Polyolefin production with chromium-based catalysts

Patent metadata

Field	Value
Publication number	US-10745501-B2
Application number	US-201816118924-A
Country	US
Kind code	B2
Filing date	Aug 31, 2018
Priority date	Sep 2, 2014
Publication date	Aug 18, 2020
Grant date	Aug 18, 2020

Abstract

A system and method for feeding a chromium-based catalyst to a polymerization reactor; adding a reducing agent to the chromium-based catalyst, and polymerizing an olefin into a polyolefin in the polymerization reactor in the presence of the chromium-based catalyst.

First claim

What is claimed is:

1. A polymerization reactor system comprising:
a mix vessel to contact a substantially continuous feed of chromium-based catalyst to a polymerization reactor with a reducing agent to form a catalyst feed composition comprising the chromium-based catalyst, the mixer having a heat transfer system for heating or cooling a content of the mixer and wherein the mix vessel includes a nozzle having a neck;
an entrance arrangement for the reducing agent entering the mix vessel, and wherein the entrance arrangement includes a conduit extension having a conduit that extends into the neck of the nozzle, where the conduit has an outlet opening to direct the reducing agent entering the mix vessel away from an interior sidewall of the mix vessel;
a polymerization reactor to receive the catalyst feed composition and to polymerize an olefin into a polyolefin in presence of the chromium-based catalyst and
a control system to adjust an addition rate of the reducing agent to the mix vessel and control the heat transfer system for heating or cooling the content of the mix vessel to give a desired flow index of the polyolefin.

2. The system of claim 1 , wherein the polymerization reactor comprises a gas phase reactor, and wherein the mix vessel comprises a stirred mixer.

3. The system of claim 1 , wherein the control system is configured to adjust the addition rate of the reducing agent to maintain a molar ratio of the reducing agent to the chromium-based catalyst to give the desired flow index of the polyolefin.

4. The system of claim 1 , wherein the control system is configured to modulate an addition rate of a solvent to the mix vessel, and wherein a residence time of the chromium-based catalyst through the mix vessel is in a range of 2 minutes to 120 minutes.

5. The system of claim 1 , wherein the chromium-based catalyst comprises an inorganic support comprising a surface area of 50 to 1000 square meters per gram and an average particle size of 20 to 300 micrometers.

6. The system of claim 1 , wherein the control system is configured to adjust an addition rate of a solvent to the mix vessel in response to operating conditions of the polymerization reactor or in response to a measured flow index of the polyolefin.

7. The system of claim 1 , wherein the control system is configured to adjust an addition rate of a solvent to the mix vessel in response to a change in a feed rate of the chromium-based catalyst to maintain substantially constant residence time of the chromium-based catalyst through the mix vessel.

8. The system of claim 1 , wherein the conduit extension of the entrance arrangement directs the reducing agent entering the mix vessel to a surface location on a mixture level that is 20% to 80% of the perpendicular distance from a vertical center line to the interior sidewall of the mix vessel.

9. The system of claim 1 , wherein the conduit extends through the neck of the nozzle into the mix vessel.

10. The system of claim 9 , wherein the conduit extends into the mix vessel by a length dimension of 0.5 to 18 inches measured along the conduit between an outlet end of the conduit and the interior sidewall of the mix vessel.

11. The system of claim 1 , wherein the conduit extension extends into the neck of the nozzle on the mix vessel but does not extend into the mix vessel.

12. A method of operating a polyolefin reactor system, the method comprising:
feeding a chromium-based catalyst through a mix vessel to a polymerization reactor, wherein the mix vessel includes an interior sidewall and a nozzle having a neck;
adding a reducing agent to the chromium-based catalyst in the mix vessel through an entrance arrangement with a conduit extension having a conduit that extends into the neck of the nozzle and the conduit having an outlet opening to direct the reducing agent away from the interior sidewall of the mix vessel, reducing an oxidation state of at least a portion of the chromium in the chromium-based catalyst, wherein the chromium-based catalyst is not contacted with reducing agent prior to feeding the chromium-based catalyst to the mix vessel; and
polymerizing an olefin into a polyolefin in presence of the chromium-based catalyst in the polymerization reactor.

13. The method of claim 12 , wherein feeding the chromium-based catalyst comprises feeding the chromium-based catalyst substantially continuously through the mix vessel to the polymerization reactor.

14. The method of claim 12 , comprising specifying a ratio of an addition rate of the reducing agent to a feed rate of the chromium-based catalyst through the mix vessel to give a desired flow index of the polyolefin.

15. The method of claim 12 , comprising adjusting a ratio of an addition rate of the reducing agent to a feed rate of the chromium-based catalyst through the mix vessel in response to a measured flow index of the polyolefin.

16. The method of claim 12 , comprising adjusting via the mix vessel an aluminum concentration on the chromium-based catalyst or an aluminum to chromium molar ratio on the chromium-based catalyst to give a desired flow index of the polyolefin.

17. The method of claim 12 , comprising adjusting an addition rate of the reducing agent to maintain an aluminum to chromium molar ratio or an aluminum concentration on the chromium-based catalyst in response to changes in a feed rate of the chromium-based catalyst to maintain a flow index of the polyolefin.

18. The method of claim 12 , comprising adjusting an addition rate of solvent to the mix vessel to adjust a contact residence time of the chromium-based catalyst and the reducing agent.

19. The method of claim 12 , comprising adjusting an addition rate of a solvent to the mix vessel in response to operating conditions of the polymerization reactor or in response to a measured flow index of the polyolefin.

Assignees

• Univation Tech Llc

Inventors

• Gross Kevin R
• Cann Kevin J
• Goode Mark G
• Moorhouse John H

Classifications

• C08F210/16 Primary

  Copolymers of ethene with alpha-alkenes, e.g. EP rubbers · CPC title

• B01J19/0066

  Stirrers (mixing per se B01F) · CPC title

• B01J8/082

  Controlling processes · CPC title

• B01J8/08

  with moving particles (with fluidised particles B01J8/18) · CPC title

• B01J2208/00663

  Concentration · CPC title