This claims priority from German Application No. 10 2016 208 653.7, filed on May 19, 2016, the disclosure of which is hereby incorporated by reference in its entirety.
The invention relates to a nozzle for spraying liquids, having a nozzle housing and a plurality of outlet openings in the nozzle housing, wherein each outlet opening is arranged at the end of an outlet passage through the wall of the nozzle housing, and wherein the plurality of outlet openings is arranged in a circle along at least one imaginary circular line on the nozzle housing.
The invention is intended to improve a nozzle for spraying liquids in respect of distribution of the droplet sprays produced.
According to the invention, a nozzle having the features of claim 1 is provided for this purpose. A nozzle according to the invention for spraying liquids has a nozzle housing and a plurality of outlet openings in the nozzle housing, wherein each outlet opening is arranged at the end of an outlet passage through the wall of the nozzle housing. The plurality of outlet openings is arranged in at least one circle on the nozzle housing. An outlet angle which the respective central axis of the outlet passage associated with the outlet opening encloses with a central longitudinal axis of the nozzle housing differs between at least one first and at least one second outlet opening. Thus, the outlet openings do not all dispense a droplet spray at the same outlet angle but the outlet angle differs between different outlet openings. It is thereby possible to cover a larger area with a droplet spray than would be the case if the outlet angle of all the outlet openings were constant. By means of the nozzle according to the invention, it is possible to provide a larger number of outlet openings on the nozzle housing than would be the case if the outlet angle of all the outlet openings were constant. This is because each outlet opening dispenses a conical droplet spray. Through a skilful choice of the individual outlet angles, the individual conical droplet sprays can be arranged adjacent to one another in such a way that they cover as large as possible an area in a process chamber but overlap only slightly, if at all. Precisely in applications in the gas cooling sector, this allows greater coverage of the water injection plane, and shorter evaporation distances can be obtained with a droplet size and droplet distribution which are otherwise the same. More specifically, it is possible, by means of the invention, to employ outlet-opening and outlet-passage geometries which produce a relatively small opening angle of the conical droplet spray emerging. Compared with the prior art, it is then possible with the invention to arrange a larger number of such outlet openings with varying outlet angles, thus ensuring that greater coverage is achieved with all the droplet sprays produced than with a conventional nozzle that has constant outlet angles for all the outlet openings. Outlet openings which produce a small opening angle of the droplet spray produced can produce a droplet spray with a droplet size distribution that fluctuates less than with outlet openings that produce a larger opening angle of the droplet spray produced. It is thereby possible to achieve advantages specifically in applications in the gas cooling sector. It is advantageous if two different outlet angles relative to the central longitudinal axis of the nozzle housing are chosen for the plurality of outlet openings although, within the scope of the invention, it is also possible to use more than two different outlet angles of the outlet openings.
As a development of the invention, a plurality of first outlet openings is arranged in a circle along an imaginary first circular line having a first radius, and a plurality of second outlet openings is arranged in a circle along an imaginary second circular line having a second radius, which is different from the first radius, wherein the first and the second circular lines are concentric with respect to one another.
In this way, it is possible to achieve an annular impingement area over a planar area arranged perpendicularly to the central longitudinal axis of the nozzle housing. As explained, the individual conical droplet sprays which emerge from the outlet openings are arranged in such a way here that they overlap each other only slightly, if at all. Within the scope of the invention, however, it is also perfectly possible for the outlet openings to be provided on more than two concentric circular lines, each with different outlet angles.
As a development of the invention, the mouth openings of the outlet passages on the inside of the wall of the nozzle housing are situated on a common imaginary circular line.
In this way, it is possible to achieve substantially identical conditions for all outlet passages in the discharge region into the outlet passages in the interior of the nozzle housing, thus making it possible to ensure that the droplet size and distribution of all the droplet sprays discharged through the outlet openings are substantially the same.
As an alternative to the arrangement described above, the mouth openings of the outlet passages on the inside of the wall of the nozzle housing can be situated on two mutually concentric imaginary circular lines, and the outlet openings can be situated on a common imaginary line.
As a development of the invention, the nozzle is designed as a dual-substance nozzle having an internal mixing chamber, wherein the mixing chamber has a liquid inlet and a gas inlet.
Dual-substance nozzles are advantageous precisely for applications in the gas cooling sector. By means of the invention, conventional dual-substance nozzles can be improved in respect of the distribution of the droplet spray produced.
As a development of the invention, the mixing chamber is of annular design, wherein the outlet passages start from the mixing chamber.
As a development of the invention, a conical distribution wall is provided, wherein the annular mixing chamber adjoins the distribution wall at the side or adjoins a circumferential edge of the distribution wall.
A conical distribution wall is used to distribute an introduced liquid jet into a uniform thin film, which is then divided into individual droplets at the entry of the mixing chamber by the gas jets, which are likewise entering the mixing chamber.
As a development of the invention, an imaginary extension of at least one gas inlet passage extends into the region of the circumferential edge of the conical distribution wall.
In this way, the gas jets from the gas inlet passage or from a plurality of gas inlet passages impinge on the water film produced by means of the distribution wall precisely where this film leaves the distribution wall. This promotes the breakup of the water film into individual droplets.
Further features and advantages of the invention will become apparent from the claims and the following description of a preferred embodiment of the invention in conjunction with the drawings, in which:
The illustration in
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In the front view in
The illustration in
Compared with the conventional dual-substance nozzle 10 in
The illustration in
The dual-substance nozzle 50 has an air inlet 52 and a water inlet 54, wherein the air inlet 52 and the water inlet are arranged concentrically with one another and wherein the water inlet 54 is arranged within the annular air inlet 52. Air entering the nozzle housing 20 is indicated by means of dashed arrows 56, and water entering the nozzle housing 20 is indicated by means of a dashed arrow 58.
Water enters through the water inlet 54, which first of all narrows in a frustoconical shape. After a section 60 of constant diameter, the water inlet passage once again widens in a conical shape. The entering waterjet then impinges upon a conical distribution wall 62, the cone tip of which lies on the central longitudinal axis of the nozzle housing 20. As illustrated by means of two small curved arrows which extend arrow 58, the entering liquid jet is divided and is split by means of the distribution wall 62 into a film which moves further out in an approximately radial direction on the conical distribution wall 62. The conical distribution wall 62 ends at an encircling circumferential edge 64. At the circumferential edge 64, the distribution wall merges into an annular mixing chamber 66.
Starting from the air inlet 52, passages 68 lead in a straight line to the mixing chamber 66. In accordance with the arrow 56, the entering air jets thus impinge in the region of the circumferential edge 64 upon the liquid film that is just leaving the distribution wall 62 at the circumferential edge 64. The liquid film is thereby broken down into individual droplets by means of the air jets. The droplet/air mixture then moves through the annular mixing chamber 66 and continues to be intimately mixed, with the result that a droplet spray can then emerge at the outlet openings 22, 24. As already explained with reference to
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