EP4023938B1 - Burner arrangement for a pre-mix burner - Google Patents

Burner arrangement for a pre-mix burner Download PDF

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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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EP
European Patent Office
Prior art keywords
combustion chamber
burner
mixture
combustion
outlet
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EP21214581.7A
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German (de)
French (fr)
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EP4023938A1 (en
EP4023938C0 (en
Inventor
Hendrik Gevers
Markus Polus
Stefan Schweitzer-de Bortoli
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Vaillant GmbH
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Vaillant GmbH
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Publication of EP4023938C0 publication Critical patent/EP4023938C0/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/02Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C9/00Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
    • F23C9/006Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber the recirculation taking place in the combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2202/00Fluegas recirculation
    • F23C2202/10Premixing fluegas with fuel and combustion air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2900/00Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
    • F23C2900/09002Specific devices inducing or forcing flue gas recirculation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2900/00Special features of, or arrangements for combustion apparatus using fluid fuels or solid fuels suspended in air; Combustion processes therefor
    • F23C2900/9901Combustion process using hydrogen, hydrogen peroxide water or brown gas as fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2203/00Gaseous fuel burners
    • F23D2203/10Flame diffusing means
    • F23D2203/101Flame diffusing means characterised by surface shape
    • F23D2203/1012Flame diffusing means characterised by surface shape tubular
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2900/00Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/14Special features of gas burners
    • F23D2900/14241Post-mixing with swirling means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2900/00Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/14Special features of gas burners
    • F23D2900/14701Swirling means inside the mixing tube or chamber to improve premixing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2900/00Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/31019Mixing 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. WO 2016/182778 A1 ) oder ein statischer Mischer, wie z. B. eine Venturi-Düse. So soll eine gleichmäßige Verteilung des Gemisches auf die Austrittsöffnungen erreicht werden und damit eine möglichst schadstoffarme Verbrennung. Eine Beeinflussung der Verbrennungstemperatur ist auf diese Weise aber kaum möglich, da diese im Wesentlichen von der Art des Brenngases und dem Mischungsverhältnis mit Luft abhängt.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. Often, but not necessarily, such 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. It is also known that flow-influencing elements can be arranged in the interior of the burner body, in particular in the inlet area. For example, 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. 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. However, it is hardly possible to influence the combustion temperature in this way, as it essentially depends on the type of fuel gas and the mixing ratio with air.

Aus der DE 100 64 259 A1 ist es auch schon bekannt, durch Rezirkulation von Verbrennungsgasen die Flammenstabilität in einem Verbrennungsraum zu beeinflussen und in der WO2004/102071 A1 wird auch schon die Reduzierung der Erzeugung von NOX durch Abgasrezirkulation in einer Art Venturi-Düse beschrieben. Allerdings erfordern die genannten Anordnungen einen relativ langen Bauraum, der oft nicht zur Verfügung steht.From the DE 100 64 259 A1 It is also already known to influence the flame stability in a combustion chamber by recirculating combustion gases and in the WO2004/102071 A1 The reduction in the production of NOX through exhaust gas recirculation in a type of Venturi nozzle is also described. However, the arrangements mentioned require a relatively long installation space, which is often not available.

Aus der EP 0 970 327 A1 und der EP 0 867 659 A1 gehen Gasbrenner hervor, bei dem ein Flammrohr an einer Stauscheibe angeordnet ist, wobei die Stauscheibe mit einem Blendeneinsatz Öffnungen und Leitbleche ausbildet, über die Luft bzw. ein Gas-LuftGemisch in das Flammrohr eintreten kann. Im Betrieb kann sich stromabwärts der Stauscheibe ein Unterdruck einstellen, wodurch über an bzw. in dem Flammrohr ausgebildete Rezirkulationsschlitze und -Öffnungen Abgas ansaugen kann, um einer Verrußung der Stauscheibe vorzubeugen bzw. die Flamme dort zu erhitzen. Im Gegensatz dazu findet bei den hier angesprochenen Heizgeräten eine Verbrennung des Gases außerhalb des Brennerkörpers in dem Verbrennungsraum statt, so dass die damit adressierten Probleme der Verrußung und der Flammenerwärmung hier nicht auftreten. Zudem verlangen diese Konzepte des Standes der Technik eine abgestimmte Einbausituation hin zur Wand des Brennraums, so dass ein erhöhter apparativer Aufwand erforderlich ist.From the EP 0 970 327 A1 and the EP 0 867 659 A1 gas burners emerge in which a flame tube is arranged on a baffle plate, the baffle plate with a diaphragm insert forming openings and baffles through which air or a gas-air mixture can enter the flame tube. During operation, a negative pressure can be created downstream of the baffle plate, whereby exhaust gas can be sucked in via recirculation slots and openings formed on or in the flame tube in order to prevent sooting of the baffle plate or to heat the flame there. In contrast, in the heaters mentioned here, the gas is burned outside the burner body in the combustion chamber, so that the gas is burned The addressed problems of sooting and flame heating do not occur here. In addition, these concepts of the prior art require a coordinated installation situation towards the wall of the combustion chamber, so that increased expenditure on equipment is required.

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 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.

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.
A schematic embodiment of the invention, to which it is not limited, and its mode of operation will now be explained in more detail with reference to the drawing. They represent:
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 .

Fig. 1 und Fig. 2 zeigen schematisch einen Ausschnitt aus einem Verbrennungsraum 1 mit einer Wand 2, in der sich eine Tür 3 (oder Klappe) befindet, an der eine Brenneranordnung befestigt ist. Ein Vormischbrenner 4, der aus einem nicht dargestellten System mit einem Gemisch aus Luft und Brennstoff versorgt werden kann, weist einen Brennerkörper 5 auf, der in einer axialen Richtung (siehe Pfeil) in den Verbrennungsraum 1 hineinragt. Der Brennerkörper 5 hat einen Innenraum 6, der sich aus einem Eintrittsbereich 7 und einem Austrittsbereich 8 zusammensetzt. Im Austrittsbereich 8 befinden sich zahlreiche Austrittsöffnungen 9, durch die das Gemisch in den Verbrennungsraum 1 strömen kann, wo es unter Bildung von Verbrennungsgasen verbrannt wird. Im Eintrittsbereich 7 befindet sich ein Element 11 zur Strömungsbeeinflussung, im vorliegenden Beispiel ein Drall-Erzeuger. Dieser bewirkt, dass sich im Eintrittsbereich 7 beim Betrieb ein geringerer Druck ausbildet als im Austrittsbereich 8 und auch als im Verbrennungsraum 1. Dies ergibt sich aus den Strömungsgeschwindigkeiten im Eintrittsbereich 7, insbesondere im Bereich des Elementes 11, bzw. im Austrittsbereich 8. Durch Verbindungsöffnungen 10 in einer Mantelfläche 12 des Eintrittsbereiches 7 werden daher beim Betrieb Verbrennungsgase aus dem Verbrennungsraum 1 in den Eintrittsbereich 7 eingesaugt und dort mit dem übrigen Gemisch vermischt, was durch einen Drall-Erzeuger oder ein Verwirbelungselement unterstützt wird. 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. In the entry area 7 there is an element 11 for influencing the flow, in the present example a swirl generator. This causes a lower pressure to develop in the inlet area 7 during operation than in the outlet area 8 and also than in the combustion chamber 1. This results from the flow velocities in the inlet area 7, in particular in the area of the element 11, or in the outlet area 8. Through connection openings 10 in a lateral surface 12 of the inlet area 7, combustion gases are therefore sucked in from the combustion chamber 1 into the inlet area 7 during operation and mixed there with the remaining mixture, which is supported by a swirl generator or a swirling element.

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 inlet area 7 and the combustion chamber 1 can be used, 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. Depending on the attachment of the element 11 for influencing the flow, 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. Not shown, but applicable individually or together with the system described, is 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. Depending on their proportion, adding combustion gases to the mixture of air and fuel gas reduces the production of pollutants, especially NOX.

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.

BezugszeichenlisteReference symbol list

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)

  1. 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.
  2. 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).
  3. 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).
  4. 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.
EP21214581.7A 2021-01-04 2021-12-15 Burner arrangement for a pre-mix burner Active EP4023938B1 (en)

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

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EP4023938A1 EP4023938A1 (en) 2022-07-06
EP4023938B1 true EP4023938B1 (en) 2023-12-06
EP4023938C0 EP4023938C0 (en) 2023-12-06

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ID=79024498

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DE (1) DE102021100007A1 (en)
ES (1) ES2969639T3 (en)

Family Cites Families (6)

* Cited by examiner, † Cited by third party
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

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DE102021100007A1 (en) 2022-07-07
EP4023938C0 (en) 2023-12-06
ES2969639T3 (en) 2024-05-21

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