Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US9944724B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9944724-B2 |
| Application number | US-201615171105-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 2, 2016 |
| Priority date | Feb 16, 2011 |
| Publication date | Apr 17, 2018 |
| Grant date | Apr 17, 2018 |
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 may include contacting ethylene monomer with Ziegler-Natta catalyst to form polyethylene. The Ziegler-Natta catalyst may be formed by contacting an alkyl magnesium compound with an alcohol and a metal reagent to form a blend, and contacting the blend with a first agent to form a solution of reaction product “A”. The solution of reaction product “A” may be contacted with a second agent to form a solid reaction product “B”, and the solid reaction product “B” may be contacted with a third agent to form a solid reaction product “C”. The solid reaction product “C” may be contacted with a fourth agent to form a solid reaction product “D”, and the solid reaction product “D” may be contacted with a fifth agent to form a catalyst component.
Opening claim text (preview).
What is claimed is: 1. A polymerization process comprising: providing ethylene monomer; contacting the ethylene monomer with a Ziegler-Natta catalyst within a polymerization reactor under conditions sufficient to form polyethylene; and recovering polyethylene from the polymerization reactor, wherein the Ziegler-Natta catalyst is formed by a process comprising: contacting an alkyl magnesium compound with an alcohol and a metal reagent to form a blend of a magnesium dialkoxide compound and a metal; contacting the blend of the magnesium dialkoxide compound and the metal with a first agent to form a solution of reaction product “A”, the first agent comprising a halogenating/titanating agent; contacting the solution of reaction product “A” with a second agent to form a solid reaction product “B”, the second agent comprising a blend of a first metal halide and a metal alkoxide; contacting the solid reaction product “B” with a third agent to form a solid reaction product “C”, the third agent comprising a second metal halide; contacting the solid reaction product “C” with a fourth agent to form a solid reaction product “D”, the fourth agent comprising a third metal halide; and contacting the solid reaction product “D” with a fifth agent to form a catalyst component, the fifth agent comprising an organoaluminum compound; wherein the metal reagent is selected from Ba(2-EHO) 2 (barium(II) 2-ethyl hexyl alkoxide), Mn(2-ethylhexanoate) 2 (manganese(II) 2-ethylhexanoate), Cr(2-ethylhexanoate) 3 (chromium(III) 2-ethylhexanoate) and 2-butylferrocene. 2. The process of claim 1 , wherein a shear response and activity for the polyethylene is greater than a shear response and activity for an identically formed polyethylene absent the metal reagent in the Ziegler-Natta catalyst. 3. The process of claim 1 , wherein the polyethylene exhibits an SR2 of from about 30 to about 50. 4. The process of claim 1 , wherein the polyethylene exhibits a Mz/Mw of from about 4.0 to about 9.0. 5. The process of claim 1 , wherein the polymerization process exhibits an activity of from about 23,000 g/g/h to about 70,000 g/g/h. 6. Polyethylene formed by the process of claim 1 . 7. A polymerization process comprising: providing ethylene monomer; contacting the ethylene monomer with a Ziegler-Natta catalyst within a polymerization reactor under conditions sufficient to form polyethylene; and recovering polyethylene from the polymerization reactor, wherein the Ziegler-Natta catalyst is formed by a process comprising: contacting an alkyl magnesium compound with an alcohol and a metal reagent to form a blend of a magnesium dialkoxide compound and a metal; contacting the blend of the magnesium dialkoxide compound and the metal with a first agent to form a solution of reaction product “A”, the first agent comprising a halogenating/titanating agent; contacting the solution of reaction product “A” with a second agent to form a solid reaction product “B”, the second agent comprising a blend of a first metal halide and a metal alkoxide; contacting the solid reaction product “B” with a third agent to form a solid reaction product “C”, the third agent comprising a second metal halide; contacting the solid reaction product “C” with a fourth agent to form a solid reaction product “D”, the fourth agent comprising a third metal halide; and contacting the solid reaction product “D” with a fifth agent to form a catalyst component, the fifth agent comprising an organoaluminum compound; wherein the metal in the metal reagent is selected from Cr 3+ , Fe 2+ , Mn 2+ , and Ba 2+ . 8. A polymerization process comprising: providing ethylene monomer; contacting the ethylene monomer with a Ziegler-Natta catalyst within a polymerization reactor under conditions sufficient to form polyethylene; and recovering polyethylene from the polymerization reactor, wherein the Ziegler-Natta catalyst is formed by a process comprising: contacting a metal component with a magnesium dihalide support material to form a Ziegler-Natta catalyst precursor, wherein the metal component is represented by the formula: MR A x wherein M is a transition metal; wherein R A is a halogen, an alkoxy, or a hydrocarboxyl group; and wherein x is the valence of M; contacting the magnesium dihalide support material in the Ziegler-Natta catalyst precursor with a dopant comprising a non-Group IV metal to form a doped catalyst precursor; and activating the doped catalyst precursor by contact with an organoaluminum compound to form the Ziegler-Natta catalyst; wherein the dopant is selected from Ba(2-EHO) 2 (barium(II) 2-ethyl hexyl alkoxide), Mn(2-ethylhexanoate) 2 (manganese(II) 2-ethylhexanoate), Cr(2-ethylhexanoate) 3 (chromium(III) 2-ethylhexanoate), 2-butylferrocene and combinations thereof. 9. The process of claim 8 , wherein a shear response and activity for the polyethylene is greater than a shear response and activity for an identically formed polyethylene absent the dopant in the Ziegler-Natta catalyst. 10. The process of claim 8 , wherein the polyethylene exhibits an SR2 of from about 30 to about 50. 11. The process of claim 8 , wherein the polyethylene exhibits a Mz/Mw of from about 4.0 to about 9.0. 12. The process of claim 8 , wherein the polymerization process exhibits an activity of from about 23,000 g/g/h to about 70,000 g/g/h. 13. Polyethylene formed by the process of claim 8 .
Bulk density · CPC title
Melt tension or melt strength · CPC title
Ethene · CPC title
Activation energy or enthalpy · CPC title
and magnesium or compounds thereof · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.