U.S. patent number 3,636,896 [Application Number 05/036,647] was granted by the patent office on 1972-01-25 for solid fuel combustion apparatus.
This patent grant is currently assigned to Coal Industry (Patents) Limited. Invention is credited to Walter Harris, James McLaren.
United States Patent |
3,636,896 |
McLaren , et al. |
January 25, 1972 |
SOLID FUEL COMBUSTION APPARATUS
Abstract
Combustion apparatus for burning solid fuel in particulate or
divided form includes a plurality of air-permeable floor elements
e.g., trays or membranes arranged within a housing. Each element is
provided for supporting a fluidized bed of the solid fuel and in
one form is inclined to assist the passage of material along the
element. In another form of apparatus each element is horizontal
and the passage of material along the tray is effected by the
buildup of a hydraulic gradient between the feed end and the
discharge end of each element. Gas-operated means are located
adjacent the discharge end of one element and to feed end of an
adjacent element, and are provided for transferring solid material
from one element to an adjacent element. The elements may be in
side-by-side relationship or they may be arranged one above the
other, adjacent trays being either oppositely inclined relative to
one another or horizontal and mutually parallel.
Inventors: |
McLaren; James (Gotherington,
near Cheltenham, EN), Harris; Walter (Carlton,
EN) |
Assignee: |
Coal Industry (Patents) Limited
(London, EN)
|
Family
ID: |
10220811 |
Appl.
No.: |
05/036,647 |
Filed: |
May 12, 1970 |
Foreign Application Priority Data
|
|
|
|
|
May 16, 1969 [GB] |
|
|
25,013/69 |
|
Current U.S.
Class: |
110/234;
110/245 |
Current CPC
Class: |
F23C
10/002 (20130101) |
Current International
Class: |
F23C
10/00 (20060101); F23g 005/00 () |
Field of
Search: |
;110/28,28J,8
;122/4,4D |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Sprague; Kenneth W.
Claims
We claim:
1. Combustion apparatus comprising a housing, a gas-permeable floor
element located in the housing and adapted in use to support a
fluidized bed of solid material in particulate or divided form, a
gaseous fluidizing medium inlet means, a solid material inlet in
the housing, a gaseous fluidizing medium outlet in the housing, and
a heat exchanger located within the housing, a plurality of said
gas-permeable floor elements located within the housing, each
element including a feed end and a discharge end, and gas-operated
means in the form of a well adapted to raise said solid material
from a location adjacent the discharge end of one element to the
feed end of an adjacent element whereby material is deposited on
the adjacent element.
2. Apparatus according to claim 1 wherein the floor elements are
mutually parallel and are arranged at the same mean level within
the housing, such that the discharge end of one element is adjacent
the feed end of an adjacent element.
3. Apparatus according to claim 2 wherein the floor elements are
positioned in close adjacency, adjacent elements being oppositely
inclined relatively to one another, the lower end of each element
forming the discharge end and the upper end of each element forming
the feed end.
4. Apparatus according to claim 1 wherein the elements are arranged
in close adjacency, the elements being horizontally disposed within
the housing.
5. Apparatus according to claim 1 wherein the gas-operated means in
the form of a well comprises a first wall connecting with the
discharge end of an element, a second wall connecting with the feed
end of an adjacent element, and a base interconnecting the first
wall and the second wall, said base including an inclined portion
connecting with the first wall and a gas-permeable portion
connecting with the second wall.
6. Apparatus according to claim 5 wherein an inlet for solid
material is provided in the base of the gas-operated means.
7. Apparatus according to claim 5 comprising a baffle extending
into the gas operated means, the lower end of the baffle being
spaced from the base of said means.
8. Apparatus according to claim 5, comprising a further baffle
situated superjacent the discharge end of each floor element the
baffle extending downwards to a predetermined distance above said
end and extending upwards to a level which is a predetermined
distance below the required bed height, and a short gas-permeable
portion provided in each element adjacent the discharge end,
whereby material flow under the further baffle is controlled by
variation of gas flow rate through the portion so that a continuous
stream of material is caused to flow over the top of the
baffle.
9. Apparatus according to claim 1 wherein the floor elements are
arranged at different levels with respect to one another.
10. Apparatus according to claim 9 wherein each element is
oppositely inclined to the superjacent and the subjacent
element.
11. Apparatus according to claim 9 wherein each element is
horizontal and is parallel to the superjacent and the subjacent
elements.
12. Apparatus according to claim 9 comprising an upper and a lower
floor element, the lower element extending across the lower region
of the housing, a gas-permeable member attached at one of its ends
to an end wall of the housing end at the other end to the feed end
of the lower element, a first vertical wall located within the
housing, the discharge end of the lower floor element being
connected to the first vertical wall.
13. Apparatus according to claim 12 comprising a second vertical
wall extending between the side walls of the housing, and a third
vertical wall adjacent the inner end of the gas-permeable member,
the upper floor element being connected at its feed end to the
second vertical wall and at its discharge end to the third vertical
wall.
14. Apparatus according to claim 13 comprising a horizontal wall
extending from the first vertical wall, and a gas-permeable portion
in the horizontal wall, said horizontal wall together with the
upper portion of the first vertical wall and the lower portion of
the second vertical wall defining the gas-operated means in the
form of a well.
15. Apparatus according to claim 12 comprising a material discharge
outlet located above and adjacent the gas-permeable member, and a
gas inlet located below and adjacent said member, the discharge end
of the upper element being in a positional relationship with said
member whereby, in use, material leaving the upper element falls
onto the member and a part of the material is discharged through
said outlet by means of the gas introduced through said gas
inlet.
16. Apparatus according to claim 9 comprising two pairs of floor
elements arranged one pair above the other.
17. Apparatus according to claim 16 wherein adjacent elements are
oppositely inclined relative to one another.
18. Apparatus according to claim 16 wherein the elements are
horizontally disposed within the housing.
19. Apparatus according to claim 16 comprising means provided on
the uppermost element adapted for recycling material.
Description
This invention relates to apparatus for the combustion of solid
fuels in particulate or divided form when in a fluidized bed, and
in particular to the combustion of such fuel using a gaseous
fluidizing medium, for example air, for the formation of the
fluidized bed.
In the case where a large diameter bed is required, especially when
the bed is shallow, it has been found that a fluidized bed ceases
to be satisfactory as a means of contacting gas and solids under
controlled conditions. This is especially true where uniform
distribution of the solid feed through the system is important and
where the fuel feed undergoes highly exothermic or endothermic
reaction or where volatile primary reaction products react with the
fluidizing gases.
One disadvantage of a large diameter shallow fluidized bed is that
of insufficient lateral movement of the solid material. Such
movement can be applied to the system by means of mechanical
stirrers, although the use of such devices is limited.
It is an object of the invention to obviate the above mentioned
disadvantages. For this purpose, according to the invention
combustion apparatus includes a housing, a gas-permeable floor
element located in the housing and adapted in use to support a
fluidized bed of solid material in particulate or divided form, a
gaseous fluidizing medium inlet means, a solid material inlet in
the housing, a gaseous fluidizing medium outlet in the housing, and
a heat exchanger located within the housing, wherein the invention
comprises a plurality of said gas-permeable floor elements located
within the housing, each element including a feed end and a
discharge end, and gas-operated means in the form of a well adapted
to raise said solid material from a location adjacent the discharge
end of one element to the feed end of an adjacent element whereby
material is deposited on the adjacent element.
Conveniently the floor elements may be in the form of inclined
trays, and may be arranged at the same mean level and mutually
parallel in the housing such that the discharge end of one element
is adjacent the feed end of an adjacent element.
The trays may be positioned in close adjacency in the housing,
adjacent trays being oppositely inclined relative to one another.
Alternatively the trays may be horizontally disposed within the
housing.
As an alternative the trays may be arranged at different levels
with respect to one another within the housing, each tray being
either oppositely inclined relative to the tray directly beneath it
or horizontal.
The said gas-operated means may be in the form of a well, the solid
material being caused to flow into and out of said well.
Conveniently the solids material feed to the apparatus may be
introduced at the bottom of one or more of the said wells for the
purpose of mixing and increasing the contact time between the
solids material and the fluidizing gas; alternatively solids
material may be introduced through a side wall of the said housing
and deposited one or more of the trays.
Reference will now be made to the accompanying drawings in
which:
FIG. 1 is a schematic plan view of a first embodiment of combustion
apparatus according to the invention;
FIG. 2 is a schematic side view of a first embodiment of a detail
of combustion apparatus of FIG. 1;
FIG. 3 is a schematic side view of a second embodiment of a detail
of combustion apparatus of FIG. 1;
FIG. 4 is a schematic cross section of a second embodiment of
combustion apparatus according to the invention;
FIG. 5 is a schematic cross section of a third embodiment of
combustion apparatus according to the invention;
FIG. 6 is a schematic cross section of a fourth embodiment of
combustion apparatus according to the invention; and
FIG. 7 is a schematic cross section of a fifth embodiment of
combustion apparatus according to the invention.
In FIG. 1 a combustion apparatus for the fluidized bed treatment of
solid materials includes a housing 1 having a rectangular cross
section in which is located an air-permeable floor comprising a
plurality of side-by-side trays 2- 10 separated by an assembly of
baffles 11 to 18, which latter are so arranged that each tray 2- 10
is in material flow connection with only one other tray.
Each tray is inclined to the horizontal so as to induce a
directional movement in any material introduced on the tray. The
arrangement of the tray inclination is such that the lower or
discharge end of any tray is located in the vicinity of the higher
or feed end of the tray on to which it is to feed material.
The arrangement of the trays 2- 10 is such that the trays are all
situated at a common mean level. Furthermore, the layout of the
baffles, in conjunction with the inclinations of the trays defines
a continuous flow path for material introduced onto the reactor.
The arrows of FIG. 1 indicate the directions of material travel
along the various trays.
The material is transferred from the discharge end of any tray to
the feed end of the tray with which it is in flow communication by
air-operated means schematically represented in FIG. 1 by a hatched
rectangle 19, and described in detail in relation to FIG. 2 or
3.
In the embodiment shown in FIG. 2, the arrangement 19, includes a
well 20 having one vertical wall 21 connecting with the lower end
of one tray, a second vertical wall 22 connecting with the upper
end of the adjacent tray and a floor 23 connecting the two walls. A
baffle 24 extends into the well the lower end of the baffle being
spaced from the floor 23. The floor 23 includes an inclined portion
25 connecting with the wall 21 and an air-permeable portion 26
connecting with the wall 22.
In operation the material at the lower end of a tray falls into the
well 20, the inclined portion 25 guiding the material to the
air-permeable portion. An airflow inlet schematically represented
by the arrow 27 enters the well through the permeable floor portion
and lifts material falling into the well upwards to deposit same on
to the higher end of the adjacent tray.
Conveniently, the supply of material for combustion, is distributed
to each tray, and is conveniently fed pneumatically to the
air-operated means so that the air of the pneumatic feed
contributes to the airlift. The coal feed to the well 20 is
represented by the arrow 28.
The unburnt coal and ash resulting from combustion flows down the
associated tray by gravity to the lower end of the tray where it
discharges into the well associated with this particular lower end.
Fines material, which is elutriated from the bed is collected in a
conventional cyclone or cyclones (not shown) and returned to the
wells by means of dip legs (not shown) from the cyclones.
Ash removal from the system is effected from one or more wells,
prior to the coal feed and any fines return positions.
Heat exchange from the combustion of material to a working fluid is
conveniently effected by an assembly of heat exchange tubes (not
shown) which are located within the beds, said tubes running
parallel to the direction of ash movement lengthwise of the
trays.
When it is desired to maintain consistent material flow under
conditions of bed segregation on the trays 2 to 10 the well
arrangement of FIG. 3 may be used. In this arrangement a baffle 29
is provided in each well. Each baffle 29 extends downwards to a
predetermined distance above the floor of the adjacent tray lower
end, and extends upwards to a level which is a predetermined
distance below the required bed height. A short air-permeable floor
portion 30, which extends across the full width of the tray,
connects with the vertical wall 21. In use the flow of material
under the baffle 29 is controlled by variation of the airflow rate
through the floor portion 30 so that a continuous stream of
material is caused to flow over the top of the baffle 29. In the
FIGS. 2 and 3 the level of the beds in the trays is shown by the
dashed lines 31 and 32 in the upper and lower trays
respectively.
In the embodiment shown in FIG. 1 the trays are inclined but the
invention also includes combustion apparatus wherein such trays are
horizontally disposed in the housing.
The above described combustion apparatus is of particular
application to fluidized combustion in shallow beds. The reactor
may also be applied to a process in which low (shallow) beds are
desirable and where exothermic or endothermic reaction occurs
between the solid feed and the fluidizing gas.
The apparatus of FIG. 4, includes a housing 1 with a top 2, a base
3, end walls 4 and 5 and sidewalls 6 (only one shown). An air
permeable floor or membrance 7 extends across the lower region of
the housing 1. The upper end of the membrane 7, which is inclined
to the horizontal, connects with a gas-permeable element 8, which
is itself connected to the end wall 4. The lower end of the
membrane 7 is connected to a vertical wall 9 extending between the
sidewalls 6. The mounting of the membrane 7 is such as to form a
wind box 10. An opening 11 is provided in the end wall 4 for the
admission of air into the wind box 10.
A second air permeable floor or membrane 12 is located above and
spaced from the membrane 7. The membrane 12 is inclined to the
horizontal in the opposite sense to the inclination of the membrane
7. The upper end of the membrane 12 is connected to a vertical wall
13 and the lower end of the membrane 12 is connected to a vertical
wall 14 adjacent to the inner edge of the element 8. The bottom
edge of the wall 13 extends between the sidewalls 6.
A horizontal wall 15 extends from the wall 9 to the end wall 5,
this wall 15 being spaced from the lower edge of the wall 13. The
wall 15 defines with the lower portion of the wall 5, and upper
portion of the wall 9 a well 16, and with the lower portion of the
wall 5, the lower portion of the wall 9 and the base 3, a wind box
17. The wall 15 has a permeable portion 18 through which air from
the wind box 17 can enter the well 16. An air inlet 19 communicates
with the wind box 17.
A heat exchange or acceptor arrangement is provided within the
housing 1. The heat exchanger comprises an assembly of tubes, for a
heat exchange fluid such as water, the tubes are schematically
represented by dashed lines 20 which illustrate the locus of the
tubes.
The above described apparatus operates as follows:
Fuel to be combusted is introduced through an inlet 21 in one of
the sidewalls 6 of the housing and falls on to the higher end of
the membrane 7. A gaseous reaction media such as air is introduced
through the opening 11 into the wind box 10 at such a volumetric
throughput and pressure that fluidizing conditions are produced
above the membrane 7 and the coal is caused to react with the air.
Initially, the gaseous media is preheated in order to raise the
temperature of the fuel to that required for combustion. By reason
of the inclination of the membrane 7 any material on the membrane
will travel along the membrane towards the lower end. The
combustion of the fuel produces heat which is transferred to the
fluid in the heat exchange arrangement. At the lower end of the
membrane 7 the material (coal, coke, ash) falls into the well 16. A
flow of air is introduced through the wall portion 18 from the wind
box 17 to entrain this material and lift it upwards between the
walls 5 and 13 and drop the lifted material onto the higher end of
the upper membrane 12. The gases above the membrane 7 pass through
the membrane 12 to produce fluidizing conditions above the membrane
12. As the material travels along the membrane 12 combustion of the
fuel is completed and further heat is given to the upper bank of
tubes of the heat exchange arrangement. At the lowermost end of the
membrane 12 the material which is by now substantially wholly ash
falls onto the element 8. Some of this ash is caused to pass out
from the housing through an ash outlet 22, by a controllable flow
of air through porous membrane 8, to maintain a constant recycle
ash burden within the reactor. The flue gases arising from the
combustion leave the housing through a flue 23.
In FIG. 5 those elements which are similar to those shown in FIG. 4
are identified by similar reference numerals. The embodiment of
FIG. 5 essentially consists of three pairs of the oppositely
inclined membranes 7 and 12 arranged one above the other, together
with the associated wind box constructions for elevating the
material travelling lengthwise of a membrane to the membrane
immediately above. For convenience suffices A, B and C will be
applied to elements associated with the successive pairs of
membranes.
An arrangement of walls similar to that defined by the walls 9, 13,
15, 18 (in FIG. 4) is located at the lower end of each membrane so
that material falling from the lower end of a membrane may be
elevated, as previously explained, to the next higher membrane.
In the apparatus of FIG. 5, the ash which remains at the lower end
of the uppermost membrane 12C is recycled as schematically shown by
arrow 24. The air used for elevating material from a lower membrane
to a higher membrane is introduced through inlet means 25 at the
left-hand side of the drawing and through inlet means 26 at the
right-hand side of the drawing, each of the inlet means
communicating with associated inlets similar to the inlet 19 of
FIG. 4.
Coal, coke or other fuel is introduced at an inlet 21 adjacent the
higher end of the lowermost membrane 7A. With this arrangement the
hottest part of the apparatus is within the chamber between the
membranes 7A and 12A, so that as the gases travel upwards through
the successive membranes, the gases are cooled. The fluid flow
through the heat exchange arrangement is from the higher membrane
downwards to the lowermost membrane 7A, with the outlet from the
heat exchange arrangement 20 located adjacent to the lower end of
the membrane 7A.
The gases passing through the membrane of FIG. 5 are progressively
cooled by reason of the heat exchange with the heat exchange tubes
20, and are finally discharged from the apparatus at the flue
23.
In the apparatus of FIG. 5 the coal, coke or other fuel may be
introduced onto any selected one of the membranes or onto more than
one of the membranes.
In FIG. 6 those elements which are similar to those shown in FIG. 4
are identified by similar reference numerals. The embodiment of
FIG. 6 is substantially the same as that shown in FIG. 4, but
differs from the second embodiment of FIG. 4 in that the membrane
7' and the membrane 12' are horizontal. The passage of material
along the membranes is effected by build up of a hydraulic gradient
from the feed end to the discharge end. The term `hydraulic
gradient` as used herein means a difference between the head of
material at the feed end and the head of material at the discharge
end, the latter being less than the first-mentioned head such that
material passes from the feed end to the discharge end under the
action of the head of material at the feed end.
In FIG. 7 those elements which are similar to those shown in FIG. 5
are identified by similar reference numerals. The fifth embodiment
shown in FIG. 7 is substantially the same as the third embodiment
of FIG. 5 but differs from the third embodiment in that the
membranes 7A', 12A', 7B', 12B', 7C', 12C' are all horizontal. As in
the apparatus of FIG. 6 the passage of material along the membranes
is effected by the build up of a hydraulic gradient from the feed
end to the discharge end.
During the transit of the coal/coke/ash through the apparatus heat
is given up to the heat exchanger tubes, whereby any fluid within
the tubes is heated.
* * * * *