Styrene-butadiene block copolymers for tubing applications
US-2016264773-A1 · Sep 15, 2016 · US
US9828455B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9828455-B2 |
| Application number | US-201615051807-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 24, 2016 |
| Priority date | Feb 24, 2016 |
| Publication date | Nov 28, 2017 |
| Grant date | Nov 28, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
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.
Opening claim text (preview).
We claim: 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 i
of vinyl-aromatic monomers and conjugated dienes · CPC title
using free radical "living" or "controlled" polymerisation, e.g. using a complexing agent · CPC title
made of rubber or flexible plastics · CPC title
obtained by reactions only involving carbon-to-carbon unsaturated bonds · CPC title
using a coupling agent · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.