Fluidized spray tower

• US 6,955,342 B2
• Filed: 07/17/2002
• Issued: 10/18/2005
• Est. Priority Date: 07/17/2001
• Status: Active Grant

• Current Assignee: Direct Contact, LLC
• Original Assignee: William D. Carson
• Inventors: Carson, William D.
• Primary Examiner(s): BUSHEY, CHARLES S
• Application Number:
  US10/198,288
• Publication Number:
  US 20030015809A1
• Time in Patent Office: 1,189 Days
• Field of Search: 261/115, 261/117, 261/118, 261/127, 261/128, 261/152, 261/DIG.9, 962/62, 963/60, 963/66, 963/67
• US Class Current: 261/127
• CPC Class Codes: F23J 15/06 of coolers
• CPC Class Codes: F23N 5/242 using electronic means
• CPC Class Codes: Y02E 20/30 Technologies for a more efficient combustion or heat usage
• CPC Class Codes: Y10S 261/09 Furnace gas scrubbers

Abstract

A fluidized spray vessel. A vessel design is provided for recovering heat from gaseous heat streams. The vessel utilizes a semi-fluidized bed for obtaining desirable liquid/vapor contact times. A spray section is provided in which liquid is sprayed through nozzles designed to provide a mean droplet size having a terminal velocity of from about sixty percent to about ninety five percent of the superficial upward gas velocity. These spray tower design criteria enhance spray tower performance, and thus enables more efficient heat recovery to be practiced, particularly in systems where relatively low grade heat sources are encountered.

Claims

1. An apparatus for recovering heat from a heat containing gaseous stream, by transfer of said heat into a liquid medium, said apparatus comprising:

(a) a containment vessel having an interior wall, said vessel extending along a central axis and having

(i) a hot gas inlet,

(ii) a cooled gas outlet, and

(iii) a condensate drain;

(b) intermediate said hot gas inlet and said cooled gas outlet, a contact liquid medium reservoir bottom plate,

(c) a first gas passageway, said first gas passageway having (i) a passageway inlet, (ii) a passageway outlet, and (iii) a passageway wall extending from said passageway inlet to said passageway outlet, said first gas passageway sealingly affixed to and upwardly extending from said contact liquid medium reservoir bottom plate a preselected distance to define, from said contact liquid medium reservoir bottom plate to said outlet, a contact liquid medium reservoir space for holding said liquid medium;

(d) a liquid medium outlet, said liquid medium outlet adapted for removing liquid medium from said liquid medium reservoir space;

(e) a liquid medium inlet, said liquid medium inlet located between said outlet end of said first gas passageway and said cooled gas outlet of said vessel;

(f) in fluid communication with said liquid medium inlet, one or more spray nozzles, said spray nozzles adapted to spray said liquid medium downward toward said first gas passageway outlet;

(g) a coalescer, said coalescer located adjacent said cooled gas outlet of said vessel, and adapted to coalesce liquid droplets attempting to escape outward through said hot gas outlet.

2. The apparatus as set forth in claim 1, further comprising a reservoir overflow drain, said reservoir overflow drain having a reservoir overflow drain inlet below the level of said first gas passageway outlet.

3. The apparatus as set forth in claim 2, wherein said reservoir overflow drain outlet is in fluid communication with said condensate drain of said vessel.

4. The apparatus as set forth in claim 1, wherein said first gas passageway further comprises one or more inlet baffles.

5. The apparatus as set forth in claim 1, wherein said first gas passageway further comprises one or more outlet baffles.

6. The apparatus as set forth in claim 1, wherein said coalescer comprises a second gas passageway, said second gas passageway located between said spray nozzles and said cooled gas outlet.

7. The apparatus as set forth in claim 6, wherein said second gas passageway further comprises one or more inlet baffles.

8. The apparatus as set forth in claim 1, further comprising an outlet nozzle, said outlet nozzle adapted to receive headed liquid medium from said contact liquid medium reservoir.

9. The apparatus as set forth in claim 1, wherein said first gas passageway is provided in a cylindrical tubular configuration.

10. The apparatus as set forth in claim 1, wherein said first gas passageway is centrally located along said longitudinal axis of said vessel.

11. The apparatus as set forth in claim 1, wherein said first gas passageway comprises a tortuous gas path for said hot gas passing through said first gas passageway, whereby passage of droplets of liquid medium therethrough are minimized.

12. The apparatus as set forth in claim 5, wherein said first gas passageway comprises a hat portion, said hat portion at or near said one or more outlet baffles, said hat portion configured to deflect droplets of liquid medium from said spray nozzles so as to prevent entry of said droplets into said first gas passageway.

13. The apparatus as set forth in claim 1, wherein said vessel comprises a semi-fluidized portion, said semi-fluidized portion including said spray nozzles, and wherein said spray nozzles are sized and shaped to develop a preselected mean droplet size of liquid medium sprayed therethrough having a terminal velocity from about sixty percent to about ninety five percent of the superficial gas velocity of hot gas traveling upward through said semi-fluidized section, such that said liquid medium droplets fall relative to a fixed reference point in said semi-fluidized section from about five percent to about forty percent of the terminal velocity of said droplets.

14. The apparatus as set forth in claim 13, wherein said vessel further comprises, a fluidized section, and wherein said vessel has an effective cross sectional area in said fluidized section sized and shaped so that the superficial gas velocity of hot gas traveling upward through said fluidized section is about 200 percent or more of the terminal velocity of droplets having said preselected mean droplet size.

15. The apparatus as set forth in claim 7, wherein said coalescing section comprises a target situated to impinge and/or intercept droplets traveling toward said cooled gas outlet.

16. The apparatus as set forth in claim 15, wherein said coalescing section comprises one or more inlet baffles, and wherein said target comprises a circular disc affixed to at least one of said one or more inlet baffles.

17. A method of recovering heat from a hot gas by transferring heat to a liquid medium, said method comprising:

(a) providing a vessel as set forth in claim 1;

(b) providing a semi-fluidized spray section in said vessel, said spray section having downwardly directed spray nozzles for spraying a liquid medium into which heat is to be recovered from said gas, said spray nozzles sized and shaped to develop a mean droplet size having a terminal velocity from about sixty percent to about ninety five percent of the superficial upward gas velocity in said semi-fluidized bed section, such that said droplets fall relative to a fixed reference point in said spray section from about five percent to about forty percent of the terminal velocity of said droplets.

18. The method as set forth in claim 17, further comprising providing, in the lower portion of said vessel, a fluidization section wherein the upward gas velocity is in excess of two hundred percent of the terminal velocity of droplets.

19. The method as set forth in claim 17, wherein said liquid medium comprises water.

20. The method as set forth in claim 17, wherein said hot gas comprises an exhaust gas from combustion of a fuel.

21. The method as set forth in claim 20, wherein said exhaust gas comprises stack gas from a boiler.

22. The method as set forth in claim 20, wherein said exhaust gas comprises exhaust from an engine.

23. The method as set forth in claim 22, wherein said engine comprises a gas turbine engine.

24. The method as set forth in claim 17, wherein said hot gas comprises a process gas stream from an industrial process plant.

25. The method as set forth in claim 24, wherein said industrial process plant comprises a paper mill.

26. The method as set forth in claim 17, wherein said hot gas directly contacts said liquid medium to be heated.

27. The method as set forth in claim 17, further comprising (1) an external heat exchanger, and (2) an intermediate heating medium, wherein said hot gas heats said intermediate heating medium, and wherein a liquid stream which does not directly contact said hot gas is heated.