Reduced polymer formation for selective ethylene oligomerizations

Patent metadata

Field	Value
Publication number	US-10414698-B2
Application number	US-201615167024-A
Country	US
Kind code	B2
Filing date	May 27, 2016
Priority date	May 27, 2016
Publication date	Sep 17, 2019
Grant date	Sep 17, 2019

Abstract

Disclosed herein are processes, systems, and reaction systems for the oligomerization of ethylene to form an ethylene oligomer product in a reaction zone using a catalyst system having i) a chromium component comprising a heteroatomic ligand chromium compound complex of the type disclosed herein, and ii) an aluminoxane. A C3+ olefin can be present in the reaction zone for a period of time, where the C3+ olefin is not an ethylene oligomer formed in-situ within the reaction zone.

First claim

What is claimed is:

1. A. process comprising:
a) contacting i) ethylene, ii) a catalyst system comprising (a) a chromium component comprising a heteroatomic ligand chromium compound complex, and (b) an aluminoxane, iii) an organic reaction medium, and iv) optionally hydrogen in a reaction zone;
b) forming an ethylene oligomer product in the reaction zone;
wherein the ethylene, the catalyst system, and the organic reaction medium are introduced into the reaction zone, and for a C 3+ olefin/ethylene feed period of time a C 3+ olefin is introduced into the reaction zone,
wherein over a reaction zone period of time the reaction zone has a C 3+ olefin:ethylene weight ratio that decreases from a value of at least 0.5:1 to a value less than 0.2:1,
wherein the C 3+ olefin in the reaction zone that is used to determine the C 3+ olefin:ethylene weight ratio in the reaction zone is not an ethylene oligomer formed in-situ within the reaction zone, and
wherein the heteroatomic ligand chromium complex has the formula

where
each X 1s is independently selected from the group consisting of N, P, O, and S;
L 1s is a C 1 to C 20 organylene linking group, a C 1 to C 30 amin-di-yl group, or a C 1 to C 30 phosphin-di-yi group linking X 1s s;
each m is independently 1 or 2;
each R 1s is independently a C 1 to C 20 organyl group;
X is a halide, a C 1 to C 20 carboxylate, a C 1 to C 20 β-diketonate, or a C 1 to C 20 hydrocarboxide; and
p is from 2 to 6.

2. The process of claim 1 , wherein over the C 3+ olefin/ethylene period of time, ethylene and the C 3+ olefin are fed to the reaction zone at a C 3+ olefin:ethylene weight ratio that decreases from a value of at least 0.5:1 to a value less than 0.2:1.

3. The process of claim 2 , wherein ethylene and the C 3+ olefin are separately introduced to the reaction zone.

4. The process of claim 2 , wherein ethylene, the C 3+ olefin, and the organic reaction medium are contacted to form a feedstock mixture and the feedstock mixture is introduced into the reaction zone.

5. The process of claim 1 , wherein the C 3+ olefin comprises 1-hexene, 1-octene, or 1-hexene and 1-octene.

6. The process of claim 1 , wherein after the C 3+ olefin/ethylene feed period of time, ethylene and the organic reaction medium are contacted to form a feedstock mixture prior to ethylene contacting the catalyst system.

7. The process of claim 6 , wherein the catalyst system is introduced into the reaction zone separately from the feedstock mixture.

8. The process of claim 1 , wherein the catalyst system is formed in-situ within the reaction zone.

9. The process of claim 1 , wherein the ethylene oligomer product comprises hexenes and/or octenes.

10. The process of claim 1 ., wherein a mass of polymer per mass of oligomer in the reaction zone is less than the mass of polymer per mass of oligomer in the reaction zone in an otherwise similar process where the C 3+ olefin is not introduced to the reaction zone.

11. The process of claim 1 , having a productivity greater than a productivity in an otherwise similar process where the C 3+ olefin is not introduced to the reaction zone.

12. A process comprising:
a) introducing into a reaction zone containing a C 3+ olefin and optionally an organic reaction medium wherein the reaction zone is substantially devoid of ethylene;
i) ethylene
ii) a catalyst system comprising (a) a chromium component comprising a heteroatomic ligand chromium compound complex, and (b) an aluminoxane,
iii) the organic reaction medium, and
iv) optionally hydrogen; and

b) forming an ethylene oligomer product in the reaction zone;
wherein over a period of time the reaction zone has a C 3+ olefin:ethylene weight ratio that decreases from a value of at least 0.5:1 to a value less than 0.2:1,
wherein the C 3+ olefin in the reaction zone that is used to determine the C 3+ olefin:ethylene weight ratio in the reaction zone is not an ethylene oligomer formed in-situ within the reaction zone, and
wherein the heteroatomic ligand chromium complex has the formula

where
each X 1s is independently selected from the group consisting of N, P, O, and S;
L 1s is a C 1 to C 20 organylene linking group, a C 1 to C 30 amin-di-yl group, or a C 1 to C 30 phosphin-di-yl group linking X 1s s;
each m is independently 1 or 2;
each R 1s is independently a C l to C 20 organyl group;
X is a halide, a C 1 to C 20 carboxylate, a C 1 to C 20 β-diketonate, or a C 1 to C 20 hydrocarboxide; and
p is from 2 to 6.

13. The process of claim 12 ., wherein the C 3+ olefin comprises 1-hexene, 1-octene, or a combination thereof, wherein the. 1-hexene and 1-octene is not an ethylene oligomer formed in-situ within the reaction zone.

14. The process of claim 12 , wherein, after the period of time, ethylene and the organic reaction medium are contacted to form a feedstock mixture prior to ethylene contacting the catalyst system.

15. The process of claim 12 , wherein the ethylene oligomer product comprises hexenes and/or octenes.

16. The process of claim 12 , wherein a mass of polymer per mass of oligomer in the reaction zone is less than the mass of polymer per mass of oligomer in the reaction zone in an otherwise similar process where ethylene is introduced into the reaction zone which does not contain the C 3+ olefin.

17. The process of claim 12 , having a productivity greater than a productivity in an otherwise similar process where ethylene is introduced into the reaction zone which does not contain the C 3+ olefin.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Fern Jared T
• Sydora Orson L
• Kilgore Uriah J
• Bischof Steven M
• Fernandez Eric R

Classifications

• C07C2531/24

  Phosphines · CPC title

• C07C2531/14

  of aluminium or boron · CPC title

• C07C2/36 Primary

  as phosphines, arsines, stilbines or bismuthines · CPC title

• Y02P20/52

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

• B01J8/00

  Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes · CPC title