Autorefrigerated isomerization process

Claim 2

In an isomerization process which comprises reacting a hydrocarbon feed stock which comprises a saturated acyclic hydrocarbon having at least four carbon atoms, a saturated alicyclic hydrocarbon having at least six carbon atoms or mixtures thereof with hydrogen in a reaction zone comprising at least one reactor having therein at least one temperature zone and with a catalyst comprising a metal halide selected from the group consisting of the bromides and the chlorides of aluminum and gallium and the chlorides, bromides and fluorides of niobium, tantalum, molybdenum or tungsten and including in said isomerization zone at least an equal molar amount, based on the metal halide, of a hydrogen halide selected from the group consisting of hydrogen fluoride, hydrogen chloride and hydrogen bromide, at least a portion of said metal halide being dissolved in said hydrogen halide, said reaction zone being maintained at isomerization conditions which include at least a portion of the catalyst and hydrocarbon feed stock being in the liquid phase, thereby forming a reaction product of enhanced octane, the improvement which comprises controlling the temperature in said at least one temperature zone by vaporizing at least a portion of said hydrogen halide.

Claim 3

The process of claim 1 wherein said reaction product contains from about 5 to about 10,000 wppm of said metal halide, and wherein at least a portion of the vaporized hydrogen halide autorefrigerant is condensed and then contacted with said reaction product to from a raffinate having a reduced content of said metal halide and an extract comprising said liquid hydrogen halide enriched in said metal halide, at least a portion of said extract being recycled to the reaction zone.

Claim 4

The process of claim 1 wherein the molar ratio of hydrogen halide to metal halide present in said reaction zone is at least 2:1.

Claim 5

The process of claim 1 wherein said isomerization is conducted at a temperature in the range of from about 0° C to about the critical temperature of the hydrogen halide.

Claim 6

The process of claim 1 wherein the metal halide is a metal fluoride and the hydrogen halide is hydrogen fluoride.

Claim 7

The process of claim 5 wherein the metal fluoride is tantalum pentafluoride, niobium pentafluoride or mixtures thereof.

Claim 8

The process of claim 6 wherein the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone is at least 2:1.

Claim 9

The process of claim 7 wherein the hydrogen partial pressure is at least 5 psig.

Claim 10

In an isomerization process which comprises reacting a hydrocarbon feed stock which comprises a saturated acyclic hydrocarbon having at least 4 carbon atoms, a saturated alicyclic hydrocarbon having at least 6 carbon atoms or mixtures thereof, with hydrogen in a reaction zone comprising at least one reactor having therein at least one temperature zone and with a catalyst comprising tantalum pentafluoride, niobium pentafluoride or mixtures thereof and hydrogen fluoride, the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone being at least 2:1, at least a portion of said metal fluoride being dissolved in said hydrogen fluoride, said reaction zone being maintained at substantially liquid phase catalyst isomerization conditions including a temperature ranging from about 0° C. to the critical temperature of the hydrogen fluoride, and a hydrogen partial pressure varying from about 5 to about 2000 psig, thereby forming a reaction product of enhanced octane, the improvement which comprises controlling the temperature in said at least, one temperature zone by vaporizing at least a portion of said hydrogen fluoride.

Claim 11

In an isomerization process which comprises reacting a hydrocarbon feed stock which comprises a saturated acyclic hydrocarbon having at least 4 carbon atoms, a saturated alicyclic hydrocarbon having at least 6 carbon atoms or mixtures thereof, with hydrogen in a reaction zone comprising at least one reactor having therein at least one temperature zone and with a catalyst comprising tantalum pentafluoride, niobium pentafluoride or mixtures thereof and hydrogen fluoride, the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone being at least 2:1, at least a portion of said metal fluoride being dissolved in said hydrogen fluoride, said reaction zone being maintained at substantially liquid phase catalyst isomerization conditions including a temperature ranging from about 0° C. to the critical temperature of the hydrogen fluoride, and a hydrogen partial pressure varying from about 5 to about 2000 psig, thereby forming a reaction product of enhanced octane, the improvement which comprises controlling the temperature in said at least, one temperature zone by vaporizing at least a portion of said hydrogen fluoride.

Claim 12

The process of claim 9 wherein the feed stock comprises a saturated acyclic hydrocarbon having from 4 to 10 carbon atoms, a saturated alicyclic hydrocarbon having from 6 to 15 carbon atoms or mixtures thereof.

Claim 13

The process of claim 9 wherein said reaction product contains from about 5 to about 10,000 wppm of metal fluoride, and wherein at least a portion of the vaporized hydrogen fluoride autorefrigerant is condensed and then contacted with said reaction product to form a raffinate having a reduced content of said metal fluoride and an extract comprising said liquid hydrogen fluoride enriched in said metal fluoride, at least a portion of said extract being recycled to the reaction zone.

Claim 14

The process of claim 9 wherein said isomerization is conducted at a temperature in the range of from about 0° to about 150° C.

Claim 15

The process of claim 9 wherein the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone is at least about 5:1.

Claim 16

In an isomerization process which comprises reacting a hydrocarbon feed stock which comprises a saturated acyclic hydrocarbon having at least four carbon atoms, a saturated alicyclic hydrocarbon having at least 6 carbon atoms and mixtures thereof, with hydrogen in a reaction zone comprising at least one reactor having therein at least two temperature zones, the isomerization temperature of the first temperature zone being greater than the isomerization temperature of the second temperature zone, and with a catalyst comprising a metal halide selected from the group consisting of the bromides and chlorides of aluminum and gallium and the chlorides, bromides and flourides of niobium, tantalum, molybdenum or tungsten and at least an equal molar amount, based on the metal halide, of a hydrogen halide selected from the group consisting of hydrogen fluoride, hydrogen chloride and hydrogen bromide, at least a portion of said metal halide being dissolved in said hydrogen halide, said reaction zone being maintained at isomerization conditions which include at least a portion of the catalyst and the hydrocarbon feed stock being in the liquid phase, the improvement which comprises forming an isomerate of enhanced octane by controlling the temperature in at least one of said temperature zones by vaporizing a portion of said hydrogen halide.

Claim 17

In an isomerization process which comprises reacting a hydrocarbon feed stock which comprises a saturated acyclic hydrocarbon having at least four carbon atoms, a saturated alicyclic hydrocarbon having at least 6 carbon atoms and mixtures thereof, with hydrogen in a reaction zone comprising at least one reactor having therein at least two temperature zones, the isomerization temperature of the first temperature zone being greater than the isomerization temperature of the second temperature zone, and with a catalyst comprising a metal halide selected from the group consisting of the bromides and chlorides of aluminum and gallium and the chlorides, bromides and flourides of niobium, tantalum, molybdenum or tungsten and at least an equal molar amount, based on the metal halide, of a hydrogen halide selected from the group consisting of hydrogen fluoride, hydrogen chloride and hydrogen bromide, at least a portion of said metal halide being dissolved in said hydrogen halide, said reaction zone being maintained at isomerization conditions which include at least a portion of the catalyst and the hydrocarbon feed stock being in the liquid phase, the improvement which comprises forming an isomerate of enhanced octane by controlling the temperature in at least one of said temperature zones by vaporizing a portion of said hydrogen halide.

Claim 18

The process of claim 14 said reaction product contains from about 5 to about 10,000 wppm of said metal halide, and wherein at least a portion of the vaporized hydrogen halide autorefrigerant is condensed and then contacted with said reaction product to form a raffinate having a reduced content of said metal halide and an extract comprising said liquid hydrogen halide enriched in said metal halide, at least a portion of said extract being recycled to the reaction zone.

Claim 19

The process of claim 14 wherein the molar ratio of hydrogen halide to metal halide present in said reaction zone is at least 2:1.

Claim 20

The process of claim 14 wherein said isomerization is conducted at a temperature in the range of from about 0° C. to about the critical temperature of the hydrogen halide.

Claim 21

The process of claim 14 wherein the metal halide is a metal fluoride and the hydrogen halide is hydrogen fluoride.

Claim 22

The process of claim 18 wherein the metal fluoride is tantalum pentafluoride, niobium pentafluoride or mixtures thereof.

Claim 23

The process of claim 19 wherein the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone is at least 2:1.

Claim 24

The process of claim 20 wherein the hydrogen partial pressure is at least 5 psig.

Claim 25

In an isomerization process which comprises reacting a hydrocarbon feed stock which comprises a saturated acyclic hydrocarbon having at least four carbon atoms, a saturated alicyclic hydrocarbon having at least six carbon atoms or mixtures thereof, with hydrogen in a reaction zone comprising at least one reactor having therein at least two temperature zones, the isomerization temperature of the first temperature zone being greater than the isomerization temperature of the second temperature zone, and with a catalyst comprising tantalum pentafluoride, niobium pentafluoride or mixtures thereof and hydrogen fluoride, the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone being at least 2:1, at least a portion of said metal fluoride being dissolved in said hydrogen fluoride, said reaction zone being maintained at substantially liquid phase catalyst isomerization conditions including a temperature ranging from about 0° C. to the critical temperature of the hydrogen fluoride and a hydrogen partial pressure varying from about 5 to about 2000 psig, the improvement which comprises forming an isomerate of enhanced octane by controlling the temperature in at least one of said temperature zones by vaporizing at least a portion of said hydrogen fluoride.

Claim 26

In an isomerization process which comprises reacting a hydrocarbon feed stock which comprises a saturated acyclic hydrocarbon having at least four carbon atoms, a saturated alicyclic hydrocarbon having at least six carbon atoms or mixtures thereof, with hydrogen in a reaction zone comprising at least one reactor having therein at least two temperature zones, the isomerization temperature of the first temperature zone being greater than the isomerization temperature of the second temperature zone, and with a catalyst comprising tantalum pentafluoride, niobium pentafluoride or mixtures thereof and hydrogen fluoride, the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone being at least 2:1, at least a portion of said metal fluoride being dissolved in said hydrogen fluoride, said reaction zone being maintained at substantially liquid phase catalyst isomerization conditions including a temperature ranging from about 0° C. to the critical temperature of the hydrogen fluoride and a hydrogen partial pressure varying from about 5 to about 2000 psig, the improvement which comprises forming an isomerate of enhanced octane by controlling the temperature in at least one of said temperature zones by vaporizing at least a portion of said hydrogen fluoride.

Claim 27

The process of claim 22 wherein the feed stock comprises a saturated acyclic hydrocarbon having from 4 to 10 carbon atoms, a saturated alicyclic hydrocarbon having from 6 to 15 carbon atoms or mixtures thereof.

Claim 28

The process of claim 22 wherein said reaction product contains from about 5 to about 10,000 wppm of metal halide, and wherein at least a portion of the vaporized hydrogen fluoride autorefrigerant is condensed and then contacted, in an extraction zone, with said reaction product, thereby forming a raffinate having a reduced content of said metal fluoride and an extract comprising said liquid hydrogen fluoride, at least a portion of said extract being recycled to the reaction zone.

Claim 29

The process of claim 22 wherein said isomerization is conducted at a temperature in the range of from about 0° to about 150° C.

Claim 30

The process of claim 22 wherein the molar ratio of hydrogen fluoride to metal fluoride present in the reaction zone is at least about 5:1.