Oligomerization of predominantly low molecular weight olefins over boron trifluoride in the presence of a protonic promoter

Claim 2

A process for oligomerizing mono olefins comprising contacting a mixture of alpha mono olefins which consists essentially of greater than 50 weight percent of at least one low molecular weight alpha olefin which is 1-butene and less than 50 weight percent of at least one higher molecular weight alpha olefin having 8 to 18 carbon atoms, with a catalyst comprising boron trifluoride in the presence of an organic, protonic promoter selected from the group consisting of alcohols and carboxylic acids at a temperature in the range of about 25° to 75° C. and a pressure that is sufficient to maintain a liquid phase reaction.

Claim 3

The process of claim 1 in which the catalyst is present in an amount of from 0.75 to 3.0 weight percent, based on the olefin mixture.

Claim 4

The process of claim 1 in which the molar ratio of organic, protonic promoter to olefin mixture is from 0.005 to 0.2.

Claim 5

The process of claim 1 in which the organic, protonic promoter is 1-butanol.

Claim 6

The process of claim 1 in which less than 50 weight percent of an inert organic solvent is employed, based on the olefin mixture.

Claim 7

The process of claim 1 in which the oligomerized olefins are subsequently hydrogenated.

Claim 8

A process for oligomerizing mono olefins comprising contacting a. a mixture of alpha olefins which consists essentially of (1) greater than 50 weight percent of at least one low molecular weight alpha olefin which is 1-butene and (2) less than 50 weight percent of at least one higher molecular weight alpha olefin having 8 to 18 carbon atoms, with b. 0.75 to 3.0 weight percent of a catalyst comprising boron trifluoride in the presence of c. an organic, protonic promoter selected from the group consisting of alcohols and carboxylic acids, the molar ratio of organic promoter to olefin mixture is from 0.005 to 0.2, at a temperature in the range of about 25° to 75° C. and a pressure that is sufficient to maintain a liquid phase reaction.

Claim 9

A process for oligomerizing mono olefins comprising contacting a. a mixture of alpha olefins which consists essentially of (1) greater than 50 weight percent of at least one low molecular weight alpha olefin which is 1-butene and (2) less than 50 weight percent of at least one higher molecular weight alpha olefin having 8 to 18 carbon atoms, with b. 0.75 to 3.0 weight percent of a catalyst comprising boron trifluoride in the presence of c. an organic, protonic promoter selected from the group consisting of alcohols and carboxylic acids, the molar ratio of organic promoter to olefin mixture is from 0.005 to 0.2, at a temperature in the range of about 25° to 75° C. and a pressure that is sufficient to maintain a liquid phase reaction.

Claim 10

The process of claim 7 in which the organic, protonic promoter is 1-butanol.

Claim 11

The process of claim 7 in which less than 50 weight percent of an inert organic solvent is employed, based on the olefin mixture.

Claim 12

The process of claim 1 in which the oligomerized olefins are subsequently hydrogenated.

Claim 13

A process for the production of a synthetic lubricant component comprising a. oligomerizing a mixture of alpha mono olefins consisting essentially of 1-butene and at least one higher molecular weight alpha olefin having 8 to 18 carbon atoms, where the weight ratio of 1-butene to the higher molecular weight alpha olefins ranges from greater than 1:1 to 3:1, by contacting the mixture with boron trifluoride in the presence of an organic, protonic promoter selected from the group consisting of alcohols and carboxylic acids, at a temperature in the range of about 25° to 75° C. and a pressure that is sufficient to maintain a liquid phase reaction to produce a crude oligomer product, b. neutralizing the crude oligomer product, c. removing the organic layer from the neutralized crude oligomer product, d. hydrogenating the oligomers in the removed organic layer, and e. stripping off the molecules having less than 20 carbon atoms, the balance being the synthetic lubricant component.

Claim 14

A process for the production of a synthetic lubricant component comprising a. oligomerizing a mixture of alpha mono olefins consisting essentially of 1-butene and at least one higher molecular weight alpha olefin having 8 to 18 carbon atoms, where the weight ratio of 1-butene to the higher molecular weight alpha olefins ranges from greater than 1:1 to 3:1, by contacting the mixture with boron trifluoride in the presence of an organic, protonic promoter selected from the group consisting of alcohols and carboxylic acids, at a temperature in the range of about 25° to 75° C. and a pressure that is sufficient to maintain a liquid phase reaction to produce a crude oligomer product, b. neutralizing the crude oligomer product, c. removing the organic layer from the neutralized crude oligomer product, d. hydrogenating the oligomers in the removed organic layer, and e. stripping off the molecules having less than 20 carbon atoms, the balance being the synthetic lubricant component.

Claim 15

The process of claim 11 in which the catalyst is present in an amount of from 0.75 to 3.0 weight percent, based on the olefin mixture.

Claim 16

The process of claim 11 in which the molar ratio of organic, protonic promoter to the olefin mixture is from 0.005 to 0.2.

Claim 17

The process of claim 11 in which the protonic promoter is 1-butanol.

Claim 18

The process of claim 11 in which less than 50 weight percent of an inert organic solvent is employed, based on the olefin mixture.

Claim 19

A synthetic lubricant component having a kinematic viscosity at 210° F. of between 3.0 and 6.0 centistokes being produced by oligomerizing a mixture of alpha mono olefins which consists essentially of 1-butene and at least one higher molecular weight alpha olefin having 8 to 18 carbon atoms, where the weight ratio of 1-butene to the higher molecular weight alpha olefins ranges from greater than 1:1 to 3:1, by means of contacting the alpha olefins with boron trifluoride in the presence of an organic, protonic promoter selected from the group consisting of alcohols and carboxylic acids, at a temperature in the range of about 25° to 75° C. and a pressure that is sufficient to maintain a liquid phase reaction and subsequently hydrogenating the oligomerized olefins.

Claim 20

A synthetic lubricant component having a kinematic viscosity at 210° F. of between 3.0 and 6.0 centistokes being produced by oligomerizing a mixture of alpha mono olefins which consists essentially of 1-butene and at least one higher molecular weight alpha olefin having 8 to 18 carbon atoms, where the weight ratio of 1-butene to the higher molecular weight alpha olefins ranges from greater than 1:1 to 3:1, by means of contacting the alpha olefins with boron trifluoride in the presence of an organic, protonic promoter selected from the group consisting of alcohols and carboxylic acids, at a temperature in the range of about 25° to 75° C. and a pressure that is sufficient to maintain a liquid phase reaction and subsequently hydrogenating the oligomerized olefins.

Claim 21

The synthetic lubricant component of claim 16 in which the catalyst is present in an amount of from 0.75 to 3.0 weight percent, based on the olefin mixture.

Claim 22

The synthetic lubricant component of claim 16 in which the molar ratio of organic, protonic promoter to the olefin mixture is from 0.005 to 0.2.

Claim 23

The synthetic lubricant component of claim 16 in which the protonic promoter is 1-butanol.

Claim 24

The synthetic lubricant component of claim 16 in which less than 50 weight percent of an inert organic solvent is present during oligomerization, based on the olefin mixture.