Preparation method for metallic oxide spherical cascade structure
US-2016083263-A1 · Mar 24, 2016 · US
US9017811B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9017811-B2 |
| Application number | US-201213536754-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 28, 2012 |
| Priority date | Jun 29, 2011 |
| Publication date | Apr 28, 2015 |
| Grant date | Apr 28, 2015 |
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A particulate material includes an aluminous material and a silica dopant. The particulate material includes crystallite particles with a crystallite particle size of less than about 10 nm. The crystallite particles are stacked together to form primary particles with a primary particle size of less than about 500 nm. The primary particles are agglomerated together to form secondary particles with a secondary particle size of greater than about 1 μm. The particulate material has a mean pore diameter of not less than 8 nm.
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What is claimed is: 1. A particulate material comprising: an aluminous material; and a silica dopant in an amount of 1.5 wt % to 10 wt % based on the total weight of the particulate material, wherein the particulate material includes crystallite particles with a crystallite particle size of less than about 10 nm, wherein the crystallite particles are stacked together to form primary particles with a primary particle size of less than about 500 nm, wherein the primary particles are agglomerated together to form secondary particles with a secondary particle size from about 1 μm to about 8 μm, and wherein the particulate material has a mean pore diameter of not less than 8 nm and a total pore volume of not less than 0.5 ml/g. 2. The particulate material of claim 1 , wherein the primary particles include rod-shaped particles. 3. The particulate material of claim 2 , wherein the rod-shaped particles have a primary aspect ratio of greater than about 2:1. 4. The particulate material of claim 1 , wherein the aluminous material comprises hydrated alumina. 5. The particulate material of claim 1 , wherein the aluminous material comprises non-hydrated alumina. 6. The particulate material of claim 1 , wherein an average particle size of the silica dopant is less than about 20 nm. 7. The particulate material of claim 1 , wherein a ratio of the aluminous material to the silica dopant is greater than about 93:7 by weight. 8. The particulate material of claim 1 , wherein the particulate material has a Hydrothermal Stability Index of not more than 25 percent, wherein the Hydrothermal Stability Index represents a change in a specific surface area of the particulate material after calcining at a temperature of about 650° C. for a time period of 3 hours and performing a hydrothermal heat treatment at a temperature of about 220° C. for a time period of 16 hours. 9. The particulate material of claim 1 , wherein the particulate material has an Acid Resistance Index of less than 15 ppm/m 2 , wherein the Acid Resistance Index represents alumina that is dissolved after calcining at a temperature of about 650° C. for a time period of 3 hours and performing an acid treatment on the particulate material at a pH of about 2 for 25 hours. 10. A method comprising: providing a precursor material, seeds, and a silica dopant in a suspension; and forming a particulate material that includes an aluminous material and the silica dopant, the silica dopant being present in an amount of 1.5 wt % to 10 wt % based on the total weight of the particulate material, wherein forming the particulate material includes hydrothermal treating of the suspension, wherein the particulate material includes crystallite particles with a crystallite particle size of less than about 10 nm, wherein the crystallite particles are stacked together to form primary particles with a primary particle size of less than about 500 nm, and wherein the primary particles are agglomerated together to form secondary particles with a secondary particle size from about 1 μm to about 8 μm, and wherein the particulate material has a mean pore diameter of not less than 8 nm and a total pore volume of not less than 0.5 ml/g. 11. The method of claim 10 , wherein forming the particulate material further comprises: drying the suspension after heat treating the suspension to form a dried gel; and crushing the dried gel. 12. The method of claim 10 , wherein the aluminous material comprises boehmite. 13. The method of claim 10 , wherein the aluminous material comprises gamma alumina. 14. The particulate material of claim 6 , wherein an average particle size of the silica dopant is less than about 12 nm. 15. The particulate material of claim 1 , wherein the particulate material has a specific surface area of not less than 150 m 2 /g. 16. The particulate material of claim 1 , wherein at least 90% of a total pore volume of the particulate material is between 10 nm and 50 nm. 17. The particulate material of claim 4 , wherein the hydrated alumina comprises boehmite. 18. The particulate material of claim 5 , wherein the non-hydrated alumina comprises gamma alumina. 19. The particulate material of claim 2 , wherein the rod-shaped particles are arranged in form of spherical grains.
Cylinders or rings · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
Compounds characterised by their crystallite size · CPC title
Spheres · CPC title
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
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