Polymer films and a process for the production thereof
AssigneeBorealis Technology Oy
InventorsAuli Nummila-Pakarinen, Ole Jan Myhre, Bjarne Jansen
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Abstract
The present invention concerns a polyethylene composition particularly suitable for film blowing. The invention also concerns a process for the production thereof. The composition comprises a low molecular weight portion having a density of more than 960 kg/m3 and a high molecular weight portion. The polyethylene composition has a density of about 925-940 kg/m3 and a melt flow rate in the range of MFR21, from 5 to 40 g/10 min. A polyethylene film blown from the polyethylene composition exhibits a tensile strength at yield in transverse direction at least 15 MPa, a 1% secant modulus in machine direction at least 300 MPa and in transverse direction at least 400 MPa, and a dart drop of at least 5 g/μm.
Claims11
A blown polyethylene film comprising a polyethylene composition having
- (i) a low molecular weight portion having a density of more than 960 kg/m3 and an MFR2 higher than 100 g/10 min;
- and
- (ii) a high molecular weight portion which has an MFR21 of less than 50 g/10 min,
- the polyethylene composition having a density between 929-934 kg/m3 and MFR2, between 12-30 g/10 min and said film exhibiting
- tensile strength, in transverse direction of at least 15 MPa;,
- 1% secant modulus in machine direction of at least 300 MPa and in transverse direction of at least 400 MPa;
- and,
- when run to a film having a thickness between 35-45 μm in a machine operating with a low neck, a dart drop of at least 5 g/μm.
A blown polyethylene film comprising a polyethylene composition having
- (i) a low, molecular weight portion having a density of more than 960 kg/m3 and an MFR2 higher than 100 g/10 min;
- and
- (ii) a high molecular weight portion which has an MFR21 of less than 50 g/10 min,
- the polyethylene composition having a density between 935-939 and MFR21 between 7-20 g/10 min and said film exhibiting
- tensile strength in transverse direction of at least 20 Mpa;
- 1% secant modulus in machine direction of at least 400 MPa and in transverse direction at least 500 MPa;
- and,
- when run to a film having a thickness between 35-45 μm in a machine operating with a low neck, a dart drop of at least 5 g/μm;
- or
- when run to a film having a thickness between 20-30 μm in a machine operating with a high neck, a dart drop of at least 8 g/μm.
A process for producing a blown polyethylene film comprising the steps of
- producing a polyethylene composition in the presence of a catalytic system of an ethylene polymerizing catalyst and cocatalyst in a multistage reaction sequence consisting of successive polymerization stages where at least one stage is carried out in a gas phase by
- subjecting ethylene, optionally hydrogen and comonomers to a first polymerization or copolymerization reaction in a first reaction zone or reactor to produce a first polymer;
- recovering the first polymer and the catalyst therein from the first reaction zone;
- feeding the first polymer into a second polymerization zone or reactor;
- feeding additional ethylene and optionally hydrogen and comonomers to the second reaction zone;
- subjecting the additional ethylene and optionally additional monomer(s) and hydrogen to a second polymerization reaction in the presence of the first polymer and the catalyst therein to produce a second polymerization product having an MFR21 of less than 50 g/10 min.;
- and
- recovering the combined polymerization product from the second reaction zone, and
- blowing the thus obtained polyethylene composition into a film having a density of 929-939 kg/m3.
A process for producing a blown polyethylene film exhibiting
- a tensile strength at yield in transverse direction at least 15 MPa,
- a density of 929 to 939 kg/m3;
- a 1% secant modulus in machine direction at least 300 MPa and in transverse direction at least 400 MP a;
- and
- a dart drop at least 5 g/mm;
- comprising the steps of
- producing a polyethylene composition by
- subjecting ethylene, optionally hydrogen and comonomers to a first polymerization or copolymerization reaction in a first reaction zone or reactor to produce a polymer having a MFR2 of 100 g/10 min or more;
- recovering the first polymerization product from the first reaction zone;
- feeding the first polymerization product to a second reaction zone or reactor,
- feeding additional ethylene and optionally hydrogen and comonomers to the second reaction zone,
- subjecting the additional ethylene and optionally additional monomer(s) and hydrogen to a second polymerization reaction in the presence of the first polymerization product to produce a second polymerization product having a MFR21 of less than 50 g/10 min, and
- recovering the combined polymerization product from the second reaction zone, and
- blowing the thus obtained polyethylene composition into a film.
Dependencies are inferred from the claim text.