Process for degassing and buffering polyolefin particles obtained by olefin polymerization

Patent metadata

Field	Value
Publication number	US-10131719-B2
Application number	US-201314651124-A
Country	US
Kind code	B2
Filing date	Dec 11, 2013
Priority date	Dec 11, 2012
Publication date	Nov 20, 2018
Grant date	Nov 20, 2018

Abstract

Process for preparing a polyolefin polymer comprising the steps of
a) forming a particulate polyolefin polymer by polymerizing one or more olefins in the presence of a polymerization catalyst system in a polymerization reactor; b) discharging the formed polyolefin particles from the polymerization reactor; c) degassing the polyolefin particles by a process comprising at least a final step of contacting the polyolefin particles with a nitrogen stream in a degassing vessel; and d) transferring the polyolefin particles from the vessel, in which the contacting of the polyolefin particles with the nitrogen stream is carried out, to a melt mixing device, in which the polyolefin particles are melted, mixed and thereafter pelletized, without passing the particles through a buffering device,

wherein the degassing vessel is only partly filled with polyolefin particles and the empty volume within the degassing vessel is sufficient to take up additional polyolefin particles for at least 3 hours if the transfer of polyolefin particles of step d) from the degassing vessel to the melt mixing device is discontinued and the discharge of polyolefin particles from the polymerization reactor according to step b) is continued with unchanged rate.

First claim

What is claimed is:

1. A process for preparing a polyolefin polymer comprising the steps of
a) forming a particulate polyolefin polymer by polymerizing one or more olefins in the presence of a polymerization catalyst system in a polymerization reactor;
b) discharging the formed polyolefin particles from the polymerization reactor to a degassing vessel;
c) degassing the polyolefin particles by a process comprising at least two degassing steps of contacting the polyolefin particles with a nitrogen stream in the degassing vessel; and
d) transferring the polyolefin particles from the vessel, in which the contacting of the polyolefin particles with the nitrogen stream is carried out, to a melt mixing device, in which the polyolefin particles are melted, mixed and thereafter pelletized, without passing the particles through a buffering device,
e) while discharging, discontinuing the transferring step for at least 4 hours, wherein the start of the discontinuing the transferring step, the degassing vessel is only partly filled with polyolefin particles.

2. The process for preparing a polyolefin polymer according to claim 1 , wherein the degassing vessel is located above the melt mixing device and the transfer from the degassing vessel to the melt mixing device is carried out by means of gravity.

3. The process for preparing a polyolefin polymer according to claim 1 , wherein the degassing process of step c) comprises the step of contacting the polyolefin particles with the nitrogen stream is the final step of the whole degassing process.

4. The process for preparing a polyolefin polymer according to claim 1 , wherein the polyolefin particles are transferred pneumatically by a gas stream from a penultimate degassing step to a final degassing step and the gas for carrying out the pneumatic transfer is at least partly composed of nitrogen which had previously been used for degassing the polyolefin particles in the final degassing step.

5. The process for preparing a polyolefin polymer according to claim 4 , wherein the degassing step carried out immediately before the final step of the degassing process, in which the polyolefin particles are contacted with the nitrogen stream, is a step which includes a deactivation of the catalyst system.

6. The process for preparing a polyolefin polymer according to claim 5 , wherein the penultimate degassing step includes contacting the polyolefin particles with a nitrogen stream comprising 2 to 20 mol. %, of steam.

7. The process for preparing a polyolefin polymer according to claim 6 , wherein the penultimate degassing step is carried out at conditions under which no condensation of water occurs.

8. The process for preparing a polyolefin polymer according to claim 6 , wherein at least a part of the nitrogen in the stream comprising nitrogen and steam, which is used in the penultimate degassing step of the degassing process of step c), had previously been used in the final step of the degassing process.

9. The process for preparing a polyolefin polymer according to claim 5 , wherein the degassing process of step c) comprises an additional degassing step before the penultimate degassing step including the deactivation of the catalyst system.

10. The process for preparing a polyolefin polymer according to claim 9 , wherein the polymerization is a gas-phase polymerization in the presence of a C 3 -C 5 alkane as polymerization diluent and the degassing in the first degassing step of the whole degassing process of step c) is carried out by contacting the polyolefin particles with a gaseous stream comprising at least 85 mol-% of the C 3 -C 5 alkane used as diluent in the gas-phase polymerization reactor.

11. The process for preparing a polyolefin polymer according to claim 1 , wherein the degassing steps are carried out by countercurrently contacting the polyolefin particles with the respective gas streams.

12. The process for preparing a polyolefin polymer according to claim 1 , wherein the polyolefin polymer is a homopolymer or copolymer of ethylene.

13. A process for preparing a polyolefin polymer comprising the steps of
a) forming a particulate polyolefin polymer by polymerizing one or more olefins in the presence of a polymerization catalyst system in a polymerization reactor;
b) discharging the formed polyolefin particles from the polymerization reactor;
c) degassing the polyolefin particles by a process comprising at least two degassing steps, wherein a final degassing step includes contacting the polyolefin particles with a nitrogen stream in a degassing vessel; and
d) transferring the polyolefin particles from the degassing vessel, in which the final step of contacting of the polyolefin particles with the nitrogen stream is carried out, to a melt mixing device, in which the polyolefin particles are melted, mixed and thereafter pelletized, without passing the particles through a buffering device,
e) while discharging, discontinuing the transferring step for at least 3 hours, wherein at the start of discontinuing the transferring step, the degassing vessel, in which the final degassing step is carried out, is only partly filled with polyolefin particles.

14. The process for preparing a polyolefin polymer according to claim 13 , wherein the degassing vessel is located above the melt mixing device and the transfer from the degassing vessel to the melt mixing device is carried out by means of gravity and/or wherein the transferring step is discontinued from 3 to 4 hours.

15. The process for preparing a polyolefin polymer according to claim 13 , wherein the degassing process of step c) comprises the step of contacting the polyolefin particles with the nitrogen stream is the final step of the whole degassing process.

16. The process for preparing a polyolefin polymer according to claim 13 , wherein the polyolefin particles are transferred pneumatically by a gas stream from a penultimate degassing step to the final degassing step and the gas for carrying out the pneumatic transfer is at least partly composed of nitrogen which had previously been used for degassing the polyolefin particles in the final degassing step.

17. The process for preparing a polyolefin polymer according to claim 16 , wherein the degassing step carried out immediately before the final step of the degassing process, in which the polyolefin particles are contacted with the nitrogen stream, is a step which includes a deactivation of the catalyst system.

18. The process for preparing a polyolefin polymer according to claim 17 , wherein the penultimate degassing step includes contacting the polyolefin particles with a nitrogen stream comprising 2 to 20 mol. %, of steam.

19. The process for preparing a polyolefin polymer according to claim 18 , wherein the penultimate degassing step is carried out at conditions under which no condensation of water occurs.

20. The process for preparing a polyolefin polymer according to claim 18 , wherein at least a part of the nitrogen in the stream comprising nitrogen and steam, which is used in the penultimate degassing step of the degassing process of step c), had previously been used in the final step of the degassing process.

Assignees

• Basell Polyolefine Gmbh

Inventors

• Penzo Giuseppe
• Mei Giulia
• Mei Gabriele
• De Lucia Antonio
• Baita Pietro

Classifications

• C08F6/005 Primary

  from solid polymers · CPC title

• B29K2023/00

  Use of polyalkenes {or derivatives thereof} as moulding material · CPC title

• B01J2208/00176

  outside the reactor · CPC title

• C08F10/00

  Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond · CPC title

• B01J2208/00274

  involving reactant vapours · CPC title