Methods of catalyst activation

Patent metadata

Field	Value
Publication number	US-9260541-B2
Application number	US-78281010-A
Country	US
Kind code	B2
Filing date	May 19, 2010
Priority date	Nov 17, 2008
Publication date	Feb 16, 2016
Grant date	Feb 16, 2016

Abstract

A method comprising preparing a multi-component catalyst system comprising a catalyst and a cocatalyst, and adjusting the level of at least one component of the catalyst system to maintain a user-desired level of catalyst activity throughout a process, wherein the component comprises a catalyst activator and wherein the catalyst activator comprises the catalyst or the cocatalyst. A method comprising contacting a polymerization catalyst system comprising a Ziegler-Natta catalyst and a cocatalyst with a catalyst activator at least twice during a polymerization process, wherein the polymerization process is carried out in a reactor system comprising multiple reactor types.

First claim

What is claimed is:

1. A method for manufacturing a bi-phasic propylene impact copolymer comprising:
contacting a propylene monomer and ethylene comonomer with a catalyst system in a reactor system comprising one or more loop reactors disposed upstream of a gas phase reactor;
introducing a first quantity of a first catalyst activator to the reactor system for contact with the propylene monomer and ethylene comonomer;
introducing a second quantity of a second catalyst activator to the reactor system for contact with the propylene monomer and ethylene comonomer;
forming the bi-phasic propylene impact copolymer;
wherein the catalyst system, the first catalyst activator, and the second catalyst activator each independently include a cocatalyst; and
wherein each independent cocatalyst is introduced into the reactor system such that the first catalyst activator is introduced downstream from a reactor in which the catalyst system is introduced into the reactor system, and wherein the second catalyst activator is introduced downstream from introduction of the first catalyst activator.

2. The method of claim 1 , wherein the catalyst system comprises a Ziegler-Natta catalyst.

3. The method of claim 1 , wherein the co-catalyst of the catalyst system, the first catalyst activator and the second catalyst activator independently comprises triethylaluminum, tri-isobutylaluminum, diethylaluminum chloride, diethylaluminum hydride, methylalumoxane, tri-isobutylaluminum, isoprenylaluminum, or combinations thereof.

4. The method of claim 1 , wherein the polymer yield is increased by greater than 5% when compared to an otherwise similar process lacking the introduction of the second quantity of catalyst activator.

5. The method of claim 4 , wherein the polymer yield is increased by greater than 10% when compared to an otherwise similar process lacking the introduction of the second quantity of catalyst activator.

6. The method of claim 4 , wherein the polymer yield is increased by greater than 20% when compared to an otherwise similar process lacking the introduction of the second quantity of catalyst activator.

7. The method of claim 4 , wherein the polymer yield is increased by greater than 30% when compared to an otherwise similar process lacking the introduction of the second quantity of catalyst activator.

8. The method of claim 1 , wherein the first catalyst activator and the second catalyst activator are of the same chemical composition.

9. The method of claim 1 further comprising introducing an external electron donor to the reactor system and contacting the external electron donor with the propylene monomer and ethylene comonomer.

10. The method of claim 9 wherein the external electron donor is cyclohexylmethyl dimethoxysilane, dicyclopentyl dimethoxysilane or diisopropyl dimethoxysilane.

11. The method of claim 1 , wherein the bi-phasic propylene impact copolymer comprises a homopolymer phase and a random copolymer phase.

12. The method of claim 11 , wherein the homopolymer phase of the bi-phasic propylene impact copolymer is comprised of propylene.

13. The method of claim 12 , wherein the copolymer phase of the bi-phasic propylene impact copolymer is comprised of a random copolymer of ethylene and propylene.

14. The method of claim 13 , wherein the random copolymer of ethylene and propylene is an ethylene/propylene rubber.

15. The method of claim 1 wherein the amount of cocatalyst in the catalyst system is more than the total amount of cocatalyst in the first catalyst activator and second catalyst activator combined.

16. The method of claim 1 , wherein the first catalyst activator is introduced upstream of the gas phase reactor.

17. The method of claim 16 , wherein the one or more loop reactors comprise a prepolymerization reactor, and wherein the first catalyst activator is introduced downstream of the prepolymerization reactor.

18. The method of claim 16 , wherein the first catalyst activator is introduced between two loop reactors of the reactor system.

19. The method of claim 16 , wherein the first catalyst activator is introduced into a loop reactor of the reactor system.

20. The method of claim 16 , wherein the second catalyst activator is introduced directly into the gas phase reactor.

21. The method of claim 1 , wherein the second catalyst activator is introduced upstream of the gas phase reactor.

Assignees

• Blackmon Kenneth P
• Ribour David
• Malbari Shabbir
• Coffy Tim
• Daumerie Michel
• Fina Technology

Inventors

• Blackmon Kenneth P
• Ribour David
• Malbari Shabbir
• Coffy Tim
• Daumerie Michel

Classifications

• C08F10/00 Primary

  Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title

• C08F210/06 Primary

  Propene · CPC title

• C08F4/642

  Component covered by group C08F4/64 with an organo-aluminium compound {(C08F4/64003 - C08F4/64196 take precedence)} · CPC title

• C08F4/6465

  containing silicium · CPC title

• C08F2500/12

  Melt flow index or melt flow ratio · CPC title