[0001] The present invention aims at providing simple devices for reducing polluting exhaust
fumes emitted by balanced flue boilers powered by any type of fuel, whether gaseous,
liquid or solid.
[0002] Balanced flue boilers have been well known for many years. In these models, the comburent
air is taken in from the exterior, and obviously the combustion gas (or fumes) is
expelled to the exterior.
[0003] For easy installation and other reasons such as the pre-heating of the comburent
air using combustion gases through heat exchange in countercurrent, for example, the
comburent air inlet flue is coaxial, and generally external to the exhaust fume flue.
Hereafter the combination of these two co-axial flues for comburent air and fume expulsion
will be referred to using the term "co-axial flues".
[0004] It is also a well-known fact that large efforts have been made to increase boiler
heating efficiency as well as to reduce toxicity and the pollution levels of the emitted
fumes.
[0005] Progress has been made in these directions using various devices, sometimes quite
simple, but often very complex and costly, which act inside the combustion chamber
during the combustion action itself, for example, by adjusting excess air and/or choosing
appropriate shapes and materials for burners, while no interventions have been applied
downstream of the combustion chamber so that the fumes are emitted into the external
environment with the chemical composition and possible solid suspensions that have
been produced in combustion, just as the comburent air used contains the same chemical
composition found in the environment.
[0006] It is obvious that however sophisticated combustion control may be, it is impossible
to generate fumes that are completely free of unburnt substances, or in the case of
particular fuels, that are free of suspended particles.
[0007] The main aim of the present invention is to identify means able to modify the chemical
composition of fumes downstream of the combustion chamber in order to reduce the concentration
of unburnt gas.
[0008] A further aim of the present invention in a balanced flue boiler is to identify means
able to destroy solid particle content in fumes downstream of the combustion chamber.
[0009] Another further aim of the present invention in a balanced flue boiler is to limit
the installation of said means adapted for at least one of the aforesaid aims, within
the co-axial flues.
[0010] These and other aims are attained through the means explained in the present description
and in the appended claims that constitute an integral part of the basic description
as well as the appended figures.
[0011] Figure 1 shows the co-axial flues of a balanced flue boiler containing a first embodiment
of the device according to the invention.
[0012] Figure 2 shows the co-axial flues of a balanced flue boiler containing a second embodiment
of the device according to the invention.
[0013] With reference to both figures, with 1 is identified the unit of the co-axial flues
that connect the boiler 2 with the external environment 3.
[0014] The combustion products 5 (or fumes) pass through the fume expulsion flue 4 and are
expelled into the external environment, while the comburent air 7 is sucked in through
the air inlet flue 6.
[0015] It is well known that the circulation of the aeriform substances that pass to and
from the boiler 2 is activated by a fan that, compared to the external environment
3, places the inlet flue 6 in a state of depression and the outlet flue 4 in a state
of overpressure.
[0016] According to the present invention, it is foreseen that a part 5.1 of the fumes recirculate
inside the combustion chamber. As stated previously, it is impossible to expel the
fumes 5 from the combustion chamber completely free of unburnt gas such as carbon
monoxide CO, or carbon dioxide CO2.
[0017] However, it has been discovered that by recirculating said part 5.1 of the fumes
inside the combustion chamber, the part 5.2 of the same fumes expelled towards the
exterior possess a lower level of unburnt gas, than fumes that are not sent for recirculation;
therefore recirculation provides a lower pollution level than fumes that are not recirculated.
[0018] Moreover, said recirculation provides an improvement in energy performance, because
more complete combustion permits greater utilization of the fuel calorific power,
and because said part 5.1 of the recirculated fumes releases heat to the comburent
air 7 instead of being lost in the environment.
[0019] To obtain said recirculation, it is sufficient to connect the outlet flue 4 with
the inlet flue 6 through appropriate passages 8.1 or 8.2. Because of the relative
pressures present, instead of being expelled towards the exterior 3, part of the fumes
5.1 pass from the outlet flue 4 to the inlet flue 6, to mix with the comburent air
7, returning in this manner into the combustion chamber.
[0020] With reference to figure 1, said appropriate passages 8.1 or 8.2 can be composed
of a simple opening 8.1, performed in the wall that separates the outlet flue 4° from
inlet flue 6.
[0021] With reference to figure 2, said appropriate passages 8.1 or 8.2 can alternatively
be composed of ducts 8.2 of an appropriate shape to deflect the said part of the fumes
5.1 towards the interior of the inlet flue 6.
[0022] As far as the scrubbing of the suspended particles in the fumes 5 is concerned, both
figures 1 and 2 show that panels 9 are appropriately positioned and maintained inside
the outlet flue 4, in a manner so that the fumes 5 can be filtered through the panels.
[0023] Said panels 9 can be composed of suitable perforated metal foil, or a well known
type obtained through so-called micro-stretching, composed of sheets that have been
previously subject to multiple cutting into regular rows, followed by stretching to
obtain a type of net or mesh. Said panels 9 are preferably maintained by suitable
means at a potential which is different from that of the fumes 5 and the suspended
particles transported by the fumes, so that the panels will attract and collect the
particles through electrostatic attraction; methods and means for attracting particles
using electrostatic attraction are well known and do not require further description.
[0024] Naturally said panels 9 must be cleaned regularly to remove all impurities attached;
for this reason it is foreseen that the panels can be removed from the outlet flue
4 for cleaning, or alternatively, at least one part of the outlet flue 4 in which
the panels 9 are mounted can be removed.
[0025] The advantages of the present invention are obvious: with the application of suitable
means described previously, or other equivalent means, it is possible to scrub fumes
5 of any chemical type, and to reduce unburnt substances of physical type while retaining
the transported powder particles. Moreover, it is possible to improve the thermal
efficiency of the boilers on which the invention is applied, because of the improved
utilization of the heating power of the combustible, as well as the fact that part
of the thermal energy of the fumes is released to heat the comburent air.
[0026] A further advantage consists in the fact all the aforesaid means according to the
present invention are enclosed within the unit formed by the co-axial flues 1.
1. Method for scrubbing exhaust fumes (5) from the combustion chamber of a balanced flue
boiler
consisting of the recirculation of part (5.1.) of said fumes (5) inside the combustion
chamber, mixing said fumes with the comburent air (7).
2. Method for scrubbing exhaust fumes (5) according to the previous claim,
characterised in that
the method also foresees the filtration of suspended particles transported by said
fumes (5).
3. Method for scrubbing exhaust fumes (5) according to any of the previous claims,
characterised in that
the method also foresees electrostatic attraction of the particles transported by
said fumes (5).
4. Device for the scrubbing of exhaust fumes (5) from the combustion chamber of a balanced
flue boiler
characterised in that
said device foresees suitable passages (8.1; 8.2) that connect the outlet flue (4)
for the expulsion of said fumes (5) with the inlet flue (6) of the comburent air (7),
said passages (8.1; 8.2) being designed to take in part (5.1) of the fumes, that are
then mixed with the comburent air (7).
5. Device for the scrubbing of fumes (5) according to the previous claim
characterised in that
said passages (8.1; 8.2) are openings (8.1) performed in the wall that separates the
outlet flue (4) of said fumes (5) and the inlet flue (6) of the comburent air (7).
6. Device for the scrubbing of fumes (5) according to claim 4
characterised in that
said passages (8.1; 8.2) are ducts (8.2) realised in the most appropriate shape and
adapted to deflect part (5.1) of said fumes (5) inside the inlet flue (6) of the comburent
air (7).
7. Device for the scrubbing of fumes (5) according to any of the previous claims from
4 to 6
characterised in that
said device foresees means (9) positioned inside the outlet flue (4) of said fumes
(5) adapted to filter and retain the suspended particles transported by said fumes
(5).
8. Device for the scrubbing of fumes (5) according to the previous claim
characterised in that
said means (9) are composed of panels realised in perforated or stretched metal foil
of various types.
9. Device for the scrubbing of fumes (5) according to the previous claim
characterised in that
said perforated or stretched foil (9) is electrostatically charged with means well
known in the art, in the most suitable manner to attract and retain said suspended
particles transported by said fumes (5).
10. Device for the scrubbing of fumes (5) according to any of the previous claims from
7 to 9
characterised in that
said means (9) adapted to filter and retain the suspended particles transported by
said fumes (5) can be removed for cleaning.
11. Device for the scrubbing of fumes (5) according to any of the previous claims from
4 to 10
characterised in that
said device is positioned inside the unit formed by the co-axial flues (1), said co-axial
flues (1) being composed of the outlet flue (4) of said fumes (5) and the inlet flue
(6) of the comburent air (7).