Composite body in which first metal-containing particles and second metal-containing particles are supported on carbon material or connected by carbon material, and method for producing same
US-2015298114-A1 · Oct 22, 2015 · US
US10105685B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10105685-B2 |
| Application number | US-201615138966-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 26, 2016 |
| Priority date | Oct 22, 2015 |
| Publication date | Oct 23, 2018 |
| Grant date | Oct 23, 2018 |
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Provided are particle size-controlled, chromium oxide particles or composite particles of iron oxide-chromium alloy and chromium oxide; a preparation method thereof; and use thereof, in which the chromium oxide particles or the composite particles of iron oxide-chromium alloy and chromium oxide having a desired particle size are prepared in a simpler and more efficient manner by using porous carbon material particles having a large pore volume as a sacrificial template. When the chromium oxide particles or the composite particles of iron oxide-chromium alloy and chromium oxide thus obtained are applied to gas-phase and liquid-phase catalytic reactions, they are advantageous in terms of diffusion of reactants due to particle uniformity, high-temperature stability may be obtained, and excellent reaction results may be obtained under severe reaction environment.
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What is claimed is: 1. A method of preparing particle size-controlled chromium oxide particles, the method comprising: Step 1a of preparing porous carbon material particles having a pore volume of 0.3 cm3/g or more; Step 2a of mixing a chromium hydrate salt and the porous carbon material particles; Step 3a of melt-infiltrating the chromium hydrate salt into pores of the porous carbon material particles at a temperature, at which the chromium hydrate salt is melted; and Step 4a of calcining the chromium hydrate salt and the porous carbon material at a high temperature of 700 to 900° C. to form chromium oxide particles, of which particle size is controlled by the pores of the porous carbon material, and also completely removing the porous carbon material by pyrolysis to remain particle size-controlled chromium oxide particles. 2. The method of claim 1 , wherein a coefficient of variation (CV) of the particle size of the chromium oxide particles is 0.3 or less. 3. The method of claim 1 , wherein an average pore size of the porous carbon material particle in Step 1a is 2 nm to 50 nm. 4. The method of claim 1 , wherein an average particle size of the porous carbon material particles in Step 1a is 200 nm˜0.2 cm. 5. The method of claim 1 , wherein the chromium hydrate salt has a melting point of 30° C.˜100° C. 6. The method of claim 1 , wherein the porous carbon material is activated carbon, activated charcoal, a synthetic porous carbon support (CMK), or a combination thereof. 7. The method of claim 1 , wherein the chromium hydrate salt is melt-infiltrated in an amount of 0.3˜3 gram per unit gram (g) of carbon. 8. The method of claim 1 , wherein the mixing of Step 2a is performed after mechanical grinding. 9. The method of claim 1 , wherein in Step 4a, an average particle size of the chromium oxide particle is 10 nm˜50 nm.
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