IP Library Granted Patent US 9,828,455
Granted Patent B2
US 9,828,455 · App. 15/051,807 · Granted Nov 28, 2017

Styrene-butadiene block copolymers with an internal butadiene block for tubing applications

Inventors: Jinping Joe Zhou (Bartlesville, OK); Walter H. Pace (Bartlesville, OK); David A. Young (Caney, KS)
Assignee: INEOS STYROLUTION GROUP GMBH
C08F293/005C08L53/02
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Quick Facts
Patent No.
US 9,828,455
App. No.
15/051,807
Granted
Nov 28, 2017
Kind
B2
Abstract

Conjugated diene monovinylarene block copolymers containing an internal conjugated diene block and having superior kink resistance properties are disclosed. These copolymers can be used to produce tubing and other end-use articles, and can be a replacement for flexible PVC.

Claims (97)

1. A conjugated diene monovinylarene block copolymer comprising from about 54 phm to about 68 phm monovinylarene monomer, and comprising polymer chains containing a block structure having formula IA:

S 1 —B 1 —(S/B) 1 —(S/B) 2   (IA);

wherein:

S 1 is a monoblock of the monovinylarene monomer, wherein S 1 is from about 28 phm to about 38 phm of the copolymer;

B 1 is a first monoblock of the conjugated diene monomer, wherein B 1 is from about 2 phm to about 8 phm of the copolymer;

(S/B) 1 is a mixed block of the conjugated diene monomer and the monovinylarene monomer, wherein the monovinylarene monomer content is from about 50 wt. % to about 65 wt. %, based on the total weight of (S/B) 1 ; and

(S/B) 2 is a mixed block of the conjugated diene monomer and the monovinylarene monomer, wherein the conjugated diene monomer content is from about 75 wt. % to about 95 wt. %, based on the total weight of (S/B) 2 ; and

wherein a kink resistance of tubing produced from the copolymer and tested in accordance with DIN EN 13868 is less than or equal to about 32 mm.

2. The copolymer of claim 1 , wherein:

S 1 is in a range from about 30 phm to about 36 phm; and

B 1 is in a range from about 3 phm to about 7 phm.

3. The copolymer of claim 1 , wherein the copolymer comprises monovinylarene monomer in a range from about 56 phm to about 66 phm.

4. The copolymer of claim 1 , wherein:

the monovinylarene monomer is styrene;

the conjugated diene monomer is a butadiene; and

the kink resistance is in a range from about 8 to about 24 mm.

5. The copolymer of claim 1 , wherein the copolymer is a styrene butadiene block copolymer.

6. The copolymer of claim 1 , wherein

the conjugated diene monomer content in (S/B) 2 is in a range from about 82 wt. % to about 92 wt. %, based on (S/B) 2 .

7. The copolymer of claim 1 , wherein S 1 is two or more monoblocks of the monovinylarene monomer.

8. The copolymer of claim 1 , wherein the copolymer further comprises polymer chains containing a block structure having formula IIA:

S 2 —B 1 —(S/B) 1 —(S/B) 2   (IIA);

wherein:

S 2 is a monoblock of the monovinylarene monomer, wherein S 2 is from about 14 phm to about 20 phm of the copolymer.

9. The copolymer of claim 1 , wherein (S/B) 1 is two mixed blocks of the conjugated diene monomer and the monovinylarene monomer having formula III:

—(S/B) 1A —(S/B) 1B —  (III);

wherein:

the monovinylarene monomer content in (S/B) 1A is from about 30 wt. % to about 80 wt. % of (S/B) 1A ; and the monovinylarene monomer content in (S/B) 1B is from about 30 wt. % to about 80 wt. % of (S/B) 1B .

10. The copolymer of claim 9 , wherein the monovinylarene monomer content in (S/B) 1A is from about 45 wt. % to about 60 wt. %, and the monovinylarene monomer content in (S/B) 1B is from about 50 wt. % to about 65 wt. %.

11. The copolymer of claim 1 , wherein the conjugated diene monovinylarene block copolymer is a styrene butadiene block copolymer with a kink resistance in a range from about 8 mm to about 26 mm.

12. The copolymer of claim 11 , wherein the copolymer has:

a melt flow rate at 200° C. with a 5 Kg load in a range from about 2 to about 20 g/10 min; and

a Shore A hardness in a range from about 65 to about 90.

13. The copolymer of claim 11 , wherein the copolymer has:

a pellet blocking force of less than or equal to about 120 lb f ; and

a re-kink resistance in a range from about 12 mm to about 28 mm.

14. An article of manufacture comprising the copolymer of claim 1 .

15. A tubing product comprising the copolymer of claim 1 .

16. A composition comprising the copolymer of claim 1 and a second polymer.

17. A process to produce a conjugated diene monovinylarene block copolymer comprising from about 35 phm to about 75 phm monovinylarene monomer, and comprising polymer chains containing a block structure having formula IA:

S 1 —B 1 —(S/B) 1 —(S/B) 2   (IA);

wherein:

S 1 is a monoblock of the monovinylarene monomer, wherein S 1 is from about 15 phm to about 45 phm of the copolymer;

B 1 is a first monoblock of the conjugated diene monomer, wherein B 1 is from about 0.5 phm to about 10 phm of the copolymer;

(S/B) 1 is a mixed block of the conjugated diene monomer and the monovinylarene monomer, wherein the monovinylarene monomer content is from about 30 wt. % to about 80 wt. %, based on the total weight of (S/B) 1 ; and

(S/B) 2 is a mixed block of the conjugated diene monomer and the monovinylarene monomer, wherein the conjugated diene monomer content is from about 70 wt. % to about 99 wt. %, based on the total weight of (S/B) 2 ; and

wherein a kink resistance of tubing produced from the copolymer and tested in accordance with DIN EN 13868 is less than or equal to about 32 mm;

the process comprising contacting:

(i) a first initiator charge and a first charge of the monovinylarene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (i) with

(ii) a second initiator charge and a second charge of the monovinylarene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (ii) with

(iii) a first charge of the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (iii) with

(iv) a first mixture of the monovinylarene monomer and the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (iv) with

(v) a second mixture of the monovinylarene monomer and the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (v) with

(vi) a third mixture of the monovinylarene monomer and the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (vi) with

(vii) a coupling agent.

18. The process of claim 17 , wherein at least one step in the process comprises polymerization in the presence of a modifier, and/or an additional initiator is used in at least one of steps (iii) to (vi).

19. A process to produce a conjugated diene monovinylarene block copolymer comprising from about 35 phm to about 75 phm monovinylarene monomer, and comprising polymer chains containing a block structure having formula IB:

S 1 —B 1 —(S/B) 1 —B 2   (IB);

wherein:

S 1 is a monoblock of the monovinylarene monomer, wherein S 1 is from about 15 phm to about 45 phm of the copolymer;

B 1 is a first monoblock of the conjugated diene monomer, wherein B 1 is from about 0.5 phm to about 10 phm of the copolymer;

(S/B) 1 is a mixed block of the conjugated diene monomer and the monovinylarene monomer, wherein the monovinylarene monomer content is from about 30 wt. % to about 80 wt. %, based on the total weight of (S/B) 1 ; and

B 2 is a second monoblock of the conjugated diene monomer, wherein B 2 is from about 8 phm to about 30 phm of the copolymer; and

wherein a kink resistance of tubing produced from the copolymer and tested in accordance with DIN EN 13868 is less than or equal to about 32 mm;

the process comprising contacting:

(i) a first initiator charge and a first charge of the monovinylarene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (i) with

(ii) a second initiator charge and a second charge of the monovinylarene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (ii) with

(iii) a first charge of the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (iii) with

(iv) a first mixture of the monovinylarene monomer and the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (iv) with

(v) a second mixture of the monovinylarene monomer and the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (v) with

(vi) a second charge of the conjugated diene monomer and allowing polymerization to occur until minimal free monomer is present; thereafter contacting all products of step (vi) with

(vii) a coupling agent.

20. The process of claim 19 , wherein at least one step in the process comprises polymerization in the presence of a modifier, and/or an additional initiator is used in at least one of steps (iii) to (vi).

21. A conjugated diene monovinylarene block copolymer comprising from about 54 phm to about 68 phm monovinylarene monomer, and comprising polymer chains containing a block structure having formula IB:

S 1 —B 1 —(S/B) 1 —B 2   (IB);

wherein:

S 1 is a monoblock of the monovinylarene monomer, wherein S 1 is from about 28 phm to about 38 phm of the copolymer;

B 1 is a first monoblock of the conjugated diene monomer, wherein B 1 is from about 2 phm to about 8 phm of the copolymer;

(S/B) 1 is a mixed block of the conjugated diene monomer and the monovinylarene monomer, wherein the monovinylarene monomer content is from about 50 wt. % to about 65 wt. %, based on the total weight of (S/B) 1 ; and

B 2 is a second monoblock of the conjugated diene monomer, wherein B 2 is from about 10 phm to about 25 phm of the copolymer; and

wherein a kink resistance of tubing produced from the copolymer and tested in accordance with DIN EN 13868 is less than or equal to about 32 mm.

22. The copolymer of claim 21 , wherein:

B 2 is from about 12 phm to about 22 phm of the copolymer;

the monovinylarene monomer is styrene;

the conjugated diene monomer is a butadiene; and

the kink resistance is in a range from about 8 to about 24 mm.

23. A tubing product comprising the copolymer of claim 22 .

24. The copolymer of claim 21 , wherein the conjugated diene monovinylarene block copolymer is a styrene butadiene block copolymer with a kink resistance in a range from about 8 mm to about 26 mm.

25. The copolymer of claim 21 , wherein:

the copolymer further comprises polymer chains containing a block structure having formula IIB:

S 2 —B 1 —(S/B) 1 —B 2   (IIB);

wherein:

S 2 is a monoblock of the monovinylarene monomer, wherein S 2 is from about 14 phm to about 20 phm of the copolymer; and

(S/B) 1 is two mixed blocks of the conjugated diene monomer and the monovinylarene monomer having formula III:

—(S/B) 1A —(S/B) 1B —  (III);

wherein:

the monovinylarene monomer content in (S/B) 1A is from about 30 wt. % to about 80 wt. % of (S/B) 1A ; and the monovinylarene monomer content in (S/B) 1B is from about 30 wt. % to about 80 wt. % of (S/B) 1B .

Assignments (3)
FIRST LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Apr 30, 2021
From: INEOS STYROLUTION GROUP GMBH
To: HSBC CORPORATE TRUSTEE COMPANY (UK) LIMITED
Reel/Frame 056103/0236 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 12, 2017
From: CHEVRON PHILLIPS CHEMICAL COMPANY LP
To: INEOS STYROLUTION GROUP GMBH
Reel/Frame 042353/0418 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 7, 2016
From: ZHOU, JINPING JOE; PACE, WALTER H.; YOUNG, DAVID A.
To: CHEVRON PHILLIPS CHEMICAL COMPANY LP
Reel/Frame 038828/0026 →
Continuity (1)
Related Publication 20170240678A1 · Aug 24, 2017