Process for the gas-phase polymerization of olefins

Patent metadata

Field	Value
Publication number	US-9469703-B2
Application number	US-201314429585-A
Country	US
Kind code	B2
Filing date	Sep 5, 2013
Priority date	Sep 21, 2012
Publication date	Oct 18, 2016
Grant date	Oct 18, 2016

Abstract

A process and apparatus for producing olefin polymers are disclosed, comprising:
a. polymerizing one or more olefins in the gas phase, in the presence of an olefin polymerization catalyst, whereby growing polymer particles flow along a cylindrically-shaped downward path in densified form under the action of gravity so as to form a densified bed of downward-flowing polymer particles

b. allowing said polymer particles to flow through a restriction of the densified bed, such restriction being positioned in a restriction zone extending from the bed upward to a distance of 15% of the total height of the densified bed; and

c. metering an antistatic agent through a feed line connected to the densified bed at a feed point being located in a feed zone extending from the top of the restriction upward, to a distance five times the diameter of the section of the densified bed above the restriction.

First claim

The invention claimed is:

1. A process for producing olefin polymers, which comprises the steps of:
a) polymerizing one or more olefins in the gas phase, in the presence of an olefin polymerization catalyst, whereby growing polymer particles flow along a cylindrically-shaped downward path in densified form under the action of gravity so as to form a densified bed of downward-flowing polymer particles;
b) allowing said polymer particles to flow through a restriction of the densified bed, such restriction being positioned in a restriction zone extending from the bed bottom upward to a distance of 15% of the total height of the densified bed; and
c) metering an antistatic agent through a feed line connected to the densified bed at a feed point being located in a feed zone extending from the top of the restriction upward, to a distance five times the diameter of the section of the densified bed above the restriction.

2. The process according to claim 1 , wherein the restriction of the bed is positioned in a zone extending from the bed bottom upward to a distance of 10% of the total height of the densified bed.

3. The process according to claim 1 , wherein the feed point line for metering the antistatic agent is located above the restriction, in a feed zone extending from said upward to a distance to of 4 times the diameter of the section of the densified bed immediately above the restriction.

4. The process according to claim 1 , wherein a stream of a dosing gas is fed into the lower part of the densified bed by means of a feed line placed at a distance above the restriction of up to 1.5 times the diameter of the section of the densified bed immediately above the restriction.

5. The process according to claim 4 , wherein the feed line for metering the antistatic agent and the feed line for metering the dosing gas are coincident.

6. The process according to claim 1 , wherein the restriction of the bed is positioned in a zone extending from the bed bottom upward to a distance of 5% of the total height of the densified bed.

7. The process according to claim 1 , wherein the feed point line for metering the antistatic agent is located in a feed zone extending from said upward to a distance to of more preferably 3 times the diameter of the section of the densified bed immediately above the restriction.

8. The process according to claim 1 , wherein the feed point line for metering the antistatic agent is located in a feed zone extending from said upward to a distance to of 2 times the diameter of the section of the densified bed immediately above the restriction.

9. The process according to claim 1 , wherein a stream of a dosing gas is fed into the lower part of the densified bed by means of a feed line placed at a distance above the restriction of between 0.6 and 1.3 times the diameter of the section of the densified bed immediately above the restriction.

10. The process according to claim 1 , wherein a stream of a dosing gas is fed into the lower part of the densified bed by means of a feed line placed at a distance above the restriction of between 0.7 and 1.0 times the diameter of the section of the densified bed immediately above the restriction.

11. An apparatus for the polymerization of olefins in the gas phase in the presence of an antistatic agent, which comprises a gas-phase polymerization reactor having interconnected polymerization zones, the reactor comprising a riser ( 1 ) through which the polymer particles flow upwards under fast fluidization or transport conditions and a downcomer ( 2 ) through which the polymer particles flow downward in a densified form under the action of gravity, the reactor being provided with:
a) a restriction ( 9 ) positioned in the lower part of the downcomer in a restriction zone extending from the bottom of the downcomer upward to a distance of 15% of the portion of the downcomer occupied by a densified bed of polymer particles, and
b) with a feed line ( 11 ) connected to the downcomer at a feed point being located in a feed zone extending from the top of the restriction upward to a distance five times the diameter of the section of the downcomer above the restriction, such feed line ( 11 ) being connected to an antistatic agent feed line ( 19 ) that is in fluid communication with an antistatic agent source.

12. The apparatus according to claim 11 , comprising one or more other feed lines ( 22 ) for metering the antistatic agent to additional positions along the height of the downcomer.

Assignees

• Basell Poliolefine Italia Srl

Inventors

• Balestra Enrico
• Caputo Tiziana
• Dorini Maurizio
• Mazzucco Antonio
• Soffritti Silvia

Classifications

• C08F10/00 Primary

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

• B01J2219/24

  Stationary reactors without moving elements inside · CPC title

• C08F10/06 Primary

  Propene · CPC title

• B01J19/24

  Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title

• B01J2219/00164

  controlling the flow · CPC title