WASTEWATER TREATMENT PLANT AND METHOD FOR TREATING WASTEWATER
20180093907 · 2018-04-05
Assignee
Inventors
Cpc classification
C02F2201/003
CHEMISTRY; METALLURGY
Y02W10/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C02F2203/006
CHEMISTRY; METALLURGY
C02F3/043
CHEMISTRY; METALLURGY
C02F3/1242
CHEMISTRY; METALLURGY
International classification
C02F3/00
CHEMISTRY; METALLURGY
Abstract
The invention concerns a wastewater treatment plant and a method for it. The plant comprising at least one main reactor module (30) having a plurality of stackable filter-modules (50), each filter-module purifying wastewater independently by being individually charged batchwise with wastewater. The wastewater is discharged on each filter-module by means of a deflector (44) referenced to a filter-module (50), the deflector creating a back pressure in dependency of the gravity-flow-force of the wastewater leading to that the wastewater is spilled from the deflector (44) in an angle of discharge relative to a horizontal plane evenly onto every independent filter-module, respectively.
Claims
1. A wastewater treatment plant, comprising at least one main reactor module (30) having a plurality of filter-modules (50) arranged one below the other, each filter-module treating wastewater independently by being individually charged with wastewater coming from a feed-element (40) which includes at least one downspout (42) for forwarding the water from the feed-element by gravitational force onto at least one deflector (44) comprised by the feed-element and associated with a filter-module, respectively, the deflector creating a deflection of wastewater at the outlet of the downspout in dependency of the pressure of the wastewater by means of a design for creating a predetermined angle of discharge relative to a horizontal plane to evenly distribute the wastewater by spilling the latter from each deflector in the same manner in every independent filter-module, respectively.
2. The wastewater treatment plant according to claim 1, characterized in that the plant comprises a feed-reservoir (10), within which feed-reservoir a minimum-water level (12) is defined which is higher in altitude as any of the filter-modules (50) and the plant further comprising a feed-valve (20) being provided downstream the feed-reservoir (10) and leading to the feed-element (40), the feed-valve enabling a batchwise feeding of wastewater to the feed-element.
3. The wastewater treatment plant according to claim 2, characterized in that the feed-valve (20) is of a construction according to which several pipes are interleaved with height- and diameter dimensions getting smaller from the outermost to the inner one so that a plurality of overflows is provided, wherein due to the predetermined diameter of each pipe a flow cross-section is essentially equal and maintained through the whole flow path along the valve.
4. The wastewater treatment plant according to claim 3, characterized in that the air-inlet (22) is connected to a ventilation device the function of which is to control the valve.
5. The wastewater treatment plant according to claim 1, characterized in that a filter-module (50) comprises an upper air-space (52), an intermediate filter-substrate (54) and a lower drainage layer (60).
6. The wastewater treatment plant according to claim 5, characterized in that the filter-substrate (54) comprises at its bottom a geotextile (56) having a mesh size small enough to prevent the substrate from permeating and a mesh cloth (58) to form a drainage channel.
7. The wastewater treatment plant according to claim 2, characterized in that a primary treatment (8) is connected upstream the feed-reservoir (10) realizing a) a buffering of wastewater to the feed-reservoir b) a sedimentation of solid matter, and c) a flotation of fat-substances.
8. The wastewater treatment plant according to claim 1, characterized in that a drainage storage container (80) is connected downstream the reactor module of filter-modules (50) gathering the purified wastewater and buffering the same.
9. The wastewater treatment plant according to claim 1, characterized in that an inspection chamber (90) is provided having accommodated an integrated technics-module (100).
10. The wastewater treatment plant according to claim 8, further comprising an inspection chamber (90) with an integrated technics-module (100), characterized in that the drainage storage container (80) and the inspection chamber (90) are combined to constitute a single reservoir.
11. A method for treating wastewater in a wastewater treatment plant comprising a main reactor module (30) having a plurality of stackable filter-modules (50), each filter-module purifying wastewater independently by being individually charged batchwise with wastewater by means of creating a pressure being determined such that the wastewater is discharged onto each filter-module by means of a deflector (44) referenced to a filter-module (50), the deflector creating a deflection for wastewater in dependency of the total pressure of the wastewater leading to that the wastewater is spilled from the deflector (44) in an angle of discharge relative to a horizontal plane evenly onto every independent filter-module, respectively.
12. The method according to claim 11, characterized in that the wastewater is fed from a feed-reservoir (10), wherein a total pressure of the flow of wastewater is created by means of a filling level of the feed-reservoir (10) along with the gravitational force aimed by a declining slope-line from the feed-reservoir towards the main reactor module, wherein the filling level within the feed-reservoir is adjusted and the pressure for batchwise charging is created by means of a feed-valve (20) being interconnected between the feed-reservoir and the main reactor module.
13. The method according to claim 12, characterized in that the total pressure is monitored by measuring the flow rate through the feed-valve (20).
14. The method according to claim 12, characterized in that the water level in the feeding-reservoir is monitored by measuring an air pressure of an air barrier created in the feed-valve (20).
Description
DETAILED DESCRIPTION OF AN EMBODIMENT
[0079] In the following the invention is elucidated with reference to the drawings in which
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[0087] Before going into the details of the drawings, it should be noted that the representation of scale for any component in the figures does not reflect a real size since they are schematically meant only.
[0088] As this is to be seen in
[0089] In between the free-fall line starting from the feed-reservoir 10 to the reactor module 30 there is interconnected a feed-valve 20. The feed-valve aims to produce a gush of wastewater being fed into the reactor module 30 and thus onto each filter-module, respectively. Only by means of a sufficient strong gush of water necessary flow velocities can be achieved which are needed for an optimal ejection and distribution of water by spilling or sprinkling the same onto the respective filter-modules.
[0090] To control the feed-valve 20 into an opened and closed state there is provided an air-inlet 22 with which an air-barrier can be produced inside the valve. When opening the feed-valve by suction of said air out of the valve a gush of water passes through the feed-valve due to the total pressure of the wastewater caused by the filling level of the feed-reservoir and the declining slope towards the feed-valve, and further on by gravitational force into the feeding element 40. The feeding element 40 comprises a downspout 42 from which the wastewater is transported onto several deflectors 44 which distribute the wastewater to be purified onto the respective filter-modules 50. Every filter-module comprises an air space 52 in which the wastewater is distributed onto a filter substrate 54 laying beneath. At the bottom of the filter substrate 54 there is arranged a textile 56 having a mesh size small enough to prevent the substrate from permeating. The lowest section of a filter-module provides a drainage layer 60 comprising a layer of mesh cloth. Every drainage layer 60 opens into a gathering drainage channel for the filtered water.
[0091] In the result, all the filtered water coming from any filter-module is united within the reactor module 30what is realised according to the shown embodiment at the inner side of the circumferential wall of the reactor module 30. From there, the filtered water is then conveyed further to for example a drainage storage container 80.
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[0093] According to the right hand embodiment of
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[0096] The primary treatment 8 into which wastewater enters from an influent 6 encompasses three primary stages which are interconnected by a free-fall line. Said primary treatment aims a buffering of the wastewater to be purified, a sedimentation of solid particles as also a floatation of light weight substances. From the last stage of the primary treatment 8 the wastewater then flows by gravitational force into the feed-reservoir 10. In the present case shown in
[0097] According to the shown embodiment, both the feed-reservoirs 10 are arranged directly above the main reactors 30, respectively. This makes it possible in a very suitable way to use a feed-valve which is shown in
[0098] From both these reactors the purified water is then further fed by free-fall and thus gravitational force into the drainage storage container 80. According to the shown embodiment, the drainage storage container 80 and the inspection chamber 90 is one and the same container combining these elements together. Within the latter there is arranged the technics-module 100 accommodating all the control and pneumatic equipment. From said combined container the purified wastewater runs out by an external effluent or alternatively to a dephosphating stage which is within the inspection chamber, too. Additional and or optional the water in the drainage storage container 80 or the inspection chamber 90 can be pumped back into the feed-reservoir or directly into the feed-element and thus is recirculated into the main reactor or the main reactors.
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[0100] The construction shows four pipes in all (however the general concept of it is not restricted to the number of four pipes). The diameter of each pipe is chosen such that a flow cross-section is equal and maintained through the whole flow path along the valve. The pipes as shown are interleaved non-concentrically but they could even be interleaved concentrically. At the top of the valve an upper closing cover 24 is shown which closes the valve except an air-inlet and -outlet 22 (see also
[0101] At the bottom of the valve there is a closing cover 24, too, which includes an outlet-opening having the same dimension as the smallest pipe from which the water leaves the valve. The arrows shown in the drawing do disclose the flow path of the water through the valve. Reference number 23 designates a supporting collar by means of which the feed-valve can be placed in the feed-reservoir (not shown in
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REFERENCE NUMERALS
[0104] 6 influent
[0105] 8 primary treatment
[0106] 10 feed-reservoir
[0107] 12 minimum level of the feed-reservoir
[0108] 14 maximum level of the feed-reservoir
[0109] 16 comfort volume water level
[0110] 20 feeding valve
[0111] 21 overflow opening
[0112] 22 air-inlet and -outlet of the feeding valve
[0113] 23 supporting collar
[0114] 24 closing cover
[0115] 30 reactor module
[0116] 40 feed-element
[0117] 42 downspout
[0118] 44 deflector
[0119] 46 deflector edge of deflector
[0120] 47 stop ridge
[0121] 48 gap between downspout outlet and deflector
[0122] 49 baffle plate for reduction of cross-section
[0123] 50 filter-module
[0124] 52 air space of the filter-module
[0125] 54 filter substrate
[0126] 56 geotextile
[0127] 58 mesh
[0128] 60 drainage layer
[0129] 61 drainage channel
[0130] 62 vertical pipe section
[0131] 63 intermediate spacer
[0132] 64 opening to drainage
[0133] 80 drainage storage container
[0134] 90 inspection chamber
[0135] 100 technics-module
[0136] 102 air container/pressure accumulator