Process for ethylene polymerization with improved ethylene feed system

Patent metadata

Field	Value
Publication number	US-9738735-B1
Application number	US-201515502376-A
Country	US
Kind code	B1
Filing date	Aug 6, 2015
Priority date	Aug 7, 2014
Publication date	Aug 22, 2017
Grant date	Aug 22, 2017

Abstract

The present disclosure relates to a process for the preparation of polyethylene by polymerizing in a slurry ethylene and optionally one or more C 3 to C 10 alpha-olefins. In some embodiments, the polymerization is carried out in a cylindrical polymerization reactor equipped with an agitator for mixing the contents of the reactor and inducing a flow of the slurry, the ethylene is fed into the reactor by an ethylene injection system comprising one or more injection nozzles which project through the bottom reactor head or through the reactor wall and extend from 0.02-0.5 times the inner diameter D into the reactor, and the ethylene exits the injection nozzle with an exit velocity from 10-200 m/s.

First claim

We claim:

1. A process for the preparation of polyethylene by polymerizing in a slurry ethylene and optionally one or more C 3 to C 10 alpha-olefins at a temperature from 60-95° C. and a pressure from 0.15-3 MPa; wherein the polymerization is carried out in a cylindrical polymerization reactor having a cylindrical reactor wall, a bottom reactor head and a top reactor head and the reactor has an inner diameter D and is equipped with an agitator for mixing the contents of the reactor and inducing a flow of the slurry; wherein the ethylene is fed into the reactor by an ethylene injection system comprising one or more injection nozzles which project through the bottom reactor head or through the reactor wall and extend from 0.02-0.5 times the inner diameter D into the reactor and wherein the ethylene exits the injection nozzle with an exit velocity from 10-200 m/s.

2. The process of claim 1 , wherein the injection nozzles projecting through the bottom reactor head or through the reactor wall have a direction into the reactor, a sloped ethylene outlet with an outlet tip and an outlet base, and an angle between the direction of the injection nozzle and the line connecting the outlet tip and the outer base of from 20-80°, and the slope of the ethylene outlet is oriented with respect to the flow of the slurry such that the outlet tip is in an upstream position and the outlet base is in a downstream position with respect to the flow of the slurry.

3. The process of claim 1 , wherein the agitator comprises a motor, a vertical rotating shaft centrally located in the reactor, and one or more stages of agitator blades attached to the rotating shaft; and wherein the agitator induces primarily a vertical flow of the slurry in a circular cross-section around the agitator shaft.

4. The process of claim 3 , wherein the vertical flow of the slurry in the circular cross-section is a downward flow.

5. The process of claim 1 , wherein the one or more injection nozzles project through the bottom reactor head and extend vertically from 0.04-0.2 times the inner diameter D into the reactor, and the horizontal distance from the center of the reactor to the outlet of the injection nozzles is from 0.1-0.45 times the inner diameter D.

6. The process of claim 5 , wherein the ethylene injection system comprises at least two injection nozzles, and all injection nozzles are arranged on a circular line around the reactor center.

7. The process of claim 6 , wherein the injection nozzles are uniformly distributed on the circular line.

8. The process of claim 1 , wherein the one or more injection nozzles project through the cylindrical reactor wall at a wall passing point positioned in the lower two thirds of the reactor, and extend from 0.02-0.48 times the inner diameter D into the reactor.

9. The process of claim 8 , wherein the injection nozzles are inclined downward.

10. The process of claim 9 , wherein the horizontal angle between the direction of the injection nozzle and the horizontal is of from 5-60°.

11. The process of claim 8 , wherein the flow of the slurry in the polymerization reactor has a circular component, and the injection nozzles are inclined towards the downstream direction of the circular flow.

12. The process of claim 11 , wherein the radial angle between the direction of the injection nozzle and a line running from the wall passing point to the center of the reactor is from 5-60°.

13. The process of claim 8 , wherein the outlets of the injection nozzles are located at a position below the agitator.

14. The process of claim 8 , wherein the wall passing points are arranged at the same height of the reactor and uniformly distributed around the reactor.

15. The process of claim 1 , wherein the reactor is in a multi-reactor polymerization system.

16. A process for the preparation of polyethylene by polymerizing in a slurry ethylene and optionally one or more C 3 to C 10 alpha-olefins at a temperature from 60-95° C. and a pressure from 0.15-3 MPa; wherein the polymerization is carried out in a cylindrical polymerization reactor having a cylindrical reactor wall, a bottom reactor head and a top reactor head, the reactor has an inner diameter D and is equipped with an agitator for mixing the contents of the reactor and inducing a flow of the slurry; wherein the ethylene is fed into the reactor by an ethylene injection system comprising one or more injection nozzles which project through the cylindrical reactor wall at a wall passing point positioned in the lower two thirds of the reactor and extend from 0.02-0.48 times the inner diameter D into the reactor; and wherein the ethylene exits the injection nozzle with an exit velocity from 10-200 m/s.

17. The process of claim 16 , wherein the injection nozzles are inclined downward and the horizontal angle between the direction of the injection nozzle and the horizontal is from 5-60°.

18. The process of claim 16 , wherein the flow of the slurry in the polymerization reactor has a circular component, the injection nozzles are inclined towards the downstream direction of the circular flow, and the radial angle between the direction of the injection nozzle and a line running from the wall passing point to the center of the reactor is from 5-60°.

19. The process of claim 17 , wherein the outlets of the injection nozzles are located at a position below the agitator.

20. A process for the preparation of polyethylene by polymerizing in a slurry ethylene and optionally one or more C 3 to C 10 alpha-olefins at a temperature from 60-95° C. and a pressure from 0.15-3 MPa; wherein the polymerization is carried out in a multi-reactor system comprising a cylindrical polymerization reactor having a cylindrical reactor wall, a bottom reactor head and a top reactor head, wherein the reactor has an inner diameter D and is equipped with an agitator for mixing the contents of the reactor and inducing a flow of the slurry; wherein the ethylene is fed into the reactor by an ethylene injection system comprising one or more injection nozzles which project through the bottom reactor head or through the reactor wall and extend from 0.02-0.5 times the inner diameter D into the reactor and wherein the ethylene exits the injection nozzle with an exit velocity from 10-200 m/s.

Assignees

• Basell Polyolefine Gmbh

Inventors

• Kuehl Reinhard
• Prang Harald
• Carvajal Rodrigo
• Damm Elke
• Pyman Phil

Classifications

• B01J2208/00902

  Nozzle-type feeding elements · CPC title

• B01J8/224

  the particles being subject to a circulatory movement (B01J8/222 takes precedence) · CPC title

• C08F10/02 Primary

  Ethene · CPC title

• B01J19/1875

  internally, i.e. the mixture circulating inside the vessel such that the upwards stream is separated physically from the downwards stream(s) · CPC title

• B01J19/18

  Stationary reactors having moving elements inside (B01J19/08, B01J19/26 take precedence) · CPC title