Elimination of polymer fouling in fluidized bed gas-phase fines recovery eductors

Patent metadata

Field	Value
Publication number	US-10457753-B2
Application number	US-201715730314-A
Country	US
Kind code	B2
Filing date	Oct 11, 2017
Priority date	Oct 14, 2016
Publication date	Oct 29, 2019
Grant date	Oct 29, 2019

Abstract

An eductor, a process and apparatus for gas phase polymerization of olefins in a polymerization reactor are disclosed. The process and apparatus employ an eductor which has an inlet which makes a bend of less than about 90° toward the outlet after entering the mixing chamber of the eductor.

First claim

What is claimed is:

1. An eductor comprising:
a first tubular body having a hollow interior and comprising
a first inlet and a first outlet spaced apart from the first inlet along a central axis, and
a sidewall circumscribing the central axis and defining a mixing chamber; and

a second tubular body having a hollow interior and comprising a second inlet and a spaced apart second outlet wherein the second tubular body extends into the mixing chamber through the sidewall of the first tubular body between the first inlet and the first outlet,
wherein the second inlet is oriented substantially perpendicular to the axis of the first tubular body,
wherein the second tubular body comprises a first bend of less than 90° from perpendicular toward the first outlet before extending into the mixing chamber, and
wherein the second tubular body comprises a second bend of less than 90° toward the first outlet after extending into the mixing chamber.

2. The eductor of claim 1 , wherein the second tubular body makes a first bend of about 45° from perpendicular toward the first outlet before entering the mixing chamber and a second bend of about 45° toward the first outlet after entering the mixing chamber.

3. The eductor of claim 1 , wherein the second tubular body is substantially parallel to the central axis at the second outlet.

4. The eductor of claim 1 , wherein the first inlet is a solid fines inlet and the second inlet is a motive gas inlet.

5. The eductor of claim 1 , wherein the first inlet is a motive gas inlet and the second inlet is a solid fines inlet.

6. The eductor of claim 1 , wherein the first tubular body and the second tubular body below the second bend after entering the mixing chamber are coaxial.

7. The eductor of claim 1 , wherein one or more of the first tubular body and the second tubular body are at least partially cylindrical in shape.

8. The eductor of claim 1 , wherein the first tubular body is at least partially conical in shape.

9. The eductor of claim 1 , further comprising a converging-diverging nozzle adjacent to the first outlet.

10. A method of motivating a gas stream containing solid fines comprising the steps of:
introducing a gas stream comprising solid fines and a gas stream comprising a motive gas into an eductor, wherein the eductor comprises:
a first tubular body having a hollow interior and comprising
a first inlet and a first outlet spaced apart from the first inlet along a central axis, and
a sidewall circumscribing the central axis and defining a mixing chamber;

a second tubular body having a hollow interior and comprising a second inlet and a spaced apart second outlet, wherein the second tubular body extends into the mixing chamber through the sidewall of the first tubular body between the first inlet and the first outlet; and
wherein the second inlet is oriented substantially perpendicular to the axis of the first tubular body,
wherein the second tubular body comprises a first bend of less than 90° from perpendicular toward the first outlet before extending into the mixing chamber, and
wherein the second tubular body comprises a second bend of less than 90° toward the first outlet after extending into the mixing chamber.

11. The method according to claim 10 , wherein the second tubular body makes a first bend of about 45° from perpendicular toward the first outlet before extending into the mixing chamber and a second bend of about 45° toward the first outlet after extending into the mixing chamber.

12. The method according to claim 10 , wherein the first inlet is a solid fines inlet and the second inlet is a motive gas inlet.

13. The method according to claim 10 , wherein the first inlet is a motive gas inlet and the second inlet is a solid fines inlet.

14. The method according to claim 10 , wherein the first tubular body and the second tubular body below the second bend after extending into the mixing chamber are coaxial.

15. The method according to claim 10 , wherein one or both of the first tubular body and the second tubular body is at least partially cylindrical in shape.

16. The method according to claim 10 , wherein the first tubular body is at least partially conical in shape.

17. The method according to claim 10 , wherein the eductor further comprises a converging-diverging nozzle adjacent to the first outlet.

18. An apparatus for polymerizing olefins, comprising:
a polymerization reactor for contacting one or more olefins with a catalyst under polymerization conditions to form a gas stream comprising solid fines and unreacted olefins;
a fines separator in fluid communication with the polymerization reactor for separating the solid fines from the unreacted olefins; and
an eductor in fluid communication with the fines separator for conveying the solid fines back to the polymerization reactor, wherein the eductor comprises:
a first tubular body having a hollow interior and comprising
a first inlet and a first outlet spaced apart from the first inlet along a central axis, and
a sidewall circumscribing the central axis and defining a mixing chamber; and

a second tubular body having a hollow interior and comprising a second inlet and a spaced apart second outlet, wherein the second tubular body extends into the mixing chamber through the sidewall of the first tubular body between the first inlet and the first outlet,
wherein the second inlet is oriented substantially perpendicular to the axis of the first tubular body,
wherein the second tubular body comprises a first bend of less than 90° from perpendicular toward the first outlet before extending into the mixing chamber, and
wherein the second tubular body comprises a second bend of less than 90° toward the first outlet after extending into the mixing chamber.

19. The apparatus of claim 18 , further comprising a heat exchanger for cooling the unreacted olefins from the fines separator, a compressor for compressing the cooled unreacted olefins, and a conduit for recycling the cooled and compressed unreacted olefins back to the polymerization reactor.

20. The apparatus of claim 18 , wherein the gas stream further comprises an inert hydrocarbon.

21. The apparatus of claim 19 , further comprising a conduit for conveying at least a portion of the cooled and compressed unreacted olefins as a motive gas to the first inlet or the second inlet of the eductor.

22. The apparatus of claim 18 , wherein the first inlet is a solid fines inlet and the second inlet is a motive gas inlet.

23. The apparatus of claim 18 , wherein the first inlet is a motive gas inlet and the second inlet is a solid fines inlet.

24. The apparatus of claim 18 , wherein the first tubular body and the second tubular body below the second bend after entering the mixing chamber are coaxial.

25. The apparatus of claim 18 , wherein one or both of the first tubular body and the second tubular body is at least partially cylindrical in shape.

26. The apparatus of claim 18 , wherein the first tubular body is at least partially conical in shape.

27. The apparatus of claim 18 , wherein the eductor further comprises a converging-diverging nozzle adjacent to the first outlet.

28. A process for polymerizing olefins comprising:
contacting one or more olefins with a catalyst in a polymerization reactor under polymerization conditions to form a gas stream comprising fine polymer particles and

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Lowell Jeffrey S
• Hendrickson Gregory G
• Price Ralph J

Classifications

• C08F6/005

  from solid polymers · CPC title

• B01J19/26

  Nozzle-type reactors, i.e. the distribution of the initial reactants within the reactor is effected by their introduction or injection through nozzles · CPC title

• B01J8/1863

  followed by a downward movement outside the reactor and subsequently re-entering it · CPC title

• B01J8/0055

  using cyclones · CPC title

• Y02P20/582

  Recycling of unreacted starting or intermediate materials · CPC title