Apparatuses and methods for cooling catalyst

Patent metadata

Field	Value
Publication number	US-9700865-B2
Application number	US-201414485563-A
Country	US
Kind code	B2
Filing date	Sep 12, 2014
Priority date	Sep 12, 2014
Publication date	Jul 11, 2017
Grant date	Jul 11, 2017

Abstract

Apparatuses and methods for cooling catalyst are provided. In one embodiment, an apparatus for cooling catalyst includes a catalyst cooler vessel having a catalyst inlet for receiving catalyst. The apparatus includes a gas distributor lance positioned in the catalyst cooler vessel and having a gas outlet configured for injecting gas into the catalyst. The apparatus also includes a heat exchange tube positioned in the catalyst cooler vessel and having an outer surface. The heat exchange tube is configured to transfer heat from the catalyst to a heat exchange fluid. The apparatus further includes a hard surfacing material located on the outer surface of the heat exchange tube.

First claim

What is claimed is:

1. An apparatus for cooling catalyst, the apparatus comprising:
a catalyst cooler vessel having a catalyst inlet for receiving the catalyst;
a gas distributor lance positioned in the catalyst cooler vessel and having a gas outlet configured for injecting gas into the catalyst;
a heat exchange tube positioned in the catalyst cooler vessel and having an outer surface, the heat exchange tube being configured to transfer heat from the catalyst to a heat exchange fluid; and
a hard surfacing material located on and welded to the outer surface of the heat exchange tube.

2. The apparatus of claim 1 wherein the hard surfacing material is located on the outer surface of the heat exchange tube adjacent the gas outlet of the gas distributor lance.

3. The apparatus of claim 1 wherein the hard surfacing material surrounds the outer surface of the heat exchange tube to form a substantially cylindrical hard surfacing sleeve.

4. The apparatus of claim 1 wherein the hard surfacing material surrounds the outer surface of the heat exchange tube to form a substantially cylindrical hard surfacing sleeve having a thickness of from about 1 mm to about 5 mm.

5. The apparatus of claim 1 wherein the hard surfacing material surrounds the outer surface of the heat exchange tube to form a substantially cylindrical hard surfacing sleeve having a thickness of from about 2 mm to about 4 mm.

6. The apparatus of claim 1 wherein the hard surfacing material surrounds the outer surface of the heat exchange tube to form a substantially cylindrical hard surfacing sleeve having a length of from about 200 mm to about 500 mm.

7. The apparatus of claim 1 wherein the hard surfacing material surrounds the outer surface of the heat exchange tube to form a substantially cylindrical hard surfacing sleeve having a length of from about 300 mm to about 400 mm.

8. The apparatus of claim 1 wherein:
the heat exchange tube has a proximal portion, a protected portion, and a distal portion; and
the hard surfacing material surrounds the outer surface of the protected portion of the heat exchange tube, wherein the outer surface of the proximal portion and the distal portion of the heat exchange tube is in contact with the catalyst.

9. The apparatus of claim 1 wherein:
the vessel defines a chamber;
the heat exchange tube has a proximal portion, a protected portion, and a distal portion, wherein the proximal portion, the protected portion, and the distal portion are positioned in the chamber; and
the hard surfacing material surrounds the outer surface of the protected portion of the heat exchange tube, wherein the outer surface of the proximal portion and the distal portion of the heat exchange tube is in contact with the catalyst.

10. The apparatus of claim 1 wherein the gas distributor lance and the heat exchange tube are substantially parallel.

11. The apparatus of claim 1 wherein the gas outlet of the gas distributor lance is separated from the heat exchange tube by a distance of from about 50 mm to about 200 mm.

12. The apparatus of claim 1 wherein the gas outlet of the gas distributor lance is separated from the heat exchange tube by a distance of from about 80 mm to about 120 mm.

13. An apparatus for processing catalyst, the apparatus comprising:
a regeneration vessel configured to receive spent catalyst and to regenerate the spent catalyst to form regenerated catalyst; and
a catalyst cooler in fluid communication with the regeneration vessel for receiving the catalyst therefrom, wherein the catalyst cooler includes a heat exchange tube having an outer surface and a hard surfacing material located on the outer surface of the heat exchange tube, wherein the hard surfacing material surrounds the outer surface of the heat exchange tube to form a cylindrical hard surfacing sleeve.

14. The apparatus of claim 13 wherein the catalyst cooler includes a gas distributor lance having a gas outlet configured for injecting gas into the catalyst.

15. The apparatus of claim 14 wherein the hard surfacing material is located on the outer surface of the heat exchange tube adjacent the gas outlet of the gas distributor lance.

16. The apparatus of claim 13 wherein the hard surfacing material surrounds the outer surface of the heat exchange tube to form a substantially cylindrical hard surfacing sleeve having a thickness of from about 1 mm to about 5 mm.

17. The apparatus of claim 16 wherein the substantially cylindrical hard surfacing sleeve has a length of from about 200 mm to about 500 mm.

18. The apparatus of claim 13 wherein:
the catalyst cooler includes a vessel defining a chamber;
the heat exchange tube has a proximal portion, a protected portion, and a distal portion, wherein the proximal portion, the protected portion, and the distal portion are positioned in the chamber; and
the hard surfacing material surrounds and is welded to the outer surface of the protected portion of the heat exchange tube, wherein the outer surface of the proximal portion and the distal portion of the heat exchange tube is in contact with the catalyst.

19. A method for cooling catalyst, the method comprising the steps of:
delivering the catalyst into a catalyst cooler vessel;
transferring heat from the catalyst to a heat exchange tube positioned in the catalyst cooler vessel, wherein the heat exchange tube has an outer surface;
injecting gas into the catalyst within the catalyst cooler vessel to cause back-mixing of the catalyst; and
preventing impingement of the outer surface of the heat exchange tube by the gas with a hard surfacing material located on and welded to the outer surface of the heat exchange tube.

Assignees

• Uop Llc

Inventors

• Umar Syed Basheer
• Mandal Ashim

Classifications

• B01J29/90

  Regeneration or reactivation · CPC title

• B01J2208/00256

  in a heat exchanger for the heat exchange medium separate from the reactor · CPC title

• B01J38/12

  Treating with free oxygen-containing gas · CPC title

• B01J8/1836 Primary

  Heating and cooling the reactor (B01J8/42 takes precedence) · CPC title

• B01J2208/00991

  Disengagement zone in fluidised-bed reactors · CPC title