Process for the preparation of multimodal high density polyethylene

US12012504B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-12012504-B2
Application numberUS-201917056855-A
CountryUS
Kind codeB2
Filing dateMay 30, 2019
Priority dateMay 30, 2018
Publication dateJun 18, 2024
Grant dateJun 18, 2024

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Abstract

Official abstract text for this publication.

The invention provides a process for the preparation of a multimodal high density polyethylene (HDPE) having a melt flow rate (MFR2) 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 MFR2 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 MFR2 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.

First claim

Opening claim text (preview).

The invention claimed is: 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 .

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What does patent US12012504B2 cover?
The invention provides a process for the preparation of a multimodal high density polyethylene (HDPE) having a melt flow rate (MFR2) 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 MFR2 from 10 to 500 g/10 min; (ii) polymerising ethylene in a se…
Who is the assignee on this patent?
Borealis Ag
What technology area does this patent fall under?
Primary CPC classification C08L23/06. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Jun 18 2024 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 10 related publications on this page (citations in our corpus or others sharing the same primary CPC).