Adhesive resin composition and film
US-2024343946-A1 · Oct 17, 2024 · US
US9732209B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9732209-B2 |
| Application number | US-201113823249-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 12, 2011 |
| Priority date | Sep 16, 2010 |
| Publication date | Aug 15, 2017 |
| Grant date | Aug 15, 2017 |
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Polypropylene composition having a melt flow rate MFR 2 (230° C.) of equal or above 15 g/10 min comprising: (a) a crystalline polypropylene matrix; (b) an elastomeric propylene copolymer phase having a propylene content in the range of 40 to 80 wt.-%, and an intrinsic viscosity in the range of more than 0.7 to less or equal 2.5 dl/g; (c) a first polyethylene having a density in the range 905 to 925 kg/m3 and melt flow rate MFR 2 (190° C.) of below 30 g/10 min; (d) a second polyethylene having a density of above 915 kg/m 3 , and a melt flow rate MFR 2 (190° C.) of equal or above 30 g/10 min.
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We claim: 1. Polypropylene composition having a melt flow rate MFR 2 measured at 230° C. according to ISO 1133 of equal or above 15 g/10 min comprising (a) a crystalline polypropylene matrix (M-PP) (b) an elastomeric propylene copolymer phase (E) having (i) a propylene content in the range of 40 to 80 wt.-%, and (ii) an intrinsic viscosity (IV) measured according to ISO 1628-1 at 135° C. in decalin in the range of more than 0.7 to less or equal 2.5 dl/g, (c) a first polyethylene (PE1) having (i) a density measured according to ISO 1183-187 in the range 905 to 925 kg/m 3 , and (ii) a melt flow rate MFR 2 measured at 190° C. according to ISO 1133 of below 30 g/10 min, and (iii) a molecular weight distribution (MWD) determined by gel permeation chromatography (GPC) of at least 10, (d) a second polyethylene (PE2) having (i) a density measured according to ISO 1183-187 of above 915 kg/m 3 , and (ii) a melt flow rate MFR 2 measured at 190° C. according to ISO 1133 of equal or above 30 g/10 min, and (iii) a molecular weight distribution (MWD) determined by gel permeation chromatography (GPC) of below 10. 2. Polypropylene composition according to claim 1 , wherein the crystalline polypropylene matrix (M-PP) has (a) a melt flow rate MFR 2 measured at 230° C. according to ISO 1133 in the range of 30 to 100 g/10 min, and/or (b) has a xylene cold soluble content (XCS) of equal or below 4.0 wt.-%, and/or (c) a melting temperature Tm determined by differential scanning calorimetry (DSC) of at least 145° C. 3. Polypropylene composition according to claim 1 , wherein the crystalline polypropylene matrix (M-PP) (a) has a comonomer content of equal or below 4.0 wt.-%, and/or (b) comprises at least two different crystalline polypropylene fractions, said fractions differ in the comonomer content. 4. Polypropylene composition according to claim 3 , wherein the crystalline polypropylene matrix (M-PP) comprises (a) at least one propylene homopolymer fraction and/or at least one random propylene copolymer fraction, and/or (b) one propylene homopolymer (H-PP) and one random propylene copolymer (R-PP), wherein further the weight ratio (H-PP/R-PP) between the propylene homopolymer (H-PP) and the random propylene copolymer n (R-PP) is 70/30 to 30/70. 5. Polypropylene composition according to claim 1 , wherein the elastomeric propylene copolymer phase (E) comprises a first elastomeric propylene copolymer (E1) and a second elastomeric propylene copolymer (E2), the first elastomeric propylene copolymer (E1) and the second elastomeric propylene copolymer (E2) differ in their intrinsic viscosity measured according to ISO 1628-1 at 135° C. in decalin. 6. Polypropylene composition according to claim 5 , wherein the weight ratio (E1/E2) between the first elastomeric propylene copolymer (E1) and the second elastomeric propylene copolymer (E2) is 80/20 to 20/80. 7. Polypropylene composition according to claim 5 , wherein the first elastomeric propylene copolymer (E1) has (i) a propylene content in the range of 25 to 60 wt.-%, and (ii) an intrinsic viscosity (IV) measured according to ISO 1628-1 at 135° C. in decalin in the range 0.5 to 2.5 dl/g. 8. Polypropylene composition according to claim 5 , wherein the second elastomeric propylene copolymer (E2) has (i) a propylene content in the range of 50 to 85 wt.-%, and (ii) an intrinsic viscosity (IV) measured according to ISO 1628-1 at 135° C. in decalin in the range 1.0 to below 3.0 dl/g. 9. Polypropylene composition according to claim 5 , wherein the elastomeric propylene copolymer phase (E) is dispersed within the crystalline polypropylene matrix (M-PP). 10. Polypropylene composition according to claim 1 , wherein the first polyethylene (PE1) has (a) an ethylene content of at least 80 wt.-%, and/or (b) a molecular weight distribution determined by gel permeation chromatography (GPC) of at least 10. 11. Polypropylene composition according to claim 1 , wherein the second polyethylene (PE2) has (a) an ethylene content of at least 80 wt.-%. 12. Polypropylene composition according claim 1 , wherein the polypropylene composition comprises additionally an α-nucleating agent (NA). 13. Polypropylene composition according to claim 1 , wherein the composition comprises (a1) 55 to 80 wt.-% of the crystalline polypropylene matrix (M-PP) (b1) 7.5 to 30 wt.-% of the elastomeric propylene copolymer phase (E), (c1) 2.5 to 15 wt.-% of the first polyethylene (PE1), (d1) 2.5 to 15 wt.-% of the second polyethylene (PE2), and (e1) 0.0005 to 1.0 wt.-% of a α-nucleating agent (NA), or (a2) 55 to 80 wt.-% of the crystalline polypropylene matrix (M-PP) (b2) 2.5 to 20 wt.-% of a first elastomeric propylene copolymer (E1), (c2) 2.5 to 20 wt.-% of a second elastomeric propylene copolymer (E2), (d2) 2.5 to 15 wt.-% of the first polyethylene (PE1), (e2) 2.5 to 15 wt.-% of the second polyethylene (PE2), and (f2) 0.0005 to 1.0 wt.-% of a α-nucleating agent (NA), or (a3) 15 to 55 wt.-% of a first crystalline polypropylene fraction being part of the crystalline polypropylene matrix (M-PP), (b3) 15 to 55 wt.-% of a second crystalline polypropylene fraction being part of the crystalline polypropylene matrix (M-PP) (c3) 2.5 to 20 wt.-% of a first elastomeric propylene copolymer (E1), (d3) 2.5 to 20 wt.-% of a second elastomeric propylene copolymer (E2), (e3) 2.5 to 15 wt.-% of the first polyethylene (PE1), (f3) 2.5 to 15 wt.-% of the second polyethylene (PE2), and (g3) 0.0005 to 1.0 wt.-% of a α-nucleating agent (NA). 14. Injection molded article comprising a polypropylene composition having a melt flow rate MFR 2 measured at 230° C. according to ISO 1133 of equal or above 15 g/10 min comprising (a) a crystalline polypropylene matrix (M-PP) (b) an elastomeric propylene copolymer phase (E) having (i) a propylene content in the range of 40 to 80 wt.-%, and (ii) an intrinsic viscosity (IV) measured according to ISO 1628-1 at 135° C. in decalin in the range of more than 0.7 to less or equal 2.5 dl/g, (c) a first polyethylene (PE1) having (i) a density measured according to ISO 1183-187 in the range 905 to 925 kg/m 3 , and (ii) a melt flow rate MFR 2 measured at 190° C. according to ISO 1133 of below 30 g/10 min, and (iii) a molecular weight distribution (MWD) determined by gel permeation chromatography (GPC) of at least 10, (d) a second polyethylene (PE2) having (i) a density measured according to ISO 1183-187 of above 915 kg/m 3 , and (ii) a melt flow rate MFR 2 measured at 190° C. according to ISO 1133 of equal or above 30 g/10 min, and (iii) a molecular weight distribution (MWD) determined by gel permeation chromatography (GPC) of below 10. 15. Process for the preparation of polypropylene composition having a melt flow rate MFR 2 measured at 230° C. according to ISO 1133 of equal or above 15 g/10 min comprising (a) a crystalline polypropylene matrix (M-PP) (b) an elastomeric propylene copolymer phase (E) having (i) a propylene content in the range of 40 to 80 wt.-%, and (ii) an intrinsic viscosity (IV) measured according to ISO 1628-1 at 135° C. in decalin in the range of more than 0.7 to less or equal 2.5 dl/g, (c) a first polyethylene (PE1) having (i) a density measured according to ISO 1183-187 in the range 905 to 925 kg/m 3 , and (ii) a melt flow rate MFR 2 measured at 190° C. according to ISO 1133 of below 30 g/10 min, and (iii) a molecular weight distribution (MWD) determined by gel permeation chromatography (GPC) of at least 10, (d) a second polyethylene (PE2) having (i) a density measured according
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