Octane upgrading of light naphtha streams using a fluorosulfonic acid, hydrofluoric acid and antimony pentafluoride catalyst

Claim 2

A catalyst composition comprising fluorosulfonic acid and antimony pentafluoride in a volume ratio of antimony pentafluoride to fluorosulfonic acid of about 0.1 to about 3 and about two to about twenty weight percent of hydrogen fluoride based upon the weight of fluorosulfonic acid.

Claim 3

The composition of claim 1 wherein said weight percent is about three to about fifteen.

Claim 4

The composition of claim 1 wherein said weight percent is about five to about ten.

Claim 5

The composition of claim 1 wherein said volume ratio is about 0.4 to about 1.6.

Claim 6

The composition of claim 2 wherein said volume ratio is about 0.4 to about 1.6.

Claim 7

The composition of claim 3 wherein said volume ratio is about 0.4 to about 1.6.

Claim 8

A process for upgrading the octane rating of pentanes, hexanes or mixtures thereof which comprises contacting under isomerizing conditions said pentanes, hexanes or mixtures thereof, an inhibitor to prevent runaway cracking and a composition comprising: (1) fluorosulfonic acid and antimony pentafluoride in a volume ratio of antimony pentafluoride to fluorosulfonic acid of about 0.1 to about 3; and (2) about two to about twenty weight percent of hydrogen fluoride based upon the weight of fluorosulfonic acid.

Claim 9

A process for upgrading the octane rating of pentanes, hexanes or mixtures thereof which comprises contacting under isomerizing conditions said pentanes, hexanes or mixtures thereof, an inhibitor to prevent runaway cracking and a composition comprising: (1) fluorosulfonic acid and antimony pentafluoride in a volume ratio of antimony pentafluoride to fluorosulfonic acid of about 0.1 to about 3; and (2) about two to about twenty weight percent of hydrogen fluoride based upon the weight of fluorosulfonic acid.

Claim 10

The process of claim 7 wherein said weight percent is about three to about fifteen

Claim 11

The process of claim 7 wherein said weight percent is about five to about ten.

Claim 12

The process of claim 7 wherein said volume ratio is about 0.4 to about 1.6.

Claim 13

The process of claim 8 wherein said volume ratio is about 0.4 to about 1.6.

Claim 14

The process of claim 9 wherein said volume ratio is about 0.4 to about 1.6.

Claim 15

A continuous process for treating a stream of dearomatized pentanes, hexanes or a mixture thereof in the presence of about two to about thirty weight percent of an inhibitor to prevent runaway cracking comprising: (a) intimately contacting under isomerising conditions said stream with a catalyst composition consisting essentially of (1) fluorosulfonic acid and antimony pentafluoride in a volume ratio of antimony pentalfuoride to fluorosulfonic acid of about one-tenth to about three, and (2) about two to about twenty weight percent of hydrogen fluoride based upon the weight of fluorosulfonic acid; (b) thereafter separating the product of (a) into a first hydrocarbon stream and a first catalyst stream; (c) returning a major portion of said first catalyst stream to (a) and a minor portion to a catalyst regeneration zone; (d) intimately contacting under isomerizing conditions said first hydrocarbon stream with additional said catalyst composition at a lower temperature than that used in (a); (e) thereafter separating the product of (d) into a second hydrocarbon stream and a second catalyst stream; (f) returning a major portion of said second catalyst stream to (d) and a minor portion to (a); and (g) adding make-up of said catalyst composition to and removing isomerized hydrocarbon product from the last contacting-separation step.

Claim 16

A continuous process for treating a stream of dearomatized pentanes, hexanes or a mixture thereof in the presence of about two to about thirty weight percent of an inhibitor to prevent runaway cracking comprising: (a) intimately contacting under isomerising conditions said stream with a catalyst composition consisting essentially of (1) fluorosulfonic acid and antimony pentafluoride in a volume ratio of antimony pentalfuoride to fluorosulfonic acid of about one-tenth to about three, and (2) about two to about twenty weight percent of hydrogen fluoride based upon the weight of fluorosulfonic acid; (b) thereafter separating the product of (a) into a first hydrocarbon stream and a first catalyst stream; (c) returning a major portion of said first catalyst stream to (a) and a minor portion to a catalyst regeneration zone; (d) intimately contacting under isomerizing conditions said first hydrocarbon stream with additional said catalyst composition at a lower temperature than that used in (a); (e) thereafter separating the product of (d) into a second hydrocarbon stream and a second catalyst stream; (f) returning a major portion of said second catalyst stream to (d) and a minor portion to (a); and (g) adding make-up of said catalyst composition to and removing isomerized hydrocarbon product from the last contacting-separation step.

Claim 17

The process of claim 13 wherein said weight percent is about three to about fifteen and said volume ratio is about four-tenths to about one and six-tenths.