Process for the preparation of a block copolymer composition

• US 5,994,476 A
• Filed: 07/14/1998
• Issued: 11/30/1999
• Est. Priority Date: 08/27/1997
• Status: Expired due to Term

• Current Assignee: Korea Kumho Petrochemical Co Limited (Korea Kumho Petrochemical)
• Original Assignee: Korea Kumho Petrochemical Co Limited (Korea Kumho Petrochemical)
• Inventors: Kim, Jin-Kyung, Kim, Jong-Geun, Shin, Hyeon-Cheol
• Primary Examiner(s): Truong, Duc
• Application Number:
  US09/114,842
• Time in Patent Office: 504 Days
• Field of Search: 525/333.3, 525/88, 525/95, 525/191, 525/192, 525/197, 525/198, 525/242, 525/250, 525/331.9
• US Class Current: 525/333.3
• CPC Class Codes: C08F 297/04 polymerising vinyl aromatic monomers and conjugated dienes

Abstract

This invention relates to a process for preparing a block copolymer composition, wherein it comprises following successive steps:

a step in which a vinyl aromatic monomer is polymerized in a reactor in the presence of an inert hydrocarbon solvent and organolithium initiator until depletion of the monomer to generate a living polymer; a step in which a conjugated diene monomer is added to the above polymer to synthesize a living diblock copolymer; a step in which a portion of polymerization terminator is added to partially inactivate the living diblock copolymer; steps in which a conjugated diene monomer and aromatic vinyl monomer are sequentially added to generate a mixture of living triblock copolymer and inactivated diblock copolymer; a step in which a polymerization terminator is added to complete the reaction.

This invention has advantages of providing easy, wide-range and fine control of block copolymer compositions in a reactor via well-controlled termination reactions during the sequential block copolymerization.

Claims

1. A Process for preparing a block copolymer composition comprising the following successive steps:

(1) a step in which a vinyl aromatic monomer and organolithium initiator are introduced into a reactor in the presence of an inert hydrocarbon solvent and polymerized until depletion of the monomer;

(2) a step in which a conjugated diene monomer is added to the polymerization mixture and polymerized until depletion of the monomer;

(3) a step in which a polymerization terminator is added to the polymerization mixture to partially inactivate the living polymer;

(4) a step in which a conjugated diene monomer is added to the polymerization mixture and polymerized until depletion of the monomer;

(5) a step in which a vinyl aromatic monomer is added to the polymerization mixture and polymerized until depletion of the monomer;

(6) a step in which a polymerization terminator is added to the polymerization mixture so as to complete the reaction.

2. The process for preparing a block copolymer composition according to claim 1, wherein said inert hydrocarbon solvent includes cyclohexane, cyclopentane, n-hexane, n-heptane and mixtures thereof.

3. The process for preparing a block copolymer composition according to claim 1, wherein said organolithium initiator includes n-butyl lithium and sec-butyl lithium.

4. The process for preparing a block copolymer composition according to claim 1, wherein said vinyl aromatic monomer includes styrene.

5. The process for preparing a block copolymer composition according to claim 1, wherein said conjugated diene monomer includes 1,3-butadiene, 2-methyl-1,3-butadiene and mixtures thereof.

6. The process for preparing a block copolymer composition according to claim 5, wherein said conjugated diene monomer includes 2-methyl-1,3-butadiene.

7. The process for preparing a block copolymer composition according to claim 1, wherein the amount of said polymerization terminator added in the partial inactivation of the living diblock copolymer is cotrolled in such a manner that the diblock content in the final polymer composition is in the range of 5 to 95 wt %.

8. The process for preparing a block copolymer composition according to claim 1, wherein the amount of said polymerization terminator added in the partial inactivation of the living diblock copolymer is cotrolled in such a manner that the diblock content in the final polymer composition is in the range of 5 to 70 wt %.

9. The process for preparing a block copolymer composition according to claim 1, wherein the molecular weight ratio between respective conjugated diene block in the diblock and triblock copolymer is in the range of 0.45 to 0.55.

10. The process for preparing a block copolymer composition according to claim 1, wherein the molecular weight ratio between two vinyl aromatic blocks in a triblock copolymer is in the range of 0.9 to 1.1.

11. The process for preparing a block copolymer composition according to claim 1, wherein the block copolymer is prepared in such a manner that the vinyl aromatic content is in the range of 10 to 95 wt. %.

12. The process for preparing a block copolymer composition according to claim 1, wherein said block copolymer is prepared in such a manner that the vinyl aromatic content is in the range of 10 to 50 wt. %.