Method and microflotation system for removing contaminants from a body of water

Abstract

The invention relates to a method for removing contaminants from a body of water, in particular from a rain basin, comprising the following steps: • producing dispersion water by enriching water under elevated pressure with a gas, • introducing the dispersion water into the body of water via a dispersion water line, which has an outlet opening at a specified water depth, wherein pressure relief occurs and a multiplicity of microbubbles are produced, which attach to contaminants and rise to the surface of the body of water, so that a flotation sludge forms on the surface, • removing the flotation sludge from a defined surface region by means of a clearing device, wherein • the outlet opening is arranged at a fixed position in the body of water, • the body of water has, in a vicinity of the outlet opening, a flow having a flow speed and having a flow direction, and • the defined surface region is arranged at a distance from the outlet opening in the flow direction.

Description

[0001] Method and microflotation system for removing contaminants from a body of water

[0002] The invention relates to a method for removing impurities from a body of water, in particular from a rainwater basin, and a microflotation system designed for this purpose.

[0003] Microflotation systems can be used in a wide variety of applications for the efficient separation of contaminants such as solid particles or oil droplets, for example, in industrial wastewater treatment or sewage treatment plants. For this purpose, the wastewater is directed into a flotation tank specifically designed for microflotation. So-called dispersion water is also added to the flotation tank; that is, water that has been enriched with air or another gas under increased pressure. The gas is dissolved in the dispersion water. As the pressure is reduced when the dispersion water is introduced into the flotation tank, countless microbubbles are formed, which slowly rise to the surface. The contaminants are then deposited on the microbubbles and also transported to the surface, where a float is formed. This float is removed using appropriate equipment.

[0004] Also known are floating microflotation systems that are arranged to float on the surface of a body of water for its purification. In this case, the dispersion water can be introduced directly into the water instead of into a special flotation basin. For example, EP 3 647 272 A1 describes a flotation system for purifying a body of water with a barrier that encloses a surface area of ​​the water and a pressure relief valve located below this surface area. The known microflotation system can, in particular, be used as a free-floating system on the water. Based on this, the object of the invention is to provide a method for removing contaminants from a body of water and a microflotation system specifically designed for this purpose, which can be used more easily and with greater efficiency in a body of water with a current.

[0005] This problem is solved by the method with the features of claim 1 and by the microflotation system with the features of claim 7. Advantageous embodiments are specified in the respective subsequent dependent claims.

[0006] The process is used to remove contaminants from a body of water, especially from a stormwater retention basin, and comprises the following steps:

[0007] • Production of dispersed water by enriching water under increased pressure with a gas,

[0008] • Introducing the dispersion water into the body of water through a dispersion water pipe that has an outlet opening at a predetermined water depth, causing a pressure release and the formation of numerous microbubbles that attach to impurities and rise to the surface of the body of water, forming a float on the surface,

[0009] • Removal of the float using a room device from a defined surface area, whereby

[0010] • the outlet opening is located at a fixed position in the body of water,

[0011] • the body of water in the vicinity of the outlet opening has a current with a flow velocity and a flow direction, and

[0012] • The defined surface area is arranged at a distance in the flow direction from the outlet opening. The production of the dispersion water can take place in a pressure saturator, i.e., in a pressure vessel to which the water and the gas to be dissolved are supplied. Preferably, enough gas is dissolved in the water until a saturation concentration is reached.

[0013] The dispersed water produced in this way is introduced into the body of water via a dispersed water line. A separate flotation tank is not used. The dispersed water line has an outlet opening located at a predetermined water depth. This water depth refers to the distance of the outlet opening from the water surface. When the dispersed water is introduced into the body of water, pressure is released, particularly at a pressure relief valve located in the dispersed water line. This causes the formation of numerous microbubbles, which attach themselves to impurities and rise to the surface of the water.Maintaining the specified water depth ensures that, even with significant fluctuations in the water level, the microbubbles travel a minimum distance to the surface and remain submerged long enough for contaminants to adhere effectively. The outlet opening can be located at or away from the pressure relief valve. It is understood that multiple dispersion lines and / or outlet openings can be used simultaneously. In this case, the multiple outlet openings can, for example, all be arranged at the same water depth, particularly side-by-side in a row perpendicular to the flow direction and / or evenly or nearly evenly distributed across the entire width of the water body.

[0014] A float containing the separated impurities forms on the surface of the water. This float is removed using a system whose function and design ensure a defined surface area.

[0015] ,.. / 4 area of ​​the treated water body. The float removed from the treatment facility can be conveyed into a collection container, which may be located in the water body, but is preferably situated on the bank of the water body.

[0016] In the invention, the outlet opening is arranged at a fixed horizontal position within the body of water. A fixed position means that the outlet opening does not move with the current present in the body of water, but is located at a fixed position relative to the bottom or a bank of the body of water, independent of the current. A current exists in the body of water, particularly in the vicinity of the outlet opening. There, the current has a flow velocity and a flow direction. Flow velocity and direction depend on the type of body of water, but also on the prevailing environmental conditions. If the body of water is a river or a canal, the flow velocity can be relatively high. It also depends on the volume of water the river or canal is carrying at any given time.In the particularly relevant application of a stormwater retention basin, stormwater treatment basin, or surface water collection basin, the flow within the basin results from the incoming and outgoing water volumes. This flow, as well as the water level in the basin, is subject to sometimes extreme fluctuations, especially during a sudden heavy rainfall event. The basin can be a natural depression in the landscape or it can be artificially constructed. In the former case, the banks and bottom of the water body are generally irregularly shaped. An artificially constructed basin, for example made of concrete, may have a uniform depth. The edge of such an artificially created basin can be formed by straight walls, which, like the irregularly shaped edge of a natural water body, are subsequently referred to as the bank.A special feature of the invention is that the defined surface area captured by the airlock is positioned at a distance from the outlet opening, specifically in the direction of flow. This ensures that the float formed by the microbubbles slowly rising to the surface, which may accumulate at a considerable lateral distance from the outlet opening due to the flow, is reliably captured by the airlock. In particular, this prevents the float, or parts thereof, from sinking again before they can be removed by the airlock. As a result, optimal float removal can be achieved with a relatively simple airlock system.In particular, it is not necessary to cover the entire surface of the water body or a large part of it with the cleaning system, as is the aim in conventional flotation tanks, for example, when using a chain cleaning system. A distance in the direction of flow means that the defined surface area is located downstream of the outlet opening with respect to the current present in the water body.

[0017] Tests have shown that, with careful coordination of the defined surface area relative to the outlet opening, very high separation rates can be achieved in flowing waters. In contrast, a freely floating microflotation system has proven disadvantageous, particularly because, firstly, the current quickly carries it to a downstream bank. At this point, the current prevents the removal of the float, or at least prevents its complete removal. Secondly, with a freely floating microflotation system, it is not guaranteed that all relevant areas of the water body will be affected by the purification process.

[0018] ...16 In the procedure according to the invention, the outlet opening can be fixedly arranged at a particularly suitable position in the body of water, and the resulting flotation can be removed almost completely. Furthermore, the fixed arrangement of the microflotation system simplifies the transport of the removed flotation to the shore.

[0019] In one embodiment, the spacing is adjusted to the flow velocity such that a large proportion of the microbubbles rising to the surface reach the defined surface area. The spacing can be adjusted experimentally or calculated from the average rise velocity of the microbubbles and the flow velocity.

[0020] In one configuration, the water body is a stormwater retention basin, a stormwater treatment basin, or a surface water collection basin. As mentioned, it can be a natural or artificial basin. Characteristic of all the basins mentioned are the highly fluctuating levels of pollution, water levels, and flow conditions. The inventive process can be well adapted to these conditions, thus achieving high efficiency even in dynamic situations.

[0021] In one embodiment, the flow velocity is measured and the distance is adjusted according to the measured flow velocity. This ensures optimal adjustment of the distance and thus high efficiency, even with changing flow velocities.

[0022] In one embodiment, the predetermined water depth at which the outlet opening is located is adjustable, with the predetermined water depth being set in particular according to the average ascent velocity of the microbubbles. The ascent velocity of the microbubbles depends on many factors, on the one hand on the size distribution of the microbubbles, and on the other hand on the nature and quantity of adhering contaminants, and thus also on the contamination level of the water. The flow velocity in the body of water can also have an influence, because the number of microbubbles per volume of water is lower due to the faster distribution of the microbubbles at higher flow velocities, and the microbubbles rise much faster in clusters than individually. Therefore, the predetermined water depth can alternatively or additionally be set according to the flow velocity.The average rise velocity of the microbubbles can be determined experimentally or during the operation of the microflotation system, or it can be calculated approximately based on one or more of the aforementioned influencing factors. The predetermined water depth can be set manually or automatically with a suitable actuator.

[0023] In one embodiment, a baffle plate is positioned in the water body between the outlet opening and the defined surface area. The baffle plate acts as a barrier for the dispersion water exiting the outlet opening and the microbubbles that form. The width of the baffle plate, measured perpendicular to the flow direction, can be selected such that at least a large proportion of the microbubbles from all the outlet openings enter the baffle plate's area of ​​influence. In particular, the baffle plate can extend across the entire width of the water body. Tests have shown that the baffle plate can significantly influence the spatial distribution of the microbubbles that form. Specifically, with a suitable baffle plate arrangement, a higher microbubble concentration and a higher probability of contact between the microbubbles and individual particles can be achieved.Both parameters have a significant influence on the separation rates and thus on the efficiency of the process.

[0024] In one embodiment, the flow velocity is measured, and the baffle plate arrangement is adjusted according to the measured flow velocity. The baffle plate arrangement refers in particular to the distance of the baffle plate from the outlet opening, the water depth at which the baffle plate is positioned, its horizontal extent, its vertical extent, and / or its inclination relative to the vertical. To adjust the horizontal or vertical extent of the baffle plate, it can have several baffle plate elements that are movable relative to each other. Tests have shown that further efficiency improvements are possible by adjusting the baffle plate arrangement to the measured flow velocity.It is assumed that the improvements are due to the fact that, particularly at high flow velocities, the appropriate arrangement of the baffle plate prevents the dispersed water exiting the outlet from being distributed too quickly and over too wide a distance in the body of water. This distribution is accompanied by a dilution of the dispersed water and can result in a significant reduction in the number of microbubbles formed.

[0025] The microflotation system with the features of claim 7 serves to remove impurities from a body of water, in particular from a rainwater retention basin, and comprises the following:

[0026] • a device for producing dispersed water by enriching water under increased pressure with a gas,

[0027] • a dispersion water line leading from the dispersion water production facility to an outlet opening,

[0028] • a room layout,

[0029] • a first positioning device to which the dispersion water line is attached in such a way that the outlet opening is located at a fixed position in the body of water and at a predetermined water depth, and

[0030] ...19 • a second positioning device to which the room device is attached, such that the room device is positioned at a fixed position in the water body and detects a defined surface area on the surface of the water body, wherein the defined surface area is located at a distance in a flow direction of the water body from the outlet opening.

[0031] The microflotation system is particularly suitable for carrying out the described process. For the features and advantages of the microflotation system, reference is made to the preceding explanations, which apply accordingly. The special arrangement of the discharge opening and the airlock in the microflotation system is achieved by the fact that the system has two positioning devices. These devices allow the arrangement of the discharge opening and the airlock in the water body to be determined such that the distance between the defined surface area and the discharge opening is specified in the direction of flow. The positioning devices adjust the vertical arrangement of the discharge opening and the airlock to the water level in the water body, thus ensuring that the discharge opening is at the specified water depth and the airlock is at the surface of the water body.This can be achieved, for example, using the floating devices described below. Alternatively, the water level in the body of water can be measured, and the vertical positions adjusted using, for example, a hydraulic or electric actuator. The actuator can be anchored, for example, to the bank or the bottom of the body of water.

[0032] In one design, it

[0033] • the first positioning device a first floating unit to which the dispersion water line is attached, and a first fastening device connected to the first floating unit, and / or • the second positioning device a second floating unit to which the room equipment is attached, and a second fastening device connected to the second floating unit.

[0034] The dispersion water line is attached to the first floating unit, ensuring it remains at a predetermined depth even with fluctuating water levels. The filtration unit is attached to the second floating unit and is therefore also positioned near the water's surface. The first floating unit is held in a fixed position by a primary mooring device and thus does not move with the current. A second mooring device secures the second floating unit, which houses the filtration unit, to a fixed position. The mooring of the two floating units ensures that the defined surface area covered by the filtration unit is positioned at a distance from the outlet opening, in the direction of the water's current.

[0035] In one embodiment, the first and / or the second mooring device is anchored to a bank or bottom of the water body. At least one of the two mooring devices is anchored to the bank or bottom of the water body to ensure the secure attachment of the first or second floating unit directly connected to it. The other mooring device, which is associated with the other floating unit, can also be anchored to a bank or bottom of the water body; alternatively, it can be attached to the first (or second) mooring device or to the first (or second) floating unit. In any case, the two mooring devices ensure that both floating units remain firmly attached to the surface of the water body, independent of the current. are arranged and the distance between the outlet opening and the defined surface area is maintained.

[0036] In one embodiment, the dispersed water production unit is positioned on the bank of the water body or attached to the first positioning device, e.g., the first floating unit. For example, the first floating unit can have a floating platform on which the dispersed water production unit is located. Due to the fixed position of the first floating unit, the dispersed water production unit can also be easily positioned on the bank, and the dispersed water line can run from there to the discharge opening. A particular advantage of this solution is that the elements of the microflotation system positioned on the water body are particularly compact and thus have less impact on the water flow.

[0037] In one configuration, the microflotation system includes a measuring device for the flow velocity of the water. The distance can be predetermined based on the flow velocity recorded by the measuring device.

[0038] In one embodiment, the first positioning device and / or the second positioning device includes an actuator that can change the position of the outlet opening in the water body, the predetermined water depth at which the outlet opening is located, and / or the position of the room fixture in the water body. This allows, in particular, the adjustment of the distance between the outlet opening and a defined surface area.

[0039] In one embodiment, the microflotation system includes a control unit connected to the measuring device and the actuator. This unit is configured to adjust the distance between the outlet opening and the defined surface area according to a measured flow velocity, and / or to adjust the predetermined water depth at which the outlet opening is located according to the average rise velocity of the microbubbles. In this way, maintaining the optimal distance can be ensured automatically.

[0040] In one embodiment, the microflotation system includes a baffle plate positioned in the water between the outlet opening and the defined surface area. In another embodiment, the microflotation system includes an actuator for the baffle plate, allowing adjustment of the baffle plate's position, in particular its distance from the outlet opening, its water depth, its horizontal extent, its vertical extent, and / or its inclination relative to the vertical. The control system is connected to the actuator for the baffle plate and is configured to adjust the baffle plate's position according to a measured flow velocity. Reference is made to the preceding explanations of the correspondingly configured method.

[0041] In one embodiment, the room equipment includes an extraction device with at least one extraction opening or at least one screw conveyor, wherein the surface area covered by the room equipment is defined by the arrangement of the at least one extraction opening or the at least one screw conveyor. In both cases, the defined surface area is determined by the arrangement and design of the room equipment.

[0042] The invention is explained in more detail below with the aid of figures. The figures show: Fig. 1 shows a microflotation system in a rainwater retention basin in a schematic side view.

[0043] Fig. 2 shows the microflotation system from Figure 1 in a schematic top view,

[0044] Fig. 3 shows another microflotation system in a stormwater retention basin in a schematic side view, and

[0045] Fig. 4 shows the microflotation system from Figure 3 in a schematic view from above.

[0046] Figure 1 shows a stormwater retention basin 10 with an inlet 12 and an outlet 14. The water flowing in and out via the inlet and outlet creates a current within the stormwater retention basin, which flows from right to left in Figure 1. Surface water from several sources is collected in the inlet 12 and discharged together into the stormwater retention basin 10.

[0047] On the bank of the stormwater retention basin 10 is a facility 16 for producing dispersed water, which in this example comprises three pressure vessels 18. Water taken from the outlet 14 of the stormwater retention basin 10 is introduced into the pressure vessels 18 via a line 56. Air is also supplied (not shown) and dissolved in the water under increased pressure in the pressure vessels 18. The dispersed water produced in this way flows via three dispersed water lines 20, each of which has a pressure relief valve assembly 22, to three outlet openings 24, each of which is located at an outlet of the respective pressure relief valve assembly 22. Downstream of the outlet- Under pressure release, countless microbubbles 26 form in the openings 24, which is represented by a cone in Fig. 1.

[0048] Each of the pressure relief valve assemblies 22 with its associated outlet opening 24 is attached to a first floating unit 28, which has a walkable platform 30. A baffle plate 32, the arrangement of which is adjustable, is also attached to the first floating unit 28. By attaching the pressure relief valve assemblies 22 with their outlet openings 24 to the first floating unit 28, the outlet openings 24 are always at a predetermined water depth, regardless of the fill level of the stormwater retention basin 10.

[0049] Also shown is a second floating unit 34, which has a room device 36. The room device 36 detects a defined surface area 38 and is designed to remove a float formed on the surface from this defined surface area 38.

[0050] A distance 40 is formed between the outlet opening 24 and the defined surface area 38 in the direction of flow; the defined surface area 38 is located downstream of the outlet opening 24 with respect to the flow formed in the rainwater retention basin 10.

[0051] In Fig. 2, the elements already described are provided with the same reference numerals as in Fig. 1. Additionally, a first fastening device with four cables 42 is visible, with which the first floating unit 28 is braced on both sides to the bank of the stormwater retention basin. The second floating unit 34 is also braced on both sides to the bank of the stormwater retention basin 10 by two cables 42 and is thus fixed in its position in the water body. The air intake device 36 has a float pipe 44 leading to the bank of the stormwater retention basin 10. Several suction openings 46 of the air intake device 36 are arranged distributed approximately over the entire width of the stormwater retention basin 10. The resulting defined surface area 38, encompassed by the air intake device 36, is strip-shaped and is located at a distance 40 from the outlet openings 24 of the three pressure relief valve assemblies 22.

[0052] Figures 3 and 4 show an alternative arrangement to that shown in Figures 1 and 2, which differs with respect to the first and second fastening devices. A base 50 is anchored to the bottom 48 of the stormwater retention basin 10. A first fastening device for the first floating unit 28 has two vertically upward-pointing rods 52 attached to the base 50, which pass through openings in the first floating unit 28. They fix the position of the first floating unit 28 without impeding its up-and-down movement as the water level in the stormwater retention basin 10 changes.

[0053] The second floating unit 34 is also attached to the base 50 via two rods 52, the position of these rods 52 in the direction of flow being adjustable by an actuator (not shown), as indicated by the double arrow 54.

[0054] In Fig. 4 it can be seen that with the described anchoring of the two floating units 28, 34 to the bottom 48 of the rainwater retention basin 10, it is not necessary to use guy wires to the banks of the rainwater retention basin 10. List of reference symbols

[0055] 10 regular retention basins

[0056] 12 Inflow

[0057] 14 Procedure

[0058] 16 Equipment for producing dispersed water

[0059] 18 pressure vessels

[0060] 20 Dispersion water line

[0061] 22 Relief valve arrangement

[0062] 24 Exit opening

[0063] 26 microbubbles

[0064] 28 first floating unit

[0065] 30 Bridge

[0066] 32 Impact plate

[0067] 34 second floating unit

[0068] 36 Room furnishings

[0069] 38 defined surface area

[0070] 40 From stand

[0071] 42 rope

[0072] 44 Fl otatl leitung

[0073] 46 Intake opening

[0074] 48 reasons

[0075] 50 sockets

[0076] 52 bars

[0077] 54 Double Arrow

[0078] 56 Management

[0079] ,.. / 17

Claims

Claims 1. Method for removing contaminants from a body of water, in particular from a stormwater retention basin, comprising the following steps: • Production of dispersed water by enriching water under increased pressure with a gas, • Introducing the dispersion water into the water body through a dispersion water pipe (20) which has an outlet opening (24) at a predetermined water depth, whereby a pressure release occurs and a large number of microbubbles (26) are formed, which attach themselves to impurities and rise to the surface of the water body, so that a float forms on the surface, • Removal of the float with a room device (36) from a defined surface area (38), characterized in that • the outlet opening (24) is located at a fixed position in the body of water, • the water in the vicinity of the outlet opening (24) has a current with a flow velocity and a flow direction, and • the defined surface area (38) is arranged at a distance (40) in the direction of flow from the outlet opening (24).

2. Method according to claim 2, characterized in that the distance (40) is adapted to the flow velocity such that a large proportion of the microbubbles (26) rising to the surface enter the defined surface area (38).

3. Method according to claim 1 or 2, characterized in that the water body is a stormwater retention basin (10), a stormwater clarification basin or a surface water collection basin.

4. Method according to one of claims 1 to 3, characterized in that the flow velocity is measured and the distance (40) is adjusted according to the measured flow velocity.

5. Method according to one of claims 1 to 4, characterized in that the predetermined water depth in which the outlet opening is arranged is adjustable, wherein the predetermined water depth is adjusted in particular according to an average ascent velocity of the microbubbles.

6. Method according to one of claims 1 to 5, characterized in that a baffle plate (32) is arranged in the water between the outlet opening (24) and the defined surface area (38), wherein in particular the flow velocity is measured and the arrangement of the baffle plate (32), in particular a distance of the baffle plate (32) from the outlet opening (24), a water depth in which the baffle plate (32) is arranged, an extent of the baffle plate (32) in a horizontal direction, an extent of the baffle plate (32) in a vertical direction and / or an inclination of the baffle plate (32) relative to the vertical is adjusted according to the measured flow velocity.

7. Microflotation system for removing contaminants from a body of water, in particular from a stormwater retention basin, wherein the microflotation system comprises the following: • a device (16) for producing dispersed water by enriching water under increased pressure with a gas, - 19 - • a dispersion water line (20) leading from the device (16) for the production of dispersion water to an outlet opening (24), and • a room furnishing (36), characterized by • a first positioning device to which the dispersion water line (20) is attached such that the outlet opening (24) is located at a fixed position in the water body and at a predetermined water depth, • a second positioning device to which the room device (36) is attached, such that the room device (36) is arranged at a fixed position in the water body and detects a defined surface area (38) on the surface of the water body, wherein the defined surface area (38) is arranged at a distance (40) in a flow direction of the water body from the outlet opening (24).

8. Microflotation system according to claim 7, characterized in that • the first positioning device comprises a first floating unit (28) to which the dispersion water line (20) is attached, and a first fastening device connected to the first floating unit (28), and / or • the second positioning device comprises a second floating unit (34) to which the room device (36) is attached, and a second fastening device connected to the second floating unit (34).

9. Microflotation system according to claim 8, characterized in that the first fastening device and / or the second fastening device is anchored to a bank of the water body or to a bottom (48) of the water body.

10. Microflotation plant according to one of claims 7 to 9, characterized in that the device (16) for producing dispersion water on the shore - 20 - of the body of water or attached to the first positioning device.

11. Microflotation system according to one of claims 7 to 10, characterized in that the microflotation system has a measuring device for the flow velocity of the water.

12. Microflotation system according to one of claims 7 to 11, characterized in that the first positioning device and / or the second positioning device has an actuator with which the position of the outlet opening (24) in the water, the predetermined water depth in which the outlet opening (24) is arranged, and / or the position of the room device (36) in the water can be changed.

13. Microflotation system according to claim 12, characterized in that the microflotation system has a control unit which is connected to the measuring device and the actuator and is configured to adjust the distance (40) between the outlet opening (24) and the defined surface area (38) according to a measured flow velocity and / or which is connected to the actuator and is configured to adjust the predetermined water depth in which the outlet opening (24) is arranged according to an average ascent velocity of the microbubbles.

14. Microflotation system according to one of claims 7 to 13, characterized in that the microflotation system has a baffle plate (32) which is arranged in the water between the outlet opening (24) and the defined surface area (38), wherein the microflotation system in particular has an actuator for the baffle plate (32) with which the arrangement of the baffle plate (32), in particular a distance of the baffle plate (32) from ,.. / 21 - 21 - the outlet opening (24), a water depth in which the baffle plate (32) is arranged, an extent of the baffle plate (32) in a horizontal direction, an extent of the baffle plate (32) in a vertical direction and / or an inclination of the baffle plate (32) relative to the vertical is adjustable, wherein the control is connected to the actuator for the baffle plate (32) and is designed to adjust the arrangement of the baffle plate (32) according to a measured flow velocity.

15. Microflotation system according to one of claims 7 to 14, characterized in that the room equipment (36) has a suction device with at least one suction opening (46) or at least one screw conveyor, wherein the surface area (38) covered by the room equipment (36) is defined by the arrangement of the at least one suction opening (46) or the at least one screw conveyor.

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