US3910235A

US3910235A - Fluidised bed combustion

Info

Publication number: US3910235A
Application number: US445282A
Authority: US
Inventors: John Highley
Original assignee: Coal Industry Patents Ltd
Current assignee: Coal Industry Patents Ltd
Priority date: 1973-03-02
Filing date: 1974-02-22
Publication date: 1975-10-07
Anticipated expiration: 1992-10-07
Also published as: GB1412033A; CA983798A; AU6599374A; DE2408649A1; DE2408649C2

Abstract

A method for burning a fuel involves the use of a fluidised combustion bed in which the fuel is burnt and a fluidised heat transfer bed in which heat generated by the combustion bed is transferred to a heat exchange fluid. Hot material from the combustion bed is circulated to the heat transfer bed and returned to the combustion bed and to this end the heat transfer bed is located adjacent the combustion bed. The rate of the circulation determines the heat output and this rate can be varied by varying the fluidising velocities in the two beds. Both beds are conveniently contained within one body and may be divided from each other by a division which allows of the circulation referred to above.

Description

United States Patent [191 Highley Oct. 7, 1975 [54] FLUIDISED BED COMBUSTION 3,717,700 2/1973 Robinson et a1 110/8 X Inventor: J g y, C en a g a d 3,763,830 10/1973 Robinson et al 110/28 [73] Assignee: Coal Industry (Patents) Limited, Primary Examiner-Kenneth W. Sprague London, England Attorney, Agent, or Firm-Stevens, Davis, Miller & 22 Filed: Feb. 22, 1974 Moshe [2 1] Appl. No.: 445,282 [57] ABSTRACT A method for burning a fuel involves the use of a flui- [30] Foreign Application priority Data dis ed combustion bed in which the fuel is burnt and a Mar 2 1973 United Kin dom 10263, fluidised heat transfer bed in which heat generated by g the combustion bed is transferred to a heat exchange fluid. Hot material from the combustion bed is circu- IIIIIIIIIIIIIIIIIIIIIII 122/4 lated to the heat transfer bed and returned to the com- [58] Fie'ld 122/4 D bustion bed and to this end the heat transfer bed is 10- cated adjacent the combustion bed. The rate of the [56] References Cited circulation determines the heat output and this rate can be varied by varying the fluidismg velocities in the UNITED STATES PATENTS two beds. Both beds are conveniently contained within 2,729,428 1/1956 Milmore 122/4 n body and may be divided from each other by a di- 3,119,379 H1964 Sweeney 110/28 vision which allows of the circulation referred to 3,306,236 2/1967 Campbell 110/8 above 3,387,590 6/1968 Bishop 122 4 3,589,313 6/1971 Smith et a] 1 10/8 18 Claims, 3 Drawing Figures sheet 1 om 3,910,235

U.S. Patent Oct. 7,1975

U.S. Patent Oct. 7,1975 Sheet 2 of3 3,910,235

NOE

US. Patent 0a. 7,1975 Sheet 3 of3 3,910,235

F LUIDISED BED COMBUSTION This invention has reference to a method and apparatus for the fluidised bed combustion of combustible matter.

The combustion of such matter in a fluidised bed of particulate matter is well known and its application to power generating systems has been the subject of investigation for many years. The heat transfer co-efficients attainable by employing the fluidised combustion technique represent a distinct improvement over conventional heat transfer modes such for example as a water tube boiler, However, one of the major difficulties attendant upon the utilisation of the technique in steam raising systems is that of variation of heat output of the bed to meet varying load demands. The variation of heat output is a particular problem as the bed temperature must be maintained at a level at which combustion is efficient. Additionally, with solid fuel there is always the danger of agglomeration and clinkering should the temperature of the bed be allowed to exceed a certain value. Thus it is necessary to have a method of varying the heat removal rate from the bed which allows the temperature of the bed to be maintained between certain temperature limits.

There have been a number of proposals for effecting such heat output variation but each has involved either expensive equipment to vary the amount of bed material and hence the amount of heat transfer surface in the bed or the danger of clinkering resulting from a section of the bed being allowed to slump i.e. the bed becomes defluidized whilst combustion is taking place.

According to a first aspect of the invention there is provided a method for the fluidised combustion of combustible matter including arranging a first fluidised bed of particulate material for heat transfer to a heat transfer medium adjacent a second fluidised bed of particulate material for the combustion of combustible matter, introducing said matter into the second bed and burning the matter therein, and circulating heat conductive material between the first and second beds.

Conveniently the first bed is arranged circumjacent the second bed.

Alternatively the first and second beds may be arranged side by side in mutual adjacency.

It is preferred that substantially all the combustion takes place within the second bed although it is to be appreciated that, in use, some unburnt combustible matter may be carried over into the first bed and burnt therein depending on the conditions prevailing therein.

The circulation of heat conductive material may conveniently be effected by the natural circulating movement of bed material from the centre of the bed to the boundaries thereof. However the rate of circulation of heat conductive material may be increased substantially over that by natural circulation by operating the According to a second aspect of the invention there is provided apparatus for the fluidised bed combustion of combustible matter including a combustor body adapted to contain particulate material, a gaspermeable support plate in the lower portion of the combustor body for supporting the material, a first, heat transfer region located adjacent a second, combustion region in said lower portion, a first fluidising medium inlet for the first region, and a second fluidising medium inlet for the second region.

Conveniently dividing means are provided in the lower portion to define the first and second regions, the dividing means being adapted to permit the circulation, in use, of material between the first and second regions. The dividing means may be so placed as to allow flow of material over and under it to give the said circulation between the regions. Alternatively the dividing means may be suitably apertured to allow such flow there through.

In an alternative form of the invention the dividing means may be omitted.

A fluidising medium plenum chamber is located subjacent the gas-permeable support plate and is divided into first and second zones corresponding to the first and second regions respectively in the lower portion of the combustor body, the first fluidising medium inlet being connected to the first zone and the second fluidising medium inlet being connected to the second zone.

Inlet means for combustible matter, e.g. fuel, is provided for the second, combustion region. Heat exchange means are provided in association with the first region. Such means may be incorporated in the wall of the combustor body, which defines a boundary of the first region. Alternatively or in addition the heat exchange means may be located within the region such that, in use, their heat exchange surfaces are immersed within the particulate material within the first region.

first and second beds at different fluidising velocities r An exhaust outlet is provided in the combustorbody and material separators may conveniently be arranged within the body intermediate the lower portion and the exhaust outlet.

According to a third aspect the invention provides a boiler system including an apparatus according to the second aspect of the invention.

Preferably two or more of such apparatus are included in the boiler system, the second, combustion region of each apparatus being connected to the second, combustion region of an adjacent apparatus.

Conveniently the exhaust outlet of each apparatus is connected to a heat exchange such that, in use, the hot gaseous products of combustion can be employed for heat exchange with an appropriate fluid.

By way of example only, a method and apparatus for the fluidised combustion of combustible matter according to the invention are described below with reference to the accompanying drawings in which:

FIG. 1 is a side elevation of a single apparatus;

FIG. 2 is a plan view of a boiler system incorporating the apparatus of FIG. 1; and

FIG. 3 is a side elevation of the system shown in FIG. 2.

Referring to FIG. 1, apparatus for the fluidised combustion of combustible matter includes a combustor body 1 of circular cross-section having towards its lower end a perforate support grid 2 adapted to support particulate material. The body 1 is provided with a plenum chamber 4, located below the grid 2, and this serves to distribute air or other fluidising medium through the grid 2. The chamber 4 has two inlets 6, 8

each adapted for introducing a fluidising medium into the plenum chamber 4 which is divided into a first, outer zone or section 10, and a second, inner zone or section 12. The inlets 6, 8 serve the

sections

10, 12 respectively.

The lower portion 14 of the body 1 is adapted to contain and support particulate material 16 and is divided into two regions by a cylinder 18, the first outer region 20 being of annular form and the second inner region 22 being of cylindrical form. The cylinder 18 is so disposed within portion 14 that material transfer between the first and

second regions

20, 22 can, in use, be effected. The lower end of the cylinder 18 is spaced from the support grid 2 to allow of material flow from one region to its adjacent region. Similarly material flow can take place, in use, over the upper end of the cylinder 18.

The second inner region 22, in use, contains a second bed of material in which combustion of fuel is to take place and accordingly a fuel inlet 24 is provided for this region 22.

The first outer region 20, in use, contains a first bed of material from which heat is to be transferred to a fluid medium and to this end the combustor body 1 is provided with a heat exchange jacket 26 having a suit able inlet 28 and outlet 30.

The combustor body 1 has an exhaust gas outlet 31 and separators 32 are located within the body 1 as shown for the purpose in use of arresting particulate material which may be carried up from the bed by the exhaust gases of combustion or fluidising medium. A weir 34 is provided for regulating the level of material 36 within the combustor.

The operation of the apparatus is as follows:

Finely divided particulate material, eg inert material such as ash residue from the combustion of coal, is placed within the body 1 to the requisite level in the lower portion 14 thereof and supported by grid 2. A fluidising medium, e.g. air, is introduced through the inlet 8 to fluidise the material 16 in region 22. The fluidising medium may be preheated to heat the material 16 for initial start-up to raise its temperature to that at which the combustion of fuel, in this case coal, will be self-sustaining. Coal is introduced via inlet 24 only into the region 22 for combustion in a fluidised state therewithin. When the bed material is at a sufficiently high temperature a fluidising medium is introduced into the outer region 20. The fluidising velocity of the fluidising medium entering the region 22 is arranged to be higher than that entering the region 20 thus resulting in material circulation between region 22 to region 20. The hot material passes over the top of the cylinder 18 and passes from the second bed in region 22 to the first bed in region 20, material also passing below cylinder 18 from region 20 to region 22 thus providing an overall circulation of material within the combustor body; heat transfer is thus effected between the material and the heat transfer medium e.g. water in the jacket 26. In order to reduce the heat output of the apparatus the rate of circulation of bed material between the

regions

20, 22 is reduced as the fuel feed is reduced. Because of the reduction in the material circulation rate the temperature of the second bed can be maintained constant despite the lowering of the fuel feed. The reduction in the material circulation rate between the first and second beds is effected by varying the fluidising velocities in the two

regions

20, 22. Thus as the fuel feed is reduced, the flow of air to region 22 can be reduced to maintain the desired level of excess air for combustion requirements. At the same time the flow of air to region 20 may also be varied if necessary to reduce the difference between the two fluidising velocities and so reduce the material circulation rate. Since the amount of transfer of heat from the second bed in region 22 to the first bed in region 20 and thence to the heat transfer fluid in jacket 26 can be controlled as described above, the temperature in the combustion bed can be controlled within required temperature limits. Thus the problems associated with low load operation of fluidised bed heat exchangers hitherto proposed are obviated.

In order to increase the heat output of the apparatus the fuel feed rate is increased together with the flow rate of air to region 22 and the material circulation is thus increased to maintain the temperature in the second, combustion region within the required limits. This could conveniently be controlled by the automatic variation of the air flow rates to

regions

20, 22.

Referring now to FIGS. 2 and 3, a boiler system is illustrated and comprises three units of apparatus as described with reference to FIG. 1 designated 101, 102 and 103. The constructional features of the units are the same as those of FIG. 1 and no further description thereof is included with reference to FIGS. 2 and 3. The second region 22 of unit 101 is-connected to the second region of unit 102 by a conduit and that of unit 102 is connected to the second region of 103 by a conduit 107. The exhaust gas outlet of each unit is connected to

heat exchangers

104, 106 arranged in series as shown in FIGS. 2 and 3, the outlets of each exchanger 106 being connected to a common exhaust manifold 108.

The unit 101 is the main unit of the three and is provided with controls (not shown) including an on-off control for a fluidising air fan (not shown), a damper to vary the flow rate to region 20, and a control for the fuel feed rate. Each of units 102, 103 is provided with similar controls to those for unit 101 but their fuel feeders may be interconnected.

The operation of the boiler system is as follows:

The material within the region 22 of unit 101 is fluidised and heated to a temperature sufficient for selfsustaining combustion of the-fuel feed. Fuel is introduced into the bed for combustion therein and is controlled according to the heat output required of the region 20, material transfer between the

regions

20, 22 additionally being varied according to the demand.

When the maximum heat output of unit 101 is attained, unit 102 is brought into operation. This is effected by fluidising material in region 22 thereof and by introducing hot material from the region 22 of unit 101 through conduit 105 into the region 22 of unit 102. This introduction of hot material heats the bed in unit 102 to a suitable temperature and thereafter fuel feed is commenced. Thus additional heat output of the system is achieved by bringing unit 102 into operation and the individual heat output of this unit and thus the combustion temperature of the second bed thereof can be controlled by material transfer between the first and second regions of that unit 102. If additional heat output is required, unit 103 can be brought into operation in similar manner as unit 102 with initial heating of the second bed region 22 thereof being effected by hot material being transferred along conduit 107.

As the heat demand is reduced the units 103, 102 can be gradually shut-down one by one by stopping fuel feed and, after combustion is complete by stopping material transfer between the first and second beds.

It is to be appreciated that any number of units similar to units 102, 103 may be utilised for the same purposes i.e. increasing heat output of the system, each unit having

similar heat exchangers

104 and 106.

It is to be understood that whilst a circular section combustor has been described, a combustor body of rectangular or any other section falls within the scope of the invention. In the case of a rectangular section combustor body the first region need not completely surround the second region but only partially, for example adjacent two opposite side walls of the combustor body. However, the first region may completely surround the second region in a combustor body of rectangular section.

The principle of operation described in relation to FIGS. 2 and 3 could be applied to a boiler system in which the

apparatus

101, 102 and 103 comprise adjacent rectangular bodies housed in a single casing with intervening baffles separating the beds of each apparatus.

ln alternative embodiments the first heat transfer region may be sub-divided into two or more sections each having a separate plenum chamber for the fluidising medium. This would facilitate control of the combustion temperature particularly during operation for long periods at low heat output.

Additionally in further alternative embodiments the cylinder 18 of the apparatus of FIG. 1 or corresponding dividing means may be omitted.

I claim:

l. A method for the fluidised combustion of combustible matter including the steps of arranging a first, heat transfer bed of particular material adjacent a second, combustion bed of particular material, introducing a fluidising medium into the first and second beds, introducing combustible matter into the second bed, burn ing the matter in the second bed, circulating heat conductive material between the first and second beds, passing a heat transfer medium in association with the first bed, and varying the rate of heat transfer in the first bed to the heat transfer medium by varying the rate of circulation of the heat conductive material between the first and second beds.

2. Fluidised combustion apparatus including a combustor body, a lower portion in the combustor body, a particulate material gas-permeable support plate in the lower portion, a first, heat transfer region in the lower portion above the plate, heat exchange means associated with the first, heat transfer region, a second, combustion region in the lower portion located adjacent the first region, a first fluidising medium inlet means located below the plate and adapted to introduce a fluidising medium to the first region, and a second fluidising medium inlet means located below the plate and adapted to introduce a fluidising medium to the second region.

3. A method according to claim 1 in which the rate of circulation of heat conductive material between the first and second beds is varied by varying velocities of the fluidising medium to each of the first and second beds.

4. A method according to claim 3 in which the velocity of the fluidising medium in the second bed is equal to the velocity of the fluidising medium in the first bed.

5. A method according to claim 3 in which the velocity of the fluidising medium in the second bed is greater than the velocity of the fluidising medium in the first bed.

6. A method according to claim 1 in which substantially all the combustion of the combustible matter takes place within the second bed.

7. A method according to claim 1 in which the first bed is arranged circumjacent the second bed.

8. A method according to claim 1 in which the first and second beds are arranged side-by-side in mutual adjacency.

9. Apparatus according to claim 2 in which dividing means are provided in the lower portion of the combustor body to define the first and second regions.

10. Apparatus according to claim 9 in which the dividing means are adapted to permit circulation of material between the first and second region,

1 1. Apparatus according to claim 10 in which the dividing means are spaced from the gas-permeable support plate.

12. Apparatus according to claim 2 in which a fluidising medium plenum chamber is located subjacent the gaspermeable support plate, a first zone is defined within the chamber and is connected to the first fluidising medium inlet, and a second zone is defined adjacent the first zone and is connected to the second fluidising medium inlet.

13. Apparatus according to claim 2 in which inlet means for combustible material are provided for the second, combustion region.

14. Apparatus according to claim 2 in which the heat exchange means is incorporated in the combustor body wall.

15. Apparatus according to claim 2 in which an exhaust outlet means is provided in the combustor body, and material separators are arranged within the body intermediate the lower portion and the exhaust outlet means.

16. A boiler system including an apparatus according to claim 2.

17. A boiler system according to claim 16 in which the system includes more than one apparatus, and the second region of the combustor body of one apparatus is connected to the second region of an adjacent apparatus.

18. A boiler system according to claim 17 in which the combustor body of each apparatus has an exhaust outlet means and a heat exchanger is connected to the

Claims

1. A method for the fluidised combustion of combustible matter including the steps of arranging a first, heat transfer bed of particular material adjacent a second, combustion bed of particular material, introducing a fluidising medium into the first and second beds, introducing combustible matter into the second bed, burning the matter in the second bed, circulating heat conductive material between the first and second beds, passing a heat transfer medium in association with the first bed, and varying the rate of heat transfer in the first bed to the heat transfer medium by varying the rate of circulation of the heat conductive material between the first and second beds.

2. Fluidised combustion apparatus including a combustor body, a lower portion in the combustor body, a particulate material gaspermeable support plate in the lower portion, a first, heat transfer region in the lower portion above the plate, heat exchange means associated with the first, heat transfer region, a second, combustion region in the lower portion located adjacent the first region, a first fluidising medium inlet means located below the plate and adapted to introduce a fluidising medium to the first region, and a second fluidising medium inlet means located below the plate and adapted to introduce a fluidising medium to the second region.

11. Apparatus according to claim 10 in which the dividing means are spaced from the gas-permeable support plate.

12. Apparatus according to claim 2 in which a fluidising medium plenum chamber is located subjacent the gas-permeable support plate, a first zone is defined within the chamber and is connected to the first fluidising medium inlet, and a second zone is defined adjacent the first zone and is connected to the second fluidising medium inlet.

16. A boiler system including an apparatus according to claim 2.

18. A boiler system according to claim 17 in which the combustor body of each apparatus has an exhaust outlet means and a heat exchanger is connected to the exhaust outlet means.