Alumina isomerization process

Claim 2

A process for regenerating an isomerization catalyst consisting essentially of alumina having a surface area of at least about 100 m 2 /g and having coke deposited thereon comprising heating said catalyst at a temperature in the range of about 425° C. to about 705° C. in the presence of a free oxygen-containing gas containing about 0.3 to about 10 mole percent water based on the moles of free oxygen-containing gas for a time sufficient to burn off substantially all the coke on said catalyst.

Claim 3

A process according to claim 1 wherein said isomerization catalyst is selected from the group consisting of eta-alumina and gamma-alumina.

Claim 4

A process according to claim 2 wherein the temperature of regeneration is no greater than about 650° C.

Claim 5

A process according to claim 3 wherein said catalyst contains less than 0.1 weight percent alkali metal based on the weight of the catalyst and a surface area greater than 150 m 2 /g.

Claim 6

In a process for the isomerization of an olefin-containing feedstream using an isomerization catalyst consisting essentially of alumina having a surface area of at least about 100 m 2 /g wherein one isomerization run is followed by catalyst regeneration and then an additional isomerization run, the improvement which comprises carrying out said regeneration by heating said catalyst at a temperature in the range of about 425° C. to about 705° C. in the presence of a free oxygen-containing gas containing about 0.3 to about 10 mole percent water based on the moles of free oxygen-containing gas for a time sufficient to burn off substantially all the coke on said catalyst.

Claim 7

In a process for the isomerization of an olefin-containing feedstream using an isomerization catalyst consisting essentially of alumina having a surface area of at least about 100 m 2 /g wherein one isomerization run is followed by catalyst regeneration and then an additional isomerization run, the improvement which comprises carrying out said regeneration by heating said catalyst at a temperature in the range of about 425° C. to about 705° C. in the presence of a free oxygen-containing gas containing about 0.3 to about 10 mole percent water based on the moles of free oxygen-containing gas for a time sufficient to burn off substantially all the coke on said catalyst.

Claim 8

A process in accordance with claim 5 wherein said isomerization catalyst is selected from the group consisting of eta-alumina and gamma-alumina.

Claim 9

A process in accordance with claim 6 wherein the temperature of regeneration is no greater than about 650° C.

Claim 10

A process in accordance with claim 7 wherein the said olefin-containing feedstream contains one or more n-olefins having four to 10 carbon atoms per molecule.

Claim 11

A process in accordance with claim 8 wherein the isomerizations are conducted upon a feedstream of gasoline.

Claim 12

A process in accordance with claim 9 wherein the gasoline comprises at least one catalytically cracked gasoline fraction.

Claim 13

A process in accordance with claim 10 wherein said catalyst contains less than 0.1 weight percent alkali metal based on the weight of the catalyst and has a surface area greater than 150 m 2 /g.

Claim 14

A cyclic process for the isomerization of at least one olefin having from 4 to 10 carbon atoms per molecule comprising: (a) contacting an active isomerization catalyst consisting essentially of alumina having a surface area of at least about 100 m 2 /g with a feedstream containing one or more olefins having from 4 to 10 carbon atoms per molecule under conditions suitable for isomerizing said one or more olefins to more highly branched olefins, (b) regenerating the catalyst employed in step (a) by heating said catalyst at a temperature in the range of about 425° C. to about 705° C. in the presence of a free oxygen-containing gas containing about 0.3 to about 10 mole percent water based on the moles of free oxygen-containing gas for a time sufficient to burn off substantially all the coke on said catalyst, and thereafter (c) contacting the regenerated catalyst from step (b) with a feedstream containing one or more olefins having 4 to 10 carbon atoms per molecule under conditions suitable for isomerizing said one or more olefins to more highly branched olefins.

Claim 15

A cyclic process for the isomerization of at least one olefin having from 4 to 10 carbon atoms per molecule comprising: (a) contacting an active isomerization catalyst consisting essentially of alumina having a surface area of at least about 100 m 2 /g with a feedstream containing one or more olefins having from 4 to 10 carbon atoms per molecule under conditions suitable for isomerizing said one or more olefins to more highly branched olefins, (b) regenerating the catalyst employed in step (a) by heating said catalyst at a temperature in the range of about 425° C. to about 705° C. in the presence of a free oxygen-containing gas containing about 0.3 to about 10 mole percent water based on the moles of free oxygen-containing gas for a time sufficient to burn off substantially all the coke on said catalyst, and thereafter (c) contacting the regenerated catalyst from step (b) with a feedstream containing one or more olefins having 4 to 10 carbon atoms per molecule under conditions suitable for isomerizing said one or more olefins to more highly branched olefins.

Claim 16

A process in accordance with claim 12 wherein said alumina isomerization catalyst is selected from the group consisting of eta-alumina and gamma-alumina.

Claim 17

A process in accordance with claim 13 wherein the temperature of regeneration is no greater than about 650° C.

Claim 18

A process in accordance with claim 14 wherein said feedstream contains one or more n-olefins having four to 10 carbon atoms per molecule.

Claim 19

A process in accordance with claim 15 wherein the isomerizations are conducted upon a feedstream of gasoline.

Claim 20

A process in accordance with claim 16 wherein the gasoline comprises at least one fraction of catalytically cracked gasoline.

Claim 21

A process in accordance with claim 16 wherein the free oxygen-containing gas employed in the regeneration contains about 2.5 to about 3.0 mole percent water based on the moles of the free oxygen-containing gas.

Claim 22

A process according to claim 4 wherein said free-oxygen-containing gas contains about 2.5 to about 3.0 mole percent water based on the moles of the free oxygen-containing gas.

Claim 23

A process according to claim 11 wherein said free-oxygen-containing gas contains about 2.5 to about 3.0 mole percent water based on the moles of the free oxygen-containing gas.