which dehydrated exclusively on the weak B acid sites resulting in a maximum conversion of glucose (83.8%) and HMF yield (46.6%). The adjusted acidic and basic sites with large mesopore sizes make the m-ZrP yield a higher reaction rate (2.78 mmol gcat–1 h–1) and turnover frequency (11.68/h) for conversion of glucose to HMF, which showed higher catalytic activity than those of a small-pore m-ZrP and other mesoporous heterogeneous and homogeneous acid catalysts.
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