Patent Application
20140299535
1. Field
The invention relates to a contact filter device for separating suspended floating matter, sludge particles and solid matter particles from water.
2. Related Arts
Contact filter devices are already known, for example from U.S. Pat. No. 3,886,064, U.S. Pat. No. 4,151,084, U.S. Pat. No. 4,889,624, WO86/05412 and WO94/411312. All these devices have the disadvantage that they are poorly to be cleaned and maintained and that they can only separate suspended solid matter which is heavier than water. Also the efficiency in separating the solid matter hardly exceeds 85 to 90 percent.
It is an object of the invention to provide a contact filter device with a higher efficiency which is also able to separate suspended matter which is lighter than water.
For this purpose, the inventive contact filter device for filtering of untreated water and delivering clean water comprises a rectangular filter box in which an admission duct is arranged on a wall of the filter box, and in which a contact tube bundle is provided between the admission duct and a side of the filter box laying opposite to the admission duct, wherein the widths of the admission duct is approximately equal to the widths of the filter box, and the depth of the admission duct is a fraction of the widths of the filter box, and the admission duct has, at its upper area, an admission stub for the untreated water and, at the bottom, is open towards the interior of the filter box. Preferably, the admission duct is also open at its top.
The inventive contact filter device can separate suspended matter which is lighter than water, and an efficiency of the separation of more than 96 percent can be achieved in the contact filter device. Besides suspended matter and matter which are heavier than water, also living microorganisms of the output of biological cleaning stages can be separated from water by the inventive contact filter device. By means of the presence of the admission duct which hydraulically homogenizes the input of the water to be treated, the separation efficiency of the contact filter device is maximized.
An advantageous embodiment of the inventive contact filter device is characterized in that the filter box comprises a plane filter bottom and, subsequently thereto, four equally high side walls, a north side, a south side, an east side and a west side, wherein, in particular, also the admission duct has the shape of a rectangular box which is formed out of four equally high side walls, a north side, a south side, an east side and a west side. Thereby, a structure of the contact filter device clearly arranged and easily to produce, is resulting.
A further advantageous embodiment of the inventive contact filter device is characterized in that the relationship of the breadth of the south side of the filter box to the breadth of the south side of the admission duct amounts to approximately 5 to 15, whereby the hydraulic homogenization of the water stream to be cleaned, is improved.
A further advantageous embodiment of the inventive contact filter device is characterized in that the admission duct mounted in the filter box is removably mounted on the filter box such that it may be preferably taken out upwards from the filter box whereby, in an advantageous way, the cleaning of the contact filter device is facilitated.
A further advantageous embodiment of the inventive contact filter device is characterized in that the admission duct mounted to the filter box, overtops the filter box by at least one breadth of the south side of the admission duct, whereby, in an advantageous way, an easy mounting and demounting of the admission duct is ensured and, furthermore, the input stub may be placed at a position in the admission duct which is advantageous in view of process technology.
A further advantageous embodiment of the inventive contact filter device is characterized in that the filter box comprises an inclined discharge weir for floating sludge whereby the discharge weir preferably is arranged in form of an inclined rectangular plate having a horizontal weir edge as well as two side plates. Through the discharge weir, the floating sludge which is forming on the surface of the water, may be discharged, in an advantageous way, in a simple and efficient way for example to a waste removal container.
A further advantageous embodiment of the inventive contact filter device is characterized in that the discharge weir is arranged at a U-shaped, rectangular cut-out from the upper edge of the south side of the filter box, and that the breadth of the discharge weir approximately corresponds to the difference in length between the breadth of the south side of the filter box minus the breadth of the south side of the admission duct.
A further advantageous embodiment of the inventive contact filter device is characterized in that, in at least one side wall next to the transition to the filter bottom, a discharge stub is inserted for sludge sediment which stub is hydraulically connected to a sludge discharge valve, preferably a flap or ball valve. In advantageous way, it is possible thereby to discharge the sludge sediment deposited at the filter bottom easily from the contact filter device by temporarily, quickly opening the sludge discharge valve.
A further advantageous embodiment of the inventive contact filter device is characterized in that a collector for purified water in the shape of a vertically mounted tube piece being open at the top and at the bottom which is immersed by half into the water level forming at the top of the filter box with a horizontal level line A-A, and that a horizontally mounted clear water conduit is inserted into the collector which clear water conduit leads out of the contact filter device and, preferably, is shut off by a valve. By means of this arrangement, the clear water may be discharged in an advantageous way from the contact filter device while circumventing the floating sludge.
A further advantageous embodiment of the inventive contact filter device is characterized in that the contact tube bundle which is preferably implemented as a construction unit, comprises a plurality of equally long, vertical tube elements out of metal or plastics mounted in an honeycombed way close to each other, the upper ends and lower ends thereof being open, wherein, preferably, the opening diameter of the upper end and the lower end corresponds approximately to the tube diameter minus two times the wall thickness of the tube elements. By means of these contact tube bundle, a high efficiency in separating solid matter is achieved in an advantageous way.
A further advantageous embodiment of the inventive contact filter device is characterized in that the tube element has a shell surface (34) being formed ripped or as a perforated structure or as net structure, wherein a perforated structure is preferred. Thereby, the efficiency of the separation of solid matter is further put up in an advantageous way, in particular when the texturing of the shell surface is implemented such that a wetted surface of 100 to 300 m2 per cubic meter contact tube bundle is available.
A further advantageous embodiment of the inventive contact filter device is characterized in that the rectangular filter box is provided with reinforcement rips provided on the outside, whereby, in an advantageous way, a material saving light construction of the contact filter device is made possible while maintaining the required stability of the filter box.
Further advantages, features and potential applications of the present invention may be gathered from the sub-claims.
Throughout the description, the claims and the drawings, those terms and associated reference signs will be used as are notable from the enclosed list of reference signs. In the drawings:
The inventive device in
The admission duct 7 has the shape of a rectangular sheet metal box which is open at the top and at the bottom and formed out of four equally high side walls, a south side 8, a north side 9, a west side 10, an east side 18 as well as an upper opening 12 and a lower opening 11. The admission duct 7 is mounted in the filter box 1 such that the west side 10 of the admission duct lies against the west side 6 of the filter box 1.
The relationship of the breadth of the south side 4 of the filter box 1 to the breadth of the south side 8 of the admission duct amounts to about 5 to 15
The north side 3 of the filter box 1 has the same breadth as the south side 4 of the filter box 1. The north side 9 of the admission duct has the same breadth as the south side 8 of the admission duct.
The relationship between the breadth of the south side 4 of the filter box 1 to the distance H of the admission duct 7 from the filter bottom 2 amounts approximately to 1 to 3
The admission duct 7 comprises an inlet stub 13 for untreated water. The input stub 13 opens, as shown in
As mounted in the filter box 1, the admission duct 7 surmounts the same by at least a breadth of the south side 8 of the admission duct 7 whereby an easy mounting and demounting of the admission duct is ensured and, furthermore, the inlet stub 13 can be arranged at a position at the admission duct 7 which is advantageous in view of process technology. The admission duct 7 can also be simply pulled off upwards from the filter box 1 such that the cleaning of the same can be carried out in an easy way.
The filter box 1 has an inclined discharge weir 14 for floating sludge. The discharge weir 14 in the shape of an inclined, rectangular plate comprises a horizontal weir edge 15 as well as two side plates 16 and 17. As shown in
As experiments have shown, the inventive contact filter device comprises an optimized separation efficiency if the relationship of the length is:
A discharge stub 20 for sludge sediment is inserted into at least one of the side walls 3, 4, 5 or 6 of the filter box 1 near to the transition to the filter bottom 2. The discharge stub 20 is hydraulically connected to the sludge discharge valve 21. The sludge discharge valve 21 is in the shape of a flap or ball valve so that the sludge sediment as deposited on the filter bottom 2, can be discharged from the contact filter device by temporarily, quickly opening of 21.
The contact filter device comprises, furthermore, a collector 22 for purified water. The collector 22 has the shape of a vertically mounted tube piece which is open at the top and at the bottom and which is submerged by half into the water level being formed at the top in the filter box 1 with the horizontal level line A-B.
As is shown in
As explained in
Further, a rectangular shaped contact tube bundle 30 is arranged in the filter box 1. The contact tube bundle 30 comprises a plurality of equally long, vertical and honeycombed shaped tube elements 31 out of metal or plastics mounted next to each other, the upper ends 32 and the lower ends 33 thereof being open. Preferably, the opening diameter of 32 and 33 corresponds to the tube diameter minus two times the wall thickness of the tube elements 31.
Furthermore, the shell surface 34 of the tube element 31 is arranged to be textured, ripped or as perforated net. As experiments have shown, the contact filter device shows an optimized separation efficiency when the texturing of the shell surface 34 is implemented such that a wetted surface of 100 to 300 m2 is available per cubic meter of contact tube bundle. The length of the contact tube bundle 30 corresponds to the interior breadth of the east side 5 of the filter box 1. The breadth of the contact tube bundle 30 corresponds approximately to the length difference between the breadth of the south side 4 of the filter box 1 minus the breadth of the south side 8 of the admission duct 7.
As experiments have shown, the contact filter device comprises an improved separation efficiency if the distance J of the contact tube bundle 30 from the filter bottom 2 as measured from the lower end 33 of a tube element 31 on mounting in the filter box is chosen such that:
J=1×H to 3×H
is true.
The height of the contact tube bundle 30 amounts to 1 to 3 meters, and tube elements 31 if they are shorter than 1 to 3 meters, are arranged vertically on top of each other if necessary.
As experiments have shown, the contact filter device comprises an optimized separation efficiency if the distance L of the clear water line 24 from the contact tube bundle 30 is measured from the upper end 32 of the tube element 31, is structurally dimensioned in the filter box 1 such that:
L=1×H to 3×H
is true.
The tube elements 31 of the contact tube bundle are completely accessible on the top thereof such that an eventual cleaning process can be carried out easily.
As can be seen from
The untreated water 3 which is contaminated by suspended floating matter, sludge particles and solid state particles, enters into the admission duct 7 through the input stub 13 and continuously flows downwards to the filter bottom 2 where sludge materials which are heavier than water, are deposited.
The untreated water purified in this way, further-on flows vertically upwards and continuously enters the lower tube opening 33 of the tube elements 31 of the contact tube bundle 30.
Upon flowing through the contact tube bundle 30, the water is further cleaned of finest, floating materials and of living microorganisms.
The water purified in this way, exits on top from the upper tube openings 32 of the tube elements 31 of the contact tube bundle 30 and flows upwards to the collector 22. From the collector 22, the purified water P exits the inventive device through the opened valve 26 and through the clear water conduit 24.
From time to time, the deposited sludge L deposited on the filter bottom 2 is removed or discharged, respectively, from the inventive device by opening the valve 21. The inflow of the untreated water R to the inventive device is not interrupted during this sludge discharge operation.
Certain residual amounts of suspended floating materials, sludge particles and solid state particles may collect on the water level with the level line A-B above the contact tube bundle 30, and they form a layer of floating sludge F there. For the removal of the floating sludge F collected at the height of the level line A-B on the water, the shut-off valve 26 for clear water is closed during running input of untreated water R to the inventive device.
By means of this measure, the water in the contact filter device is accumulated, and as a consequence, the height of the level line A-B slowly increases until the water level reaches the height of the weir edge 15 and the floating sludge F flows through the discharge weir for floating sludge 14 out of the inventive contact filter device.
The output of an aerobic, biological clarification plant for commercial untreated water and constructed according to WO2010145810 (method and device for purifying untreated water), was introduced into the inventive contact filter device as untreated water stream R.
The dwelling time of the untreated water to be cleaned, in the contact filter device amounted to about 80 to 160 minutes.
After each 72 hours, the deposited sludge as deposited at the filter bottom 2 was discharged through the discharge stub 20 together with about 9 volume percent of the total water amount present in the contact filter device by opening the valve 21.
As a result, the cleared discharge stream B of about 1 m3h which exited the inventive contact filter device via the clear water conduit 24, constantly shows only a content of unfilterable materials (ATV Rules No. 2-2) of less than 20 milligrams per liter which corresponds to a efficiency of the separation of 99 percent.
| Number | Date | Country | Kind |
|---|---|---|---|
| 202011051065.4 | Aug 2011 | DE | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2012/066322 | 8/22/2012 | WO | 00 | 4/10/2014 |
