[0001] The invention relates to a burner, in particular a gas-fired fan burner for a central
heating installation.
[0002] Such a burner, comprising a substantially cylindrical burner housing, of which one
end, being the outlet end, is connectable to an opening in a furnace wall of a central
heating boiler, while to the other end thereof, being the inlet end of the burner
housing, a burner fan for forced supply of combustion air and a fuel supply line are
connectable, a mixing tube extending concentrically within the burner housing and
connecting to a burner head at the outlet end of the burner housing, which burner
head, in mounted condition of the burner, extends into the furnace by a flame cup
surrounding the burner head, while an annular space between the burner housing wall
and the mixing tube is in open communication with the furnace at the outlet end and
with the inner space of the mixing tube at the inlet end of the burner housing, is
described as a burner for liquid fuel in U.S. patent specification 3,741,166.
[0003] When the known burner is in operation, combustion air is blown by the fan in a forced
manner through the mixing tube to the burner head, while fuel is supplied to the burner
head. The combustible mixture is combusted at the burner head, the flame being stabilized
within the flame cup. Due to the pressure prevailing in the furnace and also due to
the underpressure created in the mixing tube by the air flowing through, a portion
of the combustion or flue gases is returned from the furnace via the annular channel
and mixed with the combustion air in the mixing tube.
[0004] When mixed with the combustion air, the flue gas thus recirculated reduces the partial
oxygen pressure, thereby increasing the heat capacity of the flue gas and reducing
the flame temperature. Thus, a reduction of the NO
x emission is achieved.
[0005] In the known burner, where both the burner housing and the mixing tube are cylindrical
while the resistance of the furnace remains substantially the same, the flue gas recirculation
does not decrease in proportion to the air flow rate when the burner is modulated,
for instance adjusted from full load to partial load. An excess of recirculated flue
gas (more than 20-30%) has an adverse effect on the combustion process and may cause
an unstable flame.
[0006] If the known burner housing construction were used in gas burners of the type as
described in NL patent No. 153322, where the burner head is designed as one or more
concentric, hollow gas-conducting rings round which axially supplied air flows, each
ring having gas outlet openings in a plane perpendicular to the burner axis and distributed
in circumferential direction, while upstream of the gas outlet openings flange-shaped
radial projections have been provided forming vortex elements promoting the gas/air
mixture, the outflowing air may also meet with so much resistance that even in the
case of full load more flue gas is being recirculated than is desirable for a stable
combustion with low NO
x emission.
[0007] The object of the invention is to provide a gas burner of the type described in the
preamble, in which the above-mentioned drawbacks of the known burner are avoided.
[0008] To this end, according to the invention, the inner side of the mixing tube in the
burner chamber is designed as a venturi.
[0009] Air injected by the fan at the inlet end of the mixing tube is compressed in the
venturi throat and, after the throat, expanded over a particular distance. Due to
the underpressure generated thereby, substantially proportional to the air flow rate,
flue gas is drawn in from the furnace via the annular channel and mixed with through-flowing
air in the mixing tube. From the furnace to the inlet in the mixing tube, the recirculated
flue gas is cooled (from approx. 1,000°C to approx. 600°C), and at the burner head
a flue gas/air mixture of relatively low temperature is delivered to be mixed with
combustion gas, which contributes to the reduction of the flame temperature and hence
to a reduction of the NO
x emission.
[0010] In the burner according to the invention, a higher or lower furnace and/or burner
resistance hardly influences the transport of flue gases. Accordingly, the percentage
of flue gas in the combustion air can be kept the same at full load and partial load,
so that the NO
x reduction remains the same throughout the entire control range.
[0011] By mounting in the blow-out opening of the burner fan an air injection nozzle which
is constricted relative to the cross-sectional area of the blow-out opening, air can
be injected into the venturi at high speed.
[0012] If the air injection nozzle is of an axially adjustable construction, the blow-in
speed at the inlet of the venturi, and hence the amount of recirculated flue gas,
can be controlled without having to deploy a fan with adjustable rotational speed.
[0013] In a further elaboration of the invention, the burner may comprise an intermediate
ring, accommodated concentrically in the burner housing, downstream from the air injection
nozzle and upstream from the mixing tube inlet, which intermediate ring is provided
with a flange.
[0014] Due to the presence of the intermediate ring, flue gases are already drawn in before
the combustion air is blown into the mixing tube. Consequently, a flue gas/air mixture
is blown into the venturi, while due to the underpressure in the venturi, flue gases
are once again drawn in by the venturi. This enables operation with an air injector
having a larger cross-sectional area than is conventional, so that the resistance
experienced by the combustion air is lower and the engine power of the fan can be
kept low. Hence, by virtue of the intermediate ring, sufficient flue gases can be
drawn in even at a lower combustion air speed in the venturi. Because the required
combustion air speed can be chosen to be lower, a lower fan pressure can be employed,
so that a fan with a lower power and hence a lower cost price can be used.
[0015] For the further reduction of the NO
x emission, in a further development of the burner according to the invention, the
burner head may be adapted for two-stage combustion, by providing, in addition to
a first series of gas outlet openings, a second series of gas outlet openings downstream
from the first series.
[0016] The amount of air supplied via the mixing tube is sufficient for combusting a specific
amount of gas. As only a portion of this gas amount flows out via the first series
of gas outlet openings, an excess of air is present at that location. The relatively
large amount of air can take up heat of the flames at the first series of gas outlet
openings. The combustion air is consumed entirely only at the second series of gas
outlet openings. Because the second, downstream combustion zone is located in the
vicinity of the open end of the flame cup, the heat developed at that location can
quickly be delivered to the furnace. In total, this yields a significant reduction
of the flame temperature and, accordingly, a reduction of the NO
x emission.
[0017] Preferably, the gas outlet openings are adjusted such that at the first series approx.
25% and at the second series approx. 75% of the gas flows out.
[0018] In accordance with the invention, in a constructively simple embodiment wherein the
burner head comprises one or several concentric, hollow gas-conducting rings, each
ring having gas outlet openings perpendicular to the burner axis and distributed in
circumferential direction, which openings form the first series of gas outlet openings,
and flange-shaped radial projections provided upstream from the gas outlet openings,
one or several hollow gas-conducting rings may be provided with tubes, directed downstream,
whose ends are closed off, which tubes, in the vicinity of the closed ends thereof,
comprise gas outlet openings in a plane perpendicular to the burner axis, forming
the second series of gas outlet openings.
[0019] In this connection, the tubes and/or gas-conducting rings may be provided with axial,
plate-shaped elements increasing the heated surface, which elements have a cooling
effect on the air and the flue gases from the first combustion stage flowing past.
[0020] With such two-stage venturi burner an NO
x reduction of approximately 75% can be realized.
[0021] Typically, the furnace wall, through which, in mounted condition, a burner extends,
is covered with a fire-resisting brickwork at the furnace side thereof. To obtain
a proper conduction of flue gas from the furnace to the annular space between the
mixing tube and the burner housing wall, the burner housing, at the outlet end thereof,
may be extended by an outer flame cup which, when the burner is in mounted condition,
extends into the furnace and surrounds the mixing tube at a radial distance.
[0022] In explanation of the invention, some exemplary embodiments of the venturi burner
in single-stage and two-stage embodiments will be described with reference to the
accompanying drawings.
Fig. 1 is a sectional view of the boiler having connected thereto a burner with burner
fan;
Fig. 2 is a sectional view taken on line II-II of Fig. 3 of the burner;
Fig. 3 is a sectional view taken on line III-III of Fig. 2 of the burner;
Fig. 4 is a sectional view taken on line IV-IV of Fig. 5 of the burner ring and the
burner plate;
Fig. 5 is a side view of the burner ring and the burner plate taken on line V-V of
Fig. 4;
Fig. 6 is a similar view as shown in Fig. 2 of another embodiment of the venturi burner;
and
Fig. 7 is a view similar to Fig. 3 of the exemplary embodiment shown in Fig. 6.
[0023] Fig. 1 shows a boiler 1 with a burner 3 connected to the boiler front 2, which burner
comprises a burner housing 4 and an air supply fan 5. The boiler comprises a furnace
6, a heat exchanger 7 and a flue gas discharge 8. The burner housing 4 of the burner
3 is connected to an opening in the boiler front 2 by an outlet end 9 and to the blow-out
opening 11 of the air supply fan 5 by the inlet end 10. The burner 3, shown in detail
in Figs 2 and 3, comprises a mixing tube 12, extending concentrically within the burner
housing 4 and connecting to a burner head 13 at the outlet end of the burner housing
4. The burner head 13 is surrounded by a flame cup 14. The burner head 13 and the
flame cup 14 extend into the furnace 6 of the boiler 1. Located between the burner
housing 4 and the mixing tube 12 is an annular space 15, being in open communication
with the furnace 6 at the outlet end and with the inner space 16 of the mixing tube
12 at the inlet end of the burner housing 4. Via an axially adjustable injection nozzle
17, the fan 5 blows combustion air into the inner space 16 of the mixing tube 12.
The flow rate of the combustion air at the inlet of the mixing tube 12 depends on
the distance of the injection nozzle 17 from the inlet of the mixing tube 12. In the
case of a greater distance, the combustion air must travel a greater distance before
it reaches the mixing tube 12 and, accordingly, has a lower flow rate at the inlet
of the mixing tube 12. The injection nozzle 17 being axially adjustable, the fan 5
need only be designed for rotation at a fixed speed. The fuel is supplied via the
fuel connection 18 and passed to the burner head 13 via a fuel channel 19.
[0024] The mixing tube 12 is designed as a venturi. As the combustion air coming from the
fan 5 is compressed in the venturi and, after the throat, expanded over a particular
distance, an underpressure is produced at the venturi inlet which is proportional
to the combustion air flow rate. Due to the underpressure and the overpressure prevailing
in the furnace 6, a portion of the flue gas is conducted via the annular space from
the furnace 6 to the inlet of the mixing tube 12. Mixture of the combustion air with
flue gas reduces the partial oxygen pressure of the combustion air, so that the heat
capacity of the flue gas is increased and, accordingly, the flame temperature is reduced,
so that the NO
x emission is reduced. As the underpressure in the mixing tube 12 is substantially
proportional to the combustion air flow rate, the amount of flue gas that is recirculated
will decrease proportionally to the combustion air flow rate even when the burner
3 is modulated.
[0025] Figs 6 and 7 show an alternative exemplary embodiment of the burner according to
the invention, wherein the parts with the same function as the parts of the exemplary
embodiment shown in Figs 2 and 3 are designated by the same reference numerals. The
alternative exemplary embodiment comprises an intermediate ring 28, accommodated concentrically
in the burner housing 4 downstream from the air injection nozzle 17 and upstream from
the mixing tube inlet 12, which intermediate ring 28 comprises a flange 29.
[0026] Due to the presence of the intermediate ring 28, combustion air supplied by means
of the fan 5 is already mixed with flue gases before the combustion air reaches the
mixing tube 12. Subsequently, due to the underpressure in the inner space 16 of the
venturi 12, additional flue gas is drawn in and mixed with the combustion air. This
enables operation with an air injector 17 having a larger cross-sectional area than
is conventional, so that the resistance experienced by the combustion air is lower
and the engine power of the fan 5 can be chosen to be low. Consequently, the intermediate
ring 28 enables sufficient flue gases to be drawn in, even at a lower combustion air
rate in the venturi 12.
[0027] Optionally, the flange 29, extending perpendicularly to the burner housing center
line in the exempary embodiment shown, may be funnel-shaped, the wide mouth of the
funnel being directed to the injection nozzle 17. Such design of the flange 29 reduces
the chance of combustion air, injected via air injector 17, being blown directly into
the boiler furnace via the annular space 15 round the venturi 12.
[0028] The burner head 13 comprises two concentric burner rings 20, 21, the inner ring being
designed as a burner plate 21. The flue gas/combustion air mixture flows round the
burner ring 20 and the burner plate 21 in axial direction, i.e. in the direction of
the burner axis. The burner ring 20 and the burner plate 21 comprise radial combustion
medium outlet openings 22 which are directed radially, i.e. perpendicularly to the
burner axis. Arranged upstream from these outlet openings are radial projections 23
promoting the fuel/air mixture by causing a vortex in the combustion air. Such burner
head provides a stable flame front.
[0029] For the further reduction of the NO
x emission, an alternative burner head 13a is proposed, shown in detail in Figs 4 and
5. The burner head 13a is designed for two-stage combustion in that, in addition to
the fuel outlet openings 22a of the or each burner ring 20a, a second series of fuel
outlet openings 24 is arranged downstream therefrom. In the exemplary embodiment shown
in Figs 4 and 5, this is realized through the arrangement of tubes 25, directed axially
downstream, on the outer burner ring 20a, which tubes 25 are closed at the outer ends
thereof and which comprise radially directed outlet openings 24. Also, upstream from
the gas outlet openings 24 of the second combustion zone, radial projections are provided
for obtaining a proper mixture, created by vortex, between the outflowing gas and
the combustion air. In this exemplary embodiment, the flow-through surface of the
first series of outlet openings 22a is 25% and the flow-through area of the second
series of outlet openings 24 is 75% of the total flow-through area. As only 25% of
the total amount of fuel is released at the first series of outlet openings and is
combusted at that location, an excess of air is present at that location. The relatively
large amount of air can take up the heat of the flames at the hollow rings. At the
second series of fuel outlet openings, the combustion air is consumed entirely. As
the second, downstream combustion zone is located in the vicinity of the open end
of the flame cup 14, the heat developed at that location can be delivered directly
to the furnace 6. In total, this yields a significant reduction of the flame temperature
and, accordingly, a reduction of the NO
x emission.
[0030] In addition, the burner plate 21a and the tubes 25 comprise plate-shaped elements
26 and 26a, increasing the heated surface and having a cooling effect on the air and
the flue gases from the first combustion zone flowing past.
[0031] With a gas burner provided with a mixing tube 12, designed as a venturi, and a two-stage
combustion head 13a, a reduction of the NO
x emission of approx. 75% is realized.
[0032] To improve the conduction of the flue gas from the furnace 6 to the annular space
15 between the mixing tube 12 and the burner housing 4, the burner housing 4, at the
outlet side thereof, has been extended to include a flame cup 27, exending into the
furnace 6 and surrounding mixing tube 12 at a radial distance.
[0033] It will be understood that the invention is not limited to the exemplary embodiment
described, but that various modifications are possible within the scope of the invention.
1. A burner, in particular a gas-fired fan burner for a central heating installation,
comprising a substantially cylindrical burner housing, of which one end, being the
outlet end, is connectable to an opening in a furnace wall of a central heating boiler,
while to the other end thereof, being the inlet end of the burner housing, a burner
fan for forced supply of combustion air and a fuel supply line are connectable, a
mixing tube extending concentrically within the burner housing and connecting to a
burner head at the outlet end of the burner housing, said burner head, in mounted
condition of the burner, extending into the furnace by a flame cup surrounding the
burner head, while an annular space between the burner housing wall and the mixing
tube is in open communication with the furnace at the outlet end and with the inner
space of the mixing tube at the inlet end of the burner housing, characterized in
that the inner side of the mixing tube (12) in the burner housing (4) is designed
as a venturi.
2. A burner according to claim 1, characterized in that in the blow-out opening (11)
of the burner fan (5) an air injection nozzle (17) is provided, which is constricted
relative to the cross-sectional area of the blow-out opening (11).
3. A burner according to claim 2, characterized in that the air injection nozzle (17)
is axially adjustable.
4. A burner according to claim 2 or 3, characterized by an intermediate ring (28), accommodated
concentrically in the burner housing (4), downstream from the air injection nozzle
(17) and upstream from the mixing tube inlet (12), provided with a flange (29).
5. A burner according to any one of the preceding claims, characterized in that the burner
head (13a) is adapted for two-stage combustion through providing, in addition to a
first series of gas outlet openings (22a), a second series of gas outlet openings
(24) downstream from the first series.
6. A burner according to claim 5, characterized in that the gas outlet openings (22a,
24) are adjusted such that at the first series approx. 25% and at the second series
approx. 75% of the gas flows out.
7. A burner according to claim 5 or 6, characterized in that the burner head (13a) comprises
one or several concentric, hollow gas-conducting rings (20a, 21a), each ring having
gas outlet openings (22a) perpendicular to the burner axis and distributed in circumferential
direction, said openings forming the first series of gas outlet openings (22a), and
flange-shaped radial projections provided upstream from the gas outlet openings (22a),
one or a plurality of the gas-conducting rings (20a) being provided with tubes (25),
directed downstream, whose ends are closed off, said tubes (25), in the vicinity of
the closed ends thereof, comprising gas outlet openings (24) in a plane perpendicular
to the burner axis, forming the second series of gas outlet openings.
8. A burner according to claim 7, characterized in that the tubes (25) and/or gas-conducting
rings (20a, 21a) are provided with axial, plate-shaped elements (26, 26a) enlarging
the heated surface.
9. A burner according to any one of the preceding claims, characterized in that the burner
housing (4) at the outlet end thereof is extended by an outer flame cup (27), said
outer flame cup (27), when the burner (3) is in mounted condition, extending into
the furnace (6) and surrounding the mixing tube (12) at a radial distance.