Claims
- 1. A process for isomerizing an alkylaromatic hydrocarbon which comprises contacting said hydrocarbon at isomerization conditions with a catalytic composite comprising a porous alumina carrier containing, on an elemental basis, about 0.01 to about 2 weight percent platinum or palladium, about 0.01 to about 2 weight percent rhodium, about 0.01 to about 5 weight percent tin and about 0.1 to about 10 weight percent halogen, wherein said platinum or palladium, rhodium and tin are uniformly dispersed throughout said alumina carrier, wherein substantially all of said platinum or palladium and rhodium are present in the corresponding elemental metallic states and wherein substantially all of said tin is present in an oxidation state above that of the elemental metal.
- 2. A process as defined in claim 1 wherein the halogen is chlorine.
- 3. A process as defined in claim 1 wherein the atomic ratio of tin to platinum or palladium contained in the composite is about 0.1:1 to about 3:1.
- 4. A process as defined in claim 1 wherein the atomic ratio of rhodium to platinum or palladium contained in the composite is about 0.1:1 to about 2:1.
- 5. A process as defined in claim 1 wherein the catalytic composite contains about 0.01 to about 0.5 weight percent sulfur, calculated on an elemental basis.
- 6. A process as defined in claim 1 wherein the composite contains about 0.05 to about 1 weight percent platinum, about 0.05 to about 1 weight percent rhodium, about 0.1 to about 1 weight percent tin and about 1 to about 5 weight percent halogen.
- 7. A process as defined in claim 1 wherein the catalytic composite additionally contains 1 weight percent up to about 100 weight percent of a Friedel-Crafts metal halide based on said composite.
- 8. A process as defined in claim 1 wherein said catalytic composite additionally contains 1 weight percent up to about 100 weight percent aluminum chloride based on said composite.
- 9. A process as defined in claim 1 wherein said isomerization conditions include a temperature of about 0.degree. to about 600.degree. C., a pressure of about atmospheric to about 100 atmospheres, a liquid hourly space velocity of about 0.1 to about 20 hr..sup.-.sup.1, and a hydrogen-hydrocarbon mole ratio of from 0.1:1 to about 25:1.
- 10. A process as defined in claim 1 wherein said alkylaromatic hydrocarbon is a C.sub.8 alkylaromatic or a non-equilibrium mixture of C.sub.8 alkylaromatic hydrocarbons.
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is a division of a copending application Ser. No. 584,438, filed June 6, 1975, and now U.S. Pat. No. 3,992,476, which is in turn a continuation-in-part of my prior application Ser. No. 480,793 filed June 19, 1974, and now U.S. Pat. No. 3,898,154, which in turn is a continuation-in-part of my prior application Ser. No. 376,841 filed July 5, 1973 and now U.S. Pat. No. 3,846,283, which in turn is a continuation-in-part of my prior application Ser. No. 201,576 filed Nov. 23, 1971 and now U.S. Pat. No. 3,745,112, and which in turn is a continuation-in-part of my prior application Ser. No. 807,910 filed Mar. 17, 1969 and now U.S. Pat. No. 3,740,328. All of the teachings of these prior applications are specifically incorporated herein by reference.
US Referenced Citations (4)
Divisions (1)
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Date |
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Parent |
584438 |
Jun 1975 |
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Continuation in Parts (4)
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Number |
Date |
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480793 |
Jun 1974 |
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Parent |
376841 |
Jul 1973 |
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Parent |
201576 |
Nov 1971 |
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807910 |
Mar 1969 |
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