Polymer flake degassing system and methods

Patent metadata

Field	Value
Publication number	US-10730032-B2
Application number	US-201815981532-A
Country	US
Kind code	B2
Filing date	May 16, 2018
Priority date	May 16, 2018
Publication date	Aug 4, 2020
Grant date	Aug 4, 2020

Abstract

Systems and methods for improved degassing of polymer flake are provided herein. These systems include a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid; a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream; and a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream.

First claim

What is claimed is:

1. A system for polymerizing one or more olefin monomers, comprising:
a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid;
a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream, wherein the fluid stream comprises the solid polymer flake in a lower concentration than in the product stream, and wherein the concentrated stream comprises the solid polymer flake in a higher concentration than in the product stream;
a fluid stream recycle line configured to recycle the fluid stream from the flash chamber to the polymerization reactor;
a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a first purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream, wherein the partially degassed polymer flake stream comprises the fluid in a lower concentration than in the concentrated stream and the purge fluid stream comprises the solid polymer flake in a lower concentration than in the concentrated stream,
wherein the polymerization reactor, the flash chamber, and the first degassing chamber are distinct from each other.

2. The system of claim 1 , further comprising a second degassing chamber configured to produce a fully degassed polymer flake stream by contacting the partially degassed polymer flake stream with a second purge fluid comprising nitrogen to produce the fully degassed polymer flake stream and a used nitrogen stream, wherein the fully degassed polymer flake stream comprises the fluid at a lower concentration than in the partially degassed polymer flake stream and the used nitrogen stream comprises the solid polymer flake in a lower concentration than in the partially degassed polymer flake stream.

3. The system of claim 1 , wherein the first purge fluid comprises at least one of the one or more olefin monomers.

4. The system of claim 1 , wherein the fluid is a gas.

5. The system of claim 1 , wherein the fluid is a liquid.

6. The system of claim 1 , further comprising a first purge recycle line configured to recycle the purge fluid stream from the first degassing chamber to the polymerization reactor.

7. The system of claim 1 , wherein the one or more olefin monomers comprises ethylene and the polymer flake comprises polyethylene.

8. The system of claim 1 , wherein the polymerization reactor is further configured to polymerize one or more olefin monomers in the presence of one or more heavy hydrocarbons.

9. The system claim 1 , wherein the first degassing chamber has a residence time of from about 30 minutes to about 180 minutes.

10. The system of claim 1 , wherein the second degassing chamber has a residence time of from about 30 minutes to about 180 minutes.

11. The system of claim 1 , wherein a weight ratio of the first purge fluid to the solid polymer flake in the concentrated stream is from about 0.005 to about 1.

12. The system of claim 1 , wherein a weight ratio of the second purge fluid to the solid polymer flake in the partially degassed polymer flake stream is from about 0.001 to about 0.03.

13. The system of claim 1 , wherein the first degassing chamber has a length, and wherein an introduction point of the first purge fluid is less than about 20% along the length of the first degassing chamber, in the direction of the flow of the first purge fluid.

14. A process for polymerizing one or more olefin monomers comprising:
polymerizing one or more olefin monomers in a polymerization reactor to form a product stream comprising solid polymer flake entrained in a fluid;
passing the product stream to a flash chamber to produce a fluid stream and a concentrated stream of solid polymer flake entrained in the fluid, wherein the fluid stream comprises the solid polymer flake in a lower concentration than in the product stream and the concentrated stream comprises the solid polymer flake in a higher concentration than in the product stream;
recycling the fluid stream from the flash chamber to the polymerization reactor;
passing the concentrated stream to a first degassing chamber, wherein a first purge fluid comprising one or more light hydrocarbons contacts the concentrated stream to produce a partially degassed polymer flake stream and a purge fluid stream wherein the partially degassed polymer flake stream comprises the fluid in a lower concentration than in the concentrated stream and the purge fluid stream comprises the solid polymer flake in a lower concentration than in the concentrated stream;
passing the partially degassed polymer flake stream to a second degassing chamber, wherein a second purge fluid comprising nitrogen contacts the partially degassed polymer flake stream to produce a fully degassed polymer flake stream and a used nitrogen stream, wherein the fully degassed polymer flake stream comprises the fluid at a lower concentration than in the partially degassed polymer flake stream and the used nitrogen stream comprises the solid polymer flake in a lower concentration than in the partially degassed Polymer flake stream,
wherein a weight ratio of the second purge fluid to the solid polymer flake in the partially degassed polymer flake stream is from about 0.001 to about 0.03.

15. The process of claim 14 , wherein the first purge fluid consists essentially of ethylene.

16. The process of claim 15 , wherein the fluid comprises at least one of the one or more olefin monomers.

17. The process of claim 15 , wherein the fluid is a gas.

18. The process of claim 15 , wherein the fluid is a liquid.

19. The process of claim 15 , further comprising recycling the first purge fluid stream to the polymerization reactor.

20. The process of claim 15 , wherein a weight ratio of the first purge fluid to the solid polymer flake in the concentrated stream is from about 0.005 to about 1.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Dooley Kenneth A
• Lowell Jeffrey S
• Curren Joseph

Classifications

• C08F210/16

  Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title

• C08F2/01

  characterised by special features of the polymerisation apparatus used · CPC title

• B01D19/0005 Primary

  with one or more auxiliary substances · CPC title

• B01D19/0036

  Flash degasification (the other groups take precedence) · CPC title

• C08F6/005

  from solid polymers · CPC title