IP Library Granted Patent US 12,012,504
Granted Patent B2
US 12,012,504 · App. 17/056,855 · Granted Jun 18, 2024

Process for the preparation of multimodal high density polyethylene

Inventors: Anh Tuan Tran (Linz, AT); Alexandra Romina Albunia (Linz, AT); Joy Jie Cheng (Linz, AT); Joseph Thorman (Porvoo, FI); John Jamieson (Porvoo, FI); Ravindra Tupe (Porvoo, FI)
Assignee: BOREALIS AG
C08L23/06B29C43/003B29C45/0001C08F2/001C08F2/34C08F210/02C08F210/08C08F210/16B29L2031/56C08F2500/12C08F2500/17C08L2203/10C08L2203/30C08L2205/025C08L2205/03C08L2207/062C08L2314/02
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Quick Facts
Patent No.
US 12,012,504
App. No.
17/056,855
Granted
Jun 18, 2024
Kind
B2
Abstract

The invention provides a process for the preparation of a multimodal high density polyethylene (HDPE) having a melt flow rate (MFR 2 ) of 0.1 to 4.0 g/10 min, said process comprising: (i) polymerising ethylene in a first polymerisation stage in the presence of a Ziegler-Natta catalyst to prepare a first ethylene homopolymer having a MFR 2 from 10 to 500 g/10 min; (ii) polymerising ethylene in a second polymerisation stage in the presence of said catalyst and said first ethylene homopolymer to prepare an ethylene homopolymer mixture comprising said first ethylene homopolymer and a second ethylene homopolymer, said mixture having a MFR 2 from 50 to 1000 g/10 min; and (iii) polymerising ethylene and at least one alpha-olefin comonomer in a third polymerisation stage in the presence of said catalyst and said ethylene homopolymer mixture to prepare said multimodal HDPE.

Claims (24)

1. A process for the preparation of a multimodal high density polyethylene (HDPE) having a melt flow rate (MFR 2 ) of 0.1 to 4.0 g/10 min and a MFR 5 of 2.5 to 12 g/10 min, wherein the multimodal HDPE has a FNCT (6 MPa, 50° C.) of at least 30 hours, said process comprising:

(i) polymerising ethylene in a first polymerisation stage in the presence of a Ziegler-Natta catalyst to prepare a first ethylene homopolymer having a MFR 2 from 10 to 500 g/10 min;

(ii) polymerising ethylene in a second polymerisation stage in the presence of said catalyst and said first ethylene homopolymer to prepare an ethylene homopolymer mixture comprising said first ethylene homopolymer and a second ethylene homopolymer, said mixture having a MFR 2 from 50 to 1000 g/10 min; and

(iii) polymerising ethylene and at least one alpha-olefin comonomer in a third polymerisation stage in the presence of said catalyst and said ethylene homopolymer mixture to prepare said multimodal HDPE.

2. The process as claimed in claim 1 , wherein said first polymerisation stage and/or said second polymerisation stage are carried out in a slurry loop reactor.

3. The process as claimed in claim 1 , wherein said third polymerisation stage is carried out in a gas phase reactor.

4. The process as claimed in claim 1 , wherein said at least one alpha-olefin has 3 to 12 carbon atoms.

5. The process as claimed in claim 4 , wherein said at least one alpha-olefin is selected from the group consisting of 1-butene, 1-hexene and 1-octene.

6. The process as claimed in claim 4 , wherein said at least one alpha-olefin is 1-butene.

7. The process as claimed in claim 1 , wherein the multimodal HDPE has a density of 950 to 960 kg/m 3 .

8. The process as claimed in claim 1 , wherein the multimodal HDPE has a MFR 2 of 0.5 to 1.5 g/10 min.

9. The process as claimed in claim 1 , wherein the multimodal HDPE has a tensile modulus of at least 850 MPa, more preferably at least 900 MPa.

10. A multimodal high density polyethylene (HDPE) having a melt flow rate (MFR 2 ) of 0.1 to 4.0 g/10 min obtained by a process as defined in claim 1 .

11. A multimodal high density polyethylene (HDPE) having a density of 940 to 970 kg/m 3 and a melt flow rate (MFR 2 ) of 0.1 to 4.0 g/10 min, a MFR 5 of 2.5 to 12 g/10 min, wherein said multimodal HDPE comprises a low molecular weight ethylene homopolymer component and a high molecular weight ethylene copolymer component and wherein said multimodal HDPE has a Mz/Mn of at least 95 and/or Mz of at least 680000;

wherein said low molecular weight ethylene homopolymer component is an ethylene homopolymer mixture comprising a first ethylene homopolymer and a second ethylene homopolymer; and

wherein the multimodal HDPE has a FNCT (6 MPa, 50° C.) of at least 30 hours.

12. An injection or compression molded article, comprising the multimodal HDPE as defined in claim 11 .

13. The injection or compression molded article of claim 12 , wherein the injection or compression molded article is a cap or a closure.

14. A cap or closure comprising the multimodal HDPE as defined in claim 11 .

15. A process for the manufacture of an injection or compression molded moulded article, said process comprising preparing the multimodal HDPE as defined in claim 11 ;

optionally pelletizing the multimodal HDPE to form pellets; and

injection or compression moulding the formed pellets or HDPE to form said article.

16. A process for a manufacture an injection or compression molded cap or closure comprising:

injection or compression molding of the multimodal HDPE of claim 11 .

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 Mar 25, 2021
From: TRAN, ANH TUAN; ALBUNIA, ALEXANDRA ROMINA; CHENG, JOY JIE; THORMAN, JOSEPH; JAMIESON, JOHN; TUPE, RAVINDRA
To: BOREALIS AG
Reel/Frame 055718/0268 →
Priority Claims (1)
EP 18175206 · May 30, 2018 · regional
Continuity (1)
Related Publication 20210147660A1 · May 20, 2021
Cited By (1)
US 12,612,475