Isomerization process for upgrading low-octane light paraffinic feeds using a chlorided platinum-alumina-rhenium catalyst

Claim 2

A process for increasing the octane number of an isomerizable light paraffinic hydrocarbon feed containing, calculated as sulfur, less than about 5 ppmw of sulfur-containing impurities, which comprises: (I) contacting in a reaction zone a porous alumina-based catalytic composite with a mixture of said feed, hydrogen gas and at least one chloride source selected from the group consisting of hydrogen chloride, chlorine gas, phosgene and chlorinated hydrocarbons which liberate hydrogen chloride at said contacting, said contacting being under isomerizing conditions, including (1) a temperature in the range of from about 350° to 420° C., (2) a hydrogen partial pressure in the range of from about 25 to 500 psia, (3) a liquid hourly space velocity, V/V/Hr, in the range of from about 0.5 to 5, (4) a hydrogen-to-feed mol ratio in the range of from about 2 to 10, and (5) a feed-to-chloride mol ratio in the range of from about 1.0×10 3 to 1.0×10 5 ; said composite, based by weight upon alumina and calculated as the element, containing an amount of chloride in the range of from about 1 to 3.0 weight percent, and an amount each of platinum and rhenium in the range of from about 0.1 to 1 weight percent; (II) separating the mixture resulting from step (1) in a liquid-gas separation zone into (1) a gaseous fraction comprising mainly hydrogen gas, hydrogen chloride and a minor amount of normally gaseous hydrocarbons, and (2) a first liquid hydrocarbon fraction; (III) withdrawing said gaseous fraction from said separation zone and passing at least a portion thereof in recycle to said reaction zone; (IV) fractionally distilling said separated first liquid fraction into a second liquid fraction and a normally gaseous hydrocarbon fraction, said second liquid fraction, relative to said feed, having an improved octane number.

Claim 3

A process as in claim 1 wherein said temperature is in the range of from about 365° to 390° C.

Claim 4

A process as in claim 1 wherein said chlorinated hydrocarbon is a butyl chloride.

Claim 5

A process as in claim 1 wherein said feed is a light straight-run naphtha.

Claim 6

A process for increasing the octane number of a light paraffinic hydrocarbon feed containing, calculated as sulfur, less than about 5 ppmw of sulfur-containing impurities, which comprises: (I) contacting in a reaction zone a mixture of said feed, and a gaseous recycle stream with a porous alumina-based catalytic composite under isomerizing conditions, including (1) a temperature in the range of from about 350° to 420° C., (2) hydrogen partial pressure in the range of from about 25 to 300 psia, (3) a liquid hourly space velocity, V/V/Hr, in the range of from about 0.5 to 5, (4) a hydrogen-to-feed mol ratio in the range of from about 2 to 10, and (5) a feed-to-chloride mol ratio in the range of from about 1.0×10 3 to 1.0×10 5 ; said recycle stream having a hydrogen chloride content in the range of from about 10 to 250 ppm by volume, said chloride content of said recycle stream being maintained by continuously or intermittently introducing into said reaction zone a minor amount of at least one fresh chloride source selected from the group consisting of hydrogen chloride, and chlorinated hydrocarbons which liberate hydrogen chloride under said contacting conditions, said minor amount, based by weight upon said feed and calculated as hydrogen chloride, being in the range of from about 10 to 500 ppmw; said composite, based by weight upon alumina and calculated as the element, containing an amount of chloride in the range of from about 1 to 3.0 weight percent, and an amount each of platinum and rhenium in the range of from about 0.1 to 1 weight percent; (II) separating the mixture resulting from step (1) in a liquid-gas separation zone into (1) a gaseous fraction comprising mainly hydrogen gas, hydrogen chloride and a minor amount of normally gaseous hydrocarbons, and (2) a first liquid hydrocarbon fraction; (III) withdrawing said gaseous fraction from said separation zone and passing at least a portion thereof in recycle to said reaction zone; (IV) fractionally distilling said separated first liquid fraction into a second liquid fraction and a normally gaseous hydrocarbon fraction, said second liquid fraction, relative to said feed, having an improved octane number.

Claim 7

A process for increasing the octane number of a light paraffinic hydrocarbon feed containing, calculated as sulfur, less than about 5 ppmw of sulfur-containing impurities, which comprises: (I) contacting in a reaction zone a mixture of said feed, and a gaseous recycle stream with a porous alumina-based catalytic composite under isomerizing conditions, including (1) a temperature in the range of from about 350° to 420° C., (2) hydrogen partial pressure in the range of from about 25 to 300 psia, (3) a liquid hourly space velocity, V/V/Hr, in the range of from about 0.5 to 5, (4) a hydrogen-to-feed mol ratio in the range of from about 2 to 10, and (5) a feed-to-chloride mol ratio in the range of from about 1.0×10 3 to 1.0×10 5 ; said recycle stream having a hydrogen chloride content in the range of from about 10 to 250 ppm by volume, said chloride content of said recycle stream being maintained by continuously or intermittently introducing into said reaction zone a minor amount of at least one fresh chloride source selected from the group consisting of hydrogen chloride, and chlorinated hydrocarbons which liberate hydrogen chloride under said contacting conditions, said minor amount, based by weight upon said feed and calculated as hydrogen chloride, being in the range of from about 10 to 500 ppmw; said composite, based by weight upon alumina and calculated as the element, containing an amount of chloride in the range of from about 1 to 3.0 weight percent, and an amount each of platinum and rhenium in the range of from about 0.1 to 1 weight percent; (II) separating the mixture resulting from step (1) in a liquid-gas separation zone into (1) a gaseous fraction comprising mainly hydrogen gas, hydrogen chloride and a minor amount of normally gaseous hydrocarbons, and (2) a first liquid hydrocarbon fraction; (III) withdrawing said gaseous fraction from said separation zone and passing at least a portion thereof in recycle to said reaction zone; (IV) fractionally distilling said separated first liquid fraction into a second liquid fraction and a normally gaseous hydrocarbon fraction, said second liquid fraction, relative to said feed, having an improved octane number.

Claim 8

A process as in claim 5 wherein (1) said temperature is in the range of from about 365° to 390° C., and (2) said recycle stream hydrogen chloride content is in the range of from about 20 to 150 ppmv.

Claim 9

A process as in claim 5 wherein said recycle stream hydrogen chloride content is about 60 ppmv.

Claim 10

A process as in claim 5 wherein said hydrogen partial pressure is a generated hydrogen partial pressure.

Claim 11

A process as in claim 5 wherein said fresh chloride source is a butyl chlorde.

Claim 12

A process as in claim 5 wherein there is no net make or consumption of hydrogen gas.