Pre-polymerized catalyst components for the polymerization of olefins
US-2016137759-A1 · May 19, 2016 · US
US12509533B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12509533-B2 |
| Application number | US-202017777365-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 5, 2020 |
| Priority date | Nov 20, 2019 |
| Publication date | Dec 30, 2025 |
| Grant date | Dec 30, 2025 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A process for preparing a catalyst component made from or containing Mg, Ti, and at least an electron donor compound (ID), including the steps of: (a) reacting a Mg based compound with a Ti compound, having at least a Ti—Cl bond, in an amount such that the Ti/Mg molar ratio is greater than 3 and at a temperature ranging from 0 to 150° C., thereby yielding an intermediate solid catalyst component containing Mg and Ti; and (b) contacting the intermediate solid catalyst component with a gaseous stream containing the electron donor compound (ID) in a gaseous dispersing medium, thereby yielding a final solid catalyst component having an ID/Ti molar ratio ranging from 0.5:1 to 20:1.
Opening claim text (preview).
What is claimed is: 1 . A process for preparing a catalyst component comprising Mg, Ti, and at least an electron donor compound (ID) comprising the steps of: (a) reacting a Mg based compound with a Ti compound, having at least a Ti—Cl bond, in an amount such that the Ti/Mg molar ratio is greater than 3 and at a temperature ranging from 0 to 150° C., thereby yielding an intermediate solid catalyst component containing Mg and Ti; and (b) contacting the intermediate solid catalyst component with a gaseous stream containing the electron donor compound (ID) in a gaseous dispersing medium, thereby yielding a final solid catalyst component having an ID/Ti molar ratio ranging from 0.5:1 to 20:1. 2 . The process according to claim 1 , wherein the electron donor compound (ID) is a molecule containing at least one functional group selected from the group consisting of esters, ketones, amines, amides, carbamates, carbonates, aliphatic ethers, nitriles, alkoxysilanes, and glycols. 3 . The process according to claim 2 , wherein the ID compound is selected from the group consisting of C 2 -C 20 aliphatic ethers and alkyl esters of C 1 -C 20 aliphatic carboxylic acids. 4 . The process according to claim 2 , wherein the ID compound is monofunctional. 5 . The process according to claim 2 , wherein the electron donor compound (ID) is a molecule containing at least one functional group selected from the group consisting of tetrahydrofuran, methylformiate, ethylacetate ethylformiate, methylacetate, propylacetate, i-propylacetate, n-butylacetate, i-butylacetate, methyltrimethoxysilane, dimethyldimethoxysilane, and trimethylmethoxysilane. 6 . The process according to claim 2 , wherein two or more IDs are used. 7 . The process according to claim 6 , wherein a first ID is selected from aliphatic ethers and a second ID is selected from aliphatic acid esters. 8 . The process according to claim 1 , wherein the Mg compound is a Lewis adduct of formula MgCl 2 (ROH) m adducts, wherein R groups are C 1 -C 20 hydrocarbon groups and m is from 0.1 to 6. 9 . The process according to claim 1 , wherein the intermediate solid catalyst component is pre-polymerized before being subjected to step (b). 10 . The process according to claim 1 , wherein, in step (b), the amount of ID compound fixed on the catalyst component is such that ID/Ti molar ranges from 1.0:1 to 15:1. 11 . The process according to claim 1 , wherein the gaseous stream comprises an inert gas carrying the ID compound in gaseous or liquid form. 12 . The process according to claim 11 , wherein the ID compound is in gaseous form. 13 . The process according to claim 11 , wherein the inert gas is nitrogen. 14 . The process according to claim 11 , wherein step (b) is carried out in a gas-phase reactor, wherein the gaseous stream comprises a fluidizing gas and wherein the fluidizing gas is an inert gas. 15 . The process according to claim 1 , wherein the contact temperature in step (b) is in the range from 10 to 120° C.
Additive used together with the catalyst, excluding compounds containing Al or B · CPC title
characterised by special features of the polymerisation apparatus used · CPC title
Polymerisation in gaseous state · CPC title
and metals of C08F4/64 or compounds thereof · CPC title
Pretreating with non-metals or metal-free compounds · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.