Methods of catalytic hydrogenation for ethylene glycol formation
US-2015375209-A1 · Dec 31, 2015 · US
US10137440B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10137440-B2 |
| Application number | US-201514983849-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 30, 2015 |
| Priority date | Jul 29, 2015 |
| Publication date | Nov 27, 2018 |
| Grant date | Nov 27, 2018 |
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The present invention relates to a core-shell cobalt catalyst used for a Fischer-Tropsch synthesis reaction and a method for preparing the same. More particularly, it relates to a cobalt catalyst, which has a core-shell structure including a cobalt-supported and sintered alumina particle as a core and a zeolite powder coated on the surface of the alumina particle to a thickness of 50 μm or greater through mechanical alloying as a shell and is used to prepare hydrocarbons with high octane numbers through a Fischer-Tropsch synthesis reaction, and a method for preparing the same.
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What is claimed is: 1. A core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction, which comprises a core composed of a spherical, cobalt-supported and sintered alumina particle having a diameter of 1-5 mm; a shell composed of a zeolite powder having a SiO2/Al2O3 molar ratio of 5-40 coated on the surface of the core to a thickness of 50-300 μm through a mechanical alloying process; and a bimodal porous structure with the core having mesopores with an average pore size of 10.5-21.1 nm and a pore volume of 0.18-0.37 cm 3 /g, and the shell having micropores with an average pore size of 0.6-0.82 nm and with a pore volume of 0.057-0.116 cm 3 /g. 2. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 1 , wherein the alumina particle constituting the core is an α- or γ-alumina particle. 3. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 1 , wherein the zeolite powder coated through the mechanical alloying process is ZSM-5 zeolite. 4. A core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction, which comprises: a spherical, cobalt-supported and sintered alumina particle having a diameter of 1-5 mm as a core; a zeolite powder having a SiO2/Al2O3 molar ratio of 5-40 coated on the surface of the core to a thickness of 50-300 μm through a mechanical alloying process as a shell; and a bimodal porous structure with the core having mesopores with an average pore size of 10.5-21.1 nm and the shell having micropores with an average pore size of 0.6-0.82 nm. 5. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 4 , wherein the core comprises a cobalt active metal infiltrated in the core at an amount of 2-20 wt % with respect to the amount of alumina support in the core. 6. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 4 , wherein the core comprises a cobalt active metal infiltrated in the core at an amount of 5-10 wt % with respect to the amount of alumina support in the core. 7. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 4 , wherein core having mesopores with a pore volume of 0.18-0.37 cm 3 /g. 8. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 4 , wherein shell having micropores with a pore volume of 0.057-0.116 cm 3 /g. 9. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 4 , wherein core having a specific surface area of 47-163 m 2 /g. 10. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 4 , wherein shell having a specific surface area of 173-251 m 2 /g. 11. A core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction, which comprises a core composed of a spherical cobalt-supported sintered alumina particle; a shell from zeolite powder having a SiO2/Al2O3 molar ratio of 5-40 coated on the surface of the core to a thickness of 50-300 μm; and a bimodal porous structure with the core having mesopores with an average pore size of 10.5-21.1 nm and the core having a specific surface area of 47-163 m 2 /g, and the shell having micropores with an average pore size of 0.6-0.82 nm and the shell having a specific surface area of 173-251 m 2 /g. 12. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 11 , wherein the zeolite powder is ZSM-5 zeolite. 13. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 11 , wherein the alumina particle of the core is an α- or γ-alumina particle. 14. The core-shell cobalt catalyst for a Fischer-Tropsch synthesis reaction according to claim 11 wherein the zeolite powder has a SiO2/Al2O3 molar ratio of 5-40 and is coated on the surface of the core to a thickness of 50-300 μm through a mechanical alloying process.
Iron group metals or copper · CPC title
Operations & Transport · mapped topic
Operations & Transport · mapped topic
Operations & Transport · mapped topic
Iron group metals or copper · CPC title
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