Hydrocarbon dehydrocyclization
US-9815749-B2 · Nov 14, 2017 · US
US9545622B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9545622-B2 |
| Application number | US-201113821957-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 20, 2011 |
| Priority date | Oct 11, 2010 |
| Publication date | Jan 17, 2017 |
| Grant date | Jan 17, 2017 |
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A hydroalkylation catalyst comprising a molecular sieve and a compound of a hydrogenation metal is activated by treating the catalyst at a temperature of less than about 250° C. in the presence of hydrogen.
Opening claim text (preview).
The invention claimed is: 1. A process comprising: (a) providing a hydroalkylation catalyst comprising an MCM-22 family molecular sieve and a compound of a hydrogenation metal selected from palladium, ruthenium, nickel, zinc, tin, cobalt and mixtures thereof; and (b) activating the hydroalkylation catalyst in the presence of hydrogen and a liquid phase diluent comprising an aromatic compound to provide for a reduction of the compound of the hydrogenation metal; wherein the majority of the activation step (b), based on activation time, occurs at temperatures below 250° C. 2. The process of claim 1 , wherein substantially the entire activation step (b), based on activation time, occurs at temperatures below 200° C. 3. The process of claim 1 , wherein the majority of the activation step (b), based on activation time, occurs at temperatures greater than 25° C. 4. The process of claim 1 , further comprising: (c) reducing the water content of the hydroalkylation catalyst prior to activating step (b). 5. The process of claim 1 , wherein the activating step (b) is conducted in situ. 6. The process of claim 1 , wherein the activating step (b) is conducted for at least 1 hour. 7. The process of claim 1 , wherein the activating step (b) is conducted for at least 5 hours. 8. The process of claim 1 , wherein the majority of the activation step (b), based on activation time, occurs at temperatures between 0° C. and 200° C. 9. The process of claim 1 , wherein the majority of the activation step (b), based on activation time, occurs at temperatures between about 0° C. and about 150° C. 10. The process of claim 1 , wherein the activating step (b) is conducted at a pressure of about 0 to about 4000 kPa, gauge. 11. The process of claim 1 , wherein the diluent comprises benzene. 12. The process of claim 1 , wherein the hydrogenation metal comprises palladium. 13. A process for activating a hydroalkylation catalyst, the process comprising: (a) providing a hydroalkylation catalyst comprising an MCM-22 family molecular sieve and a compound of a hydrogenation metal selected from palladium, ruthenium, nickel, zinc, tin cobalt, and mixtures thereof; (b) reducing the moisture of the hydroalkylation catalyst; and (c) activating the hydroalkylation catalyst in the presence of hydrogen and in the presence of a liquid phase diluent comprising an aromatic compound to provide for a reduction of the compound of the hydrogenation metal wherein the hydrogen at least partially dissolves in the liquid phase diluent; wherein the majority of the activation step (c), based on activation time, occurs at temperatures of below 250° C.
Special temperature treatment, i.e. other than just for template removal · CPC title
using catalysts, e.g. selective catalysts · CPC title
Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof · CPC title
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Noble metals · CPC title
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