Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US12359005B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12359005-B2 |
| Application number | US-202017764238-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 1, 2020 |
| Priority date | Oct 4, 2019 |
| Publication date | Jul 15, 2025 |
| Grant date | Jul 15, 2025 |
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The present invention relates to substituted 2-iso-propyl-1,3-dialkoxypropanes, and more particularly to their use as internal donors in Ziegler-Natta catalysts to obtain ethylene (co)polymers with desirable properties. The present disclosure further concerns use of Ziegler-Natta catalyst components comprising said substituted 2-iso-propyl-1,3-dimethoxypropanes and use of Ziegler-Natta catalysts in ethylene (co)polymerization comprising said Ziegler-Natta catalyst components.
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The invention claimed is: 1. A Ziegler-Natta catalyst component comprising an internal donor selected from compounds of formula (I) wherein R 1 is nonyl; and R 2 and R 3 are each independently C 1-3 -alkyl. 2. The Ziegler-Natta catalyst component according to claim 1 further comprising: (ii) a compound of a transition metal Group 4 to 6 of the Periodic Table (IUPAC, Nomenclature of Inorganic Chemistry, 2005); (iii) a compound of metal Group 1 to 3 of the Periodic Table (IUPAC, 2005); and (iv) optionally, a compound of a element of Group 13 of the Periodic Table (IUPAC, 2005). 3. The Ziegler-Natta catalyst component according to claim 1 wherein the Ziegler-Natta catalyst component comprises: (ii) a Group 4 to 6 metal content (determined by ICP Analysis) in a range of 1.0 wt % to 15.0 wt % of a total weight of the Ziegler-Natta catalyst component; (iii) a Group 1 to 3 content (determined by ICP Analysis) in a range of 5.0 wt % to 30.0 wt % of the total weight of the Ziegler-Natta catalyst component; (iv) a Group 13 element content (determined by ICP Analysis) in a range of 0 wt % to 3.0 wt % of the total weight of the Ziegler-Natta catalyst component. 4. A Ziegler-Natta catalyst component according to claim 1 , wherein the Ziegler-Natta catalyst component is prepared by a method comprising: (M-a) providing a solid support; (M-b) pre-treating the solid support of step (M-a) with a compound of Group 13 element, thereby generating a pre-treated solid support; (M-c) treating the pre-treated solid support of step (M-b) with a transition metal compound of Group 4 to 6; (M-d) recovering the Ziegler-Natta catalyst component; wherein the solid support is contacted with one or more internal organic compounds of formula (I) before treating the solid support in step (M-c). 5. The Ziegler-Natta catalyst component according to claim 1 , wherein compound of formula (I) is selected from compounds of formula (I-a) and (I-b) wherein R 1 is nonyl. 6. A method for producing a Ziegler-Natta catalyst component according to claim 1 , comprising adding an internal donor selected from compounds of formula wherein R 1 is nonyl; and R 2 and R 3 are each independently C 1-3 -alkyl, to a constituent step of the method for preparing the Ziegler-Natta catalyst component. 7. A Ziegler-Natta catalyst for ethylene (co) polymerization, wherein the Ziegler-Natta catalyst comprises: (A) the Ziegler-Natta catalyst component as defined in claim 1 ; (B) a cocatalyst selected from element compounds of Group 13 of the Periodic Table (IUPAC, 2005); and (C) optionally, an external donor. 8. A method of ethylene (co) polymerization optionally with C 3-20 comonomers, comprising: a) introducing into a polymerization reactor a Ziegler-Natta catalyst component comprising an internal donor of formula (I) wherein R 1 is nonyl; and R 2 and R 3 are each independently linear or branched C 1-3 -alkyl. 9. The method as claimed in claim 8 , wherein the internal donor of formula (I) is selected from compounds of formula (I-a) or (I-b) wherein R 1 is nonyl. 10. The method according to claim 8 , wherein the internal donor is comprised in a Ziegler-Natta catalyst component further comprises: (ii) a transition metal compound of Group 4 to 6 of the Periodic Table (IUPAC, Nomenclature of Inorganic Chemistry, 2005); (iii) a metal compound of Group 1 to 3 of the Periodic Table (IUPAC, 2005); and (iv) optionally, a compound of group 13 of the Periodic Table (IUPAC, 2005). 11. A process for producing an ethylene homo- or copolymer, comprising: (P-a) introducing a Ziegler-Natta catalyst component, comprising: (i) an internal donor selected from compounds of formula (I), or from formulas (I-a) and (I-b) wherein R 1 is nonyl; and R 2 and R 3 are each independently linear or branched C 1-3 -alkyl; (ii) a transition metal compound of Group 4 to 6 of the Periodic Table (IUPAC, Nomenclature of Inorganic Chemistry, 2005); (iii) a metal compound of Group 1 to 3 of the Periodic Table (IUPAC, 2005); and (iv) optionally, a compound of group 13 of the Periodic Table (IUPAC, 2005) into a polymerisation reactor, (P-b) introducing a cocatalyst that activates the Ziegler-Natta catalyst component into the polymerisation reactor; (P-c) introducing ethylene, optionally C 3 -C 20 α-olefin comonomers, and optionally hydrogen into the polymerisation reactor; and (P-d) maintaining said polymerisation reactor in such conditions as to produce an ethylene homo- or copolymer. 12. The process according to claim 11 , wherein (co) polymerizing ethylene is accomplished in a multi-stage polymerization process comprising at least one gas phase reactor for producing ethylene (co) polymers. 13. The process according to claim 11 , wherein (co) polymerizing ethylene is accomplished in a multi-stage polymerization process comprising at least one slurry reactor, and one gas phase reactor.
with aluminium or compounds thereof · CPC title
Pretreating with non-metals or metal-free compounds · CPC title
Additive used together with the catalyst, excluding compounds containing Al or B · CPC title
Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title
Ethene · CPC title
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