U.S. patent number 3,834,327 [Application Number 05/352,304] was granted by the patent office on 1974-09-10 for cyclone furnace having ash removal means.
This patent grant is currently assigned to Gotaverkens Angtekniska AB (Gotaverken Heat Engineering Co. Ltd.). Invention is credited to Ingmar Astrom, Bengt Hellstrom, Ulf Karsberg.
United States Patent |
3,834,327 |
Hellstrom , et al. |
September 10, 1974 |
CYCLONE FURNACE HAVING ASH REMOVAL MEANS
Abstract
In cyclone furnaces used for burning bark and similar wood
refuse, the real of ash and cinder involves a delicate problem
because the combustion residues are easily fused when subjected to
elevated temperature. The commonly used openings in a grate
covering an ash pit is not satisfactory to remove the rotating
products, and it is now proposed to arrange an opening in the side
wall of the cyclone, just above the grate, and to fit an ejector
means into said opening for continuously removing the combustion
residues.
Inventors: |
Hellstrom; Bengt (Goteborg,
SW), Karsberg; Ulf (Saffle, SW), Astrom;
Ingmar (Stenungsund, SW) |
Assignee: |
Gotaverkens Angtekniska AB
(Gotaverken Heat Engineering Co. Ltd.) (Goteborg,
SW)
|
Family
ID: |
20272359 |
Appl.
No.: |
05/352,304 |
Filed: |
April 18, 1973 |
Foreign Application Priority Data
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Jun 14, 1972 [SW] |
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007803/72 |
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Current U.S.
Class: |
110/216;
110/165A; 110/234; 110/244 |
Current CPC
Class: |
F23G
5/32 (20130101); F23G 7/105 (20130101); F22B
21/04 (20130101) |
Current International
Class: |
F23G
7/00 (20060101); F23G 7/10 (20060101); F23G
5/32 (20060101); F22B 21/04 (20060101); F22B
21/00 (20060101); F23g 007/00 () |
Field of
Search: |
;110/8R,18R,28F,28L,49R,165A |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Sprague; Kenneth W.
Attorney, Agent or Firm: Holman & Stern
Claims
What we claim is:
1. In a cyclone furnace having a vertical axis, a combustion
chamber provided with upper and lower portions, a grate in the
lower portion of the combustion chamber, means for feeding solid
fuel onto the grate to form, in use, a conical mound of burning
matter thereon, said grate having such an extension in relation to
the desired combustion capacity and to the angle of response of the
fuel utilized that an annular passage, free of fuel is formed
around the mound, a number of nozzles in the upper portion of the
combustion chamber for the introduction of secondary air
tangentially with respect to an imaginary cylinder concentric with
the longitudinal axis of the chamber, and an axial outlet for the
combustion gases, a gas passage to which said axial outlet leads,
the improvement including an exit passage in a side wall of the
cyclone furnace located level with an open towards the annular
passage and directed tangentially away therefrom, an ejector means
fitted into said exit passage, the ejector means having an outlet
end, a first passage connecting said ejector means with a source of
pressure fluid, and
a second conduit connecting the outlet end of the ejector means
with the gas path downstream of the air introduction nozzles.
2. The cyclone furnace according to claim 1, in which said source
of pressure fluid supply is the conduit conveying secondary air to
the air introduction nozzles.
3. The cyclone furnace according to claim 1, in which said gas
passage forms part of a heat producing plant having a smoke stack
and a dust collector connected to the smoke stack and in which the
second conduit opens into said dust collector.
4. The cyclone furnace according to claim 3, including a device for
cooling of the mixture of gases and solid matter therein through
which the second conduit passes before entering the dust collector.
Description
BACKGROUND OF THE INVENTION
For the combustion of wood refuse, such as bark, chips and the
like, a cyclone furnace is often used. Such a furnace comprises a
cylindrical, vertical combustion chamber, which, in its lower part
is provided with a grate and usually also a mechanical stoking
device feeding the fuel to the central portion thereof, in such a
manner that the fuel will form a substantially conical mound
thereon. Other ways of feeding the fuel include a chute for feeding
the fuel onto the grate in a downward direction. In its upper part,
the combustion chamber is provided with a number of tangentially
directed air nozzles, which impart a forceful whirling motion upon
the combustion gases.
The diameter of the grate is selected in such a manner with respect
to the desired combustion capacity and to the angle of repose of
the fuel to be used that an annular passage, free of fuel will be
formed around the mound of fuel. The grate is, within this annular
passage, usually provided with openings forming a connection with
ash collecting pockets located below the grate.
Due to the forceful rotation within the combustion chamber, a lot
of un-burnt particles will slide down the slopes of the mound of
fuel and will collect in the annular passage. Bark contains a
rather substantial amount of mineral components, and wood refuse is
often contaminated with sand which has been entrained when the logs
are dragged along the ground. Such incombustible matter will fuse
when subjected to elevated temperature, and it very often happens
that particles of fuel still un-burnt falling into the annular
passage will be intermingled with and fused together with the
mineral particles, which leads to a clogging of the ash removal
openings in the grate.
SUMMARY OF THE INVENTION
One object of the present invention is to provide a continuous
collection of such particles as are circulated along this annular
passage by the rotating gases and to remove them from the mound of
fuel. The invention is characterized in an exit passage open
towards the annular passage and directed tangentially with respect
to the wall of the combustion chamber, in an ejector connected to
said passage, and in a conduit connecting the ejector with a
conduit conveying air under pressure in such a manner that a
continuous ejection is obtained in the exit passage. An outlet
conduit from the ejector may be connected to the upper part of the
combustion chamber, or alternatively to a combustion plant located
downstream of the cyclone furnace.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a vertical section through a cyclone furnace suitable for
the combustion of bark and connected to a steam boiler,
FIG. 2 shows part of a section along line II -- II in FIG. 1, the
view looking in the direction of the arrows, and
FIG. 3 is a view partly in elevation and partly in cross section
showing a cyclone furnace fitted to a steam boiler.
DESCRIPTION OF THE PREFERRED EMBODIMENT
The cyclone furnace has a cylindrical combustion chamber 10 with a
vertical axis and is provided with a grate 11 in its lower portion.
The fuel, which on this occasion consists of bark and similar wood
refuse, is fed centrally onto this grate by means of a stoking
apparatus 12, the details of which are not shown on the drawing, in
such a manner that a substantially conical mound 13 will be formed
upon the grate. The diameter of the grate and of the furnace
chamber is selected in such a manner with respect to the desired
combustion capacity and the angle of repose of the fuel to be used
that, during use, an annular passage 14, free of fuel, will be
formed around the mound of burning fuel.
In the upper part of the combustion chamber a number of nozzles 16
for the injection of secondary air are provided. These nozzles are
directed tangentially with respect to an imaginary cylinder
concentric with the axis of rotation and are supplied with
preheated air from a duct 17 connected to a fan (not shown). The
combustion chamber is connected to a furnace 18 of a steam boiler,
which is indicated above the cyclone furnace.
The air issuing from the secondary air nozzles 16 induce a forceful
whirling motion within the chamber. A great many particles of
un-burnt matter are carried by this vortex and will be finally
combusted carried by the gases. A number of heavier particles will,
however, slide down along the wall of the combustion chamber,
ending up in the annular passage, where they, while still burning,
may be baked together with ash particles sliding down along the
slope of the mound of fuel and will form a sintered slag clogging
the air entrance opening in the outer portion of the grate, as well
as possible ash removal openings in the annular passage.
As long as the glowing particles are kept in motion they will do no
harm, but if a local braking of the movement occurs, the building
up of a solid coating starts. It therefore is important that the
particles are continuously removed.
An exit passage 19 is provided in the wall of the combustion
chamber, just above the grate and is directed towards the rotating
gas-swirl. All larger particles will be collected in this passage.
The passage is connected to an ejector 20, which, by way of a first
conduit 21, is connected to the duct 17 supplying secondary
combustion air. The particles collected will, in this manner, by
way of a second conduit 22, be transported from the ejector to the
furnace of the steam boiler, downstream of the cyclone furnace, in
which they will be finally burnt. The resulting ash has the
consistency of light cinder, and will facilitate the cleaning of
the heating surfaces of the steam boiler while passing through the
latter.
As indicated at 23, it is, of course possible, to connect the
conduit 22 to the upper part of the combustion chamber to the
cyclone furnace, above the level of the secondary air nozzles 16.
The final combustion of the collected particles will then start in
the cyclone furnace, but will be finalized in the second furnace,
with the particles following the gas stream passing through the
throat connecting the two furnaces.
An inspection and cleaning opening having a cover 15 is provided at
the ejector 20 in such a manner that the latter, as well as the
exit passage may be cleaned, which may be brought about by means of
a whisk which is periodically introduced into the passage.
FIG. 3 shows the cyclone furnace 10 fitted to a steam boiler, the
combustion chamber 18 of which is provided with oil burners 30 or
other fuel combustion means operable independently of the cyclone
furnace.
The combustion gases leaving the steam boiler will pass through a
dust separator 31 connected to the smoke stack. Conduit 22 from the
ejector 20 at the cyclone furnace is connected to the dust
separator at 32, and will pass through a feed water heater 33 or
some similar heat exchanger for cooling of the mixture of air and
ash particles.
* * * * *