Process for polymerizing olefins in a fluidized bed

Patent metadata

Field	Value
Publication number	US-9539556-B2
Application number	US-201515033010-A
Country	US
Kind code	B2
Filing date	Feb 27, 2015
Priority date	Feb 28, 2014
Publication date	Jan 10, 2017
Grant date	Jan 10, 2017

Abstract

The present invention is directed to a process for polymerizing olefins in gas phase in a fluidized bed reactor having a vertical body, a generally conical downwards tapering bottom zone, a generally cylindrical middle zone above the bottom zone, and a generally conical upwards tapering top zone above the middle zone. The fluidization gas is withdrawn from the top zone of the reactor, compressed and cooled so that a part of the fluidization gas condenses and then introduced to the bottom zone of the reactor. The bed is thus cooled upon evaporation of the liquid. There is no fluidization grid in the reactor.

First claim

The invention claimed is:

1. An olefin polymerization process comprising polymerizing at least one olefin in gas phase in a fluidized bed in the presence of an olefin polymerization catalyst in a polymerization reactor having a vertical body, a generally conical downwards tapering bottom zone, a generally cylindrical middle zone above and connected to said bottom zone, and a generally conical upwards tapering top zone above and connected to said middle zone and wherein (i) fluidization gas is introduced to the bottom zone of the reactor from where it passes upwards through the reactor; (ii) the fluidization gas is withdrawn from the top zone of the reactor, compressed and cooled so that a part of the fluidization gas condenses thus forming a mixture of liquid and gas, and the mixture is returned into the bottom zone of the reactor; (iii) a fluidized bed is formed within the reactor where the growing polymer particles are suspended in the upwards rising gas stream; (iv) the bed is cooled upon evaporation of the liquid; and (v) there is no fluidization grid in the reactor; characterized in that the amount of the liquid in the mixture introduced into the bottom zone of the reactor is from 0.5 to 20% by weight.

2. The process according to claim 1 characterized in that the gas velocity is maintained in the reactor such that N Br is within the range of from 2.5 to 7 wherein

N
Br

=

d
90

-

d
10

d
50

U
s

U
t

wherein do represents the smallest equivalent particle diameter so that 90% of the particles have a smaller equivalent diameter than d 90 ; d 10 represents the smallest equivalent particle diameter so that 10% of the particles have a smaller equivalent diameter than d 10 ; d 50 represents the median equivalent particle diameter; U s is the superficial gas velocity within the middle zone; and U t is the terminal velocity of the particles within the reactor.

3. The process according to claim 2 characterized in that N Br is within the range of from 3 to 5.

4. The process according to claim 1 wherein the amount of the liquid in the mixture introduced into the bottom zone of the reactor is from 1 to 17% by weight.

5. The process according to claim 1 wherein the ratio L/D of the height of the middle zone, L, to the diameter of the middle zone, D, is from 4 to 15.

6. The process according to claim 5 wherein the ratio L/D is from 5 to 10.

7. The process according to claim 1 comprising the step of removing polymer from the fluidization gas which has been withdrawn from the top zone of the reactor before the compression and cooling steps.

8. The process according to claim 7 wherein the polymer removed from the fluidization gas is recovered and passed to further processing.

9. The process according to claim 7 wherein the polymer removed from the fluidization gas is returned to the polymerization reactor.

10. The process according to claim 1 wherein the fluidization gas is filtered before being passed to the compressor.

11. The process according to claim 1 wherein polymer is withdrawn from the reactor through an outlet located in the middle zone.

12. The process according to claim 11 wherein the polymer is withdrawn from the reactor continuously.

13. The process according to claim 11 wherein polymer or polymer agglomerates are withdrawn from the bottom zone of the reactor.

14. The process according to claim 1 wherein the bottom zone comprises multiple conical segments having different cone angles.

15. The process according to claim 12 wherein polymer or polymer agglomerates are withdrawn from the bottom zone of the reactor.

Assignees

• Borealis Ag

Inventors

• Al-Haj Ali Mohammad
• Krallis Apostolos
• Kanellopoulos Vasileios

Classifications

• C08F10/00 Primary

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

• B01J8/24 Primary

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• C08F10/02

  Ethene · CPC title

• C08F2500/12

  Melt flow index or melt flow ratio · CPC title

• B01J2208/00796

  Details of the reactor or of the particulate material · CPC title