<p>It is crucial to enlarge the pore size of spherical alumina while maintaining its high mechanical strength. In this work, acrylamide, maleimide and phenol were introduced as cross-linker into Al sol to prepare spherical alumina supports by the oil-drop method. By conducting crosslinking polymerization reactions using these cross-linkers with formaldehyde, the consumption of formaldehyde reduces its evaporation and thereby minimizes the disruption to the pore structure of the spherical alumina prepared by the oil-drop method. As a result, the pore structure of the spherical alumina is optimized from wedge-shaped pores to interconnected pores, with the proportion of pores in the range of 25–40&#xa0;nm increasing by ~ 10% while maintaining strength exceed 60&#xa0;N/P. This pore structure optimization effectively alleviates the reduction in catalytic activity caused by mass transfer limitations, the H<sub>2</sub>O<sub>2</sub> productivity of the Pd/Al<sub>2</sub>O<sub>3</sub>-PH-3% (3% phenol as cross-linker) catalyst increased by 9.3% compared to that of Pd/Al<sub>2</sub>O<sub>3</sub> without cross-linker.</p> Graphical Abstract <p></p>

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Optimization of the Pore Structure of Spherical Alumina by Crosslinking Polymerization Technology

  • Jiale Li,
  • Xingye Lin,
  • Guandong Wu,
  • Xijia Sun,
  • Yufei He,
  • Dianqing Li

摘要

It is crucial to enlarge the pore size of spherical alumina while maintaining its high mechanical strength. In this work, acrylamide, maleimide and phenol were introduced as cross-linker into Al sol to prepare spherical alumina supports by the oil-drop method. By conducting crosslinking polymerization reactions using these cross-linkers with formaldehyde, the consumption of formaldehyde reduces its evaporation and thereby minimizes the disruption to the pore structure of the spherical alumina prepared by the oil-drop method. As a result, the pore structure of the spherical alumina is optimized from wedge-shaped pores to interconnected pores, with the proportion of pores in the range of 25–40 nm increasing by ~ 10% while maintaining strength exceed 60 N/P. This pore structure optimization effectively alleviates the reduction in catalytic activity caused by mass transfer limitations, the H2O2 productivity of the Pd/Al2O3-PH-3% (3% phenol as cross-linker) catalyst increased by 9.3% compared to that of Pd/Al2O3 without cross-linker.

Graphical Abstract