EP4023938B1 - Burner arrangement for a pre-mix burner - Google Patents
Burner arrangement for a pre-mix burner Download PDFInfo
- Publication number
- EP4023938B1 EP4023938B1 EP21214581.7A EP21214581A EP4023938B1 EP 4023938 B1 EP4023938 B1 EP 4023938B1 EP 21214581 A EP21214581 A EP 21214581A EP 4023938 B1 EP4023938 B1 EP 4023938B1
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- European Patent Office
- Prior art keywords
- combustion chamber
- burner
- mixture
- combustion
- outlet
- 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.)
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- UHZZMRAGKVHANO-UHFFFAOYSA-M chlormequat chloride Chemical compound [Cl-].C[N+](C)(C)CCCl UHZZMRAGKVHANO-UHFFFAOYSA-M 0.000 title 1
- 238000002485 combustion reaction Methods 0.000 claims description 49
- 239000000203 mixture Substances 0.000 claims description 26
- 239000000567 combustion gas Substances 0.000 claims description 16
- 239000002737 fuel gas Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000007789 gas Substances 0.000 description 8
- 239000003344 environmental pollutant Substances 0.000 description 7
- 231100000719 pollutant Toxicity 0.000 description 7
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000004323 axial length Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000008236 heating water Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/02—Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C9/00—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
- F23C9/006—Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber the recirculation taking place in the combustion chamber
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C2202/00—Fluegas recirculation
- F23C2202/10—Premixing fluegas with fuel and combustion air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
- F23C2900/09002—Specific devices inducing or forcing flue gas recirculation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN A CARRIER GAS OR AIR
- F23C2900/00—Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
- F23C2900/9901—Combustion process using hydrogen, hydrogen peroxide water or brown gas as fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2203/00—Gaseous fuel burners
- F23D2203/10—Flame diffusing means
- F23D2203/101—Flame diffusing means characterised by surface shape
- F23D2203/1012—Flame diffusing means characterised by surface shape tubular
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
- F23D2900/14—Special features of gas burners
- F23D2900/14241—Post-mixing with swirling means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
- F23D2900/14—Special features of gas burners
- F23D2900/14701—Swirling means inside the mixing tube or chamber to improve premixing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D2900/00—Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
- F23D2900/31019—Mixing tubes and burner heads
Definitions
- the invention relates to a heater with a combustion chamber and a burner arrangement with a premix burner.
- Modern heaters are operated with a mixture of air and fuel gas.
- air mixed with a suitable proportion of fuel gas is conveyed by a fan into a burner which has outlet openings for the mixture, which is burned in a combustion chamber after exiting the burner.
- the mixture is regulated very precisely to avoid the formation of pollutants so that combustion can take place as completely as possible.
- the resulting combustion gases contain only a little oxygen, but depending on the fuel gas, water vapor, carbon dioxide and mainly nitrogen.
- Small quantities of nitrogen oxides, hereinafter referred to as NOX can also be formed during combustion, which is undesirable but not entirely avoidable, especially at high combustion temperatures.
- Particularly high combustion temperatures arise with certain fuel gases, including e.g. B. a large proportion of hydrogen in the fuel gas, as planned in the future, can increase the combustion temperature.
- the present invention is not just about large systems, but also about e.g. B. Wall devices for heating water and generally heating devices for heating buildings and/or providing warm water.
- a burner typically used for such devices today has a burner body that is attached to or in a wall of a combustion chamber (usually in a door or maintenance hatch) and protrudes into the combustion chamber.
- a burner body is designed to be rotationally symmetrical, in particular cylindrical, to a longitudinal axis. Its lateral surface is limited an interior.
- the mixture of air and fuel gas is fed to an inlet area of the interior of the burner body and blown from an outlet area with many outlet openings into the combustion chamber, where it burns and releases the resulting heat to heat exchanger surfaces.
- flow-influencing elements can be arranged in the interior of the burner body, in particular in the inlet area.
- guide vanes or similar elements for generating swirl and/or turbulence can be arranged there (see e.g. WO 2016/182778 A1 ) or a static mixer, such as B. a Venturi nozzle.
- a static mixer such as B. a Venturi nozzle.
- the aim is to achieve an even distribution of the mixture across the outlet openings and thus ensure combustion with as few pollutants as possible.
- the object of the present invention is to at least partially solve the problems described with reference to the prior art and, in particular, to reduce the generation of pollutants, in particular NOX, by making changes to the burner, without additional components or other significant changes to existing or new ones Investments.
- the combustion temperature should be reduced, which is particularly important for future fuels containing hydrogen or pure hydrogen.
- a heater according to claim 1 is used to solve this problem.
- Advantageous refinements and developments of the invention are specified in the dependent claims. The description, especially in connection with the drawing, illustrates the invention and gives further exemplary embodiments.
- the heater proposed here with a combustion chamber and a burner arrangement comprising a premix burner, has a burner body to which a mixture of air and fuel gas can be supplied, which is attached to or in a wall of a combustion chamber, projects into it and has outlet openings in the combustion chamber for the mixture to exit having.
- the burner body has an interior with an inlet area and an outlet area, the interior in the inlet area having at least one element for generating swirl or turbulence, so that when the mixture flows through in the inlet area, a lower internal pressure is created than in the outlet area and than in the combustion chamber, and There are connection openings to the combustion chamber in the entry area.
- the area in which an element for such a flow influence is located is included here and in the following as part of the entry area.
- the static pressure in a system with a flow is inversely related to the flow velocity, which in turn depends on the flow cross section while the volume flow remains the same, so that a higher static pressure is achieved in areas with slow flow There is more pressure than in areas with faster currents.
- the present invention makes use of this to suck combustion gases from the combustion chamber into the interior of the burner body during operation of the burner and add them to the mixture there. For various reasons, this leads to a lower combustion temperature and thus to a lower production of pollutants, especially NOX.
- combustion gases contain little oxygen and can therefore be viewed as almost inert, this lowers the combustion temperature and reduces the formation of pollutants, although the combustion gases remain after a certain cooling Due to heat exchange during recirculation, they still have a higher temperature than the rest of the mixture.
- One element for generating swirl or turbulence is sufficient to generate a sufficient pressure difference.
- the entry area in the axial direction is very short, namely 3 mm to 20 mm [millimeters], preferably 5 mm to 10 mm, whereby the area that the element occupies for influencing the flow is also included in the entry area.
- the inlet area has a smaller flow cross section than the outlet area. This leads to a faster flow with the same volume flow as in the outlet area with a larger cross section and thus to a pressure difference that can be used for exhaust gas recirculation. Since the pressure in the combustion chamber, at least in most heaters, is close to atmospheric pressure (1 bar), small constrictions in the cross-section of the inlet area are sufficient for exhaust gas recirculation, in particular constrictions with 5 to 30% [percent] less cross-sectional area than that of the exit area. The proportion of recirculated combustion gases depends on the size of the restriction (and/or the design of elements for influencing flow) and an effective total cross-sectional area of the connecting openings. This can be between 2% and 20% [volume percent] of the mixture emerging from the outlet openings, preferably between 5% and 10%.
- the entry area preferably forms approximately 2% to 20%, in particular 5% to 10%, of the axial length of the interior and has a lateral surface which is predominantly formed from connecting openings. Since only a small pressure difference can be utilized between the combustion chamber and the inlet area, it is important that the connecting openings have a sufficiently large effective cross-sectional area in order to suck in a quantity of exhaust gases that sufficiently influences the combustion temperature. This not only depends on the number of connection openings and their individual cross-sectional areas, but also their shape. The aim is therefore to provide as many and/or large connection openings as possible, as long as the size of the inlet area allows this and the stability of the burner body is not impaired.
- connection openings particularly preferably form a type of annular gap (at least one or, if necessary, several) which is interrupted by holding webs which carry the remaining burner body.
- annular gap can have an axial width of 0.5 mm to 5 mm, in particular 1 mm to 3 mm.
- FIG. 1 and Fig. 2 show schematically a section of a combustion chamber 1 with a wall 2 in which there is a door 3 (or flap) on one Burner assembly is attached.
- a premix burner 4 which can be supplied with a mixture of air and fuel from a system not shown, has a burner body 5 which projects into the combustion chamber 1 in an axial direction (see arrow).
- the burner body 5 has an interior 6, which is composed of an entry area 7 and an exit area 8.
- In the outlet area 8 there are numerous outlet openings 9 through which the mixture can flow into the combustion chamber 1, where it is burned to form combustion gases.
- the entry area 7 there is an element 11 for influencing the flow, in the present example a swirl generator.
- the connecting openings 10 preferably have the largest possible cross-sectional area overall in order to be able to recirculate as much combustion gases as possible. Since the inlet area 7 is usually only a few millimeters long in the axial direction, there is not much lateral surface 12 available, so that the connecting openings 10 take up a large part of it, although the stability of the burner body 5 must be maintained.
- a type of annular gap 13 is advantageous as a connecting opening 10, which is interrupted by (as narrow and/or as few as possible) retaining webs 14 due to the stability of the burner body.
- this annular gap 13 can lie approximately in the same axial position as the element 11.
- He can run around the Burner body 5 may be designed with a width (in the axial direction) of 0.5 mm to 5 mm, preferably 1 mm to 3 mm, being interrupted by three to ten holding webs 14, which have a width (in the circumferential direction) of 1 mm to have 10 mm.
- a cross-sectional narrowing of the inlet area 7 which leads to an (additionally) reduced pressure and enables or supports the described recirculation of combustion gases.
- adding combustion gases to the mixture of air and fuel gas reduces the production of pollutants, especially NOX.
- the present invention enables a reduction in the combustion temperature and thus a reduction in pollutant emissions in heaters, in particular those that are operated with hydrogen or hydrogen-containing fuel gases, through simple design changes to the burner of a heater.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gas Burners (AREA)
Description
Die Erfindung betrifft ein Heizgerät mit einer Verbrennungskammer und einer Brenneranordnung mit einem Vormischbrenner.The invention relates to a heater with a combustion chamber and a burner arrangement with a premix burner.
Moderne Heizgeräte werden mit einem Gemisch aus Luft und Brenngas betrieben. Dazu wird mit einem geeigneten Anteil an Brenngas gemischte Luft von einem Gebläse in einen Brenner gefördert, der Austrittsöffnungen für das Gemisch aufweist, welches nach dem Austritt aus dem Brenner in einem Verbrennungsraum verbrannt wird. Das Gemisch wird zur Vermeidung des Entstehens von Schadstoffen sehr genau geregelt, so dass eine möglichst vollständige Verbrennung stattfinden kann. Die entstehenden Verbrennungsgase enthalten nur noch wenig Sauerstoff, aber je nach Brenngas Wasserdampf, Kohlendioxid und hauptsächlich Stickstoff. In geringen Mengen können bei der Verbrennung auch Stickoxide, im Folgenden mit NOX bezeichnet, entstehen, was unerwünscht, aber besonders bei hohen Verbrennungstemperaturen nicht ganz vermeidbar ist. Besonders hohe Verbrennungstemperaturen entstehen bei bestimmten Brenngasen, wobei auch z. B. ein großer Anteil an Wasserstoff im Brenngas, wie er in Zukunft geplant ist, die Verbrennungstemperatur erhöhen kann. Bei der vorliegenden Erfindung geht es nicht nur um große Anlagen, sondern auch um z. B. Wandgeräte zur Erwärmung von Wasser und generell um Heizgeräte für die Beheizung von Gebäuden und/oder die Bereitstellung von warmem Wasser.Modern heaters are operated with a mixture of air and fuel gas. For this purpose, air mixed with a suitable proportion of fuel gas is conveyed by a fan into a burner which has outlet openings for the mixture, which is burned in a combustion chamber after exiting the burner. The mixture is regulated very precisely to avoid the formation of pollutants so that combustion can take place as completely as possible. The resulting combustion gases contain only a little oxygen, but depending on the fuel gas, water vapor, carbon dioxide and mainly nitrogen. Small quantities of nitrogen oxides, hereinafter referred to as NOX, can also be formed during combustion, which is undesirable but not entirely avoidable, especially at high combustion temperatures. Particularly high combustion temperatures arise with certain fuel gases, including e.g. B. a large proportion of hydrogen in the fuel gas, as planned in the future, can increase the combustion temperature. The present invention is not just about large systems, but also about e.g. B. Wall devices for heating water and generally heating devices for heating buildings and/or providing warm water.
Ein für solche Geräte heute typischerweise verwendeter Brenner weist einen Brennerkörper auf, der an oder in einer Wand eines Verbrennungsraumes befestigt ist (meistens in einer Tür oder Wartungsklappe) und in den Verbrennungsraum hineinragt. Oft, aber nicht notwendigerweise, ist ein solcher Brennerkörper rotationssymmetrisch, insbesondere zylindrisch, zu einer Längsachse ausgebildet. Seine Mantelfläche begrenzt einen Innenraum. Das Gemisch aus Luft und Brenngas wird einem Eintrittsbereich des Innenraums des Brennerkörpers zugeführt und aus einem Austrittsbereich mit vielen Austrittsöffnungen in den Verbrennungsraum geblasen, wo es verbrennt und die dabei entstehende Wärme an Wärmetauscher-Flächen abgibt. Es ist auch bekannt, dass in dem Innenraum des Brennerkörpers strömungsbeeinflussende Elemente angeordnet sein können, insbesondere im Eintrittsbereich. Dort können beispielsweise Leitschaufeln oder ähnliche Elemente zur Drall-Erzeugung und/oder Verwirbelung angeordnet sein (vergleiche z. B.
Aus der
Aus der
Aufgabe der vorliegenden Erfindung ist es, die mit Bezug auf den Stand der Technik geschilderten Probleme wenigstens teilweise zu lösen und ganz besonders durch Veränderungen am Brenner die Erzeugung von Schadstoffen, insbesondere NOX, zu verringern, ohne zusätzliche Komponenten oder andere wesentliche Änderungen an vorhandenen oder neuen Anlagen. Dabei soll insbesondere die Verbrennungstemperatur gesenkt werden, was für zukünftige Brennstoffe mit Anteilen von Wasserstoff oder aus reinem Wasserstoff besonders von Bedeutung ist.The object of the present invention is to at least partially solve the problems described with reference to the prior art and, in particular, to reduce the generation of pollutants, in particular NOX, by making changes to the burner, without additional components or other significant changes to existing or new ones Investments. In particular, the combustion temperature should be reduced, which is particularly important for future fuels containing hydrogen or pure hydrogen.
Zur Lösung dieser Aufgabe dient ein Heizgerät gemäß dem Anspruch 1. Vorteilhafte Ausgestaltungen und Weiterbildungen der Erfindung sind in den abhängigen Ansprüchen angegeben. Die Beschreibung, insbesondere im Zusammenhang mit der Zeichnung, veranschaulicht die Erfindung und gibt weitere Ausführungsbeispiele an.A heater according to
Das hier vorgeschlagene Heizgerät mit einem Verbrennungsraum und einer Brenneranordnung, umfassend einen Vormischbrenner hat einen Brennerkörper, dem ein Gemisch aus Luft und Brenngas zuführbar ist, der an oder in einer Wand eines Verbrennungsraums befestigt ist, in diesen hineinragt und im Verbrennungsraum Austrittsöffnungen zum Austritt des Gemisches aufweist. Dabei hat der Brennerkörper einen Innenraum mit einem Eintrittsbereich und einem Austrittsbereich, wobei der Innenraum im Eintrittsbereich mindestens ein Element zur Drall-Erzeugung oder Verwirbelung aufweist, sodass bei Durchströmung mit dem Gemisch im Eintrittsbereich ein niedrigerer Innendruck als im Austrittsbereich und als im Verbrennungsraum entsteht, und wobei im Eintrittsbereich Verbindungsöffnungen zum Verbrennungsraum vorhanden sind.The heater proposed here with a combustion chamber and a burner arrangement, comprising a premix burner, has a burner body to which a mixture of air and fuel gas can be supplied, which is attached to or in a wall of a combustion chamber, projects into it and has outlet openings in the combustion chamber for the mixture to exit having. The burner body has an interior with an inlet area and an outlet area, the interior in the inlet area having at least one element for generating swirl or turbulence, so that when the mixture flows through in the inlet area, a lower internal pressure is created than in the outlet area and than in the combustion chamber, and There are connection openings to the combustion chamber in the entry area.
Der Bereich, in dem sich ein Element zu einer solchen Strömungsbeeinflussung befindet, wird hier und im Folgenden mit zum Eintrittsbereich gerechnet.The area in which an element for such a flow influence is located is included here and in the following as part of the entry area.
Wie aus der Strömungslehre bekannt ist (und z. B. bei Saugstrahlpumpen angewendet wird), verhält sich der statische Druck in einem durchströmten System umgekehrt zur Strömungsgeschwindigkeit, die wiederum bei gleichbleibendem Volumenstrom vom Strömungsquerschnitt abhängt, so dass in Bereichen mit langsamer Strömung ein höherer statischer Druck herrscht als in Bereichen mit schneller Strömung. Dies macht sich die vorliegende Erfindung zu Nutze, um Verbrennungsgase aus dem Verbrennungsraum während des Betriebes des Brenners in den Innenraum des Brennerkörpers einzusaugen und dort dem Gemisch hinzuzufügen. Das führt aus verschiedenen Gründen zu einer geringeren Verbrennungstemperatur und damit zu einer geringeren Erzeugung von Schadstoffen, insbesondere NOX.As is known from fluid mechanics (and is used, for example, in suction jet pumps), the static pressure in a system with a flow is inversely related to the flow velocity, which in turn depends on the flow cross section while the volume flow remains the same, so that a higher static pressure is achieved in areas with slow flow There is more pressure than in areas with faster currents. The present invention makes use of this to suck combustion gases from the combustion chamber into the interior of the burner body during operation of the burner and add them to the mixture there. For various reasons, this leads to a lower combustion temperature and thus to a lower production of pollutants, especially NOX.
Untersuchungen haben gezeigt, dass z. B. ein Drall-Erzeuger oder ein ähnliches Element im Eintrittsbereich eines Brennerkörpers trotz geringer Baulänge dazu führt, dass im Eintrittsbereich, besonders im Bereich des Drall-Erzeugers, ein deutlich niedrigerer Druck als im Austrittsbereich herrscht. Das geht so weit, dass der Druck sogar niedriger ist als im Verbrennungsraum, wo der Druck wiederum niedriger als im Austrittsbereich des Brennerkörpers sein muss, damit Gemisch aus den Austrittsöffnungen in den Verbrennungsraum austreten kann. Diese Bedingungen erlauben es, Verbrennungsgase aus dem Verbrennungsraum durch erfindungsgemäße Verbindungsöffnungen in den Eintrittsraum einzusaugen, wo sie sich mit dem dort eingeblasenen Gemisch aus Luft und Brenngas vermischen (oder jedenfalls in dem nachfolgenden Element), so dass zu den Austrittsöffnungen nunmehr ein Gemisch aus Luft, Brenngas und rückgeführten Verbrennungsgasen gelangt. Da Verbrennungsgase wenig Sauerstoff enthalten, also fast als inert angesehen werden können, senkt dies die Verbrennungstemperatur und vermindert die Entstehung von Schadstoffen, obwohl die Verbrennungsgase nach einer gewissen Abkühlung durch Wärmeaustausch bei Rückführung noch eine höhere Temperatur haben als das übrige Gemisch. Ein Element zur Drall-Erzeugung oder Verwirbelung reicht aus, um eine genügende Druckdifferenz zu erzeugen. Dabei ist der Eintrittsbereich in axialer Richtung sehr kurz, nämlich 3 mm bis 20 mm [Millimeter], vorzugsweise 5 mm bis 10 mm, wobei der Bereich, den das Element zur Strömungsbeeinflussung einnimmt, auch mit zum Eintrittsbereich gerechnet wird.Studies have shown that e.g. B. a swirl generator or a similar element in the inlet area of a burner body, despite the short overall length, results in a significantly lower pressure in the inlet area, especially in the area of the swirl generator, than in the outlet area. This goes so far that the pressure is even lower than in the combustion chamber, where the pressure in turn must be lower than in the outlet area of the burner body so that mixture can escape from the outlet openings into the combustion chamber. These conditions allow combustion gases to be sucked in from the combustion chamber through connection openings according to the invention into the inlet chamber, where they mix with the mixture of air and fuel gas blown in there (or at least in the subsequent element), so that a mixture of air, Fuel gas and recirculated combustion gases arrive. Since combustion gases contain little oxygen and can therefore be viewed as almost inert, this lowers the combustion temperature and reduces the formation of pollutants, although the combustion gases remain after a certain cooling Due to heat exchange during recirculation, they still have a higher temperature than the rest of the mixture. One element for generating swirl or turbulence is sufficient to generate a sufficient pressure difference. The entry area in the axial direction is very short, namely 3 mm to 20 mm [millimeters], preferably 5 mm to 10 mm, whereby the area that the element occupies for influencing the flow is also included in the entry area.
In einer besonderen Ausführungsform hat der Eintrittsbereich einen geringeren Strömungsquerschnitt als der Austrittsbereich. Dies führt zu einer schnelleren Strömung bei gleichem Volumenstrom wie im Austrittsbereich mit größerem Querschnitt und damit zu einer Druckdifferenz, die zur Abgasrückführung ausgenutzt werden kann. Da der Druck im Verbrennungsraum, jedenfalls bei den meisten Heizgeräten, in der Nähe des Atmosphärendruckes (1 bar) liegt, sind geringe Verengungen des Querschnitts des Einlassbereiches ausreichend für eine Abgasrückführung, insbesondere Verengungen mit 5 bis 30 % [Prozent] weniger Querschnittsfläche gegenüber der des Austrittsbereiches. Von der Größe der Verengung (und/oder der Bauart von Elementen zur Strömungsbeeinflussung) und einer effektiven Gesamtquerschnittsfläche der Verbindungsöffnungen hängt der Anteil an rückgeführten Verbrennungsgasen ab. Dieser kann zwischen 2 % und 20 % [Volumenprozent] des an den Austrittsöffnungen austretenden Gemisches liegen, vorzugsweise zwischen 5 % und 10 %.In a special embodiment, the inlet area has a smaller flow cross section than the outlet area. This leads to a faster flow with the same volume flow as in the outlet area with a larger cross section and thus to a pressure difference that can be used for exhaust gas recirculation. Since the pressure in the combustion chamber, at least in most heaters, is close to atmospheric pressure (1 bar), small constrictions in the cross-section of the inlet area are sufficient for exhaust gas recirculation, in particular constrictions with 5 to 30% [percent] less cross-sectional area than that of the exit area. The proportion of recirculated combustion gases depends on the size of the restriction (and/or the design of elements for influencing flow) and an effective total cross-sectional area of the connecting openings. This can be between 2% and 20% [volume percent] of the mixture emerging from the outlet openings, preferably between 5% and 10%.
Dabei bildet der Eintrittsbereich bevorzugt etwa 2 % bis 20 %, insbesondere 5 % bis 10 % der axialen Länge des Innenraumes und weist eine Mantelfläche auf, die zum überwiegenden Teil aus Verbindungsöffnungen gebildet ist. Da zwischen Verbrennungsraum und Eintrittsbereich nur eine geringe Druckdifferenz ausgenutzt werden kann, ist es für das Ansaugen einer die Verbrennungstemperatur genügend beeinflussenden Menge an Abgasen wichtig, dass die Verbindungsöffnungen eine genügend große effektive Querschnittsfläche haben. Diese hängt nicht nur von der Zahl der Verbindungsöffnungen und deren einzelnen Querschnittsflächen ab, sondern auch von deren Form. Es wird daher angestrebt, möglichst viele und/oder große Verbindungsöffnungen vorzusehen, soweit die Größe des Eintrittsbereiches dies zulässt und die Stabilität des Brennerkörpers nicht beeinträchtigt wird.The entry area preferably forms approximately 2% to 20%, in particular 5% to 10%, of the axial length of the interior and has a lateral surface which is predominantly formed from connecting openings. Since only a small pressure difference can be utilized between the combustion chamber and the inlet area, it is important that the connecting openings have a sufficiently large effective cross-sectional area in order to suck in a quantity of exhaust gases that sufficiently influences the combustion temperature. This not only depends on the number of connection openings and their individual cross-sectional areas, but also their shape. The aim is therefore to provide as many and/or large connection openings as possible, as long as the size of the inlet area allows this and the stability of the burner body is not impaired.
Besonders bevorzugt bilden die Verbindungsöffnungen eine Art Ringspalt (mindestens einen oder bei Bedarf auch mehrere), der von Haltestegen unterbrochen ist, die den restlichen Brennerkörper tragen. Ein solcher Ringspalt kann eine axiale Breite von 0,5 mm bis 5 mm aufweisen, insbesondere 1 mm bis 3 mm.The connection openings particularly preferably form a type of annular gap (at least one or, if necessary, several) which is interrupted by holding webs which carry the remaining burner body. Such an annular gap can have an axial width of 0.5 mm to 5 mm, in particular 1 mm to 3 mm.
Es sei erwähnt, dass ein solcher Brenner beim Starten unter Umständen zusätzliche Luft aus dem Verbrennungsraum (in dem sich dann möglicherweise noch keine Verbrennungsgase befinden) ansaugt, wodurch das zum Zünden vorgesehene Gemisch magerer ist als ohne Rückführung. Dies kann aber durch eine entsprechend fettere Einstellung des Gemisches beim Zündvorgang oder andere gleichwirkende Maßnahmen ausgeglichen werden, um eine sichere Zündung zu gewährleisten.It should be mentioned that when starting, such a burner may suck in additional air from the combustion chamber (which may then not yet contain any combustion gases), which means that the mixture intended for ignition is leaner than without recirculation. However, this can be compensated for by setting the mixture to be correspondingly richer during the ignition process or other measures with the same effect in order to ensure reliable ignition.
Ein schematisches Ausführungsbeispiel der Erfindung, auf das diese jedoch nicht beschränkt ist, und dessen Funktionsweise werden nun anhand der Zeichnung näher erläutert. Es stellen dar:
- Fig. 1:
- einen Brennerkörper mit Verbindungsöffnungen zur Verbrennungsgasrückführung in perspektivischer Ansicht und
- Fig. 2:
- einen zentralen axialen Längsschnitt durch den Brennerkörper von
Fig. 1 .
- Fig. 1:
- a burner body with connection openings for combustion gas recirculation in a perspective view and
- Fig. 2:
- a central axial longitudinal section through the burner body
Fig. 1 .
Die Verbindungsöffnungen 10 haben, da im Allgemeinen nur eine geringe Druckdifferenz zwischen Eintrittsbereich 7 und Verbrennungsraum 1 genutzt werden kann, bevorzugt insgesamt eine möglichst große Querschnittsfläche, um möglichst viel Verbrennungsgase rückführen zu können. Da der Eintrittsbereich 7 in axialer Richtung meist nur wenige Millimeter lang ist, steht nicht viel Mantelfläche 12 zur Verfügung, so dass die Verbindungsöffnungen 10 einen großen Teil davon einnehmen, wobei aber die Stabilität des Brennerkörpers 5 erhalten bleiben muss. Günstig ist eine Art Ringspalt 13 als Verbindungsöffnung 10, wobei dieser wegen der Stabilität des Brennerkörpers von (möglichst schmalen und/oder möglichst wenigen) Haltestegen 14 unterbrochen ist. Je nach Befestigung des Elementes 11 zur Strömungsbeeinflussung kann dieser Ringspalt 13 etwa auf gleicher axialer Position mit dem Element 11 liegen. Er kann umlaufend um den Brennerkörper 5 ausgebildet sein mit einer Breite (in axialer Richtung) von 0,5 mm bis 5 mm, vorzugsweise 1 mm bis 3 mm, wobei er von drei bis zehn Haltestegen 14 unterbrochen ist, die eine Breite (in Umfangsrichtung) von 1 mm bis 10 mm haben. Nicht dargestellt, aber einzeln oder mit dem beschriebenen System gemeinsam anwendbar ist eine Querschnittsverengung des Eintrittsbereiches 7, die zu einem (zusätzlich) verringerten Druck führt und die beschriebene Rückführung von Verbrennungsgasen ermöglicht oder unterstützt. Beimischungen von Verbrennungsgasen zum Gemisch aus Luft und Brenngas verringern je nach ihrem Anteil die Produktion von Schadstoffen, insbesondere von NOX.Since generally only a small pressure difference between the
Die vorliegende Erfindung ermöglicht durch einfache konstruktive Änderungen am Brenner eines Heizgerätes eine Reduzierung der Verbrennungstemperatur und damit eine Verringerung des Schadstoffausstoßes bei Heizgeräten, insbesondere solchen, die mit Wasserstoff oder wasserstoffhaltigen Brenngasen betrieben werden.The present invention enables a reduction in the combustion temperature and thus a reduction in pollutant emissions in heaters, in particular those that are operated with hydrogen or hydrogen-containing fuel gases, through simple design changes to the burner of a heater.
- 11
- Verbrennungsraumcombustion chamber
- 22
- WandWall
- 33
- Tür (Klappe)door (flap)
- 44
- VormischbrennerPremix burner
- 55
- Brennerkörperburner body
- 66
- Innenrauminner space
- 77
- EintrittsbereichEntry area
- 88th
- AustrittsbereichExit area
- 99
- AustrittsöffnungenExit openings
- 1010
- VerbindungsöffnungenConnection openings
- 1111
- Element zur StrömungsbeeinflussungElement for influencing flow
- 1212
- MantelflächeLateral surface
- 1313
- RingspaltAnnular gap
- 1414
- Haltestegeretaining bars
Claims (4)
- Heating device with a combustion chamber (1) and a burner arrangement, comprising a premix burner (4), which has a burner body (5) with an inner chamber (6), which burner body is attached to or in a wall (2) of the combustion chamber (1) and projects into this combustion chamber (1), to which a mixture of air and fuel gas can be supplied, and towards the combustion chamber (1) has a plurality of outlet openings (9) for the outlet of the mixture and for combustion outside the inner space (6) in the combustion chamber (1), wherein the inner space (6) is composed of an inlet region (7) starting from the wall (2) of the combustion chamber (1) in a region of up to 20 mm in an axial direction of the burner body (5) and an outlet region (8) with the plurality of outlet openings (9), wherein the inlet region (7) of the inner space (6) has at least one element (11) at least for swirl generation or turbulence, so that when the mixture flows through it a lower internal pressure is produced in the inlet region (7) than in the outlet region (8) and than in the combustion chamber (1), and wherein in the inlet region (7) connecting openings (10) are provided to the combustion chamber (1) through which the combustion gases are drawn in from the combustion chamber (1) and are mixed in the inlet region (7) with the remaining mixture.
- Heating device according to claim 1, wherein the inner space (6) has a smaller flow cross-section in the inlet region (7) than in the outlet region (8).
- Heating device according to any one of claims 1 or 2, wherein the inlet region (7) forms 1% to 20% of the inner space (6) and has a casing surface (12) which is predominantly formed by the connecting openings (10).
- Heating device, according to any one of the preceding claims, wherein the connecting openings (10) form a kind of annular gap (13) interrupted by retaining webs (14), which annular gap has an axial width of 0.5 to 5 mm.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102021100007.6A DE102021100007A1 (en) | 2021-01-04 | 2021-01-04 | Burner arrangement for a premix burner |
Publications (3)
Publication Number | Publication Date |
---|---|
EP4023938A1 EP4023938A1 (en) | 2022-07-06 |
EP4023938B1 true EP4023938B1 (en) | 2023-12-06 |
EP4023938C0 EP4023938C0 (en) | 2023-12-06 |
Family
ID=79024498
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP21214581.7A Active EP4023938B1 (en) | 2021-01-04 | 2021-12-15 | Burner arrangement for a pre-mix burner |
Country Status (3)
Country | Link |
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EP (1) | EP4023938B1 (en) |
DE (1) | DE102021100007A1 (en) |
ES (1) | ES2969639T3 (en) |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0687854A1 (en) | 1994-06-13 | 1995-12-20 | N.V. Acotech S.A. | Burner with recirculation of exhaust gas |
CA2284706A1 (en) * | 1997-03-24 | 1998-10-01 | Vth Verfahrenstechnik Fur Heizung Ag | A boiler fitted with a burner |
EP0867659A1 (en) * | 1997-03-24 | 1998-09-30 | VTH Verfahrentechnik für Heizung AG | Process and device for combustion of gaseous fuel |
DE10064259B4 (en) | 2000-12-22 | 2012-02-02 | Alstom Technology Ltd. | Burner with high flame stability |
NL1023439C2 (en) | 2003-05-16 | 2004-11-17 | Nederlandse Gasunie Nv | Burner. |
US10767900B2 (en) * | 2015-05-14 | 2020-09-08 | Lochinvar, Llc | Burner with flow distribution member |
-
2021
- 2021-01-04 DE DE102021100007.6A patent/DE102021100007A1/en active Pending
- 2021-12-15 EP EP21214581.7A patent/EP4023938B1/en active Active
- 2021-12-15 ES ES21214581T patent/ES2969639T3/en active Active
Also Published As
Publication number | Publication date |
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EP4023938A1 (en) | 2022-07-06 |
DE102021100007A1 (en) | 2022-07-07 |
EP4023938C0 (en) | 2023-12-06 |
ES2969639T3 (en) | 2024-05-21 |
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