Process for making crosslinked cable insulation using high melt strength ethylene-based polymer made in a tubular reactor and optionally modified with a branching agent
US-11912852-B2 · Feb 27, 2024 · US
US8946359B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-8946359-B2 |
| Application number | US-201113812693-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 29, 2011 |
| Priority date | Jul 30, 2010 |
| Publication date | Feb 3, 2015 |
| Grant date | Feb 3, 2015 |
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The present invention relates to a process of preparing a polyolefin in a loop reactor by introducing anti-fouling agent through a sleeve provided around at least part of the shaft of the pump. Also, the invention relates to the use of anti-fouling agent to prevent or reduce fouling by feeding the anti-fouling agent against the impeller of the pump upon introduction to the loop reactor.
Opening claim text (preview).
The invention claimed is: 1. A process of preparing a polyolefin in a loop reactor in the presence of anti-fouling agent, said loop reactor comprising interconnected pipes, defining a reactor path, and an axial pump comprising a motor, a shaft and an impeller, characterized in that at least part of the anti-fouling agent is introduced into said loop reactor through a sleeve provided around at least part of the shaft of said axial pump. 2. The process according to claim 1 , wherein at least part of the anti-fouling agent is fed against a side of the impeller which is connected to the shaft of said axial pump. 3. The process according to claim 1 , wherein all anti-fouling agent is fed through the sleeve into the loop reactor. 4. The process according to claim 1 , wherein the anti-fouling agent is dissolved at a concentration of 0.1-10% by weight in a solvent. 5. The process according to claim 1 , wherein the anti-fouling agent is fed under flushing with diluent. 6. The process according to claim 5 , wherein the diluent comprises less than 15% by weight of monomer. 7. The process according to claim 1 , wherein said polyolefin is produced in slurry conditions. 8. The process according to claim 1 , wherein said loop reactor is a double loop reactor. 9. The process according to claim 8 , wherein the anti-fouling agent is introduced into a first loop reactor of the double loop reactor through the sleeve provided around at least part of the shaft of the axial pump of the first loop reactor. 10. The process according to claim 1 , wherein the polyolefin is polyethylene. 11. A process for using anti-fouling agent to prevent or reduce fouling of a loop reactor during a polymerization process comprising a pump with a shaft and an impeller comprising introducing the anti-fouling agent into the loop reactor against a side of the impeller which is connected to the shaft of said pump. 12. The process according to claim 11 , wherein at least part of the anti-fouling agent is introduced in the loop reactor through a sleeve provided around at least part of the shaft of said pump. 13. The process according to claim 12 , wherein all anti-fouling agent is fed through the sleeve into the loop reactor. 14. The process according to claim 11 , wherein the anti-fouling agent is dissolved at a concentration of 0.1-10% by weight in a solvent. 15. The process according to claim 1 , wherein the anti-fouling agent comprises cationic agents, anionic agents, nonionic agents, organometallic agents, polymeric agents or mixtures thereof. 16. The process according to claim 5 , wherein the diluent comprises less than 10% by weight of monomer. 17. The process according to claim 5 , wherein the diluent comprises less than 5% by weight of monomer. 18. The process according to claim 5 , wherein the diluent comprises less than 1% by weight of monomer.
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