High-pressure polymerization process of ethylenically unsaturated monomers

Patent metadata

Field	Value
Publication number	US-9908950-B2
Application number	US-201615550256-A
Country	US
Kind code	B2
Filing date	Feb 22, 2016
Priority date	Feb 23, 2015
Publication date	Mar 6, 2018
Grant date	Mar 6, 2018

Abstract

A process for polymerizing or copolymerizing ethylenically unsaturated monomers in the presence of free-radical polymerization initiators, wherein the polymerization is carried out at temperatures from 100° C. to 350° C. and pressures in the range of from 110 MPa to 500 MPa in a continuously operated polymerization reactor which is controlled by a pressure control valve at the outlet of the polymerization reactor, the process comprising continuously monitoring the pressure within the polymerization reactor, feeding a pressure signal to a controller for controlling the control valve and having the controller altering the opening of the pressure control valve to control the pressure within the polymerization reactor, wherein the controller starts an emergency shutdown program when the pressure control valve closes more than a preset threshold value and the pressure within the polymerization reactor decreases below a preset pressure threshold.

First claim

The invention claimed is:

1. A process for polymerizing or copolymerizing ethylenically unsaturated monomers in the presence of free-radical polymerization initiators, wherein the polymerization is carried out at temperatures from 100° C. to 350° C. and pressures in a range of from 110 MPa to 500 MPa in a continuously operated polymerization reactor which is controlled by a pressure control valve at the outlet of the polymerization reactor and the monomer mixture is brought to the polymerization pressure by a combination of a primary compressor and a secondary compressor,
the process comprising continuously monitoring the pressure within the polymerization reactor by one or more pressure sensors creating a pressure signal indicative of the pressure within the polymerization reactor, feeding the pressure signal to a controller for controlling the control valve and having the controller altering the opening of the pressure control valve to control the pressure within the polymerization reactor,
wherein the controller starts an emergency shutdown program when the pressure control valve closes more than a preset threshold value and the pressure within the polymerization reactor decreases below a preset pressure threshold.

2. The process of claim 1 , wherein the controller starts the emergency shutdown program only as long as the secondary compressor is operating.

3. The process of claim 1 , wherein the polymerization is carried out in one or more tubular reactors or in one or more autoclave reactors or in combinations thereof.

4. The process of claim 1 , wherein the polymerization reactor is a tubular reactor.

5. The process of claim 1 , wherein the pressure within the polymerization reactor is monitored at the inlet of the polymerization reactor.

6. The process of claim 1 , wherein the pressure is monitored by two or more pressure sensors which are located at the same position and an average pressure value, which is calculated as the middle value for the pressures as measured by the two or three pressure sensors, is indicative of the pressure within the polymerization reactor.

7. The process of claim 1 , wherein the emergency shutdown program releases the content of the reactor including the pre-heater and the post reactor cooler, and the content of the secondary compressor including the high-pressure gas recycle line and the high-pressure product separator reactor, to the atmosphere.

8. The process of claim 7 , wherein the emergency shutdown program first activates a deluge or sprinkler system which sprays water on the polymerization reactor before releasing the content of the reactor and the secondary compressor to the atmosphere.

9. The process of claim 8 , wherein the deluge or sprinkler system comprises a supporting structure, pumps, pipes and nozzles which are distributed along the reactor.

10. The process of claim 1 , wherein the controller outputs an alarming signal when the pressure control valve closes more than a preset threshold value and the pressure is above the preset pressure threshold.

11. A process for polymerizing or copolymerizing ethylenically unsaturated monomers in one or more tubular reactors or in one or more autoclave reactors, or in combinations thereof in the presence of free-radical polymerization initiators, wherein the polymerization is carried out at temperatures from 100° C. to 350° C. and pressures from 110 MPa to 500 MPa in a continuously operated polymerization reactor, which is controlled by a pressure control valve at the outlet of the polymerization reactor, and the monomer mixture is brought to the polymerization pressure by a combination of a primary compressor and a secondary compressor,
the process comprising continuously monitoring the pressure within the polymerization reactor by one or more pressure sensors creating a pressure signal indicative of the pressure within the polymerization reactor, feeding the pressure signal to a controller for controlling the control valve and having the controller altering the opening of the pressure control valve to control the pressure within the polymerization reactor,
wherein the controller starts an emergency shutdown program when the pressure control valve closes more than a preset threshold value, and the pressure within the polymerization reactor decreases below a preset pressure threshold.

12. The process of claim 11 , wherein the pressure is monitored by two or more pressure sensors which are located at the same position and an average pressure value, which is calculated as the middle value for the pressures as measured by the two or three pressure sensors, is indicative of the pressure within the polymerization reactor.

13. The process of claim 11 , wherein the emergency shutdown program releases the content of the reactor, including the pre-heater and the post reactor cooler, and the content of the secondary compressor, including the high-pressure gas recycle line and the high-pressure product separator reactor, to the atmosphere.

14. The process of claim 13 , wherein the emergency shutdown program first activates a deluge or sprinkler system which sprays water on the polymerization reactor before releasing the content of the reactor and the secondary compressor to the atmosphere.

15. The process of claim 14 , wherein the deluge or sprinkler system comprises a supporting structure, pumps, pipes and nozzles which are distributed along the reactor.

16. A process for polymerizing or copolymerizing ethylenically unsaturated monomers in one or more tubular reactors, or in one or more autoclave reactors, or in combinations thereof in the presence of free-radical polymerization initiators, wherein the polymerization is carried out at temperatures from 100° C. to 350° C. and pressures from 110 MPa to 500 MPa in a continuously operated polymerization reactor, which is controlled by a pressure control valve at the outlet of the polymerization reactor, and the monomer mixture is brought to the polymerization pressure by a combination of a primary compressor and a secondary compressor,
the process comprising continuously monitoring the pressure within the polymerization reactor by one or more pressure sensors, creating a pressure signal indicative of the pressure within the polymerization reactor, feeding the pressure signal to a controller for controlling the control valve and having the controller altering the opening of the pressure control valve to control the pressure within the polymerization reactor,
wherein the controller starts an emergency shutdown program when the pressure control valve closes more than a preset threshold value, and the pressure within the polymerization reactor decreases below a preset pressure threshold,
wherein the emergency shutdown program releases the content of the reactor including pre-heater and post reactor cooler and the content of the secondary compressor including high-pressure gas recycle line and high-pressure product separator reactor to the atmosphere.

17. The process of claim 16 , wherein the emergency shutdown program releases the content of the reactor, including pre-heater and post reactor cooler, and the content of the secondary compressor, including high-pressure gas recycle line and high-pressure product separator reactor, to the atmosphere.

18. The process of claim 17 , wherein the emergency shutdown program first activates a deluge or sprinkler system which sprays water on the polymerization reactor before releasing the content of the reactor and the secondary compressor to the atmosphere.

19. The process of claim 18 , wh

Assignees

• Basell Polyolefine Gmbh

Inventors

• Wolfram Sven
• Finette Andre Armand
• Backes Udo
• Gonioukh Andrei
• Cabuk Hicran

Classifications

• B01J2219/00211

  comparing a sensed parameter with a pre-set value · CPC title

• G01L19/0092

  Pressure sensor associated with other sensors, e.g. for measuring acceleration or temperature (G01L9/025, G01L9/045, G01L9/065, G01L9/085, G01L9/105, G01L9/125, G01L19/02, G01L19/04 take precedence; measuring two or more variable G01D21/02; temperature sensors with pressure compensation G01K1/26) · CPC title

• C08F2/01 Primary

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

• B01J2219/00051

  Controlling the temperature · CPC title

• B01J19/0006

  Controlling or regulating processes (controlling or regulating in general G05) · CPC title