Method for producing heterophasic propylene polymerization material particles

US2020308317A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2020308317-A1
Application numberUS-202016829479-A
CountryUS
Kind codeA1
Filing dateMar 25, 2020
Priority dateMar 29, 2019
Publication dateOct 1, 2020
Grant date

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

Provided is a particle drying method capable of sufficiently removing the volatile component and down-regulating the increase of the viscosity of the particles after the removal of the volatile component. There is provided a method for producing heterophasic propylene polymerization material particles, the method including: (1) performing monomer polymerization in the presence of a catalyst including a solid catalyst component so as to obtain a component I; (2) performing monomer polymerization in the presence of the component I so as to obtain the component II, so that particles including a volatile component are produced; and (3) causing the particles to contact with an inert gas-containing stream so as to remove the volatile component from the particles.

First claim

Opening claim text (preview).

1 . A method for producing heterophasic propylene polymerization material particles, the method comprising: (1) performing monomer polymerization in the presence of a catalyst including a solid catalyst component so as to obtain a component (I) recited below; (2) performing monomer polymerization in the presence of the component (I) so as to obtain a component (II), so that particles including a volatile component, the component (I), and the component (II) are produced; and (3) causing the particles to contact with an inert gas-containing stream so as to remove the volatile component from the particles, the particles including the component (I) by 20 to 70 mass %, and the component (II) by 30 to 80 mass %, and the method satisfying Inequation (1): 19.5≤ T 1.12 ·t 0.17 ·( C/ 100) 0.61 /( d ·(0.85· P ) 1/3 ) 0.13 ≤51.4  (1) where T [° C.] is a temperature that the particles have when the particles contact with the inert gas-containing stream, t [h] is a contact time period in which the particles contact with the inert gas-containing stream, d [μm] is a median diameter that the solid catalyst component has at the time of start of step (1), P [g/g] is a mass of the particles per 1 g of the solid catalyst component, and C [mass %] is the content of the component (II) in the particles, the component (I) including a component (I-1) and/or a component (I-2), the component (I-1) being a propylene homopolymer, the component (I-2) being a propylene copolymer including a propylene-derived structural unit and at least one type of olefin-derived structural unit selected from the group consisting of ethylene and C4 to C12 α-olefins, wherein a mass ratio of the at least one type of olefin-derived structural unit in the mass of the copolymer is less than 15 mass %, and the component (II) being a propylene copolymer including a propylene-derived structural unit and at least one type of olefin-derived structural unit selected from the group consisting of ethylene and C4 to C12 α-olefins, wherein a mass ratio of the at least one type of olefin-derived structural unit in the mass of the copolymer is in a range of 15 to 80 mass %. 2 . The method according to claim 1 , wherein counter currents of the particles and the inert gas-containing stream are caused to contact with each other. 3 . The method according to claim 1 , wherein the following Inequation (2) is further satisfied: 26.5≤ T 1.12 ·t 0.17 ·( C/ 100) 0.61 /( d ·(0.85· P ) 1/3 ) 0.13   (2). 4 . The method according to claim 2 , wherein the following Inequation (2) is further satisfied: 26.5≤ T 1.12 ·t 0.17 ·( C/ 100) 0.61 /( d ·(0.85· P ) 1/3 ) 0.13   (2).

Assignees

Inventors

Classifications

  • C08F6/00Primary

    Post-polymerisation treatments (C08F8/00 takes precedence; of conjugated diene rubbers C08C) · CPC title

  • Propene · CPC title

  • Propene · CPC title

  • Polypropene · CPC title

  • Chemical blending or stepwise polymerisation process with the same catalyst · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US2020308317A1 cover?
Provided is a particle drying method capable of sufficiently removing the volatile component and down-regulating the increase of the viscosity of the particles after the removal of the volatile component. There is provided a method for producing heterophasic propylene polymerization material particles, the method including: (1) performing monomer polymerization in the presence of a catalyst inc…
Who is the assignee on this patent?
Sumitomo Chemical Co
What technology area does this patent fall under?
Primary CPC classification C08F6/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Oct 01 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).