Moving bed heat exchanger for circulating fluidized bed boiler

Patent metadata

Field	Value
Publication number	US-9163829-B2
Application number	US-95485507-A
Country	US
Kind code	B2
Filing date	Dec 12, 2007
Priority date	Dec 12, 2007
Publication date	Oct 20, 2015
Grant date	Oct 20, 2015

Abstract

A moving bed heat exchanger ( 155 ) includes a vessel having an upper portion ( 200 ), a lower portion ( 210 ) with a floor ( 272 ) including a discharge opening therein, and an intermediate portion ( 205 ). The vessel directs a gravity flow of hot ash particles ( 140 ) received thereby from the upper portion ( 200 ) through the intermediate portion ( 205 ) to the floor ( 272 ) of the lower portion ( 210 ) of the vessel, where the hot ash particles ( 140 ) are collected. Tubes in the intermediate portion ( 205 ) of the vessel direct a flow of working fluid in a direction substantially orthogonal to the direction of the gravity flow of the hot ash particles ( 140 ) through the intermediate portion ( 205 ) of the vessel such that heat from the hot ash particles ( 140 ) is transferred to the working fluid thereby cooling the hot ash particles ( 140 ).

First claim

We claim:

1. A moving bed heat exchanger, comprising:
a vessel including an upper portion having a hot ash feed opening, a lower portion having a floor including a discharge opening therein, and an intermediate portion disposed between said upper portion and said lower portion, said vessel being configured so as to thereby direct a gravity flow from said upper portion through said intermediate portion to said floor of said lower portion of said vessel of hot ash particles received in said vessel via said feed opening and to effect the collection of said hot ash particles on said floor of said lower portion of said vessel;
a plurality of tubes disposed only in said intermediate portion of said vessel and configured so as to thereby direct a flow of working fluid in a direction substantially orthogonal to the direction of the directed gravity flow of said hot ash particles through said intermediate portion of said vessel, such that heat from said hot ash particles is transferred to said working fluid to thereby cool said hot ash particles as the gravity flow of said hot ash particles is directed to said lower portion of said vessel;
a discharge pipe extending through the discharge opening into the lower portion of the vessel;
a hood arranged as a low pressure ash control valve including a labyrinth chamber formed at said floor;
an air inlet is configured to inject air into the hood for driving collected cooled hot ash particles through an inlet opening of the discharge pipe and said discharge opening of said vessel by creating a pressure condition in the hood that is lower relative to a pressure formed by a static head of the collected cooled ash; and
the floor is configured to collect hot ash particles only in the lower portion of the vessel.

2. The moving bed heat exchanger as claimed in claim 1 , wherein:
the amount of the heat transferred from said hot ash particles to said working fluid corresponds to the amount of the collected cooled hot ash particles that are discharged through said discharge opening of said vessel.

3. The moving bed heat exchanger as claimed in claim 1 , wherein:
the amount of the collected cooled hot ash particles that are discharged through said discharge opening of said vessel is controlled based on the temperature of the gas in a furnace that is operatively connected to said vessel and to which are directed the collected cooled hot ash particles that are discharged through said discharge opening of said vessel.

4. The moving bed heat exchanger as claimed in claim 1 , wherein:
said relatively higher pressure of said collected cooled hot ash particles is approximately 200 inches WG; and
said relatively lower pressure of the air injected by said plurality of air inlets is approximately 65 inches WG.

5. The moving bed heat exchanger as claimed in claim 1 , wherein:
the air injected by said air inlet is operative to fluidize said collected cooled hot ash particles and to transport said collected cooled hot ash particles through said discharge opening of said vessel.

6. The moving bed heat exchanger as claimed in claim 1 , wherein said feed opening is a first feed opening, said floor is a first floor, said discharge opening is a first discharge opening, said air inlet is a first air inlet, and said hot ash particles are first hot ash particles, and further comprising:
a plurality of second air inlets;
wherein said upper portion, said intermediate portion and said lower portion form a first compartment of said vessel;
wherein said vessel also includes a second compartment with a second feed opening and a second floor including a second discharge opening therein, said vessel being further configured so as to be operative to thereby direct a gravity flow to said floor of said second compartment of second hot ash particles received in said vessel via said second feed opening and to effect the collection of said second hot ash particles on said second floor of said second compartment;
wherein said plurality of second air inlets is configured to inject air into said second compartment of said vessel to control the amount of said collected second hot ash particles that are discharged through said second discharge opening of said second compartment.

7. The moving bed heat exchanger as claimed in claim 6 , wherein:
the amount of said collected second hot ash particles that are discharged through said second discharge opening of said second compartment is controlled such that the amount of said second hot ash particles collected on said floor of said second compartment is sufficient to seal said second compartment against a flow of an external gas through said second discharge opening into said second compartment.

8. The moving bed heat exchanger as claimed in claim 1 , wherein:
the plurality of tubes disposed in said intermediate portion of said vessel are configured as finned tubes.

9. A method of recouping heat from hot ash particles in a moving bed heat exchanger, the moving bed heat exchanger including, a vessel including an upper portion having a hot ash feed opening, a lower portion having a floor including a discharge opening therein, and an intermediate portion disposed between the upper portion and the lower portion, a plurality of tubes disposed only in the intermediate portion of the vessel, a discharge pipe extending through the discharge opening into the lower portion of the vessel, a hood arranged as a low pressure ash control valve including a labyrinth chamber formed at said floor, an air inlet, the floor configured to collect hot ash particles only in the lower part of the vessel the method comprising the steps of:
directing a gravity flow of hot ash particles from the upper portion through the intermediate portion to the floor of the lower portion of the vessel of hot ash particles received in the vessel via the feed opening and for collecting the hot ash particles on the floor of the lower portion of the vessel;
directing a flow of working fluid along a path intersecting the gravity flow of the hot ash particles and in a direction substantially orthogonal to the direction of the gravity flow of the hot ash particles through the intermediate portion of the vessel so as to thereby transfer heat from the hot ash particles to the working fluid for cooling of the hot ash particles;
collecting the cooled hot ash particles in a collector;
injecting air through the air inlet into the hood to drive collected cooled hot ash particles of the collection of hot ash particles through an inlet opening of the discharge pipe and said discharge opening of said vessel by creating a pressure condition in the hood that is lower relative to a pressure formed by a static head of the collected cooled ash to a furnace.

10. The method as claimed in claim 9 , wherein:
the amount of heat transferred from the hot ash particles to the working fluid corresponds to the amount of collected cooled hot ash particles that are discharged from the collector.

11. The method as claimed in claim 9 , wherein:
the amount of the collected cooled hot ash particles that is discharged from the collector is controlled based on the temperature of the gas in the furnace that is operatively connected to the collector and to which are directed the collected cooled hot ash particles that are discharged from the collector.

12. The method as claimed in claim 9 , wherein:
the collected cooled hot ash particles are at a relatively higher pressure; and the injected air is at a relatively lower pressure.

13. The method as claimed in claim 12 , wherein:
the relatively higher pressure of the collected cooled hot ash particles is approximately 200 inches WG;

Assignees

• Jacobs Robert V
• Jukkola Glen D
• Mylchreest George D
• Teigen Bard C
• Waryasz Richard E
• Ferguson Laurie
• Ferguson John E
• Alstom Technology Ltd

Inventors

• Jacobs Robert V
• Jukkola Glen D
• Mylchreest George D
• Teigen Bard C
• Waryasz Richard E
• Ferguson Laurie
• Ferguson John E

Classifications

• F28D13/00

  Heat-exchange apparatus using a fluidised bed · CPC title

• F23C2206/103

  Cooling recirculating particles · CPC title

• F28D2021/0045

  for granular materials · CPC title

• F23C10/32

  by controlling the rate of recirculation of particles separated from the flue gases · CPC title

• F28D7/00

  Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall · CPC title