IP Library Granted Patent US 10,400,056
Granted Patent B2
US 10,400,056 · App. 16/008,781 · Granted Sep 3, 2019

Block copolymers including high vinyl segments

Inventors: Christine M. Rademacher (Akron, OH); Daniel F. Graves (Canal Fulton, OH)
Assignee: Firestone Polymers, LLC
C08F297/04C08F293/00C08F297/00
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Quick Facts
Patent No.
US 10,400,056
App. No.
16/008,781
Granted
Sep 3, 2019
Kind
B2
Abstract

A method for the preparation of block copolymers including at least one high vinyl segment, the method comprising (i) charging into a reactor a diene monomer in a hydrocarbon solvent, a catalytically effective amount of anionic initiator, and an oligomeric oxolanyl propane, whereby the reactor is optionally cooled; (ii) allowing the diene monomer to polymerize at a peak polymerization temperature of at least about 18° C. and less than about 60° C. to form a first block where the vinyl content is at least about 50 percent by weight; (iii) after step (ii), charging into the reactor a vinyl aromatic monomer, whereby the reactor is optionally heated to a temperature up to about 60° C.; (iv) allowing the vinyl aromatic monomer to polymerize to form a second block; and (v) optionally charging into the reactor a quenching agent.

Claims (41)

1. A method for the preparation of block copolymers including at least one high vinyl segment the method comprising steps of:

(i) charging into a reactor 1,3-butadiene monomer in a hydrocarbon solvent, a catalytically effective amount of anionic initiator, and an oligomeric oxolanyl propane, where the concentration of the oligomeric oxolanyl propane is at least 0.1 and less than 20 moles per mole of initiator, whereby the reactor is optionally cooled;

(ii) allowing the 1,3-butadiene monomer to polymerize at a peak polymerization temperature of at least about 18° C. and less than about 60° C. to form a first polybutadiene block characterized by a vinyl content of at least 70 percent by weight, the first polybutadiene block having less than 180 mer units;

(iii) after step (ii), charging into the reactor a vinyl aromatic monomer, whereby the reactor is optionally heated to a temperature up to about 60° C.;

(iv) allowing the vinyl aromatic monomer to polymerize to form a second block;

(v) after step (iv), charging additional monomer into the reactor, wherein the additional monomer is conjugated diene monomer;

(vi) allowing the additional conjugated diene monomer to polymerize to thereby form a third block; and

(vii) charging into the reactor a quenching agent;

where the method produces a block copolymer having an overall vinyl content that is greater than 70 percent by weight.

2. The method of claim 1 , where the concentration of the oligomeric oxolanyl propane in step (i) is at least 0.1 and less than 5 moles per mole of initiator.

3. The method of claim 1 , where step (ii) includes allowing the 1,3-butadiene monomer to polymerize at a peak polymerization temperature of at least about 18° C. and less than about 46° C.

4. The method of claim 1 , further comprising, between step (iv) and step (v), a step of dropping to a temperature below 30° C.

5. The method of claim 1 , where the peak polymerization temperature achieved during step (vi) is at least 18° C. and less than 55° C.

6. The method of claim 1 , further comprising, between steps (vi) and (vii), steps of:

a. further charging into the reactor additional vinyl aromatic monomer; and

b. allowing the additional vinyl aromatic monomer to polymerize to thereby form a fourth block.

7. The method of claim 1 , where step (iii) includes the reactor being heated to a temperature up to about 60° C.

8. The method of claim 1 , where the first polybutadiene block is characterized by a vinyl content of at least 80 percent by weight.

9. The method of claim 1 , where the first polybutadiene block is characterized by a vinyl content of at least 85 percent by weight.

10. The method of claim 1 , where the method produces a block copolymer having an overall vinyl content that is greater than 80 percent by weight.

11. The method of claim 1 , where the method produces a block copolymer having an overall vinyl content that is greater than 85 percent by weight.

12. The method of claim 1 , where the third block is characterized by a vinyl content of at least 70 percent by weight.

13. A method for the preparation of block copolymers including at least one high vinyl segment the method comprising steps of:

(i) charging into a reactor conjugated diene monomer in a hydrocarbon solvent, a catalytically effective amount of anionic initiator, and an oligomeric oxolanyl propane, where the concentration of the oligomeric oxolanyl propane is at least 0.1 and less than 20 moles per mole of initiator, whereby the reactor is optionally cooled;

(ii) allowing the conjugated diene monomer to polymerize at a peak polymerization temperature of at least about 18° C. and less than about 60° C. to form a first block characterized by a vinyl content of at least 70 percent by weight, the first block having less than 180 mer units;

(iii) after step (ii), charging into the reactor a vinyl aromatic monomer, whereby the reactor is optionally heated to a temperature up to about 60° C.;

(iv) allowing the vinyl aromatic monomer to polymerize to form a second block;

(v) after step (iv), charging additional conjugated diene monomer into the reactor;

(vi) allowing the additional conjugated diene monomer to polymerize to thereby form a third block; and

(vii) charging into the reactor a quenching agent;

where the method produces a block copolymer having an overall vinyl content that is greater than 70 percent by weight.

14. A method for the preparation of block copolymers including at least one high vinyl segment the method comprising steps of:

(i) charging into a reactor conjugated diene monomer in a hydrocarbon solvent, a catalytically effective amount of anionic initiator, and an oligomeric oxolanyl propane, whereby the reactor is optionally cooled;

(ii) allowing the conjugated diene monomer to polymerize to form a first block, the first block having less than 180 mer units;

(iii) after step (ii), charging into the reactor a vinyl aromatic monomer, whereby the reactor is optionally heated to a temperature up to about 60° C.;

(iv) allowing the vinyl aromatic monomer to polymerize to form a second block;

(v) after step (iv), charging additional conjugated diene monomer into the reactor;

(vi) allowing the additional conjugated diene monomer to polymerize to thereby form a third block;

(vii) after step (vi), further charging into the reactor additional vinyl aromatic monomer;

(viii) allowing the additional vinyl aromatic monomer to polymerize to thereby form a fourth block; and

(ix) charging into the reactor a quenching agent.

Assignments (6)
TERMINATION AND RELEASE OF SECURITY INTEREST IN PATENTS Recorded Sep 19, 2023
From: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
To: LION ELASTOMERS ORANGE, LLC
Reel/Frame 064950/0272 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 27, 2019
From: FIRESTONE POLYMERS, LLC
To: LION ELASTOMERS ORANGE, LLC
Reel/Frame 050178/0292 →
SECURITY INTEREST Recorded Aug 2, 2019
From: LION ELASTOMERS ORANGE, LLC
To: CORTLAND CAPITAL MARKET SERVICES LLC
Reel/Frame 049947/0650 →
NOTICE OF GRANT OF SECURITY INTEREST IN PATENTS Recorded Aug 1, 2019
From: LION ELASTOMERS ORANGE, LLC
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 049933/0229 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 22, 2019
From: BRIDGESTONE CORPORATION
To: FIRESTONE POLYMERS, LLC
Reel/Frame 049249/0605 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 14, 2018
From: RADEMACHER, CHRISTINE; GRAVES, DANIEL
To: BRIDGESTONE CORPORATION
Reel/Frame 046092/0116 →
Continuity (5)
Continuation 15665849 · Aug 1, 2017
Continuation 14330468 · Jul 14, 2014
Continuation 12508296 · Jul 23, 2009
Provisional Application 61083305 · Jul 24, 2008
Related Publication 20180291135A1 · Oct 11, 2018