# US 11,441,024 B2 · Process for preparing a polypropylene composition > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 11,441,024 B2 - Document ID: US11441024B2 - Status: Granted - Kind: B2 - Application number: 16/770,704 - Filed: 2018-12-11 - Published: 2020-10-01 - Granted: 2022-09-13 - Earliest claimed: 2017-12-14 - Assignees: Borealis AG - Applicants: Borealis AG - Inventors: Jingbo Wang; Markus Gahleitner; Elisabeth Potter; Jani Aho; Klaus Bernreitner; Luc Monnissen; Meta Cigon - Web page: https://patentgrep.com/patent/US11441024B2 ## CPC - C08L 23/14: Copolymers of propene (C08L23/16 takes precedence) - C08L 2203/16: used for films - C08L 2205/025: containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure - C08L 2205/03: containing three or more polymers in a blend - C08L 2314/02: Ziegler natta catalyst - C08L: COMPOSITIONS OF MACROMOLECULAR COMPOUNDS (compositions based on polymerisable monomers C08F, C08G; artificial filaments or fibres D01F; textile treating compositions D06) ## Abstract The invention relates to a process for producing a polypropylene composition having an improved balanced combination of high flowability, high stiffness and impact, and high level of optical properties. Further, the invention relates to the polypropylene composition having the above-mentioned properties, as well as an article comprising the polypropylene composition. ## Claims ### Claim 1 A process for producing a polypropylene composition by sequential polymerization, the process comprising the steps of: a) polymerizing in a first reactor monomers comprising propylene and optionally one or more comonomers selected from ethylene and C4-C10 alpha-olefins, to obtain a first propylene polymer fraction having a comonomer content in the range of 0.0 to 1.0 wt %, b) polymerizing in a second reactor monomers comprising propylene and one or more comonomers selected from ethylene and C4-C10 alpha-olefins, in the presence of the first propylene polymer fraction to obtain a second propylene polymer fraction having a comonomer content in the range of from 4.5 to 20.0 wt %, c) pelletizing the second propylene polymer fraction, and d) melt-mixing the pelletized second propylene polymer fraction in the presence of: i. a propylene polymer (PP-c) produced in a process comprising at least two reactors connected in series, the propylene polymer (PP-c) containing one or more comonomers selected from ethylene and C4-C10 alpha-olefins wherein the comonomer content is in the range of from 0.5 to 2.5 wt %, and ii. at least one alpha-nucleating agent, wherein the polypropylene composition has: i—an MFR2 in the range of from 11.0 to 60.0 g/10 min, as measured according to ISO 1133 at 230° C. under a load of 2.16 kg; ii—a haze value of <20%, as measured according to ASTM D1003 on injection moulded plaques having 1 mm thickness produced as described in EN ISO 1873-2; iii—a tensile modulus >950 MPa, as measured according to ISO 527-1:2012/ISO 527-2:2012 on an injection moulded test specimen at 23° C.; iv—15 to 84 wt % of the pelletized second polymer fraction relative to the total amount of polypropylene composition; v—15 to 84% of the propylene polymer (PP-c) relative to the total amount of polypropylene composition; and vi—0.01 to 1.0 wt % of at least one alpha-nucleating agent relative to the total amount of polypropylene composition. ### Claim 2 (depends on 1) The process according to claim 1, wherein the polypropylene composition has a comonomer content in the range of from 1.5 to 5.0 wt %, relative to the total amount of monomers present in the polypropylene composition. ### Claim 3 (depends on 1) The process according to claim 1, wherein the melt-mixing of the pelletized second propylene polymer fraction is carried out at a temperature in the range of 190° C. to 260° C. ### Claim 4 (depends on 1) The process according to claim 1, wherein the melt-mixing of the pelletized second propylene polymer fraction is carried out in a single-screw extruder or a twin-screw extruder. ### Claim 5 (depends on 1) The process according to claim 1, wherein the second propylene polymer fraction and the propylene polymer (PP-c) are free of a phthalic compound. ### Claim 6 (depends on 1) The process according to claim 1, wherein the first reactor is a slurry reactor. ### Claim 7 (depends on 1) The process according to claim 1, wherein the second reactor is a gas-phase reactor. ### Claim 8 (depends on 1) A polypropylene composition obtainable by the process according to claim 1. ### Claim 9 (depends on 8) The polypropylene composition according to claim 8, wherein the polypropylene composition has a xylene soluble content (XCS) in the range of from 5.5 to 18.0 wt %, as determined according to ISO 16152 at 25° C. ### Claim 10 (depends on 8) The polypropylene composition according to claim 8, wherein the polypropylene composition has a melting temperature >152° C. and a crystallization temperature >120° C. as measured according to ISO 11357/3. ### Claim 11 (depends on 8) The polypropylene composition according to claim 8, wherein the polypropylene composition has a Charpy notched impact strength >4.8 kJ/m2, as measured according to ISO 179/1eA at 23° C. on injection moulded test specimens as described in EN ISO 1873-2. ### Claim 12 (depends on 8) The polypropylene composition according to claim 8, wherein the polypropylene composition is free of a phthalic compound. ### Claim 13 (depends on 8) An article comprising the polypropylene composition according to claim 8. ### Claim 14 (depends on 13) The article according to claim 13, wherein the article is a cast film, an injection moulded article, a closure cap, a screw cap, or a closure system for food or fluid packaging.