IP Library Granted Patent US 11,198,658
Granted Patent B2
US 11,198,658 · App. 16/969,297 · Granted Dec 14, 2021

Process for the oligomerization of olefins

Inventors: Christine-Joy Richardson (King of Prussia, PA); Laurent Germanaud (Saint Alyre d'Arlanc, FR); Stéphane Kressmann (Communay, FR)
Assignee: TOTAL MARKETING SERVICES
C07C2/12C07C1/24C07C11/08C07C2521/12C07C2529/06
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Quick Facts
Patent No.
US 11,198,658
App. No.
16/969,297
Granted
Dec 14, 2021
Kind
B2
Abstract

A process for preparing a hydrocarbon fluid includes a step of oligomerising an initial hydrocarbon composition which contains, in relation to the total weight of said initial hydrocarbon composition, at least 2% by weight of 3-methyl-but-1-ene, at least 5% by weight of 2-methyl-but-2-ene and at least 5% by weight of 2-methyl-but-1-ene.

Claims (20)

1. A process for preparing a hydrocarbon fluid, comprising an oligomerization step of an initial hydrocarbon composition comprising at least 2% wt. of 3-methyl-but-1-ene, at least 5% wt. of 2-methyl-but-2-ene and at least 5% wt. of 2-methyl-but-1-ene relative to the total weight of the initial hydrocarbon composition.

2. The process according to claim 1 , wherein the initial hydrocarbon composition is derived from biomass.

3. The process according to claim 1 , wherein the initial hydrocarbon composition is obtained via dehydration of alcohol(s).

4. The process according to claim 1 , wherein the initial hydrocarbon composition comprises at least 20% wt. of branched olefins having 5 carbon atoms selected from among 3-methyl-but-1-ene, 2-methyl-but-2-ene and 2-methyl-but-1-ene, relative to the total weight of the initial composition.

5. The process according to claim 1 , wherein the initial hydrocarbon composition comprises at least 20% wt. of 2-methyl-but-2-ene, relative to the total weight of the composition.

6. The process according to claim 5 , wherein the initial hydrocarbon composition comprises 3-methyl-but-1-ene in a weight proportion such that the 3-methyl-but-1-ene represents the olefin having 5 carbon atoms present in majority amount in the initial hydrocarbon composition.

7. The process according to claim 1 , wherein the oligomerization step is conducted in the presence of a catalyst selected from among alumina and aluminosilicates.

8. The process according to claim 1 , wherein the catalyst is an aluminosilicate and the SiO 2 /Al 2 O 3 molar ratio of the catalyst ranges from 10 to 80.

9. The process according to claim 1 , wherein the catalyst is a mesoporous aluminosilicate having a BET specific surface area greater than or equal to 50 m 2 /g.

10. The process according to claim 1 , wherein the catalyst is an amorphous Si Al catalyst (ASA) with 5 to 95% wt. of silica (SiO 2 ), a BET specific surface area ranging from 100 to 550 m 2 /g and accessible pore size ranging from 2 to 14 nm.

11. The process according to claim 1 , implemented at a temperature ranging from 80 to 220° C.

12. The process according to claim 1 , implemented at a pressure ranging from 2 to 50 bars.

13. The process according to claim 1 , further comprising at least one treatment step.

14. The process according to claim 1 , comprising a step to recycle an effluent comprising non-reacted C5 olefins.

15. A hydrocarbon fluid capable of being obtained with a process comprising an oligomerization step of an initial hydrocarbon composition comprising at least 2% wt. of 3-methyl-but-1-ene, at least 5% wt. of 2-methyl-but-2-ene and at least 5% wt. of 2-methyl-but-1-ene relative to the total weight of the initial hydrocarbon composition.

16. A process for the formulation of inks, paints, varnishes, cleaning products, lubricants for metal working, dielectric fluids, drilling fluids, cosmetic products, said process comprising using the hydrocarbon fluid according to claim 15 as crude or hydrogenated and/or fractionated solvent cut.

17. The process according to claim 3 , wherein the alcohol(s) are selected from fusel oil.

18. The process according to claim 1 , further comprising a hydrogenation step and/or fractionation step.

19. The process according to claim 4 , wherein the initial hydrocarbon composition comprises at least 50% wt. of branched olefins having 5 carbon atoms selected from among 3-methyl-but-1-ene, 2-methyl-but-2-ene and 2-methyl-but-1-ene, relative to the total weight of the initial composition.

20. The process according to claim 5 , wherein the initial hydrocarbon composition comprises at least 50% wt. of 2-methyl-but-2-ene, relative to the total weight of the composition.

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE THE NAME OF THE ASSIGNEE PREVIOUSLY RECORDED AT REEL: 67096 FRAME: 320. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Jun 26, 2024
From: TOTALENERGIES MARKETING SERVICES (PREVIOUSLY TOTAL MARKETING SERVICES)
To: TOTALENERGIES ONETECH
Reel/Frame 067845/0906 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 12, 2024
From: TOTALENERGIES MARKETING SERVICES (PREVIOUSLY TOTAL MARKETING SERVICES)
To: TOTALENERGIES ONETECH (PREVIOUSLY TOTALENERGIES ONE TECH)
Reel/Frame 067096/0320 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 6, 2020
From: RICHARDSON, CHRISTINE-JOY; GERMANAUD, LAURENT; KRESSMANN, STÉPHANE
To: TOTAL MARKETING SERVICES
Reel/Frame 053989/0144 →
Priority Claims (2)
EP 18305298 · Mar 16, 2018 · regional
EP 19305166 · Feb 11, 2019 · regional
Continuity (1)
Related Publication 20210024437A1 · Jan 28, 2021