Patent Application
20210063013
The invention relates to a burner for burning liquid or aerosol fuels, in particular, gaseous fuels, which can be used for heating, melting and keeping warm in the case of processes with high temperature requirements, such as in melting furnaces. A corresponding method is also indicated.
Examples of gaseous fuels include natural gas (with a main component of methane), ethane, propane, butane, ethene, pentane and hydrogen.
One of the formation mechanisms of NOx (nitrogen oxide) is thermal NOx. This occurs when a mixture of nitrogen and oxygen reaches very high temperatures over a period of time. Thereby, the influence of high temperatures is at a disproportionately high level. Regenerative burners of aluminium melting furnaces are very susceptible to the formation of thermal NOx. The reason for this is that the temperatures in the furnace can become very high and that the air is preheated to a very high temperature even before combustion. This results in very high peak temperatures in the flame, which in turn can lead to high levels of NOx emissions.
From prior art, the following options for reducing NOx emissions are already known:
Oxygen burners reduce NOx emissions due to the lack of nitrogen. However, combustion must be controlled in a precise manner. In the event that leaks of the furnace chamber or other phenomena air come into contact with the flame, NOx emissions sharply increase.
A large distance between the air and gas nozzles promotes better internal recirculation. However, this has the disadvantage that the burner head is enlarged, thereby giving rise to a lack of space. In addition, the mixing of air and gas can be interrupted in the event of unfavourable charging in the case of a decentralized gas lance, which can result in CO (carbon monoxide) emissions.
External recirculation between air and gas is possible, however, this reduces the efficiency of the burner and is complex to carry out.
Alternatively, a stepped combustion can be conducted, but this can only reduce emissions to a certain point or degree.
DE 41 42 401 A1 describes a method for operating a furnace heating system based on one or a plurality of burners. Thereby, among other things, oxygen is used to reduce nitrogen oxide formation to burn the fuel.
The object of the present invention is to reduce the NOx emissions and simultaneously provide an efficient and cost-effective burner.
For this purpose, the invention specifies a burner according to the invention for burning liquid or aerosol fuels, in particular, gaseous fuels, particularly according to Claim 1. In particular, it has to do with a refractory burner body. The burner body comprises a gas nozzle and a plurality of air nozzles, which are at least partially formed as integral mouldings in the burner body and flow out at a front side of the burner body. Here, the air nozzles are symmetrically arranged around the gas nozzle and diverge at an angle α to the gas nozzle.
This has the advantage that the emission and distribution of air away from the flame results in lower NOx emissions. Thus, the gas is not completely burned immediately upon being discharged from the gas nozzle, but first distributed in the furnace. The angle can therefore eject the air at a diverging angle, prolong the flame, and increase the mixing of air and natural gas with exhaust gas, resulting in lower peak temperatures and thereby, lower NOx emissions as well.
The longer flame front, which is formed due to the symmetrical distribution of the air emitted from the air nozzles, results in a more uniform heat transfer with no temperature peaks or only low-level ones.
As a result, but also due to the stronger temperature distribution, the refractory material, in particular, that of the burner, is subjected to a lower load, thereby extending the life of the material and the device equipped with it.
The symmetrical arrangement of the air nozzles, in particular, their outlet opening(s) at the outlet or front side of the burner, means, among other things, that these are arranged concentrically around the gas nozzle and have at least one axis of symmetry. In the case of a plurality of symmetry axes, each axis of symmetry can have the same angle to the adjacent axis of symmetry. In addition, the air nozzles can assume different spacings to the gas nozzle. Preferably, the air nozzles lie on one or a plurality of concentric circles in particular around the gas nozzle and are evenly distributed on this or these, i.e. on the respective circle at the same distance to one another. In a preferred embodiment, the air nozzles are aligned on an outer circle with an angle β, and the air nozzles on the inner circle or the inner circles with an angle α, wherein angle α is less than angle β; alternatively, the angle of the air nozzles of a circle becomes linearly or exponentially smaller with each circle closer to the gas nozzle.
Likewise, the symmetry axes may affect not only the arrangement of the air nozzles, but also their embodiment, in particular, their outlet opening(s). Here, their shape and/or size or outlet surface are to be understood, which are formed to be point- and/or axis-symmetric.
The use of air as a gas mixture additionally facilitates the production and use of a corresponding plant, in particular, a furnace, with one or a plurality of burners according to the invention. Here, the ambient air is sucked in and then preferably filtered (for gas and/or dust), dried, pre-cooled and/or pre-heated before it is fed into the air nozzles of the burner.
The gas nozzle is preferably supplied with gaseous fuel but can also be operated with other liquid or aerosol fuels. In the case of aerosols, i.e. solid particles or liquid particles in a gas, the particles indicated form the fuel. In addition, the burner, in particular, the gas outlet nozzle, can comprise an atomizer to distribute and mix the particles in the gas.
Furthermore, it has been shown to be favourable if the angle between the gas nozzle and one or a plurality of air nozzles, in particular, one or a plurality of main combustion air nozzles, is at a range of 1 to 45 degrees. Preferably, the angle α is 4 degrees. The smaller the angle α is, the better the air emitted can carry the gas. The larger the angle α, the better the distribution of the air emitted in front of the burner or in the furnace becomes. The air enters the combustion chamber via the air nozzle. Since the air nozzles are simultaneously arranged diverging with each other, the air first flows away from the gas jet. Due to the increasing mixing with exhaust gas, however, the gas jet and the air jets spread in such a way that, after a certain period of time, the gas jet and the air jets meet. The angle between the two air nozzles is therefore smaller than the angle at which the rays spread from the outlet opening (also known as the beam or outlet angle). Here, the outlet angle is preferably 18° and describes the directional effect of the nozzle. The directional effect of a nozzle is to be understood, in particular, as the angle of the velocity vectors of the gas particles; the more portions of the outgoing gas having a velocity that is parallel to the axis of a nozzle there are, the smaller the angle of the emanating gas is and the more far-reaching the emanating gas is and the more impetus is generated.
In order to achieve a better air distribution with a simultaneously good directional effect of the air nozzles, the burner body can comprise two to eight, preferably four, air nozzles. In addition, the symmetrical and simultaneously directed air distribution increases with the number of air nozzles. While a small number of air nozzles allow for better mixing of air with exhaust gases, thus reducing combustion of the gas, combustion temperature and NOx emission, a larger number of air nozzles has a better symmetrical distribution characteristic. Four air nozzles form an optimal embodiment between NOx emission and the symmetrical distribution of the emitted air.
Another advantageous embodiment option lies in the size adaptation of the outlet openings of the air nozzles. Thereby, the air nozzles should comprise outlet openings with a total surface that is not more than half of a circular surface of the front side of the burner body.
Likewise, the air nozzles can comprise outlet openings, the width of which grows radially from the gas nozzle. Here, the outlet openings can form trapezoidal outlet surfaces on the front side of the burner. As a result, the amount or air volume of the air emitted increases towards the outer edge of the front side so that a mixing of the air with the gas does not take place abruptly and at a spatial point, but steadily and spatially distributed.
In a further advantageous embodiment, the gas nozzle has a pre-combustion chamber, which is formed in the burner body. In addition, each or at least one air nozzle comprises a pre-combustion air nozzle that connects the air nozzle to the pre-combustion chamber. By feeding part of the air from the air nozzle into the pre-combustion chamber, a stepped combustion by the burner is carried out, which avoids or at least reduces temperature peaks. In addition, a better ignition of the gas-air mixture in the pre-combustion chamber is possible, in particular, due to the better mixing of the fuel by a swirl nozzle and the supplied air via the pre-combustion air nozzle(s).
Furthermore, the gas nozzle preferably has a swirl nozzle for swirling the fuel, which is used in the burner body. This has the advantage of promoting a mixture of the fuel with the air in and/or after the swirl nozzle and thus, a spatially distributed combustion of the gas.
Preferably, the burner body is formed by a first quarl with the front side, a second quarl, which is arranged coaxially to the first quarl, and a third quarl, in particular, with a burner orifice, as the outer sheath of the first and second firing stone. The split burner head or body is substantiated on a manufacturing engineering level since it can be cast better in this way. The quarls are preferably cast in a separate steel casing. The division of the burner body into a first and second quarl allows for simpler insertion of the gas outlet nozzle and the swirl nozzle to take place. The burner orifice is funnel-shaped and can comprise an angle to the longitudinal or gas-flame axis at a range of 15 to 75 degrees. Furthermore, in preferred embodiments, these angles are always greater than the angle, so as not to compress and mix the combustible gas and the air immediately at the outlet from the burner. Likewise, the burner orifice can be provided by the inner geometry of the furnace instead of at the third quarl, which is why the third quarl can be dispensed with from the burner body in other embodiments.
The quarls are preferably cylindrical but can also be square or elliptical in shape. In the case of a rectangular front side, attention is furthermore paid to a symmetrical arrangement of the air nozzles around the gas nozzle, wherein the arrangement is also symmetrical to the rectangular front side of the burner, in particular, the first and third quarl.
In addition or alternatively, the air nozzles, in particular, their outlet opening(s), can comprise an orifice or frame tapering towards the outside to accelerate the air and thus improve the directional effect of the emitted air. As an addition or an alternative, the same feature with regard to the tapering can be formed in the case of the gas nozzle, in particular, its outlet opening(s). Furthermore, the said outlet openings may be shaped in such a way to eject the air and/or the gas in a certain direction and thus form the said angle.
The gas nozzle and/or the air nozzles may be partially or completely formed as a single piece in the burner body by means of mouldings and/or mechanical post-machining. In addition, components may be used in the burner body, which form the nozzles and their paths or conduits at least partially. These components can serve as a connecting piece between multi-part quarls, which influence the direction and/or velocity of the gas or air and/or seal the corresponding nozzle from external gases, as may be the case, for example, with the swirl nozzle. Preferably, pressed refractory wool or paper is used as a filling and/or sealing material in and/or around the burner, in particular between the quarls.
When using the burner, the air preferably emits at a velocity of 80 to 200 m per second. The gas preferably emits at a velocity of 30 to 100 m per second.
The present invention also indicates a method according to the invention for burning liquid or aerosol fuels, in particular, gaseous fuels with reduced NOx emissions, in particular, according to Claim 9. In this method, at least the following steps are carried out:
The resulting advantages, such as lower NOx emissions, a more uniform heat transfer and a lower load on the refractory material, were explained in the case of the burner according to the invention.
Preferably, when emitting and igniting the liquid fuel or aerosol fuel, in particular, gaseous fuel, a partial volume of the gas mixture is provided to the fuel in such a way that a certain percentage of the fuel undergoes pre-combustion. This pre-combustion results in a gradual pre-combustion of the gas, a stronger temperature distribution and the elimination or at least the reduction of temperature peaks during combustion.
Furthermore, the gaseous fuel is swirled before being discharged and/or rotated. This allows for a better mixing with the gas mixture and thus a better spatially distributed combustion instead of selective combustion areas.
Favourably, the gas mixture is emitted in such a way that the at least two directions are equally spaced to each other or have the same angle around the gas flame. In other words, the exit directions on a plane perpendicular to the gas flame or its longitudinal axis form intended (intersection) points, which lie on a concentric circle around the flame and are evenly distributed on this circle.
The figures described below refer to preferred exemplary embodiments of the burner according to the invention, wherein these figures do not serve as a limitation, but essentially serve as an illustration of the invention. Elements from different figures, but with the same reference numbers are identical; therefore, the description of an element from one figure is also valid for equal or numbered elements from other figures.
The figures show:
In
The burner 15 shown is equipped with a gas nozzle and four air nozzles. In this case, the gas nozzle preferably comprises the following components, which are arranged sequentially and coaxially or along a longitudinal axis 14 to each other: a hollow-cylindrical outlet nozzle 11 made of metal, which is supplied with gas via a feed line 12; a swirl nozzle 9 for swirling the gas, which is used in the second quarl 2; a tubular mixing path 10, through which the swirled gas is passed; a pre-combustion chamber 7, into which the mixing path 10 as well as four pre-combustion air nozzles or conduits 5 of the air nozzles flow. In this pre-combustion chamber 7, the swirled gas is mixed with the air from the pre-combustion air nozzles 5 and preferably initially ignited. The mixing path 10 and the pre-combustion chamber 7 are formed as a single piece in the first quarl 1. The swirl nozzle 9 is located at the transition from the second quarl 2 to the first quarl 1. In this case, the swirl nozzle 9 can be created in such a way that no gases from the (boundary) layer between the first and second quarl 1, 2 can enter into the gas nozzle; i.e. the outer side of the swirl nozzle 9 preferably seals the gas nozzle against unwanted gases or against gas leaks. The outlet nozzle 11 is arranged in a cavity in the second quarl 2, wherein the gas supply 12 is arranged in a cooling line 13, which feeds for cooling the feed line 12 and the outlet nozzle 11 preferably cooled air. This prevents premature ignition of the gas due to elevated temperatures, especially before the gas enters the swirl nozzle 9. In addition, the air of the cooling line 13 protects the metallic components of the burner. In other embodiments, a burner may comprise a plurality of gas-feed and cooling-air lines. Each air nozzle preferably has the following components: an air conduit 4, which is formed in the second quarl 2; a main combustion air nozzle or conduit 6, which is formed in the first quarl 1 and connected to the air conduit 4; as well as a pre-combustion air nozzle or conduit 5, which is also formed in the first quarl 1 and branches off from the main burner air nozzle 6 into the pre-combustion chamber 7. Thus, except for the outlet nozzle 11, the feed line 12 and the swirl nozzle 9 all other, in particular mentioned above components of the burner 15 in the quarls 1, 2, 3 are formed by cavities.
In
Preferably, the burner body or at least one or all of the quarls 1, 2, 3 is refractory. The first quarl 1 comprises a circular front side/surface 16 and the third quarl 3 comprises a burner orifice 8 enlarging in the shape of a funnel. In particular, these components 16, 8 as well as the pre-combustion chamber 7 are designed to be at least refractory; or alternatively formulated, components that stand up against the combustion or gas flame and/or are subjected to the heat/radiation thereof. The four main combustion air nozzles 6 and the pre-combustion chamber 7 flow out on the front side 16. Thereby, these components form openings or outlet surfaces, which are arranged symmetrically around the longitudinal axis 14.
The cross-section shown in
In
The four openings of the main combustion air nozzles 6 are radially aligned from the longitudinal axis of the burner 15, in particular, cross-shaped and identical to the four pre-combustion air nozzles 5. It is noted that the area of an outlet opening of the main combustion air nozzle 6 is the same size and/or shaped as the cross-section of the main combustion air nozzle 6 within the first quarl 1. In other embodiments, the outlet openings and their connected conduits, such as the main combustion air nozzles 6, the pre-combustion air nozzle 5 and the air conduits 4, can differ in their shape and/or size. The openings shown each form a trapezoidal surface, which tapers toward the longitudinal axis or widens towards the outer circumference of the burner 15. Instead of the trapezoidal shape, other shapes of the plate are possible in other embodiments.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102019122940.5 | Aug 2019 | DE | national |
