Method of polymerizing olefins in slurry reactors

Patent metadata

Field	Value
Publication number	US-9260547-B2
Application number	US-201514723016-A
Country	US
Kind code	B2
Filing date	May 27, 2015
Priority date	Dec 7, 2012
Publication date	Feb 16, 2016
Grant date	Feb 16, 2016

Abstract

A process including polymerizing ethylene in the presence of a polymerization catalyst and hydrogen in a first polymerization reactor to produce a first slurry; withdrawing a first stream of the slurry from the first polymerization reactor; directing the slurry stream into a second polymerization reactor; polymerizing ethylene in the presence of the first ethylene polymer, the polymerization catalyst, and hydrogen in a second polymerization reactor to produce a second slurry; withdrawing from the second polymerization reactor a second slurry stream having a solids concentration higher than the average solids concentration of the second slurry within the second polymerization reactor; withdrawing from the second polymerization reactor a third slurry stream having a solids concentration lower than the average solids concentration of the second slurry within the second polymerization reactor; and directing at least a part of the second slurry stream into one of the first and second polymerization reactors.

First claim

The invention claimed is:

1. A process for producing ethylene polymers in at least two cascaded polymerization reactors comprising the steps of:
polymerizing ethylene in the presence of a polymerization catalyst, hydrogen and optionally one or more alpha-olefin comonomers in a diluent in a first polymerization reactor to produce a first slurry comprising a first ethylene polymer and fluid phase comprising said diluent;
withdrawing a first stream of said slurry from said first polymerization reactor;
directing said slurry stream into a second polymerization reactor;
polymerizing ethylene in the presence of the first ethylene polymer, the polymerization catalyst, hydrogen and optionally one or more alpha-olefin comonomers in a diluent in a second polymerization reactor to produce a second slurry comprising an ethylene polymer mixture and a fluid phase comprising said diluent;
withdrawing from said second polymerization reactor a second slurry stream having a solids concentration which is higher than the average solids concentration of the second slurry within the second polymerization reactor;
withdrawing from said second polymerization reactor a third slurry stream having a solids concentration which is lower than the average solids concentration of the second slurry within the second polymerization reactor; and
directing at least a part of said second slurry stream into one of said first and second polymerization reactor.

2. The process according to claim 1 wherein from 50 to 100% by weight of said second slurry stream is directed to one of the first and second polymerization reactor.

3. The process according to claim 2 wherein the whole second slurry stream is returned into one of the first and second polymerization reactor.

4. The process according to claim 1 wherein said third slurry stream is directed to at least one separation step to separate the solids from the fluid phase.

5. The process according to claim 1 wherein said third slurry stream is directed to a subsequent polymerization step.

6. The process according to claim 1 wherein at least one of the first and second polymerization reactors is operated in such conditions that the fluid phase of the slurry is in supercritical state.

7. The process according to claim 1 wherein at least one of said first, second and third slurry streams is withdrawn continuously.

8. The process according to claim 7 wherein all of said first, second and third slurry streams are withdrawn continuously.

9. The process according to claim 1 wherein the second slurry stream is directed to the first polymerization reactor.

10. The process according to claim 1 wherein the first and second polymerization reactors are loop reactors.

11. A process for producing ethylene polymers in at least two cascaded polymerization reactors comprising the steps of:
polymerizing ethylene in the presence of a polymerization catalyst, hydrogen and optionally one or more alpha-olefin comonomers in a diluent in a first polymerization reactor to produce a first slurry comprising a first ethylene polymer and fluid phase comprising said diluent;
withdrawing a first stream of said slurry from said first polymerization reactor;
directing said slurry stream into a second polymerization reactor;
polymerizing ethylene in the presence of the first ethylene polymer, the polymerization catalyst, hydrogen and optionally one or more alpha-olefin comonomers in a diluent in a second polymerization reactor to produce a second slurry comprising an ethylene polymer mixture and a fluid phase comprising said diluent;
withdrawing from said second polymerization reactor a second slurry stream having a solids concentration which is higher than the average solids concentration of the second slurry within the second polymerization reactor;
withdrawing from said second polymerization reactor a third slurry stream having a solids concentration which is lower than the average solids concentration of the second slurry within the second polymerization reactor;
providing a minimum limit value for solids concentration within the first polymerization reactor;
determining the solids concentration within the first polymerization reactor; and
directing the second slurry stream into a separation step or a further polymerization stage if said solids concentration within the first polymerization reactor is greater than said minimum limit value for solids concentration within the first polymerization reactor and directing the second slurry stream into the first polymerization reactor if said solids concentration within the first polymerization reactor is lower than said minimum limit value for solids concentration within the first polymerization reactor.

12. The process according to claim 11 comprising the step of returning the third slurry stream into the first polymerization reactor if said solids concentration within the first polymerization reactor is greater than said minimum limit value for solids concentration within the first polymerization reactor and directing the third slurry stream into the separation step or subsequent polymerization step if said solids concentration within the first polymerization reactor is lower than said minimum limit value for solids concentration within the first polymerization reactor.

13. The process according to claim 11 comprising the step of stopping the withdrawal of the third slurry stream from the second polymerization reactor if said solids concentration within the first polymerization reactor is greater than said minimum limit value for solids concentration within the first polymerization reactor and directing the third slurry stream into the separation step or subsequent polymerization step if said solids concentration within the first polymerization reactor is lower than said minimum limit value for solids concentration within the first polymerization reactor.

14. The process of starting up a polymerization reaction in at least two cascaded polymerization reactors comprising the steps of claim 11 .

Assignees

• Borealis Ag

Inventors

• Senol Ilke
• Eriksson Erik
• Alastalo Kauno
• Leskinen Pauli
• Nyfors Klaus

Classifications

• C08F110/02 Primary

  Ethene · CPC title

• C08F2/14 Primary

  Organic medium · CPC title

• C08F2500/12

  Melt flow index or melt flow ratio · CPC title

• C08F10/02

  Ethene · CPC title

• C08F2/001

  Multistage polymerisation processes characterised by a change in reactor conditions without deactivating the intermediate polymer (C08F295/00, C08F297/00 take precedence) · CPC title