Processes for converting biomass-derived feedstocks to chemicals and liquid fuels
US-9382185-B2 · Jul 5, 2016 · US
US10384196B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10384196-B2 |
| Application number | US-201514979721-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 28, 2015 |
| Priority date | Dec 26, 2014 |
| Publication date | Aug 20, 2019 |
| Grant date | Aug 20, 2019 |
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The invention relates to isomerization catalysts and can be used in the petroleum processing and petrochemical industry. The catalyst contains sulfated zirconium oxide and a binder—aluminum oxide in a ratio of ZrO2/SO4 to Al2O3 from 70 to 30 to 90 to 10, as well as promoter, a group II metal, Ca, in a quantity ranging from 0.01 to 1 wt % of the weight of the catalyst. The catalyst also contains platinum and/or palladium in a quantity ranging from 0.1 to 0.45 wt % of the metal. Isomerization of C4-C7 paraffinic hydrocarbons in the presence of hydrogen at a temperature of 110-200° C., a pressure of 1-5 MPa, a hydrogen:hydrocarbon ratio of 0.5-4, and a feedstock space velocity of 0.5-4 h −1 is carried out on a catalyst having the claimed composition. The proposed catalyst offers an enhanced degree of isomerization, improved selectivity of the process, and increased strength of the granules.
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What is claimed is: 1. An isomerization catalyst for C4-C7 paraffinic hydrocarbons, the catalyst comprising a sulfated zirconium oxide, an inorganic oxide as a binder, a group VIII metal as a hydrogenating component, and a group II metal as a promoter, the catalyst being made at least by mixing powders of a sulfated zirconium hydroxide and an inorganic oxide and/or hydroxide binder, a solution of a group II metal inorganic salt, and a nitric acid and sulfuric acid solution, wherein the content of the group II metal promoter in the isomerization catalyst is greater than 0.5 wt. % and less than 1 wt. %. 2. The catalyst according to claim 1 , wherein the group II metal used as the promoter is calcium added in a form of calcium chloride and/or nitrate. 3. The catalyst according to claim 1 , wherein an aluminum oxide and/or hydroxide is used as a binder, wherein a ratio of the sulfated zirconium oxide to the aluminum oxide in the isomerization catalyst ranges from 7:3 up to 9:1. 4. The catalyst according to claim 1 , wherein platinum and/or palladium in an amount of 0.1-0.45 wt % are used as the group VIII metal. 5. The catalyst according to claim 1 , wherein the content of sulfate ions in the zirconium oxide is no less than 5% of a calcined material. 6. The catalyst according to claim 1 , wherein the catalyst provides a selectivity to an isomerizate greater than that of a catalyst comprising no group II metal promoter. 7. The catalyst according to claim 1 , wherein the catalyst exhibits a strength of catalyst granules greater than that of a catalyst comprising no group II metal promoter.
Sulfates · CPC title
Alumina · CPC title
Platinum · CPC title
Alkanes · CPC title
Impregnation · CPC title
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