A heterophasic polypropylene copolymer having an MFR2 of 0.05 to 20 g/10 min (ISO 1133 at 230° C. with a loading of 2.16 kg) and a melting point (Tm) of 156 to 164° C. (measured by DSC according to ISO 11357) wherein the heterophasic polypropylene copolymer comprises at least the following components: (A) 55.0 to 95.0 wt % of a crystalline fraction (CF) having a comonomer content of 0 to 3.0 wt %; and (B) 5.0 to 45.0 wt % of a soluble fraction (SF) having a comonomer content of 12 to 45 wt %; wherein the intrinsic viscosity (IV) (in decalin at 135° C.) of the soluble fraction (SF) is 2.5 to 11 dl/g, and wherein the amount of crystalline fraction (CF) and the amount of soluble fraction (SF) are determined in 1,2,4-trichlorobenzene at 40° C.

The present invention relates to melt-blown webs having no shots and improved barrier properties, whereby the melt-blown webs are made of a visbroken metallocene-catalyzed propylene homopolymer composition with specified melting temperature T.sub.m, content of 2,1 erythro regiodefects and molecular weight distribution (MWD).

The present invention relates to melt-blown webs having no shots and improved barrier properties, whereby the melt-blown webs are made of a visbroken metallocene-catalyzed propylene homopolymer composition with specified melting temperature T.sub.m, content of 2,1 erythro regiodefects and molecular weight distribution (MWD).

The present invention relates to a method for preparing a vinyl chloride-based polymer, including: bulk polymerizing a vinyl chloride-based monomer in a polymerization reactor to prepare a vinyl chloride-based polymer; and adding water and vapor to the polymerization reactor, and heating to remove an unreacted vinyl chloride-based monomer, wherein an addition amount of the water is 0.500 to 5.000 parts by weight based on 100 parts by weight of the vinyl chloride-based polymer.

The present invention relates to a method for preparing a vinyl chloride-based polymer, including: bulk polymerizing a vinyl chloride-based monomer in a polymerization reactor to prepare a vinyl chloride-based polymer; and adding water and vapor to the polymerization reactor, and heating to remove an unreacted vinyl chloride-based monomer, wherein an addition amount of the water is 0.500 to 5.000 parts by weight based on 100 parts by weight of the vinyl chloride-based polymer.

The present invention relates to a new multimodal ethylene copolymer (P), to the use of the copolymer in film applications and to a film comprising the copolymer of the invention.

The present invention relates to a new multimodal ethylene copolymer (P), to the use of the copolymer in film applications and to a film comprising the copolymer of the invention.

Provided are a heterophasic propylene polymerization material and an olefin polymer having a small high-boiling-point component amount index (FOG). The heterophasic propylene polymerization material satisfies the following formula (3): (X2×Y2)/Z2≤7.0 (3) wherein X2 represents a cold xylene soluble component amount (mass %) of the heterophasic propylene polymerization material; Y2 represents a percentage (%) of a component having a molecular weight of 104.0 or less in terms of polystyrene and contained in a cold xylene soluble component of the heterophasic propylene polymerization material based on all components of the cold xylene soluble component of the heterophasic propylene polymerization material as measured by gel permeation chromatography; and Z2 represents a content (mass %) of a propylene-based copolymer contained in the heterophasic propylene polymerization material and containing a propylene-derived monomer unit and a monomer unit derived from at least one compound selected from the group consisting of ethylene and C4-12 α-olefins.

Provided are a heterophasic propylene polymerization material and an olefin polymer having a small high-boiling-point component amount index (FOG). The heterophasic propylene polymerization material satisfies the following formula (3): (X2×Y2)/Z2≤7.0 (3) wherein X2 represents a cold xylene soluble component amount (mass %) of the heterophasic propylene polymerization material; Y2 represents a percentage (%) of a component having a molecular weight of 104.0 or less in terms of polystyrene and contained in a cold xylene soluble component of the heterophasic propylene polymerization material based on all components of the cold xylene soluble component of the heterophasic propylene polymerization material as measured by gel permeation chromatography; and Z2 represents a content (mass %) of a propylene-based copolymer contained in the heterophasic propylene polymerization material and containing a propylene-derived monomer unit and a monomer unit derived from at least one compound selected from the group consisting of ethylene and C4-12 α-olefins.

A bimodal polymer composition comprising a lower molecular weight homopolymer and a higher molecular weight copolymer wherein the bimodal polymer composition has a density of from about 0.930 gram per cubic centimeter (g/cc) to about 0.970 g/cc, a ratio of high load melt index:melt index of from about 10 to about 150 and an Environmental Stress Crack Resistance (ESCR) of from about 25 hours to about 300 hours when measured in accordance with ASTM D1693 or ASTM D2561. A chromium-catalyzed polymer composition comprising (i) a lower molecular weight homopolymer and (ii) a higher molecular weight copolymer, wherein the bimodal polymer composition has an Environmental Stress Crack Resistance (ESCR) of from about 25 hours to about 300 hours when measured in accordance with ASTM D1693 or ASTM D2561.