IP Library Granted Patent US 11,845,857
Granted Patent B2
US 11,845,857 · App. 17/270,789 · Granted Dec 19, 2023

Polypropylene composition with excellent stiffness and impact strength

Inventors: Katja Klimke (Abu Dhabi, AE); Hans Jozef Francois Van Cauwenberghe (Abu Dhabi, AE)
Assignees: ABU DHABI POLYMERS CO. LTD (BOROUGE) L.L.C.; BOREALIS AG
C08L23/142B01J19/06B01J19/245B01J19/2455C08F210/16C08K5/0083C08L23/16C08L2205/025C08L2205/03C08L2205/24C08L2207/02C08L2314/02
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Quick Facts
Patent No.
US 11,845,857
App. No.
17/270,789
Granted
Dec 19, 2023
Kind
B2
Abstract

The present invention is directed to a polypropylene composition (C) comprising an α-nucleated heterophasic composition (HECO) comprising a (semi)crystalline polypropylene (PP1), an elastomeric ethylene/propylene copolymer (EPR) and a first α-nucleating agent (NU1), an impact modifier comprising a polyethylene (PE) being a copolymer of ethylene and a C 4 -C 12 α-olefin and a second α-nucleating agent (NU2). The present invention is further directed to a method for preparing said polypropylene composition (C) and an article comprising said polypropylene composition (C). The present invention is also directed to the use of a composition comprising a polyethylene (PE) being a copolymer of ethylene and a C 4 -C 12 α-olefin and an α-nucleating agent (NU2) as an impact modifier.

Claims (42)

1. A polypropylene composition (C), comprising:

(a) at least 80.0 wt. % of an α-nucleated heterophasic composition (HECO), comprising

(a1) a (semi)crystalline polypropylene (PP1),

(a2) an elastomeric ethylene/propylene copolymer (EPR) dispersed in said (semi)crystalline polypropylene (PP1),

(a3) a first α-nucleating agent (NU1),

(b) at least 5.0 wt. % of a polyethylene (PE) being a copolymer of ethylene and a C 4 -C 12 α-olefin having a density in the range of 890 to 940 kg/m 3 , and

(c) at least 1.4 wt. % of a second α-nucleating agent (NU2) which is different from the first α-nucleating agent (NU1),

based on the overall weight of the polypropylene composition (C).

2. The polypropylene composition (C) according to claim 1 , wherein the heterophasic composition (HECO) has:

i) a melt flow rate MFR 2 (230° C., 2.16 kg) determined according to ISO 1133 in the range of 5.0 to 40.0 g/10 min, and/or

ii) a comonomer content in the range of 2.0 to 15.0 mol.

3. The polypropylene composition (C) according to claim 1 , wherein the (semi)crystalline polypropylene (PP1) comprises at least two (semi)crystalline polypropylene fractions which differ in the melt flow rate MFR 2 (230° C., 2.16 kg) determined according to ISO 1133.

4. The polypropylene composition (C) according to claim 1 , wherein the (semi)crystalline polypropylene (PP1) comprises:

(a) a first (semi)crystalline polypropylene fraction (PP1a) having a melt flow rate MFR 2 (230° C./2.16 kg) in the range of 30.0 to 120.0 g/10 min, and

(b) a second (semi)crystalline polypropylene fraction (PP1b) having a melt flow rate MFR 2 (230° C./2.16 kg) in the range of 5.0 to 25.0 g/10 min.

5. The polypropylene composition (C) according to claim 1 , wherein the heterophasic composition (HECO) has a xylene soluble fraction (XCS) in the range of 5.0 to 30.0 wt.-%.

6. The polypropylene composition (C) according to claim 1 , wherein the xylene soluble fraction (XCS) of the heterophasic composition (HECO) has:

i) an ethylene content in the range of 25.0 to 60.0 mol-%, and/or

ii) an intrinsic viscosity (IV) determined according to DIN ISO 1628/1, October 1999 (in Decalin at 135° C.) in the range of 3.0 to 4.5 dl/g.

7. The polypropylene composition (C) according to claim 1 , wherein:

i) the first α-nucleating agent (NU1) is a polymeric nucleating agent, and

ii) the second α-nucleating agent (NU2) is a non-polymeric nucleating agent.

8. The polypropylene composition (C) according to claim 7 , wherein the first α-nucleating agent (NU1) is a polymeric vinylcycloalkane.

9. The polypropylene composition (C) according to claim 7 , wherein the second α-nucleating agent (NU2) is selected from the group consisting of talc, salts of diesters of phosphoric acid or mixtures thereof.

10. The polypropylene composition (C) according to claim 1 , comprising:

(a) 80.0 to 95.0 wt. % of the heterophasic composition (HECO),

(b) 5.0 to 15.0 wt. % of the polyethylene (PE) being a copolymer of ethylene and a C 4 -C 12 α-olefin, and

(c) 1.4 to 5.0 wt. % of the second α-nucleating agent (NU2).

11. The polypropylene composition (C) according to claim 1 , wherein the polyethylene (PE) is a copolymer of ethylene and 1-butene.

12. The polypropylene composition (C) according to claim 1 , wherein the polyethylene (PE) has:

a melt flow rate MFR 5 (190° C., 5.0 kg) determined according to ISO 1133 equal or below 3.0 g/10 min.

13. The polypropylene composition (C) according to claim 1 , having:

i) a flexural modulus determined according to ISO 178 of at least 1400 MPa, and/or

ii) a Charpy notched impact strength determined according to ISO 179/1eA at 23° C. of at least 8.0 kJ/m 2 .

14. The polypropylene composition (C) according to claim 1 , wherein the (semi)crystalline polypropylene (PP1) is a propylene homopolymer (H-PP) comprising:

(a) a first propylene homopolymer fraction (H-PP1a) having a melt flow rate MFR 2 (230° C./2.16 kg) in the range of 30.0 to 120.0 g/10 min, and

(b) a second propylene homopolymer fraction (H-PP1b) having a melt flow rate MFR 2 (230° C./2.16 kg) in the range of 5.0 to 25.0 g/10 min.

15. An article comprising the polypropylene composition (C) according to claim 1 .

16. The article according to claim 15 , wherein said article is a car seat, a stroller, a baby walker, a toy, a heavy duty pail or a transport packaging.

17. A method for preparing the polypropylene composition (C) according to claim 1 , comprising the steps of:

i) preparing the α-nucleated heterophasic propylene copolymer (HECO) in a sequential polymerization process comprising at least three reactors, wherein the (semi)crystalline polypropylene (PP1) is produced in the first and/or second reactor in the presence of the first α-nucleating agent (NU1) and the elastomeric ethylene/propylene copolymer (EPR) is produced in a subsequent reactor, and

ii) blending the α-nucleated heterophasic propylene copolymer (HECO) obtained in step i) with the polyethylene (PE) being a copolymer of ethylene and a C 4 -C 12 α-olefin and the second α-nucleating agent (NU2).

Assignments (2)
CHANGE OF ADDRESS Recorded Feb 23, 2022
From: BOREALIS AG
To: BOREALIS AG
Reel/Frame 059219/0949 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 21, 2021
From: KLIMKE, KATJA; CAUWENBERGHE, HANS JOZEF FRANCOIS VAN
To: ABU DHABI POLYMERS CO. LTD (BOROUGE) L.L.C.; BOREALIS AG
Reel/Frame 057699/0823 →