Method for converting a high-boiling hydrocarbon feedstock into lighter boiling hydrocarbon products
US-2016369185-A1 · Dec 22, 2016 · US
US10898885B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10898885-B2 |
| Application number | US-202016789879-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 13, 2020 |
| Priority date | Apr 11, 2016 |
| Publication date | Jan 26, 2021 |
| Grant date | Jan 26, 2021 |
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According to one or more embodiments described, a zeolite supported catalyst may be synthesized by a process that includes combining a colloidal mixture with a metal oxide support material to form a support precursor material, processing the support precursor material to form a support material, and impregnating the support material with one or more metals to form the zeolite supported catalyst. The colloidal mixture may include nano-sized zeolite crystals, and the nano-sized zeolite crystals may have an average size of less than 100 nm.
Opening claim text (preview).
The invention claimed is: 1. A zeolite supported catalyst suitable for hydrocracking reactions, the zeolite supported catalyst comprising: from 20 wt. % to 75 wt. % of porous alumina; from 20 wt. % to 30 wt. % of metal catalyst material comprising WO 3 ; and from 5 wt. % to 50 wt. % of nano-sized zeolite; where: the nano-sized zeolite has an average size of less than 100 nm; and the zeolite supported catalyst has a surface area of at least 180 m 2 /g. 2. The zeolite supported catalyst of claim 1 , where the zeolite supported catalyst has a pore volume of at least 0.45 mL/g. 3. The zeolite supported catalyst of claim 1 , where the zeolite supported catalyst has a pore size of at least 9.5 nm. 4. The zeolite supported catalyst of claim 1 , where the metal catalyst material further comprises one or more of MoO 3 , NiO, and CoO. 5. The zeolite supported catalyst of claim 1 , where the porous alumina comprises: a small pore size alumina having a pore volume of from 0.4 mL/g to 0.6 mL/g; and a large pore size alumina having a pore volume of from 0.8 mL/g to 1.2 mL/g. 6. The zeolite supported catalyst of claim 5 , comprising: from 15 wt. % to 25 wt. % of the small pore size alumina; and from 10 wt. % to 65 wt. % of the large pore size alumina. 7. The zeolite supported catalyst of claim 1 , where the zeolite support catalyst has a surface area of at least 190 m 2 /g. 8. The zeolite supported catalyst of claim 1 , where the nano-sized zeolite is zeolite A, mordenite, zeolite Y, ZSM-5, or combinations of these.
Cobalt · CPC title
Nickel · CPC title
Molybdenum · CPC title
Tungsten · CPC title
containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
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