Catalytic composition and process for the selective dimerization of ethylene to 1-butene

Patent metadata

Field	Value
Publication number	US-9931622-B2
Application number	US-201514790841-A
Country	US
Kind code	B2
Filing date	Jul 2, 2015
Priority date	Jul 4, 2014
Publication date	Apr 3, 2018
Grant date	Apr 3, 2018

Abstract

The invention describes a catalytic composition obtained by interaction of an alkyl titanate on the one hand with a preformed mixture of an alkylaluminium and a Lewis base on the other hand. The invention also describes the use of said composition in a process for the selective dimerization of ethylene to 1-butene.

First claim

The invention claimed is:

1. A catalytic composition comprising at least one alkoxy or aryloxy titanium compound and at least one preformed mixture of a Lewis base (LB) additive and an aluminium compound (Al),
wherein the aluminium compound (Al) is a tris(hydrocarbyl)aluminium compound of the formula AlR″ 3 in which R″ is a hydrocarbyl radical and wherein the composition is provided as a solution containing the recited components in solution, and
wherein the Lewis base (LB) additive is a cyclic ether which may be substituted or not substituted with alkyl, aryl, or aralkyl groups containing 2 to 30 carbon atoms,
wherein a molar ratio LB/Al is greater than 0.5 and less than or equal to 5,
wherein the at least one alkoxy or aryloxy titanium compound is in mixture with an ether solvent, in a molar ratio between the ether solvent and the at least one alkoxy or aryloxy titanium compound in the range of 20/1 to 1/1, and
wherein a molar ratio of the aluminium compound and the titanium compound is in the range of 1/1 to 100/1.

2. The catalytic composition according to claim 1 , wherein the aluminium compound (Al) is a tris(hydrocarbyl)aluminium compound of the formula AlR″ 3 in which R″ is an alkyl radical containing 1 to 6 carbon atoms.

3. The catalytic composition according to claim 1 , which comprises an alkoxy titanium compound of the formula [Ti(OR) 4 ], in which R is a linear or branched alkyl radical containing 2 to 30 carbon atoms.

4. The catalytic composition according to claim 1 , which comprises an aryloxy titanium compound of the formula [Ti(OR′) 4 ], in which R′ is an aryl radical which may or may not be substituted with alkyl, aryl or aralkyl groups containing 2 to 30 carbon atoms.

5. The catalytic composition according to claim 1 , in which the preformed mixture of the Lewis base (LB) additive and the aluminium compound (Al) is used as a mixture with a solvent selected from the group consisting of aliphatic and cyclo-aliphatic hydrocarbons, unsaturated hydrocarbons, diolefins, and aromatic hydrocarbons, pure or as a mixture.

6. A process for the preparation of a catalytic composition according to claim 1 , which comprises preparing the preformed mixture by adding the Lewis base (LB) additive to the aluminium compound (Al).

7. The process for the preparation of the catalytic composition according to claim 6 , in which the preformed mixture is prepared at a temperature in the range −80° C. to +200° C.

8. The process according to claim 6 , wherein the preformed mixture is prepared in a medium which is diluted using a solvent.

9. A process for the selective dimerization of ethylene to 1-butene which comprises contacting ethylene with the catalytic composition according to claim 1 .

10. The process for the selective dimerization of ethylene to 1-butene according to claim 9 , in which the dimerization reaction is carried out at a total pressure of 0.5 to 20 MPa and at a temperature of 20° C. to 180° C.

11. The process for the selective dimerization of ethylene to 1-butene according to claim 9 , in which the selective ethylene dimerization reaction is carried out in a batch or continuous mode.

12. The process for the selective dimerization of ethylene to 1-butene according to claim 9 , carried out such that solutions of the titanium compound and preformed mixture of the Lewis base additive and the aluminium compound are introduced into a reactor provided with stirring, heating and cooling means, then pressurizing the reactor with ethylene and adjusting the temperature.

13. The process for the selective dimerization of ethylene to 1-butene according to claim 9 , wherein the titanium compound and the preformed mixture of the Lewis base additive and the aluminium compound are separately introduced into a reactor maintained under a constant pressure of ethylene.

14. The process for the selective dimerization of ethylene to 1-butene according to claim 9 , wherein the titanium compound and the preformed mixture of the Lewis base additive and the aluminium compound are introduced into a first reactor/mixer, and said composition is then continuously introduced into a second reactor maintained under a constant pressure of ethylene.

Assignees

• Ifp Energies Now

Inventors

• Magna Lionel
• Olivier-Bourbigou Helene

Classifications

• B01J31/143 Primary

  of aluminium · CPC title

• C07C2531/12

  containing organo-metallic compounds or metal hydrides · CPC title

• B01J2231/20

  Olefin oligomerisation or telomerisation · CPC title

• C07C2531/14

  of aluminium or boron · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title