This invention relates to a catalytic combustion burner made of a porous material suitable for cooperation with a wick that will carry an combustible composition to the burner penetrating into the pores of the said porous material, the said burner comprising a peripheral zone that supports a catalyst and that surrounds a central zone without a catalyst forming a vaporization zone, the peripheral zone and the central zone being located in the upper part of the burner.
Conventionally, this type of catalytic combustion burner has an approximately cylindrically shaped peripheral surface.
However, it is relatively difficult to manufacture burners with such an approximately cylindrically shaped peripheral surface.
Actually, many parts have to be scrapped during the mould removal step because they include weak zones, particularly around the periphery of the burner.
Even a slight taper flaring upwards of the order of one degree or two degrees, conventionally on the peripheral surface of the burner, cannot satisfactorily solve all the difficulties mentioned above encountered during mould removal.
Therefore the purpose of this invention is to correct the above-mentioned disadvantage of known burners and to propose a burner of the type mentioned above in which mould removal is facilitated and which also has improved functional characteristics.
According to a first aspect of the invention, this catalytic combustion burner has a tapered peripheral surface flaring upwards.
Obviously, this peripheral surface is tapered much more than the slight taper mentioned above.
Thus, the tapered structure facilitates removal of the burner from its mould without damaging the peripheral surface of the burner.
Furthermore, during comparative tests of the operation of a burner according to the invention and of burners with a cylindrical structure according to prior art, the applicant made measurements demonstrating that better results are obtained in terms of odour destruction if a catalytic combustion flask is used fitted with a burner with a tapered structure.
It can be understood that the tapered burner according to the invention has a larger peripheral exchange surface area than a burner according to prior art with a comparable burner height and an approximately cylindrical peripheral surface, due to its inherent construction.
In the case of a burner with an approximately cylindrical peripheral surface, air circulating in the immediate vicinity of the peripheral surface of the burner warms up as it comes into contact with this surface and rises vertically parallel to the said surface of the burner. Therefore, the result is that contact between this hot air and the peripheral surface of the burner is only very slight, even in the case in which there is a slight taper of the order of 1° or 2° making this type of burner flare very slightly upwards. Therefore heat exchange and chemical exchanges between the peripheral surface of the burner and air are limited.
On the contrary, in the case of a burner with the same height but with a tapered peripheral surface, hot air circulating vertically close to the burner makes stronger contact with the tapered peripheral surface of the burner, thus facilitating heat and chemical exchanges and therefore catalytic destruction of fumes and other components carried by this hot air, thus enabling cleaner ambient air.
Furthermore, since heat exchanges are greater when a burner according to the invention is used, the air close to the burner that is more strongly heated rises more quickly and consequently generates more dynamic convection currents.
Therefore, better convection of gas flows is observed, for air and for gases produced by vaporisation of the combustible composition, in the immediate environment of tapered peripheral surface of the burner.
Preferably, the half-angle at the vertex of the tapered peripheral surface of the burner is between 10° and 40°, and is advantageously between 15° and 25°, and is preferably between 18° and 23°.
According to one advantageous version of the invention, the tapered peripheral surface of the burner has at least one shoulder approximately around the periphery and facing inwards and downwards to increase the diameter between a lower part and an upper part of the burner.
This type of structure further increases the exchange surface area between the hot air and the burner and reinforces contact between rising hot air and at least some of the peripheral surface of the burner, and therefore heat and chemical exchanges.
A second aspect of the invention also relates to a catalytic combustion flask adapted to contain a liquid combustible composition and to be fitted with a catalytic combustion burner at its neck, designed to cooperate with a wick dipping into the said composition.
According to the invention, this flask is fitted with a burner according to the first aspect of the invention.
Other special features and advantages of this invention will become clear after reading the following detailed description.
In the appended drawings given simply as non-limitative examples:
The common elements to
This flask 1 may have any shape and has a neck 4 in which the catalytic combustion burner 3 can be fitted.
The catalytic combustion burner 3 is made from an appropriate porous material adapted to resist temperatures of at least 400° C. reached in the zone supporting the catalyst during operation of the burner 3. In particular, this material may be a ceramic material, for example it may be prepared from kaolin or cordierite.
The catalytic combustion burner 3 is adapted to cooperate with a wick 5 dipping into the said composition 2. This wick 5 will bring the combustible composition 2 to the burner 3, and this combustible composition 2 will penetrate into the pores of the porous material.
The combustible composition 2 is an appropriate combustible liquid in accordance with the regulations in force and adapted to catalytic combustion and vaporization.
In particular, this combustible composition 2 may be an alcohol, particularly isopropyl alcohol, and may also comprise a perfumed material and/or an active material.
The wick 5 is any known type of wick, for example a cotton wick.
The wick 5 may also be made of a mineral material, for example it may be made of mineral fibres or of a porous material.
The catalytic combustion burner 3 may be provided with a support (not shown) near the bottom, so that it can be introduced either directly into the neck 4 of the flask 1, or into the central hole of a base (not shown), the base being adapted so that it can be fixed at the neck 4 of the flask 1.
Support and basis suitable for fixing such a burner 3 on the flask 1 have been described particularly in application WO 99/63267.
As shown in
This burner 3 comprises a peripheral zone 6 near its top part 3b, for example with an annular shape, that supports a catalyst 7 and that surrounds a central zone 8 without a catalyst forming the vaporization zone.
For example, the catalyst 7 may be a metal belonging to group VIII in the periodic table of the elements.
The half-angle A at the summit of the tapered peripheral surface 3a of the burner 3 is between 10° and 40°, and is advantageously between 15° and 25°, and preferably between 18° and 23°.
The catalytic combustion burner 3 in
This sleeve 9 is placed on the extension of the lower part 3c of the burner 3.
This sleeve 9 is also made from a porous material that may particularly be a ceramic material, for example prepared from kaolin or cordierite.
This sleeve 9 comprises an approximately axial cavity 11 designed to tighten the wick 5 so that the combustible composition 2 can migrate from the pores of the upper part 9a of the sleeve 9 towards the pores of the lower part 3c of the burner 3.
The junction between the lower part 3c of the burner 3 and the upper part 9a of the sleeve 9 must be such that migration of the combustible composition 2 from the sleeve 9 towards the burner 3 is guaranteed. The result is thus mechanical nesting and/or an assembly by means of porous bonding.
A catalytic combustion system 10 could also be made as a single part comprising the burner 3 and the sleeve 9.
This burner 13 has a tapered peripheral surface 13a having a truncatedcone form, that is flared upwards.
Each half-view shows that this peripheral surface 13a has at least one approximately peripheral first shoulder 14a, 14b, facing inwards and downwards from the said burner 13.
The effect of this first shoulder 14a, 14b is to increase the diameter between a lower part 13c and an upper part 13b of the burner 13.
On the left half-view, the first shoulder 14a is arranged in the approximately median part of the burner 13.
On the right half-view, the first shoulder 14b is formed in the lower part 13c of the burner 13.
Obviously, the height of the first shoulder can be different from the heights shown on the two half-views in
As shown on the left half view, the catalyst deposit was made as far as the first shoulder 14a, which therefore separates the peripheral zone 16 supporting the catalyst 7 from the lower part 13c of the burner 13 without a catalyst, at the peripheral surface 13a of the burner 13.
On the other hand, on the right half view, the first shoulder 14b does not correspond to a demarcation zone for localization of the catalyst 7 at the peripheral surface 13a of the burner 13. This first shoulder 14b is located in a part of the burner 13 in which there is no catalyst.
The burner 13 comprises a cavity 15 approximately axial open downwards, at least at its lower part 13c, into which fits the upper end 5a of the wick 5 that will convey the combustible composition 2 to the burner 13, over all or some of its height.
As shown in
On the view shown in
This cavity 15 is closed off by a wall 17, at the top part 13b of the burner 13.
Conventionally, as shown in
This particular structure of the upper part 13b of such a burner 13 fitted with an annular groove 19 was described particularly in patent EP 0 277 875 B1 deposited by the applicant.
As in the previous figures, this catalytic combustion burner 23 has a tapered peripheral surface 23a having a truncatedcone form, that flares upwards.
The upper part 23b of the burner 23 comprises an annular peripheral zone 26 supporting the catalyst 7 and surrounding a central zone 28 without catalyst, and a cavity 25.
The top part 25a of the cavity 25 communicates with the atmosphere through at least one open channel 29, for example formed in the top part 23b of the burner 23.
In this
This channel 29 has a narrower cross section than the cross section of the cavity 25 of the burner 23, such that the cavity 25 is at least partially closed at the top part 23b of the burner 23, by a wall 27 located in the central zone 28.
The peripheral surface 23a comprises a first approximately peripheral shoulder 24, and a second approximately peripheral shoulder 30.
Each shoulder 24, 30 separates part of the burner 23 immediately above it and with a larger diameter, from another part of the burner 23 immediately below it and with a smaller diameter.
As shown in
This type of structural arrangement provides a means of precisely determining the zone of the burner 23 on which the catalyst 7 will be deposited.
It would thus have been possible to plan to place the catalyst 7 as far as the second shoulder 30.
Obviously, this invention is not limited to the embodiments of the burner that have just been described, and many changes and modifications could be made to it without going outside the scope of the invention.
In particular, all of the different structural characteristics of the burners described above could be combined without restriction.
In particular, the burners 13 and 23 shown in
An annular groove like the annular groove 19 in
Similarly, the top part of the cavity 15 of the burner 13 in
The lower parts 3c, 13c and 23c of burners 3, 13 and 23 can also be made in any appropriate shape to facilitate their placement and to support them on the neck 4 of the flask 1, possibly but not necessarily using a support and/or a base.
Remember that the support and base suitable for the attachment of such a burner 3, 13, 23 onto flask 1 were described particularly in application WO 99/63267.
Number | Date | Country | Kind |
---|---|---|---|
03 07765 | Jun 2003 | FR | national |
Number | Name | Date | Kind |
---|---|---|---|
1956749 | Terret | May 1934 | A |
2938343 | Canfield | May 1960 | A |
3240256 | Binkley et al. | Mar 1966 | A |
6162046 | Young et al. | Dec 2000 | A |
6537061 | Gomez et al. | Mar 2003 | B1 |
Number | Date | Country |
---|---|---|
34 36 310 | Apr 1986 | DE |
0 277 875 | Aug 1988 | EP |
2 579 465 | Oct 1986 | FR |
2 821 749 | Sep 2002 | FR |
3241212 | Oct 1991 | JP |
513531 | Dec 2002 | TW |
Number | Date | Country | |
---|---|---|---|
20050037309 A1 | Feb 2005 | US |