Methods and systems for upgrading mixed pyrolysis oil to light aromatics over mixed metal oxide catalysts
US-2024010934-A1 · Jan 11, 2024 · US
US11179703B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11179703-B2 |
| Application number | US-201916958443-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 22, 2019 |
| Priority date | Feb 23, 2018 |
| Publication date | Nov 23, 2021 |
| Grant date | Nov 23, 2021 |
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A catalyst for an oxychlorination process of hydrocarbons, a preparation method thereof, and a method for preparing an oxychlorination compound of hydrocarbons using the same.
Opening claim text (preview).
The invention claimed is: 1. A catalyst for an oxychlorination process of hydrocarbons, the catalyst comprising: a catalyst material comprising (a) copper, (b) a first co-catalyst comprising one or more selected from the group consisting of an alkali metal and an alkaline earth metal, and (c) a second co-catalyst comprising a lanthanide metal; and a carrier comprising cerium oxide. 2. The catalyst of claim 1 , where the catalyst material is present in the catalyst in an amount of 5 wt % to 25 wt % based on a total weight of the catalyst. 3. The catalyst of claim 1 , wherein an amount of the first co-catalyst and an amount of the second co-catalyst is the same as or different from each other, and the amount of the first co-catalyst and the amount of the second co-catalyst are each in an amount of 10 parts by weight to 2,000 parts by weight based on 100 parts by weight of copper. 4. The catalyst of claim 1 , wherein the first co-catalyst comprises one or more selected from the group consisting of sodium, lithium, potassium, magnesium, and calcium. 5. The catalyst of claim 1 , wherein the second co-catalyst further comprises one or more selected from the group consisting of yttria and a rare earth element. 6. The catalyst of claim 1 , wherein the carrier has a specific surface area of 50 m 2 /g to 250 m 2 /g. 7. The catalyst of claim 1 , wherein cerium oxide is present in the carrier in an amount of 80 wt % or more based upon a total 100 wt % of the carrier. 8. The catalyst of claim 1 , wherein the catalyst is in the form of particles having a diameter of 0.1 mm to 1.0 mm. 9. A method for preparing the catalyst for an oxychlorination process of hydrocarbons according to claim 1 , the method comprising: preparing a carrier comprising cerium oxide; and supporting an active material comprising copper, a first co-catalyst, and a second co-catalyst on the carrier. 10. A method for preparing an oxychlorination compound of hydrocarbons, comprising: performing an oxychlorination reaction of hydrocarbons in the presence of the catalyst according to claim 1 . 11. The method of claim 10 , wherein the method is performed under a process temperature of 450° C. to 550° C., a pressure of 0.5 atm to 3 atm, and a space velocity of 2,000 h −1 to 20,000 h 31 1 . 12. The method of claim 10 , wherein the method is performed in a packed bed reactor, a fluidized bed reactor, or a circulating fluidized bed reactor. 13. The catalyst of claim 1 , wherein cerium oxide is present in the carrier in an amount of 90 wt % or more based upon a total 100 wt % of the carrier. 14. The catalyst of claim 1 , wherein cerium oxide is present in the carrier in an amount of 99 wt % or more based upon a total 100 wt % of the carrier. 15. The catalyst of claim 1 , wherein the carrier consists of cerium oxide.
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
X-ray diffraction · CPC title
Scanning electron microscopy; Transmission electron microscopy · CPC title
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
of saturated hydrocarbons · CPC title
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