Methods for terminating olefin polymerizations

Patent metadata

Field	Value
Publication number	US-11299562-B2
Application number	US-202016801314-A
Country	US
Kind code	B2
Filing date	Feb 26, 2020
Priority date	Jun 20, 2012
Publication date	Apr 12, 2022
Grant date	Apr 12, 2022

Abstract

Catalyst deactivating agents and compositions containing catalyst deactivating agents are disclosed. These catalyst deactivating agents can be used in methods of controlling polymerization reactions, methods of terminating polymerization reactions, methods of operating polymerization reactors, and methods of transitioning between catalyst systems.

First claim

We claim:

1. A composition for use in an olefin polymerization reactor system, the composition consisting of:
isobutane; and
a catalyst deactivating agent that is a natural source oil, a siloxane, or a combination thereof.

2. The composition of claim 1 , wherein:
the catalyst deactivating agent is a natural source oil; and
the natural source oil is a tallow oil, an olive oil, a peanut oil, a castor bean oil, a sunflower oil, a sesame oil, a poppy seed oil, a palm oil, an almond seed oil, a hazelnut oil, a rapeseed oil, a canola oil, a soybean oil, a corn oil, a safflower oil, a cottonseed oil, a camelina oil, a flaxseed oil, a walnut oil, or any combination thereof.

3. The composition of claim 1 , wherein:
the catalyst deactivating agent is a natural source oil; and
the natural source oil is a soybean oil, a corn oil, a canola oil, a castor bean oil, or any combination thereof.

4. The composition of claim 1 , wherein:
the catalyst deactivating agent is a natural source oil; and
the natural source oil is a corn oil.

5. The composition of claim 1 , wherein:
the catalyst deactivating agent is a siloxane; and
the siloxane has the formula:

wherein:
each R independently is a C 1 to C 18 hydrocarbyl group; and
n is an integer greater than or equal to 2.

6. The composition of claim 5 , wherein:
each R independently is methyl, ethyl, propyl, butyl, phenyl, or benzyl; and
the siloxane has a viscosity in a range from 2 to 2,500 cSt at 25° C.

7. The composition of claim 1 , wherein:
the catalyst deactivating agent is a siloxane; and
the siloxane is a polydimethylsiloxane.

8. The composition of claim 7 , wherein the polydimethylsiloxane has a viscosity in a range from 2 to 1,000 cSt at 25° C.

9. The composition of claim 1 , wherein the catalyst deactivating agent:
has a boiling point of at least 100° C.;
is miscible with a C 3 to C 10 hydrocarbon solvent; and
is a liquid throughout a temperature range of 20° C. to 80° C.

10. The composition of claim 1 , wherein the catalyst deactivating agent:
has a boiling point of at least 120° C.;
is miscible with isobutane; and
is a liquid throughout a temperature range of −20° C. to 100° C.

11. The composition of claim 1 , wherein a weight ratio of isobutane to the catalyst deactivating agent is in a range from about 1000:1 to about 1:100.

12. The composition of claim 1 , wherein a weight ratio of isobutane to the catalyst deactivating agent is in a range from about 100:1 to about 1:10.

13. A composition for use in an olefin polymerization reactor system, the composition consisting of:
an alkane solvent comprising propane, isobutane, n-butane, n-pentane, isopentane, neopentane, n-hexane, heptane, octane, cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, or a mixture thereof; and
a catalyst deactivating agent comprising a siloxane characterized by a viscosity in a range from 2 to 5,000 cSt at 25° C.

14. The composition of claim 13 , wherein the siloxane comprises a polydimethylsiloxane.

15. The composition of claim 13 , wherein the viscosity is in a range from 2 to 500 cSt at 25° C.

16. The composition of claim 13 , wherein a weight ratio of the alkane solvent to the siloxane is in a range from about 100:1 to about 1:10.

17. The composition of claim 1 , wherein:
the catalyst deactivating agent comprises the natural source oil; and
the natural source oil comprises a soybean oil.

18. The composition of claim 13 , wherein the alkane solvent comprises n-pentane, isopentane, neopentane, or a mixture thereof.

19. The composition of claim 13 , wherein the alkane solvent comprises n-hexane, heptane, octane, or a mixture thereof.

20. The composition of claim 13 , wherein the alkane solvent comprises cyclohexane, cycloheptane, methylcyclohexane, methylcycloheptane, or a mixture thereof.

21. A composition for use in an olefin polymerization reactor system, the composition consisting of:
an alkane solvent having from 3 to 18 carbon atoms; and
a catalyst deactivating agent comprising a polydimethylsiloxane characterized by a viscosity in a range from 2 to 5,000 cSt at 25° C.

22. The composition of claim 21 , wherein the viscosity is in a range from 2 to 500 cSt at 25° C.

23. The composition of claim 21 , wherein a weight ratio of the alkane solvent to the polydimethylsiloxane is in a range from about 100:1 to about 1:10.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Mcdaniel Max P
• Yang Qing
• Clear Kathy S
• Crain Tony R
• Odi Timothy O

Classifications

• C08F2/40 Primary

  using retarding agents · CPC title

• C08F2410/05

  Transitioning, i.e. transition from one catalyst to another with use of a deactivating agent · CPC title

• C08F4/65927

  two cyclopentadienyl rings being mutually bridged · CPC title

• C08F2/38

  Polymerisation using regulators, e.g. chain terminating agents {, e.g. telomerisation} · CPC title

• C08F4/65912

  in combination with an organoaluminium compound · CPC title