IP Library Granted Patent US 9,868,802
Granted Patent B2
US 9,868,802 · App. 15/190,576 · Granted Jan 16, 2018

Polymerisation process

Inventors: Andrew David Bell (Carry-le-Rouet, FR); Pierre-Marie Cagna (Lyons, FR); Fabrice Betton (Lyons, FR); David Heslop (Istres, FR); Kevin Peter Ramsay (West Lothian, GB)
Assignee: INEOS EUROPE AG
C08F210/16C08F10/00
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Quick Facts
Patent No.
US 9,868,802
App. No.
15/190,576
Granted
Jan 16, 2018
Kind
B2
Abstract

Polymerization process for the polymerization of monomer in a polymerization system having at least one component attached thereto which component is flushed with a flush medium which enters the polymerization system. Initially, the component is flushed with a first flush medium, and subsequently the component is flushed with a second flush medium.

Claims (21)

1. A process for the polymerisation of monomer in a polymerisation system having at least one component attached thereto which is flushed with a flush medium which enters the polymerisation system, wherein initially said component is flushed with a first flush medium, and subsequently said component is flushed with a second flush medium which second flush medium differs in composition from the first flush medium, the flow of flush medium being used to keep polymer and/or polymer reaction medium away from the component, wherein the polymerisation system is a slurry phase polymerisation system.

2. A process according to claim 1 wherein the at least one component is selected from seals, pressure relief valves, withdrawal lines, inlet lines, and instrument tappings.

3. A process according to claim 2 wherein the instrument tapping is a pressure tapping.

4. A process according to claim 1 wherein there are multiple components attached to the polymerisation system and which are flushed with a flush medium which enters the polymerisation system.

5. A process according to claim 1 wherein downstream recycle lines in the polymerisation system have components which are flushed.

6. A process according to claim 1 wherein downstream degassing steps in the polymerisation system have compressors with seals or filters which are flushed.

7. A process according to claim 1 wherein the at least one component is attached on a polymerisation reactor and is selected from pressure relief valves, withdrawal lines, inlet lines, and instrument tappings.

8. A process according to claim 7 wherein stand-by or unused withdrawal and inlet lines are maintained with a manual or control valve closed and the stagnant zone between the reactor and the valve is flushed.

9. A process according to claim 1 wherein one of the first and second flush mediums comprises an inert medium, and the other comprises one or more non-inert components.

10. A process according to claim 1 wherein the first and second flush mediums are first and second flush gases.

11. A process according to claim 1 which is applied during process start-up, shut-down or a process upset.

12. A process according to claim 1 which is a polymerisation system for polymerisation of an olefin monomer in one or more slurry loop reactors.

13. A process for the polymerisation of monomer in a polymerisation system having at least one component attached thereto which is flushed with a flush medium which enters the polymerisation system, wherein initially said component is flushed with a first flush medium, and subsequently said component is flushed with a second flush medium which second flush medium differs in composition from the first flush medium, the flow of flush medium being used to keep polymer and/or polymer reaction medium away from the component, wherein the at least one component is attached on a polymerisation reactor is selected from pressure relief valves, withdrawal lines, inlet lines, and instrument tappings, and wherein stand-by or unused withdrawal and inlet lines are maintained with a manual or control valve closed and the stagnant zone between the reactor and the valve is flushed.

14. A process according to claim 13 wherein there are multiple components attached to the polymerisation system and which are flushed with a flush medium which enters the polymerisation system.

15. A process according to claim 13 wherein one of the first and second flush mediums comprises an inert medium, and the other comprises one or more non-inert components.

16. A process according to claim 13 wherein the polymerisation system is a gas phase polymerisation system.

17. A process according to claim 16 wherein the polymerisation system is a fluidized bed gas phase polymerisation system.

18. A process according to claim 13 wherein the first and second flush systems are first and second flush gases.

19. A process according to claim 13 which is applied during process start-up, shut-down or a process upset.

20. A process according to claim 13 wherein the polymerisation system is a slurry phase polymerisation system.

21. A process according to claim 20 which is a polymerisation system for polymerisation of an olefin monomer in one or more slurry loop reactors.

Assignments (1)
SECURITY INTEREST Recorded May 4, 2017
From: INEOS TECHNOLOGIES USA LLC; INEOS EUROPE AG
To: BARCLAYS BANK PLC
Reel/Frame 042398/0916 →
Priority Claims (1)
EP 11195903 · Dec 28, 2011 · regional
Continuity (2)
Continuation 14368397
Related Publication 20160297908A1 · Oct 13, 2016