High molecular weight functionalized olefin copolymer quenching agent
US-10654949-B2 · May 19, 2020 · US
US11142593B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11142593-B2 |
| Application number | US-201916260518-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 29, 2019 |
| Priority date | Feb 22, 2018 |
| Publication date | Oct 12, 2021 |
| Grant date | Oct 12, 2021 |
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This disclosure describes polymerization processes and processes for quenching polymerization reactions using reactive particulates, such as lecithin, as quenching agents, typically in solution or bulk polymerization processes.
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What is claimed is: 1. A process for producing a polymer, wherein the process comprises: polymerizing a hydrocarbon monomer dissolved in a solvent in the presence of a catalyst system under conditions to obtain a first effluent stream comprising a solution of the polymer and the solvent; introducing a quenching agent into the first effluent stream to quench the polymerization reaction, wherein the quenching agent has a molecular weight (M n ) greater than about 2000 daltons and a hydrophilic lipophilic balance (HLB) of less than about 20, wherein the quenching agent comprises a lecithin. 2. A process for quenching a polymerization reaction, wherein the process comprises: introducing a quenching agent into a first effluent stream comprising polymer exiting a polymerization zone to quench the polymerization reaction, wherein the quenching agent has a molecular weight greater than about 2000 daltons and a hydrophilic lipophilic balance (HLB) of less than about 20, wherein the quenching agent comprises a lecithin. 3. The process of claim 1 , further comprising: performing a separation on the first effluent stream to produce: a second effluent stream comprising the quenching agent; and a recycle stream comprising the solvent, unreacted hydrocarbon monomer and optionally, the quenching agent, wherein the second effluent stream has a higher concentration of the quenching agent than the recycle stream. 4. The process of claim 3 , wherein less than about 5.0 wppm of the quenching agent is present in the recycle stream. 5. The process of claim 3 , wherein the separation is a liquid-liquid separation. 6. The process of claim 5 , wherein the quenching agent has a molecular weight (M n ) of greater than or equal to about 5000 daltons and an HLB of less than about 15. 7. The process of claim 5 , wherein the quenching agent has a molecular weight of greater than or equal to about 6000 daltons. 8. The process of claim 5 , wherein the quenching agent has an HLB of less than about 10. 9. The process of claim 1 , wherein the lecithin comprises a phospholipid selected from the group consisting of phosphatidylcholine, phosphatidylethanolamine, phosphatidylinositol, phosphatidylserine, and phosphatidic acid, and combinations thereof. 10. The process of claim 5 , wherein the separation is performed at a temperature of about 170° C. to about 230° C. and a pressure of about 400 psig (2800 kPa) to about 600 psig (4100 kPa). 11. The process of claim 3 , wherein the separation is a liquid-vapor separation. 12. The process of claim 11 , wherein the quenching agent has a molecular weight (M n ) of greater than or equal to about 2500 daltons and an HLB of less than about 18. 13. The process of claim 11 , wherein the quenching agent has a molecular weight of greater than or equal to about 3000 daltons. 14. The process of claim 11 , wherein the quenching agent has an HLB of less than about 15. 15. The process of claim 11 , wherein the quenching agent comprises a phospholipid selected from the group consisting of phosphatidylcholine, phosphatidylethanolamine, phosphatidylinositol, phosphatidylserine, and phosphatidic acid, and combinations thereof. 16. The process of claim 11 , wherein the separation is performed at a temperature of about 80° C. to about 150° C. and a pressure of about 50 psig (340 kPa) to about 300 psig (2100 kPa). 17. The process of claim 1 , wherein the catalyst system comprises a coordination catalyst. 18. The process of claim 1 , wherein the polymer comprises polyethylene and/or polypropylene. 19. The process of claim 1 , wherein the hydrocarbon monomer comprises C 2 -C 40 olefins and/or C 1 -C 4 paraffins. 20. A process for producing a polymer, wherein the process comprises: polymerizing a hydrocarbon monomer dissolved in a solvent in the presence of a catalyst system under conditions to obtain a first effluent stream comprising a solution of the polymer and the solvent; and introducing a quenching agent into the first effluent stream to quench the polymerization reaction, wherein the quenching agent is a lecithin. 21. The process of claim 20 , wherein the quenching agent comprises a phospholipid selected from the group consisting of phosphatidylcholine, phosphatidylethanolamine, phosphatidylinositol, phosphatidylserine, and phosphatidic acid, and combinations thereof.
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