Octane upgrading of light naphtha streams using a fluoroalkanesulfonic acid-antimony pentafluoride mixture

Claim 2

A process for increasing the octane rating of a light naphtha composed primarily of substantially dearomatized C 5 or C 6 hydrocarbons or a mixture thereof and at least some methylcyclopentane or cyclohexane to reduce "run-away cracking" comprising: (a) intimately contacting under isomerizing conditions said light naphtha with antimony pentafluoride and at least one fluoroalkane-sulfonic acid of formula RCF 2 SO 3 H wherein R= Cl, F, CF 3 , CF 2 Cl, CF 3 CFCl, C 2 F 5 , C 3 F 7 , CF 2 SO 3 H, or C 4 F 9 , and (b) subsequently separating said mixture of antimony pentafluoride and at least one fluoroalkanesulfonic acid from the product of step (a).

Claim 3

The process of claim 1 wherein said fluoroalkanesulfonic acid is trifluoromethanesulfonic acid or perfluoroethanesulfonic acid.

Claim 4

A continuous process for increasing the octane rating of a light naphtha composed primarily of substantially dearomatized C 5 or C 6 hydrocarbons or a mixture thereof comprising: (a) intimately contacting under isomerizing conditions said light naphtha feed and about two (2) to about thirty (30) weight percent of methylcyclopentane or cyclohexane to reduce "run-away cracking" with antimony pentafluoride and at least one fluoroalkane-sulfonic acid of formula RCF 2 SO 3 H wherein R= Cl, F, CF 3 , CF 2 Cl, CF 3 CFCl, C 2 F 5 , C 3 F 7 , CF 2 SO 3 H, or C 4 F 9 , and (b) separating the composition of step (a) into a primarily hydrocarbon phase and a phase primarily composed of said acid and said pentafluoride, and (c) recycling substantially all of said acid and said pentafluoride to step (a), and (d) intimately contacting said primarily hydrocarbon phase with water to form a purified hydrocarbon phase and an aqueous phase, and (e) separating said purified hydrocarbon phase from said aqueous phase.

Claim 5

A continuous process for increasing the octane rating of a light naphtha composed primarily of substantially dearomatized C 5 or C 6 hydrocarbons or a mixture thereof comprising: (a) intimately contacting under isomerizing conditions said light naphtha feed and about two (2) to about thirty (30) weight percent of methylcyclopentane or cyclohexane to reduce "run-away cracking" with antimony pentafluoride and at least one fluoroalkane-sulfonic acid of formula RCF 2 SO 3 H wherein R= Cl, F, CF 3 , CF 2 Cl, CF 3 CFCl, C 2 F 5 , C 3 F 7 , CF 2 SO 3 H, or C 4 F 9 , and (b) separating the composition of step (a) into a primarily hydrocarbon phase and a phase primarily composed of said acid and said pentafluoride, and (c) recycling substantially all of said acid and said pentafluoride to step (a), and (d) intimately contacting said primarily hydrocarbon phase with water to form a purified hydrocarbon phase and an aqueous phase, and (e) separating said purified hydrocarbon phase from said aqueous phase.

Claim 6

The process of claim 3 wherein said fluoroalkanesulfonic acid is trifluoromethanesulfonic acid or perfluoroethanesulfonic acid.

Claim 7

The process of claim 4 wherein said light naphtha is composed primarily of substantially dearomatized C 6 hydrocarbons.

Claim 8

A process for increasing the octane rating of a light naphtha composed primarily of substantially dearomatized C 6 hydrocarbons and about two (2) to about thirty (30) weight percent of methylcyclopentane or cyclohexane to reduce "run-away cracking" comprising: (a) intimately contacting under isomerizing conditions said light naphtha with antimony pentafluoride and at least one fluoroalkanesulfonic acid of formula CF 3 SO 3 H or CF 3 CF 2 SO 3 H; and (b) subsequently separating said mixture of antimony pentafluoride and at least one fluoroalkanesulfonic acid from the product of step (a).

Claim 9

A process for increasing the octane rating of a light naphtha composed primarily of substantially dearomatized C 6 hydrocarbons and about two (2) to about thirty (30) weight percent of methylcyclopentane or cyclohexane to reduce "run-away cracking" comprising: (a) intimately contacting under isomerizing conditions said light naphtha with antimony pentafluoride and at least one fluoroalkanesulfonic acid of formula CF 3 SO 3 H or CF 3 CF 2 SO 3 H; and (b) subsequently separating said mixture of antimony pentafluoride and at least one fluoroalkanesulfonic acid from the product of step (a).