Producing blocks of block copolymer in a separator downstream of a reactor

Patent metadata

Field	Value
Publication number	US-11629214-B2
Application number	US-202016943374-A
Country	US
Kind code	B2
Filing date	Jul 30, 2020
Priority date	Aug 16, 2019
Publication date	Apr 18, 2023
Grant date	Apr 18, 2023

Abstract

A method for producing block copolymers can include polymerizing a feedstock comprising a monomer and a comonomer under first polymerization conditions in the presence of a catalyst in a reactor to produce a first effluent comprising a first polyolefin block, an unreacted monomer, and an unreacted comonomer; blending the first effluent with a coordinative chain transfer polymerization agent to produce a mixture; and polymerizing the mixture in a separator under second polymerization conditions to cause the unreacted monomer and the unreacted comonomer to polymerize onto one end of the first polyolefin block as a second polyolefin block, thereby forming a block copolymer, wherein the first polyolefin block has a first comonomer content and the second polyolefin block has a second comonomer content that is different than the first comonomer content. The method can further include polymerizing in presence of a second coordinative chain transfer polymerization agent in a second separator.

First claim

The invention claimed is:

1. A method for making block copolymers, comprising:
polymerizing a feedstock comprising a monomer and a comonomer under polymerization conditions in the presence of a catalyst in a reactor to produce a first effluent comprising a first polyolefin block, an unreacted monomer, and an unreacted comonomer;
removing the first effluent from the reactor;
blending the first effluent with a coordinative chain transfer polymerization agent to produce a mixture;
introducing the mixture comprising the first effluent and the coordinative chain transfer polymerization agent to a separator;
operating the separator at a higher temperature, or lower pressure, or both higher temperature and lower pressure than in the reactor to remove volatile monomer, comonomer and solvent from the separator; and
polymerizing the mixture comprising the first effluent and the coordinative chain transfer polymerization agent in the separator at the separator conditions to cause the unreacted monomer and the unreacted comonomer to polymerize onto one end of the first polyolefin block as a second polyolefin block, thereby forming a block copolymer, wherein the first polyolefin block has a first comonomer content and the second polyolefin block has a second comonomer content that is different than the first comonomer content.

2. The method of claim 1 , wherein the polymerization conditions in the reactor differ from the separator conditions by a parameter selected from the group consisting of: a relative concentration of monomer and comonomer, a catalyst composition, and any combination thereof.

3. The method of claim 2 , wherein the polymerization conditions in the reactor comprise a polymerization temperature and wherein the separator is operated at a temperature that is about 5° C. to about 80° C. higher than the polymerization temperature.

4. The method of claim 2 , wherein the polymerization conditions in the reactor comprise a polymerization pressure and wherein the separator is operated at pressure that is about 1 psig to about 5 psig less than the polymerization pressure.

5. The method of claim 2 , wherein a relative concentration of monomer and comonomer of the polymerization conditions in the reactor differs from a relative concentration of monomer and comonomer of the separator conditions by about 1.1 times to about 100 times in the separator.

6. The method of claim 1 , further comprising adding additional monomer into the first effluent during the step of blending the first effluent with the coordinative chain transfer polymerization agent.

7. The method of claim 1 , further comprising adding additional comonomer into the first effluent during the step of blending the first effluent with the coordinative chain transfer polymerization agent.

8. The method of claim 1 , wherein a second effluent comprises the block copolymer, the unreacted monomer, and the unreacted comonomer exiting the separator, and wherein the method further comprises quenching the second effluent.

9. The method of claim 8 , further comprising devolatilizing the second effluent exiting the separator after quenching the second effluent to remove volatile components.

10. The method of claim 1 , wherein the separator is a first separator that operates under first separator conditions, wherein the coordinative chain transfer polymerization agent is a first coordinative chain transfer polymerization agent, wherein a second effluent comprises the block copolymer, the unreacted monomer, and the unreacted comonomer, and wherein the method further comprises:
removing the second effluent from the first separator;
blending the second effluent with a second coordinative chain transfer polymerization agent to produce a second mixture;
introducing the second mixture comprising the second effluent and the second coordinative chain transfer polymerization agent to a second separator;
polymerizing the second mixture in the second separator under second separator conditions to cause the unreacted monomer and the unreacted comonomer to polymerize onto one end of the second polyolefin block as a third polyolefin block of the block copolymer, wherein the third polyolefin block has a third comonomer content that is different than the second comonomer content.

11. The method of claim 10 , wherein the first separator conditions differ from the second separator conditions by a parameter selected from the group consisting of: a temperature, a pressure, a residence time, a relative concentration of monomer and comonomer, a catalyst composition, and any combination thereof.

12. The method of claim 11 , wherein the temperature of the first separator conditions differs from a temperature of the second separator conditions by about 5° C. to about 80° C.

13. The method of claim 11 , wherein the pressure of the first separator conditions differs from a pressure of the second separator conditions by about 1 psig to about 5 psig.

14. The method of claim 11 , wherein the relative concentration of monomer and comonomer of the first separator conditions differs from a relative concentration of monomer and comonomer of the second separator conditions by about 1.1 times to about 100 times.

15. The method of claim 11 , further comprising adding additional monomer into the second effluent during the step of blending the second effluent with the second coordinative chain transfer polymerization agent.

16. The method of claim 11 , further comprising adding additional comonomer into the second effluent during the step of blending the second effluent with the second coordinative chain transfer polymerization agent.

17. The method of claim 11 , wherein a third effluent comprises the block copolymer, the unreacted monomer, and the unreacted comonomer exiting the second separator, and wherein the method further comprising quenching the third effluent.

18. The method of claim 1 , wherein the monomer is selected from the group consisting of: ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, dodecene, 4-methylpentene-1,3-methylpentene-1,3,5,5-trimethylhexene-1, 5-ethylnonene-1, styrene, alpha-methylstyrene, para-alkylstyrenes, vinyltoluenes, vinylnaphthalene, allyl benzene, and indene, especially styrene, paramethylstyrene, 4-phenyl-butene-1, allylbenzene, vinylcyclohexane, vinylcyclohexene, vinylnorbornene, ethylidene norbornene, cyclopentadiene, cyclopentene, cyclohexene, cyclobutene, butadiene, pentadiene, hexadiene, heptadiene, octadiene, nonadiene, decadiene, undecadiene, dodecadiene, tridecadiene, tetradecadiene, pentadecadiene, hexadecadiene, heptadecadiene, octadecadiene, nonadecadiene, icosadiene, heneicosadiene, docosadiene, tricosadiene, tetracosadiene, pentacosadiene, hexacosadiene, heptacosadiene, octacosadiene, nonacosadiene, and triacontadiene.

19. The method of claim 1 , wherein the comonomer is different than the monomer and is selected from the group consisting of: ethylene, propylene, butene, pentene, hexene, heptene, octene, nonene, decene, dodecene, 4-methylpentene-1,3-methylpentene-1,3,5,5-trimethylhexene-1, 5-ethylnonene-1, styrene, alpha-methylstyrene, para-alkylstyrenes, vinyltoluenes, vinylnaphthalene, allyl benzene, and indene, especially styrene, paramethylstyrene, 4-phenyl-butene-1, allylbenzene, vinylcyclohexane, vinylcyclohexene, vinylnorbornene, ethylidene norbornene, cyclopentadiene, cyclopentene, cyclohexene, cyclobutene, butadiene, pentadiene, hexadiene, heptadiene, octadiene, nonadiene, decadiene, undecadiene, dodecadiene, tridecadiene, tetradecadiene, pentadeca

Assignees

• Exxonmobil Chemical Patents Inc
• Exxonmobil Chemicals Patents Inc

Inventors

• Hong Yifeng
• Zhang Shanshan
• Reimers Jay L

Classifications

• C08F297/083 Primary

  the monomers being ethylene or propylene · CPC title

• C08F293/00 Primary

  Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule (on to polymers modified by introduction of unsaturated end groups C08F290/02) · CPC title