Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US2024239727A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024239727-A1 |
| Application number | US-202218562433-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 2, 2022 |
| Priority date | Jun 3, 2021 |
| Publication date | Jul 18, 2024 |
| Grant date | — |
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A method for producing an α-olefin may include (1) continuously introducing an ethylene and a catalyst into a reactor, followed by performing a polymerization reaction to obtain a reaction mixture; and (2) continuously introducing the reaction mixture and a base into a line mixer, followed by performing mixing. The line mixer may have a stirring power in a range of from 30 to 1000 kW·sec/m3 and a number of passes may be in a range of from 5 to 50.
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1 . A method for producing an α-olefin, the method comprising: (1) continuously introducing an ethylene and a catalyst into a reactor, followed by performing a polymerization reaction to obtain a reaction mixture; and (2) continuously introducing the reaction mixture and a base into a line mixer, followed by performing mixing, wherein the line mixer has a stirring power in a range of from 30 to 1000 kW·sec/m 3 and a number of passes in a range of from 5 to 50. 2 . The method of claim 1 , further comprising: bringing the reaction mixture into contact with the base before continuously introducing the reaction mixture and the base into the line mixer, wherein a distance between a junction at which the reaction mixture contacts the base and an inlet of the line mixer is 1 m or less. 3 . The method of claim 1 , wherein the catalyst is a Ziegler-based catalyst. 4 . The method of claim 1 , wherein the base is an ammonia. 5 . The method of claim 1 , further comprising, after the continuously introducing (2): (3) deashing comprising removing the deactivated catalyst; (4) distilling for recovering the α-olefin.
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