WASTEWATER PURIFICATION DEVICE AND UTILIZATIONS

Abstract

The invention relates to a solid filtering wastewater treatment device (100) comprising a first stage (101) with a freely drained fixed culture arranged directly above a second fixed water saturated culture stage (105), and a force aeration system (110) extending under the second stage. The invention also relates to a wastewater treatment method, as well as a process for sludge mineralization, implementing such a purification device.

Claims

1-14. (canceled)

15. A sewage treatment device (10, 100) of the filtering solid type comprising a first stage (11, 101) with freely drained vertical flow culture arranged directly above a second stage (15, 105) with fixed culture saturated with vertical and/or horizontal flow water, and a forced aeration system (17, 110) extending under the second stage.

16. The sewage treatment device according to claim 15, wherein the second water saturated fixed culture stage is vertical and horizontal flow.

17. The sewage treatment device according to claim 15, wherein the first stage has a thickness between 10 and 50 cm and/or the second stage has a thickness between 100 and 200 cm.

18. The sewage treatment device according to claim 15, wherein the first stage is a filter planted with macrophytes.

19. The sewage treatment device according to claim 15, wherein the forced aeration system is capable of operating continuously or discontinuously.

20. The sewage treatment device according to claim 15, said device comprising at least two series of filters (12, 22, 13, 23; 102, 106, 103, 107) in parallel, intended to operate alternately.

21. The sewage treatment device according to claim 20, comprising two treated effluent collection systems (108, 109) each arranged at a different filter of the second stage, said collection systems being intended to operate alternately.

22. The sewage treatment device according to claim 20, wherein the forced aeration system is adapted to operate alternately and/or sequentially at one or other of the filters (106, 107), the second stage, so as to alternate the aerobic and anoxic conditions in said filters.

23. A process for treating wastewater comprising feeding the first stage of the sewage treatment device according to claim 15 with raw effluent, a phase (A) of mineralization of sludge accumulating on the surface of the first stage; a phase (B) of aerobic degradation of pollution dissolved at the second stage; a phase (C) for evacuating the treated water.

24. The process according to claim 23, wherein the forced aeration system operates alternatively or sequentially, so as to alternate the aerobic and anoxic conditions within the second stage, said treatment method comprising a phase (D) of denitrification of the nitrates at the second stage under anoxic conditions before the evacuation phase (C).

25. The process according to claim 23, wherein the aerobic degradation phase (B) of the dissolved pollution at the second saturated and aerated stage is accompanied by at least partial removal of the pathogenic germs present in the effluent.

26. The process according to claim 23, wherein the sewage treatment device comprises at least two series of filters in parallel, wherein when a second stage filter is supplied with oxygen by the forced aeration system, another filter of the second stage is not supplied to create anoxic conditions, and vice versa, said method comprising a denitrification phase (D) at the second stage filter under anoxic conditions.

27. The process according to claim 26, wherein the second stage is provided with two systems for collecting the treated effluent each disposed at a different filter of said second stage, and wherein the phase (C) is discharged through the collection system located at the unfiltered filter, so that the effluent percolates vertically from the first stage into the feed filter of the second stage, then horizontally into the unfiltered filter of the second stage. floor, before being evacuated.

28. A method of mineralization of sludge comprising said method comprising a phase (A) of feeding the sewage treatment device according to claim 15 with wastewater and forming a sludge and mineralization of the sludge accumulating on the surface of the first floor; a phase (B) of aerobic degradation of dissolved pollution at the second stage; optionally a nitrate denitrification phase (D) at the second stage level; and a phase (C) for discharging the treated wastewater.

Description

[0032] The invention will be better understood on reading the description which follows and on examining the figures that accompany it. These are presented for illustrative purposes and in no way limit the invention. The figures represent:

[0033] FIG. 1: A schematic representation in longitudinal section of a device for wastewater treatment according to an exemplary embodiment of the invention;

[0034] FIG. 2: A schematic representation in longitudinal section of a device for wastewater treatment according to another embodiment of the invention;

[0035] FIGS. 3 and 4: Two schematic representations of the water treatment device according to FIG. 2, operating in alternating mode.

[0036] A first embodiment of the device according to the invention is shown in FIG. 1, which comprises at least two filters in parallel. The configuration of the device thus shown does not allow denitrification, but only nitrification.

[0037] The water treatment device 10 comprises, more precisely, a first stage 11, each of the filters 12, 13 of which can be fed by tarpaulin by means of a feed 14 of raw wastewater. The surface of the first stage 11, planted with reeds, retains/filters the suspended matter contributing to the formation of the sludge layer and whose mechanical action of the plants allows the permeability. The first stage also comprises, under the reeds, a particulate filtering material. Directly under the particulate filter material of the first stage the particulate filter material of the second stage 15 extends. The second stage 15 is saturated with water: a loading gauge 16 makes it possible to maintain the water level.

[0038] A forced aeration system 17 makes it possible to inject oxygen into the treatment system 10. More specifically, the forced aeration system comprises a booster 18 and a network of pipes 19 extending into the bottom 20 of the water treatment device 10. For example, the pipe network 19 extends against the geomembrane covering the surface of the ground in which the device is implanted. The pipe network 19 is for example constituted by a plurality of pipes drilled in order to allow the air supplied by the booster 18 to be released. The pipes are for example spaced 5 to 20 cm apart to ensure a good distribution oxygen over the entire surface of the device. A drain 21 also extends into the bottom 20 of the device 10 for recovering the treated water and the drain to the outside of the device.

[0039] With such a treatment device 10, the screened wastewater arriving at one of the filters 12, 13 of the first stage 11 percolates vertically in said filter 12. The mineralization of the sludge accumulating on the surface of the first filter 12 of the first stage 11 is favored by the good oxygenation of the said filter 12. Indeed, the force ventilation system 17 makes it possible to increase the oxygenation of the filter 12 and thus optimizes mineralization of sludge. Furthermore, insofar as the second filter 13 is at rest, the sludge which has accumulated on the surface of the second filter 13 during a preceding feed phase may continue to mineralize and thus clogging is avoided.

[0040] After having percolated vertically in the filter 12 of the first stage 11, the water percolates vertically in a first filter 22 of the second stage 15, located under the first filter 12 of the first stage 11. The biological degradation which began in the filter 12 of the first stage 11 continues in the filter 22 of the second stage 15, including nitrification, favored by the large oxygenation of said filter by means of the forced aeration system 17.

[0041] The treated water is evacuated via the drain 21 extending on the bottom of the device 10 along the filters 22 and 23 of the second stage 15. A slope may be provided at the bottom 20 of the device 10 on either side of the drain 21, in order to avoid areas of stagnation.

[0042] FIGS. 2, 3 and 4 show a second embodiment of the device according to the invention, which also comprises two series of filters in parallel.

[0043] The water treatment device 100 also comprises a first stage 101, of which each of the filters 102, 103 can be supplied by tarpaulin by means of a feed 104 to the untreated wastewater. A second stage 105, saturated with water, is directly situated under the first stage 101. Two loading chambers 108, 109, each disposed at one end of a filter 106, 107 of the second stage 105, allow the water level to be maintained.

[0044] A forced ventilation system 110, capable of operating alternately, makes it possible to inject oxygen into the treatment device 100, from one and/or the other of the two filters 106, 107 of the second stage 105. For example, a valve system (not shown) alternately supplies oxygen to an array of pipes extending under the first filter 106 of the second stage 105 or a network of pipes extending under the second filter 107 of said second stage 105.

[0045] The loading ports 108, 109 also make it possible to collect the treated water. These collection systems can operate alternatively, in order to recover treated water from one or the other of said systems.

[0046] Device 100 may advantageously be used as described herein: A sheeting of crude raw effluent is poured onto the first filter 102 of the first stage 101 (FIGS. 2 and 3). The wastewater percolates vertically towards the first filter 106 of the second stage 105. Again, the mineralization of the sludge accumulating on the surface of the first filter 102 is promoted by the good oxygenation of the said filter 102. The second filter 103 of the first stage 101 is, on the other hand, at rest.

[0047] The forced aeration system 110 advantageously injects oxygen only at the level of the first filter 106 of the first stage. Thus, said first filter 106 is under aerobic conditions, while the second filter 107 is under anoxic conditions.

[0048] After percolating vertically in the filter 102 of the first stage 101, the waters percolate vertically in the first filter 106 of the second stage 105 located under the first filter 102 of the first stage 101. The conditions within the first filter 106 of the second stage 105 are combined to allow the treatment of dissolved pollutions including nitrification.

[0049] The collection system 109 opposite the first filter 106 of the second stage 105 is in operation, while the collection system 108 on the side of the first filter 106 does not operate (valve closed). Thus, to be evacuated, the treated water must pass through the second filter 107 of the second stage 105, in which they will percolate horizontally. The second filter 107 being in anoxic conditions, nitrification of the nitrates can then take place. A treatment of the overall nitrogen is thus obtained, leaving device 100.

[0050] During the next supply cycle (FIG. 4), the second filter 103 of the first stage 101 is supplied, the first filter 101 being put to rest. The forced aeration system 110 also changes the oxygen injection zone so that the first filter 106 of the second stage 105 is found under anoxic conditions, while the second filter 107 of the second stage 105 is in aerobic conditions. Similarly, the activated collection system is reversed. The treated water is evacuated by the system 108 opposite the second filter 107 so that the water which percolates vertically in the second filter 107 also percolates horizontally in the first filter 106 before being evacuated.

[0051] It is thus possible to alternate the cycles of active aeration phases and rest phases in the series of filters 102, 106 and 103, 107.

[0052] According to the invention, it is possible to provide more series of filters in parallel, for example three, four, etc., in particular so as to space the operating times of each of the filters.