Trim dewaxing of distillate fuel
US-2017175015-A1 · Jun 22, 2017 · US
US10669491B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10669491-B2 |
| Application number | US-201615364869-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 30, 2016 |
| Priority date | Dec 21, 2015 |
| Publication date | Jun 2, 2020 |
| Grant date | Jun 2, 2020 |
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Methods are provided for making base metal catalysts with improved activity. After forming catalyst particles based on a support comprising a zeolitic molecular sieve, the catalyst particles can be impregnated with a solution comprising a) metal salts (or other precursors) for a plurality of base metals and b) an organic dispersion agent comprising 2 to 10 carbons. The impregnated support particles can be dried to form a base metal catalyst, and then optionally sulfided to form a sulfided base metal catalyst. The resulting (sulfided) base metal catalyst can have improved activity for cloud point reduction and/or for improved activity for heteroatom removal, relative to a base metal dewaxing catalyst prepared without the use of a dispersion agent.
Opening claim text (preview).
The invention claimed is: 1. A method of forming a dewaxing catalyst, the method comprising: impregnating a support comprising about 30 wt % to about 100 wt % of a zeolitic molecular sieve, based on the total weight of the support, with a solution comprising a Group 6 metal salt, a Group 8-10 non-noble metal salt, and a dispersion agent, the dispersion agent comprising a compound having 2-10 carbon atoms and a carbon atom to oxygen atom ratio of about 0.6 to about 2.0; and drying the impregnated support at a temperature of about 80° C. to about 200° C. to form a dewaxing catalyst. 2. The method of claim 1 , wherein the zeolitic molecular sieve comprises a zeolite. 3. The method of claim 1 , wherein the zeolitic molecular sieve comprises ZSM-48, ZSM-11, a molecular sieve having a 10-member ring as a largest pore channel, or a combination thereof. 4. The method of claim 1 , wherein the Group 8-10 non-noble metal salt comprises an Ni salt, a Co salt, or a combination thereof; and wherein the Group 6 metal salt comprises a Mo salt, a W salt, or a combination thereof. 5. The method of claim 1 , wherein a molar ratio of dispersion agent to total metals in the solution is about 0.1 to about 5.0; or wherein a molar ratio of dispersion agent to Group 8-10 non-noble metal is 0.5 to 10; or a combination thereof. 6. The method of claim 1 , further comprising sulfiding the dried impregnated support under effective sulfiding conditions to form a sulfided dewaxing catalyst, the sulfiding optionally being performed without prior calcining of the dried impregnated support. 7. The method of claim 1 , wherein the dispersion agent comprises a glycol, a carboxylic acid, or a combination thereof. 8. The method of claim 1 , wherein impregnating the support comprising a zeolitic molecular sieve comprises impregnating a support comprising a bound zeolitic molecular sieve, the support optionally comprising an alumina binder. 9. The method of claim 8 , wherein the support comprises a binder having a surface area of about 150 m 2 /g or less. 10. The method of claim 1 , wherein the dispersion agent comprises citric acid, an organic acid having at least 5 carbon atoms, or a combination thereof.
not in framework positions · CPC title
Iron group metals or copper · CPC title
Ion-exchange · CPC title
Oxides · CPC title
containing arsenic, antimony, bismuth, vanadium, niobium tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
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