Hydrocarbon conversion process

Claim 2

A hydrocarbon conversion process which comprises contacting a hydrocarbon feedstock, under conversion conditions, with a catalyst comprising greater than 0.1 wt. % iridium, based on total catalyst and 0.1 to 1.0 wt. % of at least one additional catalyst metal selected from the group consisting of ruthenium, rhodium, palladium, osmium, platinum, copper and silver, based on total catalyst, said iridium and additional catalyst metal being present on a refractory support and in an atomic ratio varying from 1:10 to 10:1, the surface area of said iridium and additional catalyst metal on said support being at least 200 square meters per gram of said iridium and additional catalyst metal as determined by carbon monoxide chemisorption techniques, depositing carbonaceous materials on the surface of said catalyst as a result of the hydrocarbon conversion process, and periodically regenerating said catalyst by burning substantially all of the carbonaceous materials from said catalyst in the presence of oxygen while maintaining the temperature during said burning below about 850° F. and thereby maintaining the surface area of the iridium and additional catalyst metal above about 150 square meters per gram.

Claim 3

The process of claim 1 wherein the additional catalyst metal is platinum.

Claim 4

The process of claim 2 wherein the support is an inorganic oxide.

Claim 5

The process of claim 3 wherein the support is alumina.

Claim 6

The process of claim 3 wherein the catalyst contains less than about two atoms of sulfur per atom of iridium and additional catalyst metal and is substantially free of alkali and alkaline earth metal constituents.

Claim 7

The process of claim 5 wherein the temperature during said burning is below about 800° F.

Claim 8

A hydrocarbon reforming process which comprises contacting a normally liquid hydrocarbon feedstock at reforming conditions and in the presence of hydrogen with a catalyst comprising greater than 0.1 wt. % iridium, based on total catalyst, and 0.1 to 1.0 wt. % of at least one additional catalyst metal selected from the group consisting of ruthenium, rhodium, palladium, osmium, platinum, copper, and silver, based on total catalyst, said iridium and additional catalyst metal being present on a refractory support and in an atomic ratio varying from 1:10 to 10:1, the surface area of said iridium and additional catalyst metal on said support being at least 200 square meters per gram of said iridium and additional catalyst metal as determined by carbon monoxide chemisorption techniques, said catalyst containing less than about two atoms of sulfur per atom of iridium and additional catalyst metal and being substantially free of alkali and alkaline earth metal constituents, depositing carbonaceous materials on the surface of said catalyst as a result of the hydrocarbon reforming process, and periodically regenerating said catalyst by burning substantially all of the carbonaceous materials from said catalyst in the presence of oxygen while maintaining the temperature during said burning below about 850° F. and thereby maintaining the surface area of the iridium and additional catalyst metal above about 200 square meters per gram.

Claim 9

A hydrocarbon reforming process which comprises contacting a normally liquid hydrocarbon feedstock at reforming conditions and in the presence of hydrogen with a catalyst comprising greater than 0.1 wt. % iridium, based on total catalyst, and 0.1 to 1.0 wt. % of at least one additional catalyst metal selected from the group consisting of ruthenium, rhodium, palladium, osmium, platinum, copper, and silver, based on total catalyst, said iridium and additional catalyst metal being present on a refractory support and in an atomic ratio varying from 1:10 to 10:1, the surface area of said iridium and additional catalyst metal on said support being at least 200 square meters per gram of said iridium and additional catalyst metal as determined by carbon monoxide chemisorption techniques, said catalyst containing less than about two atoms of sulfur per atom of iridium and additional catalyst metal and being substantially free of alkali and alkaline earth metal constituents, depositing carbonaceous materials on the surface of said catalyst as a result of the hydrocarbon reforming process, and periodically regenerating said catalyst by burning substantially all of the carbonaceous materials from said catalyst in the presence of oxygen while maintaining the temperature during said burning below about 850° F. and thereby maintaining the surface area of the iridium and additional catalyst metal above about 200 square meters per gram.

Claim 10

The process of claim 7 wherein the additional catalyst metal is platinum.

Claim 11

The process of claim 8 wherein the refractory support is an inorganic oxide.

Claim 12

The process of claim 9 wherein the support is alumina.

Claim 13

The process of claim 10 wherein the catalyst additionally contains from about 0.1 to 3 wt. % of a halogen moiety, based on total catalyst.

Claim 14

A process for reforming a naphtha feed stock containing aromatic, naphthenic and paraffinic constituents, which comprises contacting said feed stock at a temperature varying from 650° to 1000° F. and at a pressure varying from 1 to 50 atmospheres in the presence of hydrogen with a catalyst comprising greater than 0.1 wt. % iridium, based on total catalyst, and 0.1 to 1.0 wt. % of platinum, based on total catalyst, said iridium and platinum being present on a refractory support and in an atomic ratio varying from 1:10 to 10:1, the surface area of said iridium and platinum on said support being at least about 200 square meters per gram of said iridium and platinum as determined by carbon monoxide chemisorption techniques, said catalyst containing from about 0.1 to 3.0 wt. % of a halogen moiety and less than about two atoms of sulfur per atom of iridium and additional catalyst metal and being substantially free of alkali and alkaline earth metal constituents, depositing carbonaceous materials on the surface of said catalyst as a result of the naphtha reforming process, and periodically regenerating said catalyst by burning substantially all of the carbonaceous materials from said catalyst in the presence of oxygen while maintaining the temperature during said burning below 850° F and thereby maintaining the surface area of the iridium and platinum above about 200 square meters per gram.

Claim 15

A process for reforming a naphtha feed stock containing aromatic, naphthenic and paraffinic constituents, which comprises contacting said feed stock at a temperature varying from 650° to 1000° F. and at a pressure varying from 1 to 50 atmospheres in the presence of hydrogen with a catalyst comprising greater than 0.1 wt. % iridium, based on total catalyst, and 0.1 to 1.0 wt. % of platinum, based on total catalyst, said iridium and platinum being present on a refractory support and in an atomic ratio varying from 1:10 to 10:1, the surface area of said iridium and platinum on said support being at least about 200 square meters per gram of said iridium and platinum as determined by carbon monoxide chemisorption techniques, said catalyst containing from about 0.1 to 3.0 wt. % of a halogen moiety and less than about two atoms of sulfur per atom of iridium and additional catalyst metal and being substantially free of alkali and alkaline earth metal constituents, depositing carbonaceous materials on the surface of said catalyst as a result of the naphtha reforming process, and periodically regenerating said catalyst by burning substantially all of the carbonaceous materials from said catalyst in the presence of oxygen while maintaining the temperature during said burning below 850° F and thereby maintaining the surface area of the iridium and platinum above about 200 square meters per gram.

Claim 16

The process of claim 12 wherein the support is alumina.

Claim 17

The process of claim 12 wherein the halogen moiety is a chlorine moiety, a fluorine moiety or mixtures thereof.

Claim 18

The process of claim 12 wherein said catalyst is capable of processing, prior to regeneration, at least about 50 barrels of feed stock per pound of catalyst to a C 5 + reformate product having a research clear octane number of at least about 100 without incurring a C 5 + reformate yield loss greater than about 3 volume % for the last 95% of the reforming cycle period.

Claim 19

The process of claim 12 wherein the flame front temperature during burning of the carbonaceous material is maintained in the range of about 700° to 850° F. for a period sufficient to burn off substantially all of the carbonaceous materials.

Claim 20

The process of claim 12 wherein the temperature during said burning is below about 800° F.