The present invention is explained in greater detail below on the basis of an exemplary embodiment. In the drawing are illustrated:
As shown in the drawing, the nozzle has an outer casing element 2 and an inner displacement body 1 having a round cross section, having a length L2 and extending in to the casing element 2 over a length L1. In this way a nozzle gap 14 is bordered. The casing tube 4 is connected by means of a detachable connector 4.1, such as a nut, to a bordering wall 4.
The displacement body 1 has a tapered area 3 on its rear end with which it is connected to a feed element 5 for a treatment medium. This feed element 5 thus forms the holding device for the displacement body 1.
The feed element 5 is held in the bordering wall 4 of a pressure space 6.1 by means of a holder 12, which allows a carrier medium 11 to flow from the pressure space 6.1 to the nozzle gap 14. A rear bordering wall 7 of the pressure space 6.1 serves to hold the feed element 5. The pressure space 6.1 is bordered on its circumference by a tubular wall 6, which has an inlet opening 10 for a carrier medium 11.
Between the holder 12 and the bordering wall 4 and the tapered area 3, a mixing chamber 18 is provided, a carrier medium 11 flowing into it the axial direction at one end and on the other end a treatment medium 9 flowing out across the direction of flow of the carrier medium 11; this treatment medium is supplied by means of the feed element 5, which has outlet openings 13 on its end facing the tapered area 3, from which the treatment medium 9 flows out and begins to mix with the carrier medium. This process is continued in the nozzle gap 14.
If L2, the length of the displacement body 1, is greater than the depth of immersion L1 in the casing element 2, there is the possibility that when the distal end of this nozzle becomes clogged or destroyed, the distal end of the displacement body might be simply cut off by means of a disk cutter, so that operation of the nozzle can be begin again within a very short period of time.
The functioning of the nozzle is as follows:
The carrier medium 11 enters the pressure chamber 6.1 through the feed opening 10 and passes through the permeable holder 12 into the mixing chamber 18, going from there into the nozzle gap 14. The treatment medium 9 enters the feed element 5 and leaves it through the opening 13, so that it enters the mixing chamber 18 across the direction of flow of the carrier medium, preferably even at a right angle to it. The mixture undergoes acceleration through the tapered area 3, so that the mixing process is continued in the nozzle gap 14.
The diameter ratio of the inside diameter D1 of the nozzle pipe 2 and the outside diameter D2 of the displacement body 1 determines the throughput of the treatment medium and the carrier medium and the momentum in the core area 16 and in the near area 17 of the nozzle, like the ratio of the static pressure p2 of the carrier medium 11 and the total pressure p1 of the treatment medium at the outlet openings 13. The length of the mixing zone, starting from the mixing chamber 18 through the nozzle gap 14, has an influence on the throughput and the momentum, so that these parameters may be used to regulate the operation of the nozzle.
Number | Date | Country | Kind |
---|---|---|---|
10 2006 037 369.3 | Aug 2006 | DE | national |
10 2007 003 665.7 | Jan 2007 | DE | national |