Propylene random copolymer composition for pipe applications

Patent metadata

Field	Value
Publication number	US-9587096-B2
Application number	US-201414782737-A
Country	US
Kind code	B2
Filing date	Apr 22, 2014
Priority date	Apr 22, 2013
Publication date	Mar 7, 2017
Grant date	Mar 7, 2017

Abstract

The present invention relates to a polypropylene composition comprising a propylene random copolymer (A) with at least one comonomer selected from alpha-olefins with 2 or 4 to 8 carbon atoms and a nucleating agent (B), wherein the polypropylene composition has a polydispersity index (PI) of from 2.0 to 7.0, a melt flow rate MFR 2 (2:16 kg, 230° C.) of from 0.05 to 1.0 g/10 min, determined according to ISO 1133 and a Charpy Notched Impact Strength at 0° C. of at least 4.0 kJ/m 2 , determined according to ISO 179/1eA:2000 using notched injection molded specimens, a process for producing said polypropylene composition, an article comprising said polypropylene composition and the use of said polypropylene composition for the production of an article.

First claim

The invention claimed is:

1. A polypropylene composition suitable for pipe applications comprising:
a propylene random copolymer (A) with at least one comonomer selected from alpha-olefins with 2 or 4 to 8 carbon atoms, wherein the polypropylene random copolymer (A) comprises at least a propylene random copolymer having a low molecular weight (low molecular weight (LMW) fraction) and a propylene random copolymer having a high molecular weight (high molecular weight (HMW fraction), wherein the weight average molecular weight of the low molecular weight fraction is lower than that of the high molecular weight fraction; and
a nucleating agent (B);
wherein the polypropylene composition has a polydispersity index (PI) of from 2.0 to 7.0, a melt flow rate MFR 2 (2.16 kg, 230° C.) of from 0.05 to 1.0 g/10 min, determined according to ISO 1133, and a Charpy Notched Impact Strength at 0° C. of at least 4.0 kJ/m 2 , determined according to ISO 179/1eA:2000 using notched injection moulded specimens.

2. The polypropylene composition according to claim 1 , wherein the propylene random copolymer (A) does not contain an elastomeric polymer phase dispersed therein.

3. The polypropylene composition according to claim 1 , wherein the polypropylene composition has a flexural modulus of at least 750 MPa to an upper limit of not more than 1400 MPa, determined according to ISO 178 at a test speed of 2 mm/min and a force of 100N on test specimens having a dimension of 80×10×4.0 mm 3 (length×width×thickness) prepared by injection moulding according to EN ISO 1873-2.

4. The polypropylene composition according to claim 1 , wherein the polypropylene composition has a tensile stress at yield of at least 15 MPa, determined according to ISO 527-2:1996 using type 1A injection moulded test specimens prepared according to ISO 527-2:1996.

5. The polypropylene composition according to claim 1 , wherein the polypropylene composition has a Charpy Notched Impact Strength at 23° C. of at least 30 kJ/m 2 , determined according to ISO 179/1eA:2000 using notched injection moulded specimens.

6. The polypropylene composition according to claim 1 , wherein the polypropylene composition has a Charpy Notched Impact Strength at 0° C. of at least 5 kJ/m 2 , determined according to ISO 179/1eA:2000 using notched injection moulded specimens.

7. The polypropylene composition according to claim 1 , wherein the polypropylene composition has a content of xylene cold solubles (XCS) of from 1.0 to 15.0 wt %, determined at 25° C. according to ISO 16152.

8. The polypropylene composition according to claim 1 , wherein the propylene random copolymer (A) is a propylene random copolymer with ethylene comonomer.

9. The polypropylene composition according to claim 1 , wherein the comonomer content of the propylene random copolymer (A) is in the range of 4.5 to 9.5 mol %.

10. The polypropylene composition according to claim 1 , wherein the propylene random copolymer having a high molecular weight (high molecular weight (HMW) fraction) has a higher content of comonomer than the propylene random copolymer having a low molecular weight fraction (LMW fraction).

11. The polypropylene composition according to claim 1 , wherein the propylene random copolymer having a low molecular weight is present in the propylene random copolymer in an amount of 30 to 50 wt %, based on the total amount of the propylene random copolymer (100 wt %), and the propylene random copolymer having a high molecular weight fraction is present in the propylene random copolymer in an amount of 70 to 50 wt %, based on the total amount of the propylene random copolymer (100 wt %).

12. The polypropylene composition according to claim 1 comprising from 0.1 to 10000 ppm by weight of a nucleating agent (B).

13. A process for producing a polypropylene composition according to claim 1 , wherein the propylene random copolymer is polymerized in a multistage polymerization process in the presence of:
(I) a solid catalyst component comprising a magnesium halide, a titanium halide and an internal electron donor; and
(II) a cocatalyst comprising an aluminium alkyl and optionally an external electron donor; and
(III) an optional nucleating agent (B);
the multistage process comprising the steps of:
(a) continuously polymerizing propylene together with a comonomer selected from alpha-olefins with 2 or 4 to 8 carbon atoms, in a first polymerization stage by introducing streams of propylene, hydrogen and said comonomer into the first polymerization stage at a temperature of 60 to 80° C. and a pressure of 3000 to 6500 kPa to produce a first propylene random copolymer, wherein said first propylene random copolymer has a melt flow rate MFR 2 (2.16 kg; 230° C.; ISO 1133) of from 0.2 to 3.0 g/min;
(b) withdrawing from the first polymerization stage a stream comprising said first propylene random copolymer and transferring said stream into a second polymerization stage;
(c) polymerizing propylene together with a comonomer selected from alpha-olefins with 2 or 4 to 8 carbon atoms, in said second polymerization stage by introducing streams of propylene, said comonomer and optionally hydrogen into said second polymerization stage at a temperature of 70 to 90° C. and a pressure of 1000 to 3000 kPa to produce a propylene random copolymer (A) of said first propylene random copolymer and a second propylene random copolymer;
(d) continuously withdrawing a stream comprising said propylene random copolymer (A) from the second polymerization stage and optionally mixing said propylene random copolymer (A) with additives; and
(e) extruding said propylene random copolymer mixture into pellets, which have a melt flow rate MFR 2 (2.16 kg; 230° C.; ISO 1133) of from 0.05 to 1.0 g/min.

14. The process according to claim 13 , wherein the multistage process comprises a further step (aa) preceding step (a), wherein
(aa) polymerising a vinyl compound of wherein the nucleating agent (B) is a polymer of a vinyl compound according to the following formula
CH 2 ═CH—CHR 1 R 2   (I)

wherein R 1 and R 2 together form a 5- or 6-membered saturated, unsaturated or aromatic ring, or independently represent an alkyl group comprising 1 to 4 carbon atoms, optionally containing substituents, or are independently selected from C 1 to C 4 -alkyl groups whereby in case R 1 and R 2 form an aromatic ring the hydrogen atom of the —CHR 1 R 2 moiety is not present, in the presence of a catalyst system comprising the solid catalyst component (I) to obtain a modified catalyst system which is the reaction mixture comprising the solid catalyst component (I) and the produced polymer of the vinyl compound of formula (I),
wherein the weight ratio (g) of the polymer of the vinyl compound of the formula (I) to the solid catalyst component (I) is up to 5 (5:1), and the obtained modified catalyst system is fed to polymerisation step (a) of the multistage process for producing the multimodal propylene copolymer (A).

15. The polypropylene composition according to claim 1 wherein the propylene random copolymer is polymerized in a multistage polymerization process in the presence of:
(I) a solid catalyst component comprising a magnesium halide, a titanium halide and an internal electrom donor; and
(II) a cocatalyst comprising an aluminium alkyl and optionally an external electron donor; and
(III) an optional nucleating agent (B);
the multistage process comprising the steps of:
(a) continuously polymerizing propylene together with a comonomer selected from alpha-olefins with 2 or 4 to 8 carbon atoms, in a first polymerization stage by introducing streams of propylene, hy

Assignees

• Hedesiu Cristian
• Alastalo Kauno
• Abu Dhabi Polymers Company Ltd
• Borealis Ag

Inventors

• Hedesiu Cristian
• Alastalo Kauno

Classifications

• C08L2205/24

  Crystallisation aids · CPC title

• C08L2203/18

  used for pipes · CPC title

• B29C48/919

  using a bath, e.g. extruding into an open bath to coagulate or cool the material · CPC title

• C08L23/16

  Ethylene-propylene or ethylene-propylene-diene copolymers · CPC title

• C08L23/142 Primary

  at least partially crystalline copolymers of propene with other olefins · CPC title