[0001] The invention relates to a boiler as specified in the heading to claim 1.
[0002] Such a boiler for burning random material, in particular waste material, is known.
The first and second combustion chambers are formed respectively in two cylinders
adjacently positioned in a casing. The mixture of combustion gas with flammable products
released in the first combustion chamber as a result of imperfect combustion is burned
up completely in the second combustion chamber with the additional combustion air
supplied by the additional air supply means. Because the connecting duct runs out
tangentially into the second combustion chamber, an eddying of the combustion gases
is caused in the second combustion chamber, which is favourable for a good combustion.
As a result of the eddying movement any ash constituents which may be left behind
are forced radially outward, as a result of which they remain behind in the second
combustion chamber. The second combustion chamber thus acts in principle in the manner
of a cyclone. The boiler is embodied such that cool air can flow along the cylinders.
The air heats up as a result and the heated air can be used for any random heating
purpose.
[0003] A drawback of the known boiler is that its manufacture is relatively complicated
and its load taking capacity is comparatively limited, since air is used as the heat
transporting medium.
[0004] The invention has for its object to improve a boiler of the type described in the
preamble such that it acquires a greater application potential as a result of a simpler
construction.
[0005] In a boiler according to the invention this is achieved with the steps of the characterizing
part of claim 1.
[0006] As a result of the coaxial arrangement of the first and second combustion chamber,
separated by a dividing wall provided with a tangential passage opening, a very simple
construction is obtained. A good operation, i.e. complete combustion, is ensured by
the discharge chamber with the air feed pipe debouching opposite the central passage
opening.
[0007] It has been found that as a result of the tangential passage opening in the dividing
wall a very good spiral flow is generated in the second combustion chamber. The central
passage opening is likewise passed through in a spiral-like flow. The additional combustion
air, which flows in via the air supply pipe running out at an interval before the
central opening, flows, as a consequence of the underpressure generated by the exhaust
device, unimpeded through the central "core" of the spiral-like flow in the passage
opening into the second combustion chamber. Here this air mixes gradually with the
combustion gases. At a comparatively short distance from the first dividing wall the
unburnt products present in the combustion gases begin to burn. Volume increase occurs
as a result, thus reinforcing the spiral flow. The supplied additional air is colder
and therefore heavier than the combustion gases and is forced as a result of the
generated centrifugal forces outward against the wall of the second combustion chamber.
The thermal loading of the wall of the second combustion chamber consequently remains
limited and the heat transfer can take place gradually over the whole surface area
of the second combustion chamber.
[0008] In the first combustion chamber the flammable material is in preference directly
burnt on the bottom of the combustion chamber. Primary combustion air is supplied
through an air supply pipe arranged just above the bottom and provided with small
outflow openings. As a result of the supply of primary air the ash of the combustion
material attains a fluidised state, which is a very suitable state for a good combustion
and gasification. Flowing above the furnace hearth is extra air which has a cooling
effect. As a result the temperature of the furnace hearth can if required be held
at a low value. This occurs in particular when the material for combustion contains
heavy metals and it is desirable that these remain behind in the ash. Because of the
relatively low temperature these heavy metals will not vapourize. The temperature
will however be such that hydrocarbons are broken down and it will therefore be possible
for them to be completely burned in the second combustion chamber. Particles of flammable
material carried along in the combustion gases burn up entirely in the second combustion
chamber. It has been found that only minimal quantities of inflammable material reach
the second combustion chamber. As a result of the centrifugal force field these solid
particles are deposited on the wall of the second combustion chamber.
[0009] The boiler according to the invention thus combines a simple construction with the
possibility of a very complete combustion and minimal contamination of the exhaust
gases. It has been found in the case of one embodiment that the content of carbon
monoxide, nitrous oxides, unburnt hydrocarbons and dust in the combustion gases is
minimal and lies well below the legally established requirements for these materials.
[0010] Designated in claims 2-7 are steps which have been found to result in a very good
operation of the boiler according to the invention.
[0011] A favourable further development of the boiler according to the invention is characterized
in claim 8. A maximum temperature indicates that the correct amount of additional
air is being supplied. An excessive or deficient amount both result in a temperature
lower than the maximum. The boiler embodied in this way thus achieves a maximum output.
[0012] Using the step from claim 9 a good flow of the additional air through the central
passage opening deep into the second combustion chamber is achieved.
[0013] The boiler according to the invention is very suitable for embodiment as hot water
or steam boiler. The coaxial ly arranged first and second combustion chambers thereby
form in a favourable manner the fire tube of such a boiler. Because of the previously
noted small heat loading of the walls of both the first and second combustion chamber,
ordinary structural steel can be used.
[0014] Achieved with the step from claim 11 is a favourable embodiment which can also be
used for later conversion of already existing hot water or steam boilers.
[0015] The invention will be further elucidated in the following description of a preferred
embodiment with reference to the annexed figures.
Fig. 1 is a partly broken away lengthwise section of a boiler according to the invention
as a steam boiler.
Fig. 2 is a partly broken away perspective view of the boiler from fig. 1.
[0016] The steam boiler 1 according to the invention comprises in the usual manner a water
jacket 2 and a fire tube 3. In accordance with the invention a first combustion chamber
4 and a second combustion chamber 5 are formed in coaxial connection in the fire tube
3 These two combustion chambers 4, 5 are separated from one another by a dividing
wall 6 which comprises a tangential passage opening 7 in the upper portion.
[0017] Connecting onto the second combustion chamber 5 via a second dividing wall 8 is a
discharge chamber 10. The second dividing wall 8 is provided with a central passage
opening 9 bounded by a cylindrical tube wall portion 19. Debouching into the discharge
chamber 10 opposite the central passage opening 9 is an air supply pipe 11. This latter
has a smaller diameter than the passage opening 9 and the diameter of the air supply
pipe 11 preferably amounts to half that of the passage opening 9. The quantity of
additional air supplied via the air supply pipe 11 is controlled with a control valve
28 arranged in this pipe 11.
[0018] The discharge chamber 10 is embodied as a return flow chamber and leads to smoke
tubes 12 debouching on the periphery thereof. These smoke tubes 12 guide hot combustion
gases out of the return flow chamber 10 to the forward side of boiler 1 where these
smoke tubes 12 run out into a discharge duct 13. This discharge duct 13 connects
via an exhaust fan 14 driven by a motor 16 onto a flue tube 15. The boiler 1 is further
provided in per se known manner with fittings for connection of mains water and steam
lines.
[0019] Fuel 21 can be introduced into the first combustion chamber 4 via a free intake opening
20 in the front wall of the boiler 1. A great variety of materials can serve as fuel.
Waste substances in particular can be burned in suitable manner using the boiler according
to the invention.
[0020] As a result of the combustion an ash layer 22 is created at the bottom of the combustion
chamber 4. Close to the bottom wall of the fire tube 3 an air pipe 23 provided with
a large number of outflow openings protrudes into the first combustion chamber 4.
A fan 24 connected to this pipe 23 supplies primary combustion air via the outflow
openings in the pipe 23. The ash layer 22 is brought into fluidised state by the outflowing
air, as a result of which all the flammable parts are provided with sufficient oxygen
to be broken down completely.
[0021] Completely burnt up ash 22 flows at the forward side of the fire tube 3 below a baffle
wall 29 and over an overflow wall 30 onto an ash discharge belt 31. In this way a
constant level of the ash layer is maintained in the first combustion chamber 4. The
fuel 21 can be introduced into combustion chamber 4 either by means of a conveyor
or manually. When a conveyor is used it can in a favourable manner also perform the
function of keeping the layer of flammable material in loose state. Blades arranged
for instance on the conveyor can "plough up" this layer at regular intervals. The
disadvantageous effects of the tendency of some fuels to form a crust are eliminated
as a result.
[0022] The fans 24 and 14 are adjusted such that the primary combustion air supplied via
the distributor pipe 23 and the additional air drawn in via the intake opening 20
are insufficient to bring about perfect combustion of the fuel. The temperature in
the first combustion chamber remains relatively low as a result. Any heavy metals
that may be present in the fuel 21 consequently do not vapourize but remain behind
in the ash 22. The additional air flowing in via the intake opening 20 moreover has
a cooling function, causing the temperature to remain relatively low.
[0023] The combustion gases with partially gasified fuel flows via the tangential opening
7 into the second combustion chamber 5. As a result of this tangential supply a spiral-like
flow is created in the second combustion chamber 5 along the cylindrical wall of this
chamber 5. This flow is indicated with the arrow 25. Consequently a spiral-like flow
into the central passage opening 9 in the dividing wall 8 likewise occurs, with the
result that additional combustion air flowing in via the air supply pipe 11 can pass
through.
[0024] The inflow of additional combustion air through the air supply pipe 11 penetrates
through the core of the spiral-like flow in the passage opening 9 deep into the second
combustion chamber 5. This is indicated schematically in the figures with the lines
27. The spiral flow in the passage opening 9 is indicated with arrows 26. As a result
of the tube wall 19 arranged at the location of the passage opening 9 a uniform flow
is ensured.
[0025] Shortly after the mixture of combustion gas and gasified fuel has found its way into
the second combustion chamber 5, combustion of the gaseous fuel particles occurs through
mixture with the additional air, which results in a great temperature increase and
consequently volume increase. The spiral eddying is reinforced as a result. Because
of the spiral eddying a centrifugal force field is moreover created, with the result
that the supplied cool additional air, which is heavier than the hot combustion gases,
displaces to the outside of the combustion chamber 5. Overheating of the wall of combustion
chamber 5 is thus prevented and a uniform heat transfer ensured.
[0026] In accordance with a preferred embodiment a temperature sensor 33 is arranged at
the location where in practical tests the highest temperature has been found to occur.
This sensor 33 is coupled to a control device 32 which actuates a control valve 28
in the additional air supply pipe 11. The control device actuates the control valve
28 such that a maximum temperature occurs at the location of sensor 33. Sensor 33
protrudes slightly from the wall of combustion chamber 5 so that the actual temperature
in the combustion is determined and not that of the cooler air around it.
[0027] As fig. 2 shows, the first dividing wall 6 can be formed in a favourable manner from
a disc of sheet steel which is provided at the top with an incision extending from
the edge to the central point. The portions of the disc on either side of the incision
are deflected away from one another so that in between them the tangential opening
7 is formed and the adjoining portions define the walls of a partly helical channel.
Good tangential admittance of the gas flow into the second combustion chamber 5 is
achieved as a result. The two portions of the disc close to the incision are preferably
deflected away from one another over a distance equal to a third of the diameter of
the fire tube 3. The tangential opening 7 thus obtains a suitable section.
[0028] It is further noted that the variation in air supply into the second combustion chamber
5 caused by the control valve 28 has hardly any or no effect on the air flow through
the first combustion chamber 4.
[0029] It has further been found that for good flow conditions a favourable ratio of the
diameter of the central passage opening 9 to the diameter of the fire tube 3 can
be selected of 1:2. The rear wall 34 of the discharge chamber 10 is formed in favourable
manner as a removable cover in order to be able to clean discharge chamber 10 and
the second combustion chamber 5 of ash remnants.
[0030] The invention is not limited to the embodiment of a two-draught steam boiler shown
in the figures. Single draught or for instance three-draught boilers can likewise
be embodied in suitable manner as according to the invention. In addition, two fire
tubes can be employed which are formed substantially identical to one another. Finally,
it is noted that the stated dimensionings indicate preferences which have been found
to result in a good operation of the boiler. The invention is not however limited
to these dimensionings.
1. Boiler for extraction by combustion from random flammable material of thermal energy
with a flow duct comprising an exhaust device connected to an outlet side of said
duct, a first cylindrical combustion chamber close to the intake side, a second cylindrical
combustion chamber connected to said first combustion chamber via a connecting duct
portion whereby said connecting duct portion runs out tangentially into said second
combustion chamber, and additional air supply means for supplying additional combustion
air into said second combustion chamber, characterized in that said first and second combustion chambers are arranged coaxially connected and are
separated from one another by a first dividing wall comprising in the upper portion
a tangential passage opening, that a discharge chamber with a discharge on the periphery
connects onto said second combustion chamber via a second dividing wall with a central
passage opening, and that said additional air supply means comprise an air supply
pipe debouching into said discharge chamber at a distance opposite said central passage
opening and having a smaller diameter than said passage opening.
2. Boiler as claimed in claim 1, characterized in that the central passage opening is bounded by a cylindrical wall.
3. Boiler as claimed in claim 1 or 2, characterized in that the diameter of the air supply pipe amounts to substantially half the diameter of
the second combustion chamber.
4. Boiler as claimed in any of the foregoing claims, characterized in that the diameter of the air supply pipe amounts to substantially half the diameter of
the central passage opening.
5. Boiler as claimed in any of the foregoing claims, characterized in that the air supply pipe debouches at an interval in the order of magnitude of 20 cm from
the central passage opening.
6. Boiler as claimed in any of the foregoing claims, characterized in that the first dividing wall is formed by a disc provided in its upper part with a radial
incision, whereby the portions of said disc adjoining said incision are deflected
on either side out of the plane thereof.
7. Boiler as claimed in any of the foregoing claims, characterized in that the portions close to the outer diameter are deflected away from one another over
a distance equal to substantially a third of the diameter of the first combustion
chamber.
8. Boiler as claimed in any of the foregoing claims, characterized in that a temperature sensor is arranged in the second combustion chamber, that a control
valve is accommodated in the air supply pipe and that a control device is arranged
connected at an intake to said temperature sensor and at an outlet to said control
valve and which actuates said control valve in the sense of maximalising the temperature.
9. Boiler as claimed in any of the foregoing claims, characterized in that the control valve is a diaphragm valve.
10. Boiler as claimed in any of the foregoing claims, characterized in that the combustion chambers are formed in the fire tube of a hot water or steam boiler
and that the discharge chamber is formed against the rear wall thereof.
11. Boiler as claimed in claim 10, characterized in that said boiler contains smoke tubes and the discharge chamber forms a return flow chamber
connecting the fire tube to the smoke tubes.