EP1598595B1 - Evaporator arrangement - Google Patents
Evaporator arrangement Download PDFInfo
- Publication number
- EP1598595B1 EP1598595B1 EP20050006431 EP05006431A EP1598595B1 EP 1598595 B1 EP1598595 B1 EP 1598595B1 EP 20050006431 EP20050006431 EP 20050006431 EP 05006431 A EP05006431 A EP 05006431A EP 1598595 B1 EP1598595 B1 EP 1598595B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fuel
- evaporator medium
- porous evaporator
- evaporator
- porous
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Not-in-force
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- 239000000446 fuel Substances 0.000 claims description 110
- 239000007788 liquid Substances 0.000 claims description 34
- 238000002156 mixing Methods 0.000 claims description 22
- 238000009826 distribution Methods 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 14
- 230000015572 biosynthetic process Effects 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims 3
- 238000003780 insertion Methods 0.000 claims 3
- 238000007599 discharging Methods 0.000 claims 1
- 230000002093 peripheral effect Effects 0.000 description 15
- 238000002485 combustion reaction Methods 0.000 description 10
- 239000000203 mixture Substances 0.000 description 10
- 238000001704 evaporation Methods 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 6
- 229930195733 hydrocarbon Natural products 0.000 description 6
- 150000002430 hydrocarbons Chemical class 0.000 description 6
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- 230000005484 gravity Effects 0.000 description 4
- 239000011810 insulating material Substances 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 230000004888 barrier function Effects 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000007769 metal material Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 2
- -1 for example Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000003225 biodiesel Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000006735 deficit Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000007373 indentation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D3/00—Burners using capillary action
- F23D3/40—Burners using capillary action the capillary action taking place in one or more rigid porous bodies
Definitions
- the present invention relates to an evaporator arrangement for delivering a fuel vapor into a mixing chamber according to the preamble of claim 1.
- Such evaporator arrangements are used for example in fuel-operated heaters for motor vehicles, these heaters can be used in turn as a heater or as a heater.
- a mixture of fuel vapor and combustion air is generated, which can be ignited and burned to generate heat.
- reformers to produce in a mixing chamber, a mixture of vaporized fuel, ie vaporized hydrocarbon, and other mixed material, for example, air or water vapor. This mixture is then passed to a catalyst assembly to produce a hydrogen-containing gas mixture by catalytic reaction.
- the selective introduction of the liquid fuel in the porous evaporator medium continues to run the risk that a very nonuniform fuel distribution by gravity on the one hand and by capillary action on the other hand occurs and thus not the entire surface of the evaporator medium can be used for Brennstoffabdampfung, but for a defined mixture formation may be required.
- An evaporator arrangement according to the preamble of claim 1 is known from DE 39 14 611 A1 known.
- a porous disk-like porous evaporator medium is received in a dish-like carrier.
- a stick glow plug At the back of the cup-like carrier is a stick glow plug which is capable of heating the porous evaporator medium and the liquid fuel contained therein.
- the DE 101 30 638 A1 discloses an evaporator assembly having a multi-layered porous evaporator medium disposed in a cup-like housing.
- a plate-like fuel deflector element may be arranged between two layers of the porous evaporator medium, which is the inlet region for the liquid fuel covered.
- the US-A 5,082,175 discloses an evaporator arrangement in which a porous evaporator medium is arranged in a pot-like housing. Between a arranged at the back of the evaporator medium glow plug and the evaporator medium is a plate-like bottom portion.
- the EP 1 484 552 A1 discloses an evaporator assembly having a pot-like housing. At a bottom region of the cup-shaped housing is arranged a combustion chamber facing a porous evaporator medium. At the back of the bottom region is an electrically energizable heating device, which can provide a projecting region for ignition conditions in the region of the porous evaporator medium which can be heated by the latter and penetrates the bottom region and the porous evaporator medium.
- an evaporator arrangement for emitting a fuel vapor into a mixing chamber according to claim 1.
- This comprises a porous evaporator medium, a liquid fuel leading to the porous evaporator medium line arrangement and a heater on a side facing away from the mixing chamber or facing away from the back of the porous Evaporator medium, wherein between the porous evaporator medium and the heater is arranged a direct contact between these suppressive separating element.
- a fuel flow guide formation is formed in the porous evaporator medium.
- Such a fuel flow guide formation comprises compressed regions or recessed regions in the porous evaporator medium, which then have a different capillary flow behavior or locally prevent the occurrence of capillary flow and thus create barriers for the fuel flow.
- a separator that not only ensures a uniform heat input into the porous evaporator medium, but also ensures that an exit from Fuel vapor at the back of the porous evaporator medium can be prevented as well as the leakage of liquid fuel at the back of the porous evaporator medium.
- fuels in the context of the present invention generally liquid hydrocarbons, such.
- Gasoline, diesel, biodiesel and the like are considered, for example, are available for combustion, but nevertheless also be used to be implemented in a reformer for hydrogen production for a fuel cell system.
- the separating element be formed from a material that conducts heat well, preferably metal.
- the separating element substantially the entire back of the porous evaporator medium covered. This ensures that practically the entire porous evaporator medium is thermally contacted and that over the entire rear side the escape of fuel or fuel vapor can be prevented.
- the separating element overlap an outer edge region of the porous evaporator medium.
- the separating element is designed like a shell and is arranged with a dish bottom at the back of the porous evaporator medium, while the shell edge then overlaps the outer edge region of the porous evaporator medium, i. surrounds this outer edge region or rests there.
- the separating element may have a fuel introduction opening for the line arrangement.
- a further improved fuel distribution behavior can be obtained by providing a fuel distribution channel arrangement on the separating element starting from the fuel introduction opening.
- the line arrangement penetrate through the fuel introduction opening and be held under pressure against the porous evaporator medium with a discharge end.
- the porous evaporator medium has a peripheral contour, which is adapted to a peripheral contour of a mixing chamber, preferably a bottom portion thereof, and that the line arrangement is introduced eccentrically to the porous evaporator medium.
- the distribution behavior of the fuel in the porous evaporator medium to achieve improved Brennstoffabdampfung can be influenced by the fact that the porous evaporator medium is constructed in multiple layers and the layers at least partially have a different fuel conductivities.
- the present invention further relates to a vehicle heater comprising an evaporation arrangement according to the invention.
- the present invention relates to a reformer assembly with an evaporator assembly according to the invention, as mentioned, to produce a mixture of fuel vapor, so hydrocarbon vapor, and air and / or water vapor and / or recirculated combustion or fuel cell exhaust gases.
- an evaporator assembly is generally designated 10.
- This evaporator assembly 10 essentially provides a peripheral region 12 and a bottom region 14, which together define a mixing chamber 16.
- a mixture of, for example, air and a fuel vapor can be generated in this mixing chamber 16.
- This mixture can be ignited by using a projecting into the mixing chamber 16 ignition element 18 to use the resulting in the then running combustion heat.
- the heat generated during combustion can be transferred to a medium to be heated, so for example air or water.
- the heat generated during combustion can be used to preheat the reformer assembly.
- the combustion is stopped or suppressed in order to be able to convert the mixture of hydrocarbon vapor, air and / or possibly other mixed material constituents into a catalyst arrangement and thereby hydrogen for a fuel cell system to be able to produce.
- the peripheral region 12 is at the in Fig. 1 shown embodiment provided by a substantially cylindrical peripheral wall member 20 having a plurality of inlet openings 22 for air or other mixed material.
- a further approximately cylindrical component 24 encompasses an axial end region-axially with respect to a longitudinal center axis of the peripheral wall component 20-of this peripheral wall component 20 and holds with a step-like region 26 a porous evaporator medium 28 configured like a disc here together with a dividing element 30 likewise configured as a disk on the circumferential wall component 20.
- the porous evaporator medium 28 may, as is well known, braid, knitted fabric, foamed ceramic or the like. which is capable of distributing the liquid fuel or hydrocarbon introduced therein by capillary action.
- the rear side 32 of the porous evaporator medium 28 here completely overlapping separating element 30 is preferably formed of metal material, such as sheet metal material. It has a nozzle 34 formed by forming, into which a fuel line 36 opens and thus promotes liquid fuel in the region of the porous evaporator medium 28.
- a heating coil 38 heating device On the side facing away from the porous evaporator medium 28 side of the partition member 30 is a configured in the form of a heating coil 38 heating device is provided, which touches the partition member 30 in the largest possible area and thus contributes to the most uniform heating of the partition member 30.
- the heating coil 38 is covered on its side facing away from the separating element 30 by insulating material 40, which in turn is covered by an insulating material 40 in a further uniform manner on the entire back side 32 of the porous evaporator medium 28 Holding plate 42 and a locking ring 44 is fixed to the component 24.
- the heating coil 38 is between the insulating material 40 and the separating element 30 locked in the direction of the longitudinal axis L.
- the separating element 30 By providing the separating element 30 on the rear side 32 of the porous evaporator medium 28, it is ensured that the liquid fuel introduced into it can evaporate only in the direction of the mixing chamber 16. A fuel evaporation to the rear, ie in the direction of the heating coil 38, is not possible, with the result that no deposits can be generated in this area. At the same time the risk of leakage of liquid fuel at the back 32 of the porous evaporator medium 28 is completely prevented. To this end, the separating element 30, which completely covers the porous evaporator medium 28, contributes to this. Furthermore contributes to that by cooperation of the line 36 with the nozzle 34 in this area fuel can not escape in liquid form.
- the escape of liquid fuel or a fuel vapor is prevented by the fact that this edge region is completely surrounded first by the component 24 and thus in cooperation with the peripheral wall member 20 is a virtually liquid and vapor-tight closure the porous evaporator medium 28 is provided to the outside.
- This can be further supported by the fact that the porous evaporator medium 28 is clamped together with the separating element 30 between the shoulder 26 and the peripheral wall member 28 and thus is compressed there. In this case, the escape of both liquid and vapor fuel over the outer peripheral edge 46 of the porous evaporator medium 28 is practically impossible.
- porous evaporator medium 28 may be prepared together with the separating element 30, for example, characterized in that the provided for the construction of the porous evaporator medium 28, the chip-like or wire-like material is applied to a metal plate blank and then subjected to a sintering process. It is thus created a solid and stable composite, which can receive its final peripheral shape, such as a circular shape, only later in a punching process.
- FIG. 2 A modified embodiment is in Fig. 2 shown.
- the separating element 30 no longer has a planar, plate-like configuration, but a shell-like configuration with a bottom region 50 and a peripheral wall region 52.
- the porous evaporator medium 28 is fitted, so that its outer peripheral edge 46 is covered by the separating element 30.
- the heating coil 38 is again located on the rear side of the separating element 30, followed by the insulating material 40 and the holding plate 42.
- the separating element 30 is now held between this holding plate 42 or the securing ring 44 and a radially inwardly extending projection 54 of the component 24.
- the assembly comprising the porous evaporator medium 28 and the separator 30 may be manufactured as described above.
- the connection between the porous evaporator medium 28 and the separating element 30 can be realized for example by sintering.
- the above-mentioned compression of the porous evaporator medium 28 in the separating element 30 can contribute to the fixation, since this can lead to an expansion of the evaporator medium 28 radially outward and thus pinching on the separating element 30.
- FIGS. 3 and 4 show with their essential components. It can be seen again the shell-like designed partition member 30 with its bottom portion 50 and its peripheral wall portion 52. In the nozzle 34, the fuel line 36 is inserted. At the bottom region 50, an example circular depression 58 is formed. In this, a deflection element 60 is added to the rear side 32 of the porous evaporator medium 28. This is opposite to an outlet end 62 of the fuel line 36 and ensures that the liquid fuel emerging there can not enter the porous evaporator medium 28 directly in this area. Rather, the initially still liquid fuel is deflected to the outside and thus pre-distributed over a larger surface area of the back of the porous evaporator medium 28.
- channels 64 are formed on the bottom region 50, which further direct the liquid fuel outwardly toward the outer edge 46 of the porous evaporator medium and thus provide for a faster and more uniform pre-distribution before the liquid fuel enters the porous evaporator medium 28 at the rear 32 thereof.
- the porous evaporator medium 28 is multi-layered, here, for example, three layers, with layers 66, 68 and 70 is constructed.
- the ply 66 provides the backside 32 while the ply 70 provides the frontal 56.
- the layer 66 may be formed so that it very quickly absorbs liquid fuel and makes a coarse distribution in its volume range.
- the then somewhat finely pored layer 68 for example, can make the liquid fuel already predistributed to it from the layer 66 uniform, while the layer 70 can also be optimized with regard to the thermal loads that occur.
- FIG. 5 Another variation is in Fig. 5 shown.
- the fuel line 36 is introduced into the bottom region 50 or the connecting piece 34 provided thereon.
- the fuel line 36 passes through not only an inlet opening 72 on the separating element 30, but also a corresponding opening in the porous evaporator medium 28 completely.
- the fuel line 36 thus protrudes beyond the front 56 of the porous evaporator medium 28 in the direction of the mixing chamber 16 and holds by a disk 74 fixed thereto the porous
- the disk 74 also serves to forcibly force an improved distribution of the liquid fuel emerging from the fuel line 36 and entering the volume range of the porous evaporator medium 28 directly, since this is not directly in the range the fuel line 36 can emerge from the porous evaporator medium 28 again.
- the fuel line 36 has a plurality of radially outwardly extending passage openings 76, the liquid supplied by a central opening 78 liquid in the discharge end region 62 directly into the under pressure lead against the outside of the fuel line 36 held porous evaporator medium 28. It will be understood that the central opening 78 is sealed at the end of the fuel line 36 which is engaged in the mixing chamber 16.
- the fuel line 36 at its discharge end 62 has a blade-like edge 80. This is held under pressure against the back 32 of the porous evaporator medium 28. In this way, too, it is ensured that the entire fuel supplied via the central opening 78 of the fuel line 36 enters the volume region of the porous evaporator medium 28 and does not run out again at the rear in the area of the junction. This is further prevented by the fact that, as already stated above, substantially the entire rear side 32 is covered by the separating element 30, namely the bottom region 50 thereof.
- the solid bond between the fuel line 36 and the separator 30 in the region of the nozzle 34 can be done for example by soldering or by clamping fit.
- a baffle 74 opposite.
- FIG. 7 Figure 3 is an axial view of a porous evaporator medium 28 as may be employed in the previously described embodiments. It can be seen with respect to the center of the here circular shaped contour of the porous evaporator medium 28 offset fuel injection in the fuel line 36. Next can be seen under the fuel inlet an approximately U-shaped formation 82 in the porous evaporator medium 28, which the flow behavior of the fuel in the porous evaporator medium 28th affected. This formation 82 can contribute, for example, by locally compacting the porous evaporator medium to build up a flow barrier, that is to say a region with increased flow resistance.
- This depression 88 serves to pre-distribute the fuel before it is picked up in the volume range of the porous evaporator medium 28, ie, similar to the embodiment according to FIGS FIGS. 3 and 4 to provide a channel arrangement that allows a rough pre-distribution of the fuel.
- the present invention provides an evaporator arrangement, which ensures that the fuel or hydrocarbon to be vaporized reaches the volume region of the porous evaporator medium as uniformly as possible, can practically no longer emerge from this volume region at the rear side facing away from a mixing chamber and at the front side facing a mixing chamber as uniformly as possible and with as efficient utilization as possible the entire surface of this front can evaporate.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fuel Cell (AREA)
- Hydrogen, Water And Hydrids (AREA)
Description
Die vorliegende Erfindung betrifft eine Verdampferanordnung zur Abgabe eines Brennstoffdampfes in eine Mischkammer gemäß dem Oberbegriff des Anspruchs 1.The present invention relates to an evaporator arrangement for delivering a fuel vapor into a mixing chamber according to the preamble of claim 1.
Derartige Verdampferanordnungen werden beispielsweise in brennstoffbetriebenen Heizgeräten für Kraftfahrzeuge eingesetzt, wobei diese Heizgeräte wiederum als Zuheizer oder als Standheizung genutzt werden können. Durch den zu verdampfenden Brennstoff und in eine Mischkammer ebenfalls einzuleitende Verbrennungsluft wird ein Gemisch aus Brennstoffdampf und Verbrennungsluft erzeugt, das gezündet und zur Wärmeerzeugung verbrannt werden kann. Gleichwohl werden derartige Verdampferanordnungen auch in so genannten Reformern genutzt, um in einer Mischkammer ein Gemisch aus verdampftem Brennstoff, also verdampftem Kohlenwasserstoff, und sonstigem Mischmaterial, beispielsweise auch Luft oder Wasserdampf, zu erzeugen. Dieses Gemisch wird dann zu einer Katalysatoranordnung geleitet, um durch katalytische Reaktion ein wasserstoffhaltiges Gasgemisch zu erzeugen.Such evaporator arrangements are used for example in fuel-operated heaters for motor vehicles, these heaters can be used in turn as a heater or as a heater. By the fuel to be evaporated and in a mixing chamber also to be introduced combustion air, a mixture of fuel vapor and combustion air is generated, which can be ignited and burned to generate heat. However, such evaporator arrangements are also used in so-called reformers to produce in a mixing chamber, a mixture of vaporized fuel, ie vaporized hydrocarbon, and other mixed material, for example, air or water vapor. This mixture is then passed to a catalyst assembly to produce a hydrogen-containing gas mixture by catalytic reaction.
Bei Verdampferanordnungen bzw. diese nutzenden Brennern oder/und Reformern besteht grundsätzlich das Problem, dass durch nicht optimal ablaufende Brennstoffverdampfung bzw. Brennstoffeinspeisung in die Mischkammer eine Beeinträchtigung sowohl des Verdampfungsbetriebs an sich als auch beispielsweise des Verbrennungsbetriebs erzeugt werden kann. So hat eine ungleichmäßige Einleitung des zu verdampfenden flüssigen Brennstoffs in ein poröses Verdampfermedium zur Folge, dass eine entsprechend ungleichmäßige Brennstoffabdampfung zur Mischkammer hin auftreten wird. Durch die Übersättigung bestimmter Bereiche des porösen Verdampfermediums mit flüssigem Brennstoff wird die Gefahr des Austretens von Brennstofftropfen aus dem porösen Verdampfermedium verstärkt. Tritt dies vor allem in dem Bereich zwischen dem porösen Verdampfermedium und der diesem zugeordneten Heizeinrichtung auf, so kann dies zur Krackbildung, also zur Bildung von Ablagerungen zwischen dem Verdampfermedium und der Heizeinrichtung, und dem Loslösen und Abheben des Verdampfermediums führen. Weiterhin besteht die Gefahr, dass der im Allgemeinen im flüssigen Zustand leicht benetzende Brennstoff sich bei Austritt aus dem porösen Verdampfermedium entlang von Oberflächen bewegt und auch in dem Bereich eines zur Heranförderung von Luft dienenden Gebläses gelangen kann. Das punktuelle Einleiten des flüssigen Brennstoffs in das poröse Verdampfermedium zieht weiterhin die Gefahr nach sich, dass eine sehr ungleichmäßige Brennstoffverteilung durch Schwerkrafteinwirkung einerseits und durch Kapillarförderwirkung andererseits auftritt und somit nicht die gesamte Oberfläche des Verdampfermediums zur Brennstoffabdampfung genutzt werden kann, was aber für eine definierte Gemischbildung erforderlich sein kann.In the case of evaporator arrangements or burners or / and reformers that use them, there is basically the problem that an impairment of both the evaporation operation per se and, for example, the combustion operation can be produced by not optimally running fuel evaporation or fuel feed into the mixing chamber. Thus, uneven introduction of the liquid fuel to be evaporated into a porous evaporator medium will result in correspondingly uneven fuel vaporization to the mixing chamber. Due to the supersaturation of certain areas of the porous evaporator medium with liquid fuel, the risk of leakage amplified by fuel droplets from the porous evaporator medium. If this occurs especially in the region between the porous evaporator medium and the associated heating device, this can lead to cracking, that is to the formation of deposits between the evaporator medium and the heating device, and the detachment and lifting of the evaporator medium. Furthermore, there is a risk that the fuel, which generally wets slightly in the liquid state, may move along surfaces as it exits the porous evaporator medium and may also get into the area of a fan for conveying air past the fan. The selective introduction of the liquid fuel in the porous evaporator medium continues to run the risk that a very nonuniform fuel distribution by gravity on the one hand and by capillary action on the other hand occurs and thus not the entire surface of the evaporator medium can be used for Brennstoffabdampfung, but for a defined mixture formation may be required.
Eine Verdampferanordnung gemäß dem Oberbegriff des Anspruchs 1 ist aus der
Die
Die
Die
Es ist die Aufgabe der vorliegenden Erfindung, eine Verdampferanordnung zur Abgabe eines Brennstoffdampfes in eine Mischkammer vorzusehen, welche ein verbessertes Verdampfungsverhalten aufweist.It is the object of the present invention to provide an evaporator arrangement for delivering a fuel vapor into a mixing chamber, which has an improved evaporation behavior.
Erfindungsgemäß wird diese Aufgabe gelöst durch eine Verdampferanordnung zur Abgabe eines Brennstoffdampfes in eine Mischkammer gemäß Anspruch 1. Diese umfasst ein poröses Verdampfermedium, eine flüssigen Brennstoff zu dem porösen Verdampfermedium führende Leitungsanordnung und eine Heizeinrichtung an einer von der Mischkammer abgewandten oder abgewandt zu positionierenden Rückseite des porösen Verdampfermediums, wobei zwischen dem porösen Verdampfermedium und der Heizeinrichtung ein einen direkten Kontakt zwischen diesen unterbindendes Trennelement angeordnet ist.This object is achieved by an evaporator arrangement for emitting a fuel vapor into a mixing chamber according to claim 1. This comprises a porous evaporator medium, a liquid fuel leading to the porous evaporator medium line arrangement and a heater on a side facing away from the mixing chamber or facing away from the back of the porous Evaporator medium, wherein between the porous evaporator medium and the heater is arranged a direct contact between these suppressive separating element.
Um die Brennstoffverteilung im porösen Verdampfermedium und somit auch die Brennstoffabdampfung aus diesem weiter beeinflussen zu können, ist in dem porösen Verdampfermedium eine Brennstoffströmungsführungsformation gebildet. Eine derartige Brennstoffströmungsführungsformation umfasst verdichtete Bereiche oder Aussparungsbereiche im porösen Verdampfermedium, welche dann ein anderes Kapillarströmungsverhalten aufweisen bzw. lokal das Auftreten einer Kapillarströmung unterbinden und somit Barrieren für den Brennstoffstrom erzeugen.To the fuel distribution in the porous evaporator medium and thus also To further influence the fuel evaporation from this, a fuel flow guide formation is formed in the porous evaporator medium. Such a fuel flow guide formation comprises compressed regions or recessed regions in the porous evaporator medium, which then have a different capillary flow behavior or locally prevent the occurrence of capillary flow and thus create barriers for the fuel flow.
Wesentlich ist bei der vorliegenden Erfindung, dass zwischen dem den flüssigen Brennstoff aufnehmenden und den Brennstoffdampf abgebenden porösen Verdampfermedium und der diesem zugeordneten Heizeinrichtung ein Trennelement liegt, das nicht nur eine vergleichmäßigte Wärmeeinleitung in das poröse Verdampfermedium sicherstellt, sondern auch dafür sorgt, dass ein Austritt von Brennstoffdampf an der Rückseite des porösen Verdampfermediums ebenso verhindert werden kann, wie das Austreten von flüssigem Brennstoff an der Rückseite des porösen Verdampfermediums.It is essential in the present invention that between the liquid fuel receiving and the fuel vapor emitting porous evaporator medium and its associated heater is a separator that not only ensures a uniform heat input into the porous evaporator medium, but also ensures that an exit from Fuel vapor at the back of the porous evaporator medium can be prevented as well as the leakage of liquid fuel at the back of the porous evaporator medium.
Es sei hier noch einmal darauf hingewiesen, dass als "Brennstoffe" im Sinne der vorliegenden Erfindung allgemein flüssige Kohlenwasserstoffe, wie z.B. Benzin, Diesel, Biodiesel und dergleichen, betrachtet werden, die beispielsweise zur Verbrennung nutzbar sind, gleichwohl aber auch dazu nutzbar sind, in einem Reformer zur Wasserstofferzeugung für ein Brennstoffzellensystem umgesetzt zu werden.It should again be noted that as "fuels" in the context of the present invention generally liquid hydrocarbons, such. Gasoline, diesel, biodiesel and the like, are considered, for example, are available for combustion, but nevertheless also be used to be implemented in a reformer for hydrogen production for a fuel cell system.
Um die vorangehend angesprochene verbesserte Wärmeeinleitung bzw. Wärmeverteilung weiter unterstützen zu können, wird vorgeschlagen, dass das Trennelement aus gut Wärme leitendem Material, vorzugsweise Metall, gebildet ist.In order to be able to further support the above-mentioned improved heat introduction or distribution, it is proposed that the separating element be formed from a material that conducts heat well, preferably metal.
Gemäß einem besonders vorteilhaften Aspekt kann vorgesehen sein, dass das Trennelement im Wesentlichen die ganze Rückseite des porösen Verdampfermediums überdeckt. Somit wird sichergestellt, dass praktisch das gesamte poröse Verdampfermedium thermisch kontaktiert wird und dass über die gesamte Rückseite das Austreten von Brennstoff oder Brennstoffdampf unterbunden werden kann.According to a particularly advantageous aspect, it can be provided that the separating element substantially the entire back of the porous evaporator medium covered. This ensures that practically the entire porous evaporator medium is thermally contacted and that over the entire rear side the escape of fuel or fuel vapor can be prevented.
Um auch am Außenrandbereich des porösen Verdampfermediums sicherzustellen, dass flüssiger Brennstoff dort nicht aus dem porösen Verdampfermedium austreten kann, wird vorgeschlagen, dass das Trennelement einen Außenrandbereich des porösen Verdampfermediums übergreift. Dies kann beispielsweise dadurch erfolgen, dass bei flächenartiger Ausgestaltung des porösen Verdampfermediums das Trennelement schalenartig ausgestaltet ist und mit einem Schalenboden an der Rückseite des porösen Verdampfermediums angeordnet ist, während der Schalenrand dann den Außenrandbereich des porösen Verdampfermediums übergreift, d.h. diesen Außenrandbereich umgibt bzw. dort anliegt.In order to ensure at the outer edge region of the porous evaporator medium that liquid fuel can not escape from the porous evaporator medium there, it is proposed that the separating element overlap an outer edge region of the porous evaporator medium. This can be done, for example, in that, in the case of a planar design of the porous evaporator medium, the separating element is designed like a shell and is arranged with a dish bottom at the back of the porous evaporator medium, while the shell edge then overlaps the outer edge region of the porous evaporator medium, i. surrounds this outer edge region or rests there.
Zur Brennstoffeinleitung in das poröse Verdampfermedium kann das Trennelement eine Brennstoffeinleitöffnung für die Leitungsanordnung aufweisen.For fuel introduction into the porous evaporator medium, the separating element may have a fuel introduction opening for the line arrangement.
Ein weiter verbessertes Brennstoffverteilungsverhalten kann dadurch erlangt werden, dass an dem Trennelement von der Brennstoffeinleitöffnung ausgehend eine Brennstoffverteilungskanalanordnung vorgesehen ist.A further improved fuel distribution behavior can be obtained by providing a fuel distribution channel arrangement on the separating element starting from the fuel introduction opening.
Um insbesondere in demjenigen Bereich, in welchem das poröse Verdampfermedium flüssigen Brennstoff von der Brennstoffleitungsanordnung aufnimmt, das Austreten von flüssigem Brennstoff zu vermeiden, wird vorgeschlagen, dass die Leitungsanordnung durch die Brennstoffeinleitöffnung hindurchgreift und mit einem Abgabeende unter Druck gegen das poröse Verdampfermedium gehalten ist.In order to avoid leakage of liquid fuel, particularly in the region in which the porous evaporator medium receives liquid fuel from the fuel line arrangement, it is proposed that the line arrangement penetrate through the fuel introduction opening and be held under pressure against the porous evaporator medium with a discharge end.
Weiterhin wird unter Berücksichtigung der Einbausituation und der dabei auch auf den flüssigen Brennstoff im porösen Verdampfermedium einwirkenden Schwerkraft vorgeschlagen, dass das poröse Verdampfermedium eine Umfangskontur aufweist, die an eine Umfangskontur einer Mischkammer, vorzugsweise eines Bodenbereichs derselben, angepasst ist, und dass die Leitungsanordnung außermittig an das poröse Verdampfermedium herangeführt ist.Furthermore, taking into account the installation situation and thereby also acting on the liquid fuel in the porous evaporator medium Gravity proposed that the porous evaporator medium has a peripheral contour, which is adapted to a peripheral contour of a mixing chamber, preferably a bottom portion thereof, and that the line arrangement is introduced eccentrically to the porous evaporator medium.
Weiterhin kann das Verteilungsverhalten des Brennstoffs im porösen Verdampfermedium zur Erlangung einer verbesserten Brennstoffabdampfung dadurch beeinflusst werden, dass das poröse Verdampfermedium mehrlagig aufgebaut ist und die Lagen wenigstens zum Teil ein unterschiedliches Brennstoffleitungsvermögen aufweisen.Furthermore, the distribution behavior of the fuel in the porous evaporator medium to achieve improved Brennstoffabdampfung can be influenced by the fact that the porous evaporator medium is constructed in multiple layers and the layers at least partially have a different fuel conductivities.
Die vorliegende Erfindung betrifft ferner ein Fahrzeugheizgerät, umfassend eine erfindungsgemäße Verdampfungsanordnung.The present invention further relates to a vehicle heater comprising an evaporation arrangement according to the invention.
Weiter betrifft die vorliegende Erfindung eine Reformeranordnung mit einer erfindungsgemäßen Verdampferanordnung, um, wie angesprochen, ein Gemisch aus Brennstoffdampf, also Kohlenwasserstoffdampf, und Luft oder/und Wasserdampf oder/und rückgeführten Verbrennungs- oder Brennstoffzellenabgasen zu erzeugen.Further, the present invention relates to a reformer assembly with an evaporator assembly according to the invention, as mentioned, to produce a mixture of fuel vapor, so hydrocarbon vapor, and air and / or water vapor and / or recirculated combustion or fuel cell exhaust gases.
Die vorliegende Erfindung wird nachfolgend mit Bezug auf die beiliegenden Zeichnungen anhand bevorzugter Ausgestaltungsformen detailliert beschrieben. Es zeigt:
- Fig. 1
- eine Längsschnittansicht der wesentlichen Komponenten einer Verdampferanordnung;
- Fig. 2
- eine der
Fig. 1 entsprechende Ansicht einer alternativen Ausge- staltungsform; - Fig. 3
- eine Detailansicht des mit einem schalenartigen Trennelement zusammenwirkenden porösen Verdampfermediums einer weiteren alternativen Ausgestaltungsform;
- Fig. 4
- das schalenartige Trennelement der
Fig. 3 in perspektivischer An- sicht; - Fig. 5
- eine der
Fig. 3 entsprechende Darstellung einer weiteren alterna- tiven Ausgestaltungsform; - Fig. 6
- eine der
Fig. 3 entsprechende Darstellung einer erfindungsgemäßen Ausgestaltungsform; - Fig. 7
- eine Draufsicht auf ein poröses Verdampfermedium, die das Brennstoffverteilungsverhalten darstellt.
- Fig. 1
- a longitudinal sectional view of the essential components of an evaporator assembly;
- Fig. 2
- one of the
Fig. 1 corresponding view of an alternative embodiment; - Fig. 3
- a detailed view of the with a shell-like separator cooperating porous evaporator medium of a further alternative embodiment;
- Fig. 4
- the shell-like separating element of
Fig. 3 in perspective view; - Fig. 5
- one of the
Fig. 3 corresponding representation of a further alternative embodiment; - Fig. 6
- one of the
Fig. 3 corresponding representation of an embodiment of the invention; - Fig. 7
- a plan view of a porous evaporator medium, which represents the fuel distribution behavior.
In
Der Umfangsbereich 12 wird bei dem in
An der vom porösen Verdampfermedium 28 abgewandten Seite des Trennelements 30 ist eine in Form einer Heizwendel 38 ausgestaltete Heizeinrichtung vorgesehen, die das Trennelement 30 in einem möglichst großen Flächenbereich berührt und somit zur möglichst gleichmäßigen Erwärmung des Trennelements 30 beiträgt. Dieses Trennelement 30 überträgt die aufgenommene Wärme in noch weiter vergleichmäßigter Art und Weise auf die gesamte Rückseite 32 des porösen Verdampfermediums 28. Um thermische Verluste zu vermeiden, ist die Heizwendel 38 an ihrer vom Trennelement 30 abgewandten Seite durch Isolationsmaterial 40 überdeckt, das wiederum durch eine Halteplatte 42 und einen Sicherungsring 44 an dem Bauteil 24 festgelegt ist. Somit ist auch die Heizwendel 38 zwischen dem Isoliermaterial 40 und dem Trennelement 30 in Richtung der Längsachse L arretiert.On the side facing away from the
Durch das Bereitstellen des Trennelements 30 an der Rückseite 32 des porösen Verdampfermediums 28 wird sichergestellt, dass der in dieses eingeleitete flüssige Brennstoff nur in Richtung zur Mischkammer 16 hin abdampfen kann. Eine Brennstoffabdampfung nach hinten, also in Richtung zur Heizwendel 38, ist nicht möglich, was zur Folge hat, dass in diesem Bereich auch keine Ablagerungen erzeugt werden können. Gleichzeitig ist auch die Gefahr des Austretens von flüssigem Brennstoff an der Rückseite 32 des porösen Verdampfermediums 28 vollständig unterbunden. Hierzu trägt das das poröse Verdampfermedium 28 vollständig überdeckende Trennelement 30 bei. Weiterhin trägt dazu bei, dass durch Zusammenwirken der Leitung 36 mit dem Stutzen 34 auch in diesem Bereich Brennstoff nicht in flüssiger Form austreten kann. Im Randbereich des porösen Verdampfermediums 28 bzw. des Trennelements 30 wird der Austritt flüssigen Brennstoffs bzw. eines Brennstoffdampfs dadurch unterbunden, dass dieser Randbereich erstens durch das Bauteil 24 vollständig umgriffen ist und somit auch in Zusammenwirkung mit dem Umfangswandungsbauteil 20 ein praktisch flüssigkeits- und dampfdichter Abschluss des porösen Verdampfermediums 28 nach außen hin vorgesehen ist. Dies kann weiter noch dadurch unterstützt werden, dass das poröse Verdampfermedium 28 zusammen mit dem Trennelement 30 zwischen dem Absatz 26 und dem Umfangswandungsbauteil 28 festgeklemmt ist und somit dort verdichtet ist. In diesem Falle ist der Austritt sowohl flüssigen als auch dampfförmigen Brennstoffs über den Außenumfangsrand 46 des porösen Verdampfermediums 28 praktisch nicht möglich.By providing the separating
Man erkennt in
Das in
Eine abgewandelte Ausgestaltungsform ist in
Auch bei dieser Ausgestaltungsform ist also dafür gesorgt, dass der einmal in den Volumenbereich des porösen Verdampfermediums 28 eingeleitete flüssige Brennstoff nur in Richtung zur Mischkammer 16 austreten kann, nicht jedoch an der Rückseite 32 aus dem porösen Verdampfermedium 28 herausgelangen kann.In this embodiment as well, it is thus ensured that the liquid fuel once introduced into the volume region of the
Die das poröse Verdampfermedium 28 und das Trennelement 30 umfassende Baugruppe kann bei dieser Ausgestaltungsform selbstverständlich so hergestellt werden, wie vorangehend beschrieben. Grundsätzlich ist es aber auch möglich, das bereits vorbereitete poröse Verdampfermedium mit seiner vorgesehenen Umfangskontur in das schalenartige Trennelement 30 einzulegen und durch Verdichten in seinen betriebsfertigen Zustand zu bringen, d.h. die gewünschte Endporosität herzustellen. Die Verbindung zwischen dem porösen Verdampfermedium 28 und dem Trennelement 30 kann beispielsweise durch Einsintern realisiert werden. Grundsätzlich ist es auch denkbar, das poröse Verdampfermedium 28 durch Übergreifen desselben mit dem Umfangswandungsbereich 52 des Trennelements 30 auch an der der Mischkammer 16 zugewandten Vorderseite 56 zu halten. Auch das vorangehend angesprochene Verdichten des porösen Verdampfermediums 28 im Trennelement 30 kann zur Fixierung beitragen, da dies eine Ausdehnung des Verdampfermediums 28 nach radial außen und somit ein Einklemmen am Trennelement 30 nach sich ziehen kann.Of course, in this embodiment, the assembly comprising the
Eine weitere Abwandlung ist in den
Man erkennt in
Eine weitere Abwandlung ist in
Um bei dieser Ausgestaltungsform eine zuverlässige Einleitung des flüssigen Brennstoffs in den Volumenbereich des porösen Verdampfermediums 28 zu erlangen, weist die Brennstoffleitung 36 mehrere nach radial außen greifende Durchtrittsöffnungen 76 auf, die den von einer Zentralöffnung 78 herangeförderten flüssigen Brennstoff im Austrittsendbereich 62 direkt in das unter Druck gegen die Außenseite der Brennstoffleitung 36 gehaltene poröse Verdampfermedium 28 führen. Es ist selbstverständlich, dass die zentrale Öffnung 78 an dem in die Mischkammer 16 greifenden Ende der Brennstoffleitung 36 abgedichtet bzw. abgeschlossen ist.In order to obtain a reliable introduction of the liquid fuel into the volume range of the
Bei der in
In
Durch die vorliegende Erfindung ist eine Verdampferanordnung bereitgestellt, die sicherstellt, dass der zu verdampfende Brennstoff bzw. Kohlenwasserstoff möglichst gleichmäßig in den Volumenbereich des porösen Verdampfermediums gelangt, aus diesem Volumenbereich an der von einer Mischkammer abgewandten Rückseite praktisch nicht mehr austreten kann und an der einer Mischkammer zugewandten Vorderseite möglichst gleichmäßig und unter möglichst effizienter Ausnutzung der gesamten Oberfläche dieser Vorderseite abdampfen kann.The present invention provides an evaporator arrangement, which ensures that the fuel or hydrocarbon to be vaporized reaches the volume region of the porous evaporator medium as uniformly as possible, can practically no longer emerge from this volume region at the rear side facing away from a mixing chamber and at the front side facing a mixing chamber as uniformly as possible and with as efficient utilization as possible the entire surface of this front can evaporate.
Es sei darauf hingewiesen, dass selbstverständlich die in den verschiedenen dargestellten Ausgestaltungsvarianten gezeigten Aspekte miteinander kombiniert werden können. So könnten selbstverständlich auch bei den Ausgestaltungsformen gemäß den
Claims (11)
- Evaporator arrangement for discharging fuel vapour into a mixing chamber, comprising a porous evaporator medium (28), a conduit arrangement (36) carrying liquid fuel to the porous evaporator medium (28) and a heating device (38) at a back side (32) of the porous evaporator medium (28) which is or may be positioned facing away from the mixing chamber (16), a separator (30) being arranged between the porous evaporator medium (28) and the heating device (38) preventing direct contact between the latter, characterized in a fuel flow guidance formation (82, 88) being formed in the porous evaporator medium (28) by means of parts of the porous evaporator medium (28) which are compressed by stamping.
- Evaporator arrangement according to claim 1,
characterized in the separator (30) being made of a material with good heat conductance, preferably of metal. - Evaporator arrangement according to claim 1 or 2,
characterized in the separator (30) covering substantially the complete back side (32) of the porous evaporator medium (28). - Evaporator arrangement according to claim 1 to 3,
characterized in the separator (30) overlapping an outer edge region (46) of the porous evaporator medium (28). - Evaporator arrangement according to claim 1 to 4,
characterized in the separator (30) comprising a fuel insertion aperture (72) for the conduit arrangement (36). - Evaporator arrangement according to claim 5,
characterized in a fuel distribution channel arrangement (64), extending from the fuel insertion aperture (72), being provided at the separator (30). - Evaporator arrangement according to claim 5 or 6,
characterized in the conduit arrangement (36) extending through the fuel insertion aperture (72) and being held under pressure against the porous evaporator medium (28) with one discharge end (62). - Evaporator arrangement according to claim 1 to 7,
characterized in the porous evaporator medium (28) comprising a circumferential outline matching a circumferential outline of a mixing chamber (16), preferably of a bottom part (14) of the latter, and in the conduit arrangement (36) being eccentrically directed towards the porous evaporator medium (28). - Evaporator arrangement according to claim 1 to 8,
characterized in the porous evaporator medium (28) being multilayered, the layers (66, 68, 70) at least partly having different fuel supply capacities. - Vehicle heating device, comprising an evaporator arrangement according to one of claims 1 to 9.
- Reformer arrangement, comprising an evaporator arrangement according to one of claims 1 to 9.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102004020129 | 2004-04-26 | ||
DE200410020129 DE102004020129B3 (en) | 2004-04-26 | 2004-04-26 | Evaporator set-up e.g. for fuel powered heater in motor vehicles, has porous evaporator medium and liquid fuel line arrangement leading to porous evaporator medium with heating mechanism at back of porous evaporator medium positioned away |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1598595A1 EP1598595A1 (en) | 2005-11-23 |
EP1598595B1 true EP1598595B1 (en) | 2010-09-08 |
Family
ID=34801988
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP20050006431 Not-in-force EP1598595B1 (en) | 2004-04-26 | 2005-03-23 | Evaporator arrangement |
Country Status (2)
Country | Link |
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EP (1) | EP1598595B1 (en) |
DE (2) | DE102004020129B3 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102014005173A1 (en) * | 2014-04-08 | 2015-10-08 | Webasto SE | Method for producing an evaporator arrangement for an evaporator burner |
RU2580751C1 (en) * | 2013-10-14 | 2016-04-10 | Эбершпехер Клаймит Контрол Системз Гмбх Унд Ко. Кг | Bottom unit for combustion chamber unit of vaporising oil burner and combustion chamber unit of vaporising oil burner |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004057757A1 (en) * | 2004-11-30 | 2006-06-01 | J. Eberspächer GmbH & Co. KG | Evaporator for vehicle heater or reformer has at least part of porous evaporator medium sintered into bowl-shaped carrier |
EP1662199B1 (en) | 2004-11-30 | 2017-03-01 | Eberspächer Climate Control Systems GmbH & Co. KG | Evaporator and process for fabricating same |
DE102005020148A1 (en) * | 2005-04-29 | 2006-11-09 | J. Eberspächer GmbH & Co. KG | Evaporator arrangement, in particular for a vehicle heater or a reformer |
DE102005045067A1 (en) * | 2005-09-21 | 2007-03-22 | J. Eberspächer GmbH & Co. KG | Reformer for preparing hydrogen for a vehicle fuel cell comprises a vaporizing arrangement for producing a hydrocarbon/mixed material mixture and having a vaporizer housing with a base wall and a peripheral wall |
DE102007053488A1 (en) | 2007-11-09 | 2009-05-14 | J. Eberspächer GmbH & Co. KG | Evaporator assembly, in particular for an evaporator burner of a vehicle heater, and method for its preparation |
DE102011005103B4 (en) * | 2011-03-04 | 2015-04-02 | Eberspächer Climate Control Systems GmbH & Co. KG | Combustion chamber assembly for an evaporator burner |
DE102011050368A1 (en) | 2011-05-15 | 2012-11-15 | Webasto Ag | evaporator assembly |
DE102012101577A1 (en) | 2012-02-27 | 2013-08-29 | Webasto Ag | Mobile liquid fueled heater |
DE102012101576A1 (en) * | 2012-02-27 | 2013-08-29 | Webasto Ag | Evaporator burner with cover for a mobile heater |
DE102012101580B4 (en) | 2012-02-27 | 2020-10-29 | Webasto Ag | Mobile heating device operated with liquid fuel |
DE102013220652B4 (en) * | 2013-10-14 | 2015-07-02 | Eberspächer Climate Control Systems GmbH & Co. KG | Combustion chamber assembly, in particular for an evaporator burner, in particular for a vehicle heater |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0619212B2 (en) * | 1986-07-08 | 1994-03-16 | いすゞ自動車株式会社 | Combustor |
DE3914611C2 (en) | 1988-06-09 | 1996-09-26 | Webasto Ag Fahrzeugtechnik | Evaporation burner for a heater operated with liquid fuel |
DE3900438A1 (en) | 1989-01-10 | 1990-07-12 | Webasto Ag Fahrzeugtechnik | HEATER, ESPECIALLY VEHICLE HEATER |
DE4003090C1 (en) * | 1990-02-02 | 1991-06-13 | Webasto Ag Fahrzeugtechnik, 8035 Stockdorf, De | |
DE4401799C1 (en) * | 1994-01-22 | 1995-06-14 | Webasto Thermosysteme Gmbh | Evaporator burner for heating appts |
DE10130638A1 (en) * | 2001-06-26 | 2003-01-02 | Eberspaecher J Gmbh & Co | Vaporizer burner used in heating devices of motor vehicles comprises an ignition heating element igniting fuel vapor, and a vaporizer heating element influencing the vaporizing characteristics of a vaporizer medium |
DE10209967C5 (en) * | 2002-03-07 | 2009-01-29 | J. Eberspächer GmbH & Co. KG | Evaporator element for an evaporator burner |
DE10325574A1 (en) | 2003-06-05 | 2004-12-30 | J. Eberspächer GmbH & Co. KG | Combustion chamber arrangement for an evaporator burner, in particular for a vehicle heater |
-
2004
- 2004-04-26 DE DE200410020129 patent/DE102004020129B3/en not_active Expired - Fee Related
-
2005
- 2005-03-23 EP EP20050006431 patent/EP1598595B1/en not_active Not-in-force
- 2005-03-23 DE DE200550010200 patent/DE502005010200D1/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2580751C1 (en) * | 2013-10-14 | 2016-04-10 | Эбершпехер Клаймит Контрол Системз Гмбх Унд Ко. Кг | Bottom unit for combustion chamber unit of vaporising oil burner and combustion chamber unit of vaporising oil burner |
DE102014005173A1 (en) * | 2014-04-08 | 2015-10-08 | Webasto SE | Method for producing an evaporator arrangement for an evaporator burner |
Also Published As
Publication number | Publication date |
---|---|
EP1598595A1 (en) | 2005-11-23 |
DE502005010200D1 (en) | 2010-10-21 |
DE102004020129B3 (en) | 2005-08-25 |
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