CA1149234A - Multi-zone fluidized bed combustor and method of operating same - Google Patents
Multi-zone fluidized bed combustor and method of operating sameInfo
- Publication number
- CA1149234A CA1149234A CA000368541A CA368541A CA1149234A CA 1149234 A CA1149234 A CA 1149234A CA 000368541 A CA000368541 A CA 000368541A CA 368541 A CA368541 A CA 368541A CA 1149234 A CA1149234 A CA 1149234A
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- CA
- Canada
- Prior art keywords
- chamber
- fuel
- combustor
- bed
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C10/00—Fluidised bed combustion apparatus
- F23C10/005—Fluidised bed combustion apparatus comprising two or more beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/36—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed through which there is an essentially horizontal flow of particles
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
MULTI-ZONE FLUIDIZED BED COMBUSTOR AND
METHOD OF OPERATING SAME
ABSTRACT OF THE DISCLOSURE
A multi-zone fluidized bed combustor and method of operating same in which a plurality of substantially vertical partitions are disposed and arranged in a housing to divide the housing into three or more zones, or chambers. A bed of parti-culate material containing fuel is established in at least two of the chambers and openings are provided in the partitions to permit flow of the material from one of the two chambers to the other and from the latter to a third chamber. Air is passed through the beds to fluidize the particulate material and promote the combustion of the fuel in the two chambers and to cool the material in the third chamber.
METHOD OF OPERATING SAME
ABSTRACT OF THE DISCLOSURE
A multi-zone fluidized bed combustor and method of operating same in which a plurality of substantially vertical partitions are disposed and arranged in a housing to divide the housing into three or more zones, or chambers. A bed of parti-culate material containing fuel is established in at least two of the chambers and openings are provided in the partitions to permit flow of the material from one of the two chambers to the other and from the latter to a third chamber. Air is passed through the beds to fluidize the particulate material and promote the combustion of the fuel in the two chambers and to cool the material in the third chamber.
Description
1~49~3~
BAC~;GROUND OF THE INVENTION
.
This invention relates to a fluidized bed combustor and a method of operating same and, more particularly, to such a combustor and method in which three or more separate beds of particulate material are established within a single housing.
The use of fluidized beds has long been recognized as an attractive means of generating heat. In a normal fluidized bed arrangement, air is passed through a bed of particulate material, which usually includes a mi~ture of inert material, a fuel material such as high sulfur bitaminous coal, and an adsorbent material for the sulfur released as a result of the co~ustion of the fuel material. As a result of the air passing through the bed, the bed behaves like a boiling liquid which promotes the combustion of the fuel. The basic advantages of such an arrangement include a relatively high heat transfer rate, a subs~antially uniform bed temperature, combustion at relatively low temperatures, ease of handling the fuel materials, a reduction in corrosion and boiler fouling and a reduction in boiler size.
In the fluidized bed combustion process, in order to insure capture by the adsorbent of the sulfur released during combustion of the fuel, the bed temperature has to be kept close to a predetermined value (normally 1500-1550F).
At this temperature, the bed material will contain ~uantities of unburned fuel material, especially in the case when low reactive fuels and/or fuels of a relatively large size are used. However, since the bed must be continuously ~9~3~
drained to discharge the spent bed material, a good portion of the unburned fuel material will also be discharged. This, of course, results in a reduction in the recovery of sensible heat in the bed and in the overall efficiency of the system.
SUMM~RY OF THE INVENTION
Accordingly, the present inven-tion seeks to provide a fluidized bed combustor and a method of operating same which enables a relatively high percentage of fuel materials to be combusted.
The invention in particular pertains to a fluidized bed combustor comprising a housing~ a plurality of substantial-ly vertical partitions disposed in the housing and dividing the housing into a first chamber, a second chamber and a third chamber. Means are provided for establishing a bed of particulate ma-terial containing fuel in the first and second chambers with means associated with the partitions for permit-ting flow of the material from the first chamber to the second chamber and from the second chamber to the third chamber. Means are respectively associated with each chamber for passing air through each of the beds to fluidize the particulate material and promote the combustion of the fuel in the first and second chambers and to cool the material in the third chamber. Means are provided for adding fuel to the bed in the first chamber to maintain continuous combustion in the first chamber and means associated with the third chamber permit the continuous discharge of cooled particulate material from the third chamber. A plurality of heat exchange tubes are disposed in the first chamber and means are provided for passing a relatively cool heat exchange fluid through the heat exchange tubes to remove heat from the bed in the first chamber. Thus, the temperature of the bed in -the first chamber can be controlled by the means for passing air through the first chamber, by the means for adding fuel to the bed in ~14~34 the first chamber, and by the means for passing a relatively cool heat exchange fluid through the heat exchange tubes.
Further, the present invention seeks to provide a combustor in which a plurality of zones, or chambers, are established within the combustor housing with one or more of the chambers being maintained at a temperature compatible with the recovery of sulfur by the adsorbent material in the bed, and another chamber being maintained at a temperature sufficient to promote complete combustion of the fuel material.
Still further, the present invention seeks to provide a combustor of the above type in which a fluidized bed is established in a main chamber and the particulate material is passed to a second chamber for further burning and to a third chamber for cooling before it is discharged from the combustor housing.
A further aspect of the present invention pertains to a combustor of the above type in which the flow of fluidizing and combustion air to each zone, or chamber, is individually regulated.
Various other aspects of the invention will become apparent from the description of a preferred embodiment herein.
BRIEF DESCRIPTION OF THE INVENTION
Figure 1 is a partial perspective view of the combustor of the present invention;
Figure 2 is a reduced plan view of the combustion of Figure l;
Figures 3 and 4 are cross-sectional views taken along the line 3-3 and 4-4, respectively, of Figure 2; and Figures 5 and 6 are views similar to Figure 2, but depicting alternative embodiments of the present invention.
v. ,~
~14~
DESCRIPTION OF T~IE PRE~ERR~D E~BODIME~TS
_ _ _ _ _ _ Referring specifically to the drawings, which depict a fluidized bed combustor of the present invention, the reference numeral 10 refers, in general, to a housing having a front wall 12, a rear wall 14 and two side walls 16 and 18. The walls 12, 14, 16 and 18 are formed by a plurality of interconnected ~ubes in a con-ventional manner, it being understood that the ends of the tubes can be connected between inlet and outlet headers to permit the flow of water through the tubes to add - heat from the combustor to the water. The housing 10 is also provided with a roof (not shown) and a floor which will be described in detail later.
A partition 20 is provided within the housing 10 in a spaced relationship to the rear wall 14 and extends from the side wall 16 to the side wall 18. A
second partition 22 extends be-tween the partition 20 and the rear wall 14 and parallel to the side walls 16 and 18 in ~ spaced relationship thereto. A third partition 23 extends immediately adjacent the rear wall 14 and parallel thereto, and between the side wall 16 and the ~artition 22. As a result of the foregoing, a main chamber 24 is defined by the walls 12, 16 and 18 and the partition 20;
a second chamber 26 is d~fined by the wall 16 and the partitions 20, 22 and 23; and a third chamber 28 is defined by the walls 14 and 18 and the partitiors20 and 22.
The floors of the chambers 24, 26 and 28 are formed by a perforated plate, or grate, 30 extending between the walls 12 r 14, 16 and 18. The partitions 20, 22 and 23 extend ver-tically from the grate 30 to a plane below the plane of the roof of the housing to define a free board space between the upper portions of the partitions and the roof.
An air plenum 32 extends immediately below the chamber 24, an air plenum 34 extends immediately below the chamber 26, and an air plenum 36 extends immediately below the chamber 28. An inlet duct, shown schematically by the reference numeral 40, receives air from an external source (not sho~n) and passes same into the air plenum 32, A duct 42 branches from the duct 40 and connects with two branch ducts 44 and ~6 which pass air from the duct ~0 into the air plenums 34 and 36, respectively. A valve 48 is asso-ciated with each of the ducts 40, 44 and 46 to control the flow of air into the plenums 32, 34 and 36, respec-tively. As a result, the flow of air into the chambers 24, 26 and 28, respectively, can be individually controlled.
A pair of openings 50 and 52 are provided in the lower portion of the,partition 20 to permit the particulate material from the chamber 24 to pass into the chamber 26. An opening 54 is provided in the partition 22 to permit the particulate material from the chamber 26 to pass into the chamber 28. A discharge opening 56 is provided in the wall 18 in communication with the chamber 28 to permit the particulate material from the chamber 28 to discharge from the housing 10 into a conduit 58 under the control of a valve 60.
3~ A bed of partic~late material is established ~l49;~3gL
in each of the chambers 2~ and 26 with the height of the material extending approximately to alevel which is slightly below the height of the partitions 20, 22 and 23, as indicated by the reference numeral 62 in Figure 1. Each bed of particulate material includes a mixture of crushed coal and an inert material such as sand or a commercial grade hematite iron ore. Also a fine limestone or dolomite is included for use as an adsorbent for the sulfur released during the combustion of the fuel.
A pair of inlet openings 64 and 66 are provided in the side wall 18 for permitting the continuous introduction of the particulate fuel material and adsorbent, respec-tively, into the upper portion of the chamber 2~.
Although not shown in the drawings, it is understood that a roof is provided over the walls 12, 14, 16 and 18 and contains a single outlet for the discharge of the mixture of air and gaseous products of combustion from the chambers 24, 26 and 28. A pair of injectors 70 and 72 are provided for reinjecting into the chambe~ 26 the particulate material entrained in the mixture of air and gaseous products of combustion exiting from the housing 10 and separated from the latter mixture by external equipment (not shown).
A notch 74 is provided in the upper portion of the partition 22 to permit the flow of the particulate material from the chamber 26 to the chamber 28 in the event the height of the material in the chamber 26 exceeds the level represented by the line 62.
An opening 76 is provided in the side wall 16 in communication with the chamber 26 to receive an igniter or the like to ignite the bed material in the ~49;~
chambe~ 26 for reasons also to be descrlbed in detail later.
A plurality of heat exchange tubes 80 are provided in the chamber 24, with one of the tubes being shown by the refer-ence numeral 80. Each tube extends between an inlet header 82 and an outlet header 84 disposed externally of the housing 10 and penetrates the front wall 12 before extending in a serpentine relationship in the bed of particulate material disposed in chamber 24. Water can then be passed through the tubes 80 to raise the temperature of the water and lower the temperature of the bed.
In operation of the combustor 10, air is introduced through the conduit 40 into the air plenum 32 which fluidizes the bed of particulate material in the chamber 24 and, after pre-ignition, the fuel material burns and releases its sensible heat to the water passing through the tubes 80.
~dditional fuel and adsorbent is introduced into the upper level of the bed in the chamber 24 through the inlets 64 and 66, respectively. In order to insure optimum adsorption of the sulfur contained in the particula-te fuel material by the adsorbent, the temperature of the bed in chamber 24 is maintained close to a predetermined value, normally 1500-1550F. The maximum bed temperature i5 maintained by the presence of the cooling tubes 80, the regulation of the flow of air into the chamber by the valve 48, tne bed height and the amount of fuel material introduced into the bed through the inlet 64.
A portion of the particulate material in the chamber 24 passes through the openings 50 and 52 into the --S--
BAC~;GROUND OF THE INVENTION
.
This invention relates to a fluidized bed combustor and a method of operating same and, more particularly, to such a combustor and method in which three or more separate beds of particulate material are established within a single housing.
The use of fluidized beds has long been recognized as an attractive means of generating heat. In a normal fluidized bed arrangement, air is passed through a bed of particulate material, which usually includes a mi~ture of inert material, a fuel material such as high sulfur bitaminous coal, and an adsorbent material for the sulfur released as a result of the co~ustion of the fuel material. As a result of the air passing through the bed, the bed behaves like a boiling liquid which promotes the combustion of the fuel. The basic advantages of such an arrangement include a relatively high heat transfer rate, a subs~antially uniform bed temperature, combustion at relatively low temperatures, ease of handling the fuel materials, a reduction in corrosion and boiler fouling and a reduction in boiler size.
In the fluidized bed combustion process, in order to insure capture by the adsorbent of the sulfur released during combustion of the fuel, the bed temperature has to be kept close to a predetermined value (normally 1500-1550F).
At this temperature, the bed material will contain ~uantities of unburned fuel material, especially in the case when low reactive fuels and/or fuels of a relatively large size are used. However, since the bed must be continuously ~9~3~
drained to discharge the spent bed material, a good portion of the unburned fuel material will also be discharged. This, of course, results in a reduction in the recovery of sensible heat in the bed and in the overall efficiency of the system.
SUMM~RY OF THE INVENTION
Accordingly, the present inven-tion seeks to provide a fluidized bed combustor and a method of operating same which enables a relatively high percentage of fuel materials to be combusted.
The invention in particular pertains to a fluidized bed combustor comprising a housing~ a plurality of substantial-ly vertical partitions disposed in the housing and dividing the housing into a first chamber, a second chamber and a third chamber. Means are provided for establishing a bed of particulate ma-terial containing fuel in the first and second chambers with means associated with the partitions for permit-ting flow of the material from the first chamber to the second chamber and from the second chamber to the third chamber. Means are respectively associated with each chamber for passing air through each of the beds to fluidize the particulate material and promote the combustion of the fuel in the first and second chambers and to cool the material in the third chamber. Means are provided for adding fuel to the bed in the first chamber to maintain continuous combustion in the first chamber and means associated with the third chamber permit the continuous discharge of cooled particulate material from the third chamber. A plurality of heat exchange tubes are disposed in the first chamber and means are provided for passing a relatively cool heat exchange fluid through the heat exchange tubes to remove heat from the bed in the first chamber. Thus, the temperature of the bed in -the first chamber can be controlled by the means for passing air through the first chamber, by the means for adding fuel to the bed in ~14~34 the first chamber, and by the means for passing a relatively cool heat exchange fluid through the heat exchange tubes.
Further, the present invention seeks to provide a combustor in which a plurality of zones, or chambers, are established within the combustor housing with one or more of the chambers being maintained at a temperature compatible with the recovery of sulfur by the adsorbent material in the bed, and another chamber being maintained at a temperature sufficient to promote complete combustion of the fuel material.
Still further, the present invention seeks to provide a combustor of the above type in which a fluidized bed is established in a main chamber and the particulate material is passed to a second chamber for further burning and to a third chamber for cooling before it is discharged from the combustor housing.
A further aspect of the present invention pertains to a combustor of the above type in which the flow of fluidizing and combustion air to each zone, or chamber, is individually regulated.
Various other aspects of the invention will become apparent from the description of a preferred embodiment herein.
BRIEF DESCRIPTION OF THE INVENTION
Figure 1 is a partial perspective view of the combustor of the present invention;
Figure 2 is a reduced plan view of the combustion of Figure l;
Figures 3 and 4 are cross-sectional views taken along the line 3-3 and 4-4, respectively, of Figure 2; and Figures 5 and 6 are views similar to Figure 2, but depicting alternative embodiments of the present invention.
v. ,~
~14~
DESCRIPTION OF T~IE PRE~ERR~D E~BODIME~TS
_ _ _ _ _ _ Referring specifically to the drawings, which depict a fluidized bed combustor of the present invention, the reference numeral 10 refers, in general, to a housing having a front wall 12, a rear wall 14 and two side walls 16 and 18. The walls 12, 14, 16 and 18 are formed by a plurality of interconnected ~ubes in a con-ventional manner, it being understood that the ends of the tubes can be connected between inlet and outlet headers to permit the flow of water through the tubes to add - heat from the combustor to the water. The housing 10 is also provided with a roof (not shown) and a floor which will be described in detail later.
A partition 20 is provided within the housing 10 in a spaced relationship to the rear wall 14 and extends from the side wall 16 to the side wall 18. A
second partition 22 extends be-tween the partition 20 and the rear wall 14 and parallel to the side walls 16 and 18 in ~ spaced relationship thereto. A third partition 23 extends immediately adjacent the rear wall 14 and parallel thereto, and between the side wall 16 and the ~artition 22. As a result of the foregoing, a main chamber 24 is defined by the walls 12, 16 and 18 and the partition 20;
a second chamber 26 is d~fined by the wall 16 and the partitions 20, 22 and 23; and a third chamber 28 is defined by the walls 14 and 18 and the partitiors20 and 22.
The floors of the chambers 24, 26 and 28 are formed by a perforated plate, or grate, 30 extending between the walls 12 r 14, 16 and 18. The partitions 20, 22 and 23 extend ver-tically from the grate 30 to a plane below the plane of the roof of the housing to define a free board space between the upper portions of the partitions and the roof.
An air plenum 32 extends immediately below the chamber 24, an air plenum 34 extends immediately below the chamber 26, and an air plenum 36 extends immediately below the chamber 28. An inlet duct, shown schematically by the reference numeral 40, receives air from an external source (not sho~n) and passes same into the air plenum 32, A duct 42 branches from the duct 40 and connects with two branch ducts 44 and ~6 which pass air from the duct ~0 into the air plenums 34 and 36, respectively. A valve 48 is asso-ciated with each of the ducts 40, 44 and 46 to control the flow of air into the plenums 32, 34 and 36, respec-tively. As a result, the flow of air into the chambers 24, 26 and 28, respectively, can be individually controlled.
A pair of openings 50 and 52 are provided in the lower portion of the,partition 20 to permit the particulate material from the chamber 24 to pass into the chamber 26. An opening 54 is provided in the partition 22 to permit the particulate material from the chamber 26 to pass into the chamber 28. A discharge opening 56 is provided in the wall 18 in communication with the chamber 28 to permit the particulate material from the chamber 28 to discharge from the housing 10 into a conduit 58 under the control of a valve 60.
3~ A bed of partic~late material is established ~l49;~3gL
in each of the chambers 2~ and 26 with the height of the material extending approximately to alevel which is slightly below the height of the partitions 20, 22 and 23, as indicated by the reference numeral 62 in Figure 1. Each bed of particulate material includes a mixture of crushed coal and an inert material such as sand or a commercial grade hematite iron ore. Also a fine limestone or dolomite is included for use as an adsorbent for the sulfur released during the combustion of the fuel.
A pair of inlet openings 64 and 66 are provided in the side wall 18 for permitting the continuous introduction of the particulate fuel material and adsorbent, respec-tively, into the upper portion of the chamber 2~.
Although not shown in the drawings, it is understood that a roof is provided over the walls 12, 14, 16 and 18 and contains a single outlet for the discharge of the mixture of air and gaseous products of combustion from the chambers 24, 26 and 28. A pair of injectors 70 and 72 are provided for reinjecting into the chambe~ 26 the particulate material entrained in the mixture of air and gaseous products of combustion exiting from the housing 10 and separated from the latter mixture by external equipment (not shown).
A notch 74 is provided in the upper portion of the partition 22 to permit the flow of the particulate material from the chamber 26 to the chamber 28 in the event the height of the material in the chamber 26 exceeds the level represented by the line 62.
An opening 76 is provided in the side wall 16 in communication with the chamber 26 to receive an igniter or the like to ignite the bed material in the ~49;~
chambe~ 26 for reasons also to be descrlbed in detail later.
A plurality of heat exchange tubes 80 are provided in the chamber 24, with one of the tubes being shown by the refer-ence numeral 80. Each tube extends between an inlet header 82 and an outlet header 84 disposed externally of the housing 10 and penetrates the front wall 12 before extending in a serpentine relationship in the bed of particulate material disposed in chamber 24. Water can then be passed through the tubes 80 to raise the temperature of the water and lower the temperature of the bed.
In operation of the combustor 10, air is introduced through the conduit 40 into the air plenum 32 which fluidizes the bed of particulate material in the chamber 24 and, after pre-ignition, the fuel material burns and releases its sensible heat to the water passing through the tubes 80.
~dditional fuel and adsorbent is introduced into the upper level of the bed in the chamber 24 through the inlets 64 and 66, respectively. In order to insure optimum adsorption of the sulfur contained in the particula-te fuel material by the adsorbent, the temperature of the bed in chamber 24 is maintained close to a predetermined value, normally 1500-1550F. The maximum bed temperature i5 maintained by the presence of the cooling tubes 80, the regulation of the flow of air into the chamber by the valve 48, tne bed height and the amount of fuel material introduced into the bed through the inlet 64.
A portion of the particulate material in the chamber 24 passes through the openings 50 and 52 into the --S--
2~
chamber 26 which is kept at a temperature c~nsistent with optimum combus-tion of the unburned fuel particles received from the chamber 2~. This temperature, of course, depends on the various operating parameters associated with the chamber 26, such as the amount of air flow through the chamber, the bed height in the chamber, the amount of fuel in the chamber, etc., and for the purpose of example, could be approximately 1800F.
As a result of the foregoing, a great percentage o~ the fuel material in the chamber 26 is combusted and the spent material along with the inert material and the adsorbent in the chamber 26 passes through the opening 54 in the parti-tion 22 and into the chamber 23. The air passing upwardly through the chamber 28 from the duct 46 under the control of the valve ~8 associated therewith, cools this material before it is discharged from the chamber 28 through the opening 56 and into the discharge duct 58. As a result of the foregoing, an unprecedented high percentage of the fuel material introduced into the housing 10 is combusted while maintaining optimum sulfur adsorption, thus increasing the sensible heat given of~ and the overall efficiency of the process.
Another advantage of the present invention is that the chamber 26 can be used as a startoff chamber, i.e., during start-up of the entire process, the fuel material in the chamber 26 can be ignited by an igniter or the like extend-ing through the opening 76 in the wall 16 in communication with the chamber 26. The level of the fuel in the bed in the chamber 26 can be increased so that the i~nited fuel spills over into the chamber 24 and ignites the fuel material in this chamber. Alternatively, an air jet, or the like, can be provided at the openings 50 and 52 into the chamber 24. Of course, after start~up in the foregoing manner, the combustor would operate in the manner described above.
Figures 5 and 6 depict alternate bed arrangements for the combustor shown in Figures 14. In particular, according to the embodiment of Figure 5, a pair of additional ~arti-tions 90 and 92 are provided in the housing 10 and extend parallel to the partition 20 to divide the chamber 24 into three chambers 24a, 24b and 24c. A pair of openings 94 are provided in each partition 90 and 92 to permit communication between the chambers 24a and 24b and between the chambers 24b and 24c. Therefore, the particulate material, including fuel material continuously introduced into each of the chambers 24a, 24b and 24c, would pass from the chamber 24a to the chamber 24b and ~rom the chambers 24b into the chamber 24c before it passes into the chamber 26 and 2~ in the manner described in connection with the previous embodiment.
The chambers 24a, 24b and 24c are maintained at a tempera-ture compatible with sulfur adsorption as discussed above in connection with the previous embodiment and chambers 26 and 28 also operate in the same manner as discussed above. In addition to insuring high sulfur capture and maximum fuel combustion as in the previous embodiment, this arrangement permits additional load turndown capability, i.e., the chamber 24a (and 24b, as necessary) may not be fluidized at relatively low loads, but can be fluidized as necessary to accomodate higher loads.
The embodiment of Figure 6 is similar to that o~ Figure 5 with the exception that a first partition 96 is provided and extends between the partition 20 and the ~ront wall 12, and a second partition 98 extends between the side walls 16 and 18 and intersects with the partition 96 to form chambers 24d, 24e, 24f and 2~g.
It is understood that inlet openings for the introduc-tion o fuel and particulate material are provided in the wall 16: 18 as necessary to supply the fuel and adsorbent material to the chambers 24d, 24e, 24f and 24g. Two openings 100 are provided in the partition 96 to permit flow of particulate material from the chambers 24d and 2~e into the chambers 24f and 24g, respectively. An opening 102 is provided in the partition 98 to permit the flow of particulate material from the chamber 24g into the chamber 24f before it flows into the chamber 26 and chamber 28 as described in connection with the previous embodiment. The chambers 24d, 24e, 24f and 24g operate in a manner similar to chamber 24 in the first embodiment, while chamhers 26 and 28 operate in the same manner as discussed above.
Thus the arrangement of Figure 6 offers the same load turndown capability as the embodiment of Figure 5 while insuring high sulfur capture and maximum fuel combustion.
It is also understood that other variations of the specific construction and arrangement of the system and method disclosed above can be made by those skilled in the art without departin~ from the invention as defined in the appended claims.
chamber 26 which is kept at a temperature c~nsistent with optimum combus-tion of the unburned fuel particles received from the chamber 2~. This temperature, of course, depends on the various operating parameters associated with the chamber 26, such as the amount of air flow through the chamber, the bed height in the chamber, the amount of fuel in the chamber, etc., and for the purpose of example, could be approximately 1800F.
As a result of the foregoing, a great percentage o~ the fuel material in the chamber 26 is combusted and the spent material along with the inert material and the adsorbent in the chamber 26 passes through the opening 54 in the parti-tion 22 and into the chamber 23. The air passing upwardly through the chamber 28 from the duct 46 under the control of the valve ~8 associated therewith, cools this material before it is discharged from the chamber 28 through the opening 56 and into the discharge duct 58. As a result of the foregoing, an unprecedented high percentage of the fuel material introduced into the housing 10 is combusted while maintaining optimum sulfur adsorption, thus increasing the sensible heat given of~ and the overall efficiency of the process.
Another advantage of the present invention is that the chamber 26 can be used as a startoff chamber, i.e., during start-up of the entire process, the fuel material in the chamber 26 can be ignited by an igniter or the like extend-ing through the opening 76 in the wall 16 in communication with the chamber 26. The level of the fuel in the bed in the chamber 26 can be increased so that the i~nited fuel spills over into the chamber 24 and ignites the fuel material in this chamber. Alternatively, an air jet, or the like, can be provided at the openings 50 and 52 into the chamber 24. Of course, after start~up in the foregoing manner, the combustor would operate in the manner described above.
Figures 5 and 6 depict alternate bed arrangements for the combustor shown in Figures 14. In particular, according to the embodiment of Figure 5, a pair of additional ~arti-tions 90 and 92 are provided in the housing 10 and extend parallel to the partition 20 to divide the chamber 24 into three chambers 24a, 24b and 24c. A pair of openings 94 are provided in each partition 90 and 92 to permit communication between the chambers 24a and 24b and between the chambers 24b and 24c. Therefore, the particulate material, including fuel material continuously introduced into each of the chambers 24a, 24b and 24c, would pass from the chamber 24a to the chamber 24b and ~rom the chambers 24b into the chamber 24c before it passes into the chamber 26 and 2~ in the manner described in connection with the previous embodiment.
The chambers 24a, 24b and 24c are maintained at a tempera-ture compatible with sulfur adsorption as discussed above in connection with the previous embodiment and chambers 26 and 28 also operate in the same manner as discussed above. In addition to insuring high sulfur capture and maximum fuel combustion as in the previous embodiment, this arrangement permits additional load turndown capability, i.e., the chamber 24a (and 24b, as necessary) may not be fluidized at relatively low loads, but can be fluidized as necessary to accomodate higher loads.
The embodiment of Figure 6 is similar to that o~ Figure 5 with the exception that a first partition 96 is provided and extends between the partition 20 and the ~ront wall 12, and a second partition 98 extends between the side walls 16 and 18 and intersects with the partition 96 to form chambers 24d, 24e, 24f and 2~g.
It is understood that inlet openings for the introduc-tion o fuel and particulate material are provided in the wall 16: 18 as necessary to supply the fuel and adsorbent material to the chambers 24d, 24e, 24f and 24g. Two openings 100 are provided in the partition 96 to permit flow of particulate material from the chambers 24d and 2~e into the chambers 24f and 24g, respectively. An opening 102 is provided in the partition 98 to permit the flow of particulate material from the chamber 24g into the chamber 24f before it flows into the chamber 26 and chamber 28 as described in connection with the previous embodiment. The chambers 24d, 24e, 24f and 24g operate in a manner similar to chamber 24 in the first embodiment, while chamhers 26 and 28 operate in the same manner as discussed above.
Thus the arrangement of Figure 6 offers the same load turndown capability as the embodiment of Figure 5 while insuring high sulfur capture and maximum fuel combustion.
It is also understood that other variations of the specific construction and arrangement of the system and method disclosed above can be made by those skilled in the art without departin~ from the invention as defined in the appended claims.
Claims (8)
1. A fluidized bed combustor comprising a housing, a plurality of substantially vertical partitions disposed in said housing and dividing said housing into a first chamber, a second chamber and a third chamber; means for establishing a bed of particulate material containing fuel in said first and second chambers; means associated with said partitions for permitting flow of said material from said first chamber to said second chamber and from said second chamber to said third chamber; means respectively associated with each chamber for passing air through each of said beds to fluid-ize the particulate material and promote the combustion of said fuel in said first and second chambers and to cool the material in said third chamber; means for adding fuel to the bed in said first chamber to maintain continuous combustion in said first chamber; means associated with said third chamber to permit the continuous discharge of cooled particulate mater-ial from said third chamber; a plurality of heat exchange tubes disposed in said first chamber; and means for passing a relativ-ely cool heat exchange fluid through said heat exchange tubes to remove heat from the bed in said first chamber, whereby the temperature of the bed in the first chamber can be controlled by the means for passing air through the first chamber, by the means for adding fuel to the bed in the first chamber, and by the means for passing a relatively cool heat exchange fluid through the heat exchange tubes.
2. The combustor of Claim 1 wherein no fuel is added to said second chamber other than that received from said first chamber so that the air passed through the bed in said second chamber promotes combustion of the fuel in said latter chamber to the extent that more complete fuel combustion is attained in said second chamber.
3. The combustor of claim 1 further comprising means associated with each of said chambers for individual-ly controlling the flow of air to and through each chamber.
4. The combustor of claim 3 wherein said control-ling means passes an amount of air to said second chamber sufficient to maintain a higher air-to-fuel ratio in said second chamber than in said first chamber.
5. The combustor of Claim 1, 2 or 3 in which the means for permitting flow of said material comprises at least one opening in each of said vertical partitions.
6. The combustor of claim 1, 2 or 3 further comprising means for igniting fuel in said second chamber and means for passing said ignited fuel from said second chamber to said first chamber during start-up of said combustor.
7. The combustor of claim 1 further comprising a single gas outlet associated with said housing and wherein the mixture of air and combustion gases from each of said chambers exit from said housing through said outlet.
8. The combustor of claim 7 further comprising means for injecting into said second chamber any parti-culate material entrained in said mixture of air and combustion gases.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12277580A | 1980-02-19 | 1980-02-19 | |
| US122,775 | 1980-02-19 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1149234A true CA1149234A (en) | 1983-07-05 |
Family
ID=22404699
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000368541A Expired CA1149234A (en) | 1980-02-19 | 1981-01-15 | Multi-zone fluidized bed combustor and method of operating same |
Country Status (11)
| Country | Link |
|---|---|
| JP (1) | JPS6022242B2 (en) |
| CA (1) | CA1149234A (en) |
| DE (1) | DE3106840A1 (en) |
| FR (1) | FR2476273B1 (en) |
| GB (1) | GB2069862B (en) |
| HU (1) | HU183338B (en) |
| IE (1) | IE50817B1 (en) |
| IN (1) | IN155322B (en) |
| IT (1) | IT1135526B (en) |
| NL (1) | NL8100818A (en) |
| ZA (1) | ZA811061B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR890002854B1 (en) * | 1982-10-15 | 1989-08-05 | 미쯔비시긴조구 가부시기가이샤 | A fluidized bed reaction apparatus with multiple chamber |
| AT401419B (en) * | 1987-07-21 | 1996-09-25 | Sgp Va Energie Umwelt | FLUIDIZED LAYER METHOD FOR THE GASIFICATION AND COMBUSTION OF FUELS AND DEVICE FOR IMPLEMENTING IT |
| JP7154888B2 (en) * | 2018-08-29 | 2022-10-18 | 川崎重工業株式会社 | Wet biomass incineration system |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1253239A (en) * | 1959-11-02 | 1961-02-10 | Cie Metaux Doverpelt Lommel | Method and apparatus for the semi-suspension combustion of heterogeneous grained material |
| US3717700A (en) * | 1970-08-25 | 1973-02-20 | Us Interior | Process and apparatus for burning sulfur-containing fuels |
| NL7106616A (en) * | 1971-05-13 | 1972-11-15 | ||
| US3736908A (en) * | 1971-10-08 | 1973-06-05 | Us Interior | System for starting a fluidized bed boiler |
| GB1426579A (en) * | 1973-09-21 | 1976-03-03 | Coal Industry Patents Ltd | Boilers |
| DE2861817D1 (en) * | 1977-09-23 | 1982-07-01 | Exxon Research Engineering Co | Method and apparatus for burning a solid, semi-solid and/or fluid fuel in a fluidized bed |
-
1981
- 1981-01-15 CA CA000368541A patent/CA1149234A/en not_active Expired
- 1981-01-27 IN IN48/DEL/81A patent/IN155322B/en unknown
- 1981-02-04 JP JP56015575A patent/JPS6022242B2/en not_active Expired
- 1981-02-12 GB GB8104457A patent/GB2069862B/en not_active Expired
- 1981-02-18 FR FR8103483A patent/FR2476273B1/en not_active Expired
- 1981-02-18 IT IT19837/81A patent/IT1135526B/en active
- 1981-02-18 ZA ZA00811061A patent/ZA811061B/en unknown
- 1981-02-19 HU HU81401A patent/HU183338B/en unknown
- 1981-02-19 IE IE337/81A patent/IE50817B1/en unknown
- 1981-02-19 NL NL8100818A patent/NL8100818A/en not_active Application Discontinuation
- 1981-02-19 DE DE19813106840 patent/DE3106840A1/en not_active Withdrawn
Also Published As
| Publication number | Publication date |
|---|---|
| IE50817B1 (en) | 1986-07-23 |
| FR2476273A1 (en) | 1981-08-21 |
| ZA811061B (en) | 1982-03-31 |
| DE3106840A1 (en) | 1981-12-24 |
| JPS56121903A (en) | 1981-09-25 |
| IT1135526B (en) | 1986-08-27 |
| IT8119837A0 (en) | 1981-02-18 |
| HU183338B (en) | 1984-04-28 |
| NL8100818A (en) | 1981-09-16 |
| GB2069862B (en) | 1984-02-29 |
| FR2476273B1 (en) | 1988-02-05 |
| JPS6022242B2 (en) | 1985-05-31 |
| IN155322B (en) | 1985-01-19 |
| IE810337L (en) | 1981-08-19 |
| GB2069862A (en) | 1981-09-03 |
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| Date | Code | Title | Description |
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| MKEX | Expiry |