Process for producing polyolefin film composition and films prepared thereof
US-11180586-B2 · Nov 23, 2021 · US
US12012504B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12012504-B2 |
| Application number | US-201917056855-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 30, 2019 |
| Priority date | May 30, 2018 |
| Publication date | Jun 18, 2024 |
| Grant date | Jun 18, 2024 |
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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.
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 .
Melt flow index or melt flow ratio · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Viscosity · CPC title
Ziegler natta catalyst · CPC title
HDPE · CPC title
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