The invention will be explained herein after with reference to an 20 exemplary embodiment illustrated in the drawing.
As can be seen from the drawing, the apparatus for separating residues comprises a housing 1 that abuts the bottom through swinging elements 2, in the case illustrated herein through compression springs. Inside the housing, a plurality of non-perforated plates 3.1 through 3.5 is connected to the housing, their inclination being adjustable. The plates are disposed in such a manner that the slag or residue 4 placed onto the uppermost and first plate 3.1 reaches first the plate 3.2, which exhibits substantially the same incline, before falling onto the plate 3.3 lying underneath, this process being continued until, via plate 3.4, the slag or the residues have reached plate 3.5 from where they are discharged to the outside.
This transport of residues or slag occurs through vibrations generated by vibrators 5. On the opposite side of the housing 1, which is not visible in the drawing, there is disposed a second vibrator 5 that generates vibration energy with movement components in the direction of the plates 3.1 through 3.5 that are extending downward.
Through a suction pipe 6, gas is drawn by means of a fan that has not been illustrated herein, said gas entering at the upper side 7 of the housing and being thereby in communication with the site in the waste treatment plant or on the firing grid in the region of which there still is a lot of unconsumed oxygen. The slag is supplied on the side indicated at 7.
The fact that this gas still contains quite a lot of oxygen is advantageous since this gas passes through the mass flows of the residues falling downward in a cascade, thereby promoting another reaction leading to improved burnout of the slag. As an alternative or in addition thereto, ambient air may also be supplied through the front side 8 of the housing.
The gas flows 9 between the oblique plates serve for wind sieving, i.e., they entrain the fines. On its further course, the suction pipe labelled at 6 is connected to a cyclone and then to a filter so that the fine fraction entrained in the gas flow may be obtained and recirculated, together with the combustion air, to the waste combustion process.
Number | Date | Country | Kind |
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10 2006 035 260.2 | Jul 2006 | DE | national |
Applicants claim priority under 35 U.S.C. § 119 of German Application No. 10 2006 035 260.2 filed Jul. 26, 2006 and Applicants also claim priority under 35 U.S.C. §119(e) of U.S. Provisional Application No. 60/897,016 filed Jan. 23, 2007.
Number | Date | Country | |
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60897015 | Jan 2007 | US |