High-pressure polymerization process of ethylenically unsaturated monomers in a production line having flanges covered by a chimney construction

Patent metadata

Field	Value
Publication number	US-10358510-B2
Application number	US-201716300147-A
Country	US
Kind code	B2
Filing date	May 9, 2017
Priority date	May 10, 2016
Publication date	Jul 23, 2019
Grant date	Jul 23, 2019

Abstract

A process for polymerizing or copolymerizing ethylenically unsaturated monomers at pressures in the range of from 110 MPa to 500 MPa in a production line comprising a continuously operated polymerization reactor, wherein at least one of a pre-heater or pre-cooler, a polymerization reactor or a post reactor cooler is composed of tubes of a length from 5 m to 25 m which are flanged together, either directly or via bends, and the flanges are covered by a chimney construction, and wherein air is conveyed through the chimney construction and the air exiting the chimney construction is monitored with respect to the hydrocarbons concentration.

First claim

The invention claimed is:

1. A process for polymerizing or copolymerizing one or more ethylenically unsaturated monomers 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,
the process comprising carrying out polymerization or copolymerization in a production line in which the monomers are brought to a polymerization pressure by one or more compressors in a sequence of compression stages in which a compressed gas mixture is cooled after each compression stage by a compression stage cooler, compressed monomers are optionally passed through a pre-heater or a pre-cooler and transferred into the polymerization reactor, which is optionally cooled by cooling jackets, a reaction mixture obtained by polymerization is leaving the reactor through a pressure control valve, and optionally cooled by an post reactor cooler, the reaction mixture is separated into polymeric and gaseous components in two or more stages, where the gaseous components separated off in a first stage at an absolute pressure of from 15 MPa to 50 MPa are recycled to the one or more compressors via a high-pressure gas recycle line, and the gaseous components separated off in a second stage at an absolute pressure in the range of from 0.1 to 0.5 MPa are recycled to a first stage of the sequence of compression stages via a low-pressure gas recycle line, and the polymeric components obtained by the polymerization are transformed into pellets,
wherein at least one of the pre-heater or pre-cooler, the polymerization reactor and the post reactor cooler is composed of tubes of a length from 5 m to 25 m which are flanged together, either directly or via bends, and the flanges are covered by a chimney construction, and wherein air is conveyed through the chimney construction and the air exiting the chimney construction is monitored with respect to hydrocarbons concentration.

2. The process of claim 1 , wherein the polymerization reactor is a tubular reactor or a reactor cascade comprising a tubular reactor and the production line comprises a pre-heater and a post reactor cooler, and
wherein the pre-heater, the polymerization reactor and the post reactor cooler are composed of tubes of a length from 5 m to 25 m which are flanged together, either directly or via bends, and the flanges are covered by a chimney construction, and wherein air is conveyed through the chimney construction and the air exiting the chimney construction is monitored with respect to the hydrocarbons concentration.

3. The process of claim 1 , wherein the polymerization reactor is an autoclave reactor or a cascade of autoclave reactors, and the production line comprises a pre-cooler or a post reactor cooler or a pre-cooler and a post reactor cooler, and
wherein the pre-cooler or the post reactor cooler or the pre-cooler and the post reactor cooler are composed of tubes of a length from 5 m to 25 m which are flanged together, either directly or via bends, and the flanges are covered by a chimney construction, and wherein air is conveyed through the chimney construction and the air exiting the chimney construction is monitored with respect to the hydrocarbons concentration.

4. The process of claim 1 , wherein at least 50% of the chimney constructions covers two or more flanges.

5. The process of claim 1 , wherein the chimney construction has openings at the bottom and at the top and the air is conveyed by natural convection.

6. The process of claim 1 , wherein the air exiting the chimney construction is monitored by one or more IR open path detectors or by an IR point detector.

7. The process of claim 1 , wherein the air exiting the chimney construction is monitored by an array of IR open path detectors which operate according to a voting logic.

8. The process of claim 1 , wherein an emergency pressure release program is automatically started when hydrocarbons are detected in the air exiting the chimney construction.

9. The process of claim 1 , wherein further measurements for detecting a leakage of hydrocarbons in a surrounding of the production line are carried out.

10. The process of claim 9 , wherein an emergency pressure release program is automatically started when hydrocarbons are detected in the air exiting the chimney construction or a leakage of hydrocarbons in the surrounding of the production line is detected by the further measurements.

11. The process of claim 9 , wherein the further measurements for detecting a leakage of hydrocarbons in the surrounding of the production line are carried out by employing IR open path detectors, IR point detector or ultrasonic detectors, or combinations thereof.

12. The process of claim 9 , wherein the further measurements for detecting a leakage of hydrocarbons in the surrounding of the production line include a monitoring of at least one of the cooling medium which cools the compression stage coolers, the cooling jackets of the polymerization reactor, the post reactor cooler or a cooler within the high-pressure gas recycle line with respect to an occurrence of a leakage of monomers or of reaction mixture into the cooling medium.

13. The process of claim 12 , wherein air is passed through the cooling medium and thereafter conveyed to an IR point detector capable of detecting hydrocarbons.

14. The process of claim 1 , wherein the polymerization reactor and optionally further parts of the production line are installed within a protective enclosure and wherein a water based deluge system is started automatically in parallel with an emergency pressure release program and the water based deluge system provides droplets of a diameter in the range from 25 μm to 20 mm to an enclosed area when a leakage of monomers or of reaction mixture is detected and the droplets are provided with a minimum flow rate of 10 L/min per m 2 of enclosed area.

15. The process of claim 1 , wherein a steam based deluge system is started automatically in parallel with an emergency pressure release program.

16. A process for polymerizing or copolymerizing one or more ethylenically unsaturated monomers 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,
wherein the polymerization is carried out in a production line in which the monomers are brought to a polymerization pressure by one or more compressors in a sequence of compression stages in which a compressed gas mixture is cooled after each compression stage by a compression stage cooler, compressed monomers are optionally passed through a pre-heater or a pre-cooler and transferred into the polymerization reactor, which is optionally cooled by cooling jackets, a reaction mixture obtained by a polymerization is leaving the reactor through a pressure control valve, and optionally cooled by an post reactor cooler, the reaction mixture is separated into polymeric and gaseous components in two or more stages, where the gaseous components separated off in a first stage at an absolute pressure of from 15 MPa to 50 MPa are recycled to the one or more compressors via a high-pressure gas recycle line, and the gaseous components separated off in a second stage at an absolute pressure in the range of from 0.1 to 0.5 MPa are recycled to a first stage of the sequence of compression stages via a low-pressure gas recycle line, and the polymeric components obtained by the polymerization are transformed into pellets,
wherein at least one of the pre-heater or pre-cooler, the polymerization reactor and the post reactor cooler is composed of tubes of a length from 5

Assignees

• Basell Polyolefine Gmbh

Inventors

• Gonioukh Andrei
• Herrmann Thomas
• Littmann Dieter
• Finette Andre-Armand
• Wolfram Sven

Classifications

• B01J2219/00092

  Tubes · CPC title

• C08F2/34

  Polymerisation in gaseous state · CPC title

• B01J19/06

  Solidifying liquids (making microcapsules B01J13/02) · CPC title

• C08F2/01 Primary

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

• B01J19/2415

  Tubular reactors · CPC title