Catalyst composition and isomerisation process
US-2018369797-A1 · Dec 27, 2018 · US
US9309170B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9309170-B2 |
| Application number | US-201213649546-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 11, 2012 |
| Priority date | Nov 14, 2011 |
| Publication date | Apr 12, 2016 |
| Grant date | Apr 12, 2016 |
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This invention is drawn to a process for isomerizing a non-equilibrium mixture of xylenes and ethylbenzene which contain a substantial concentration of nonaromatics using a catalyst system which features the ability to both convert nonaromatics and to obtain an improved yield of para-xylene from the mixture relative to processes of the known art.
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The invention claimed is: 1. A process for the conversion of a hydrocarbon feed mixture comprising a major concentration of nonequilibrium C 8 aromatics and a minor concentration of nonaromatics by contacting the mixture with a dual-catalyst system comprising a first catalyst consisting of a tungsten component and a second catalyst comprising from about 0.01 to about 0.2 mass-% on an elemental basis of at least one platinum-group metal component at hydrocarbon-conversion conditions comprising a temperature of about 300° to about 550° C., a pressure of about 100 kPa to 5 MPa and a liquid hourly space velocity of about 0.5 to 50 hr −1 with respect to the dual-catalyst system to obtain a converted product comprising a reduced concentration of ethylbenzene and a reduced concentration of nonaromatics than in the feed mixture. 2. The process of claim 1 wherein the concentration of nonaromatics is from about 0.5 to 10 mass-% of the feed mixture. 3. The process of claim 1 wherein the first catalyst comprises a layered sphere. 4. The process of claim 1 wherein the first and second catalysts are stacked sequentially. 5. The process of claim 1 wherein the catalyst system is a physical mixture of the first and second catalyst. 6. The process of claim 1 wherein the first and second catalysts are contained on the same catalyst particle. 7. The process of claim 6 wherein the first catalyst comprises a layer on the surface of the second catalyst. 8. A process for the conversion of a hydrocarbon feed mixture comprising a major concentration of nonequilibrium C 8 aromatics and a minor concentration of nonaromatics by contacting the mixture with a dual-catalyst system comprising a first catalyst consisting of a tungsten component and a second catalyst comprising from about 0.01 to about 0.2 mass-% on an elemental basis of at least one platinum-group metal component at hydrocarbon-conversion conditions comprising a temperature of about 300° to about 550° C., a pressure of about 100 kPa to 5 MPa and a liquid hourly space velocity of about 0.5 to 50 hr −1 with respect to the dual-catalyst system to obtain a converted product comprising a higher proportion of at least one xylene isomer, a reduced concentration of ethylbenzene and a reduced concentration of nonaromatics than in the feed mixture. 9. The process of claim 8 wherein the concentration of nonaromatics is from about 0.5 to 10 mass-% of the feed mixture. 10. The process of claim 8 wherein the first catalyst comprises a layered sphere. 11. The process of claim 8 wherein the first and second catalysts are stacked sequentially. 12. The process of claim 8 wherein the catalyst system is a physical mixture of the first and second catalyst. 13. The process of claim 8 wherein the first and second catalysts are contained on the same catalyst particle. 14. The process of claim 8 wherein the first catalyst comprises a layer on the surface of the second catalyst.
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