Drinking water treatment device capable of efficiently removing algae

By combining the processes of grid flocculation tank, inclined tube sedimentation tank and high-efficiency air flotation ultrafiltration tank, the problems of poor algae removal effect and large footprint in the existing technology have been solved, achieving efficient and safe drinking water treatment and reducing chemical consumption and wastewater rate.

CN223950888UActive Publication Date: 2026-02-27SHANGHAI ZHONGHAN YIJIETE VALVE CO LTD
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Patent Information

Application Number
CN202520527255.7
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-03-25
Publication Date
2026-02-27
Estimated Expiration
2035-03-25

AI Technical Summary

Technical Problem

Existing technologies are ineffective at removing algae when treating eutrophic water bodies, leading to severe membrane fouling. They also require large land areas, have high wastewater rates, and lack sufficient treatment efficiency and safety for ultrafiltration water purification processes.

Method used

By combining grid flocculation tanks, inclined tube sedimentation tanks, and high-efficiency air flotation ultrafiltration tanks, the flocculation, sedimentation, and air flotation processes enhance water flow turbulence and flocculation effects. Hollow fiber ultrafiltration membranes are used for membrane separation, and disinfection treatment is combined to ensure drinking water safety.

Benefits of technology

It significantly improves treatment efficiency, reduces algae pollution and wastewater rate, extends the service life of ultrafiltration membranes, reduces chemical consumption, and ensures the safety and economy of drinking water.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to a drinking water treatment device capable of efficiently removing algae, which comprises a grid flocculation basin, an inclined tube sedimentation basin and an efficient air floatation ultrafiltration basin, a water inlet of the grid flocculation basin is connected with a raw water pump through a water inlet pipe, and an outlet end of the grid flocculation basin is connected with a water inlet of the inclined tube sedimentation basin. An outlet end of the inclined tube sedimentation tank is connected with a water inlet of the efficient air flotation ultrafiltration tank through a flow guide pipe, an ultrafiltration membrane produced water outlet in the efficient air flotation ultrafiltration tank is respectively connected with a backflow water pipe and a produced water pipe through pipelines, and the other end of the backflow water pipe is connected with a water inlet of the dissolved air pump. An air inlet of the dissolved air tank is connected with an air pipe, the other end of the air pipe is connected with an air compressor, an outlet in the bottom end of the dissolved air tank is connected with a dissolved air water pipe, and the other end of the dissolved air water pipe is connected to a releaser at the bottom of the efficient air flotation ultrafiltration tank; according to the utility model, algae pollution can be reduced, the backwashing medicine consumption of the ultrafiltration membrane is reduced, the problem of large occupied area is solved, the safety of drinking water is ensured, and the treatment efficiency is improved.
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Description

[TECHNICAL FIELD]

[0001] The utility model relates to water treatment technical field, concretely is a kind of high-efficiency algae-removing drinking water treatment device. [BACKGROUND]

[0002] At present, the seasonal algal outbreak problem caused by water body eutrophication is more and more prominent, and the conventional water purification process has poor removal effect on algae, which seriously threatens the drinking water supply safety. Ultrafiltration technology with high pollution removal efficiency will have wide application prospect in drinking water treatment, but under the background that natural water body eutrophication phenomenon cannot be effectively controlled, membrane pollution caused by algae will seriously restrict the ultrafiltration water purification process.

[0003] The principle adopted by the prior art is: first, add polyaluminum chloride and sodium hypochlorite into raw water, carry out grid flocculation and inclined tube sedimentation conventional treatment, then use high-efficiency filter brick filter to carry out high-efficiency treatment on the settled water, and finally flow the treated clear water into the clear water tank for disinfection treatment before drinking.

[0004] The steps are mainly as follows: first, use a pipeline static mixer to mix polyaluminum chloride and residual chlorine added by polyaluminum chloride dosing system and sodium hypochlorite dosing system with raw water and enter the grid flocculation reaction tank through the input pipeline, and the vortex reaction and coagulant generated inside the grid flocculation reaction tank are mixed; then, the mixed water mixed by the pipeline static mixer and entering the grid flocculation reaction tank is subjected to multi-box automatic circulation and stirring inside the grid flocculation reaction tank, so that the suspended solids and coagulant in the water are contacted and reacted again, separated, and the sludge and particles are preliminarily settled, and the settled sludge and particles sink to the bottom of the tank and are automatically discharged through the blowdown pipe; the alumen flowers formed by the mixing and stirring of the grid flocculation reaction tank flow into the inclined tube sedimentation tank for secondary sedimentation, the particles are separated from the water again by the honeycomb inclined tube filler inside the inclined tube sedimentation tank, the alumen flowers are settled to the bottom by gravity, the suspended solids and colloidal particles in the water are further removed, the settled sludge and particles sink to the bottom of the tank and are automatically discharged through the blowdown pipe; finally, the settled water flows into the high-efficiency filter brick filter for filtration, effectively intercepts the small particles, bacteria, viruses or other particles in the water, ensures the safety of the effluent, and the filtered water flows to the backwash tank, and then is pumped back to the high-efficiency filter brick filter from the backwash tank for repeated washing and filtration, and finally the treated clear water flows into the clear water tank for disinfection treatment before drinking.

[0005] However, this existing technical solution has the following main shortcomings: The solution involves first adding polyaluminum chloride and sodium hypochlorite to the raw water for conventional treatment such as grid flocculation and inclined tube sedimentation; then using a high-efficiency filter brick to treat the settled water; finally, the treated water is discharged into a clear water tank for disinfection before drinking, thus achieving the desired treatment effect. However, under actual operating conditions, its effectiveness against fine particulate colloidal dissolved matter (organic matter, heavy metals, etc.) in the water is limited. The most advanced treatment in the process is filtration using porous granular filter media such as quartz sand (coarse filtration), which has limited effectiveness and suffers from high wastewater rates. [Utility Model Content]

[0006] The purpose of this invention is to address the aforementioned shortcomings by providing a highly efficient algae removal drinking water treatment device that can reduce algae pollution, decrease the consumption of chemicals for ultrafiltration membrane backwashing, solve the problem of large footprint, ensure the safety of drinking water, and improve treatment efficiency.

[0007] To achieve the above objectives, a high-efficiency algae removal drinking water treatment device is designed, comprising a grid flocculation tank 1, an inclined tube sedimentation tank 2, and a high-efficiency air flotation ultrafiltration tank 3. The inlet of the grid flocculation tank 1 is connected to a raw water pump 21 via an inlet pipe 22, and raw water enters the grid flocculation tank 1 through the raw water pump 21. The outlet of the grid flocculation tank 1 is connected to the inlet of the inclined tube sedimentation tank 2, and the outlet of the inclined tube sedimentation tank 2 is connected to the inlet of the high-efficiency air flotation ultrafiltration tank 3 via a guide pipe 27. The high-efficiency air flotation ultrafiltration tank 3 is equipped with an ultrafiltration membrane 29. The product water outlet of the ultrafiltration membrane 29 is connected to the return water pipe 34 and the product water pipe 30 through pipes respectively. The other end of the return water pipe 34 is connected to the inlet of the dissolved air pump 35. The outlet of the dissolved air pump 35 is connected to the inlet of the dissolved air tank 38 through a pipe. The air inlet of the dissolved air tank 38 is connected to the air pipe 36. The other end of the air pipe 36 is connected to the air compressor 37. The outlet at the bottom of the dissolved air tank 38 is connected to the dissolved air water pipe 39. The other end of the dissolved air water pipe 39 is connected to the release device 40 at the bottom of the high-efficiency air flotation ultrafiltration tank 3.

[0008] Furthermore, a pipeline mixer 25 is installed on the pipeline between the raw water pump 21 and the grid flocculation tank 1. The raw water enters the pipeline mixer 25 through the inlet pipe 22 via the raw water pump 21. A pretreatment dosing module 23 is connected to the pipeline mixer 25 via a pretreatment dosing pipe 24. Polyaluminum chloride and sodium hypochlorite are added to the raw water through the pretreatment dosing module 23 and the pretreatment dosing pipe 24. After being fully mixed by the pipeline mixer 25, the raw water enters the grid flocculation tank 1.

[0009] Further, the grid grid is arranged in the grid flocculation tank 1, the inclined tube filler 26 is arranged in the inclined tube sedimentation tank 2, and the raw water enters the inclined tube sedimentation tank 2 through the water inlet on the lower tank wall after flowing through the grid grid in the grid flocculation tank 1, and the suspended impurities in the water are deposited in the inclined tube filler 26, and the water flowing upwards along the inclined tube filler 26 enters the high-efficiency air floatation ultrafiltration tank 3 through the flow guide pipe 27, so that when the raw water flows through the grid grid in the grid flocculation tank 1, the water flow path is forced to be scaled and turned, and then complex turbulence and vortex phenomena are generated, the collision frequency is increased, the micro-particles with flocculation performance are gradually gathered into larger flocculation bodies, and the water treated by flocculation enters the inclined tube sedimentation tank 2 through the water inlet on the lower tank wall, so that the suspended impurities in the water are deposited in the inclined tube filler 26, and the water treated by deposition enters the high-efficiency air floatation ultrafiltration tank 3 through the flow guide pipe 27.

[0010] Further, the inclined tube sedimentation tank 2 comprises a water inlet area, an inclined tube filler area and a water outlet area, the water inlet area, the inclined tube filler area and the water outlet area are sequentially arranged from bottom to top, the inclined tube filler 26 is arranged in the inclined tube filler area, and the bottom of the inclined tube sedimentation tank 2 is provided with a sludge discharge outlet.

[0011] Further, the water production pipe 30 is connected with a disinfection and dosing pipe 33, one end of the disinfection and dosing pipe 33 is connected with a disinfection and dosing pump 32, and the other end of the disinfection and dosing pump 32 is connected with a disinfection and dosing module 31, so that sodium hypochlorite is added into filtered liquid through the disinfection and dosing module 31, the disinfection and dosing pump 32 and the disinfection and dosing pipe 33, and then the filtered liquid is transported to users through a pipe network, so as to ensure the safety of drinking water.

[0012] Further, the high-efficiency air floatation ultrafiltration tank 3 is provided with a sludge scraper 28, the sludge scraper 28 is used for removing floating sludge, one side of the top of the high-efficiency air floatation ultrafiltration tank 3 is provided with a blowdown outlet, and the blowdown outlet is connected with a blowdown pipe 41, so that the floating sludge removed by the sludge scraper 28 can be discharged through the blowdown pipe 41.

[0013] Further, the ultrafiltration membrane 29 is arranged in the middle of the high-efficiency air floatation ultrafiltration tank 3, and spaces are reserved between the ultrafiltration membrane 29 and the inner wall of the high-efficiency air floatation ultrafiltration tank 3 around the ultrafiltration membrane 29, the hollow fiber ultrafiltration membrane tube is arranged in the ultrafiltration membrane 29 to realize membrane separation, so that harmful substances such as iron rust, silt, suspended solids, colloids, bacteria and macromolecular organic matter in water can be filtered out, and some mineral elements beneficial to human body can be reserved.

[0014] Compared with the prior art, the utility model has the advantages of:

[0015] (1) The utility model provides a kind of more fast and convenient efficient algae-removing drinking water treatment device, can reduce algae pollution, reduce ultrafiltration membrane backwash medicine consumption, solve the problem of large floor area, ensure the safety of drinking water;

[0016] (2) The utility model is treated after high-efficiency air floatation ultrafiltration tank, and water recovery rate is high, and use cost is low, and high-efficiency air floatation ultrafiltration tank can effectively reduce water body algae pollution;

[0017] (3) The utility model combines air floatation and ultrafiltration process together, not only can significantly improve processing efficiency, save floor area, but also can reduce wastewater rate;

[0018] (4) The utility model prolongs the service life of ultrafiltration membrane by air floatation and ultrafiltration process, reduces backwash medicine consumption, and is worth promoting application. [DETAILED DESCRIPTION]

[0019] Figure 1 It is the structure diagram of the utility model;

[0020] In the drawing: 1, grid flocculation tank;2, inclined tube sedimentation tank;3, high-efficiency air floatation ultrafiltration tank;21, raw water pump;22, water inlet pipe;23, pretreatment dosing module;24, pretreatment dosing pipe;25, pipeline mixer;26, inclined tube filler;27, flow guide pipe;28, slag remover;29, ultrafiltration membrane;30, water production pipe;31, disinfection dosing module;32, disinfection dosing pump;33, disinfection dosing pipe;34, backflow pipe;35, dissolved air pump;36, air pipe;37, air compressor;38, dissolved air tank;39, dissolved air water pipe;40, releaser;41, blowoff pipe. [DETAILED DESCRIPTION]

[0021] As attached Figure 1The utility model provides a kind of high-efficiency algae-removing drinking water treatment device, including grid flocculation tank 1, inclined tube sedimentation tank 2 and high-efficiency air floatation ultrafiltration tank 3, the water inlet of grid flocculation tank 1 is connected raw water pump 21 by water inlet pipe 22, raw water enters grid flocculation tank 1 by raw water pump 21, the water inlet of inclined tube sedimentation tank 2 is connected to the export end of grid flocculation tank 1, the water inlet of high-efficiency air floatation ultrafiltration tank 3 is connected to the export end of inclined tube sedimentation tank 2 by flow guide pipe 27, high-efficiency air floatation ultrafiltration tank 3 is equipped with ultrafiltration membrane 29 inside, the water outlet of ultrafiltration membrane 29 is connected return flow pipe 34 and water production pipe 30 respectively by pipeline, the other end of return flow pipe 34 is connected the water inlet of dissolved gas pump 35, the water outlet of dissolved gas pump 35 is connected the water inlet of dissolved gas tank 38 by pipeline, the air inlet of dissolved gas tank 38 is connected air pipe 36, the other end of air pipe 36 is connected air compressor 37, the outlet of the bottom end of dissolved gas tank 38 is connected dissolved gas water pipe 39, the other end of dissolved gas water pipe 39 is connected to the release ware 40 of the bottom of high-efficiency air floatation ultrafiltration tank 3, and the release ware can be a rectangular parallelepiped box without upper cover welded with steel plate;Pipeline mixer 25 is installed on the pipeline between raw water pump 21 and grid flocculation tank 1, raw water enters pipeline mixer 25 by water inlet pipe 22 through raw water pump 21, and pretreatment dosing module 23 is connected to pretreatment dosing pipe 24 on pipeline mixer 25, so that polyaluminium chloride and sodium hypochlorite are added into raw water through pretreatment dosing module 23 and pretreatment dosing pipe 24, and the raw water is mixed fully in pipeline mixer 25 and then enters grid flocculation tank 1.

[0022] Among them, grid grating is arranged in grid flocculation tank 1, inclined tube filler 26 is arranged in inclined tube sedimentation tank 2, after raw water flows through grid grating in grid flocculation tank 1, the water inlet on the lower pool wall enters inclined tube sedimentation tank 2, suspended impurities in water are deposited in inclined tube filler 26, and water flowing along inclined tube filler 26 enters high-efficiency air floatation ultrafiltration tank 3 through flow guide pipe 27, so that when raw water enters grid flocculation tank 1 and flows through grid grating, water flow path is forced to be scaled and turned, and then complex turbulence and vortex phenomenon are generated, micro-particles with flocculation performance are gradually gathered into larger flocculation bodies by increasing collision frequency, and water treated by flocculation enters inclined tube sedimentation tank 2 through the water inlet on the lower pool wall, so that suspended impurities in water are deposited in inclined tube filler 26, and water treated by deposition enters high-efficiency air floatation ultrafiltration tank 3 through flow guide pipe 27.

[0023] The inclined tube sedimentation tank 2 comprises a water inlet area, an inclined tube filler area and a water outlet area, the water inlet area, the inclined tube filler area and the water outlet area are sequentially arranged from bottom to top, the inclined tube filler 26 is arranged in the inclined tube filler area, and the bottom of the inclined tube sedimentation tank 2 is provided with a sludge discharge outlet, which is used for centrally discharging the separated sludge, so that the sedimentation efficiency can be improved by 50-60%, and the treatment capacity can be improved by 3-5 times on the same area. The water production pipe 30 is connected with a disinfection and dosing pipe 33, the other end of the disinfection and dosing pipe 33 is connected with a disinfection and dosing pump 32, and the other end of the disinfection and dosing pump 32 is connected with a disinfection and dosing module 31, so that sodium hypochlorite is added into the filtered liquid through the disinfection and dosing module 31, the disinfection and dosing pump 32 and the disinfection and dosing pipe 33, and the filtered liquid is transported to users through a pipe network for use, so as to ensure the safety of drinking water.

[0024] The high-efficiency air floatation and ultrafiltration tank 3 is provided with a slag scraper 28 above the high-efficiency air floatation and ultrafiltration tank 3, the slag scraper 28 is used for removing floating slag, one side of the top of the high-efficiency air floatation and ultrafiltration tank 3 is provided with a blow-off port, and the blow-off port is connected with a blow-off pipe 41, so that the floating slag can be removed through the blow-off pipe 41 after being removed by the slag scraper 28; the ultrafiltration membrane 29 is arranged in the middle of the high-efficiency air floatation and ultrafiltration tank 3, and spaces are reserved between the ultrafiltration membrane 29 and the inner wall of the high-efficiency air floatation and ultrafiltration tank 3 around the ultrafiltration membrane 29, the hollow fiber ultrafiltration membrane tube is used for membrane separation in the ultrafiltration membrane 29, so that harmful substances such as iron rust, silt, suspended solids, colloids, bacteria and macromolecular organic matters in water can be filtered out, and some mineral elements beneficial to human bodies can be reserved.

[0025] The utility model is mainly by grid flocculation tank, inclined tube sedimentation tank and high -efficient air floatation and ultrafiltration tank three components. Each function introduction as follows:

[0026] The utility model mainly comprises a grid flocculation tank, an inclined tube sedimentation tank and a high-efficiency air floatation and ultrafiltration tank.

[0027] The grid flocculation tank: when the raw water carrying the medicament flows through the grid of the grid flocculation tank, the water flow path is forced to zoom and turn, and then complex turbulence and vortex phenomena are generated. This process not only enhances the turbulence of the water flow, but also significantly increases the relative movement speed between the small particles in the water, increasing the opportunity for particle collision. With the increase of collision frequency, the micro-particles with flocculation performance gradually aggregate into larger flocculation bodies, creating favorable conditions for subsequent sedimentation and separation.

[0028] The inclined tube sedimentation tank: the inclined tube sedimentation tank mainly comprises a water inlet area, an inclined tube filler area and a water outlet area. The water treated by flocculation is introduced into the inclined tube sedimentation tank through the water inlet on the lower tank wall, so that the suspended impurities in the water are precipitated in the inclined tube. The water flows upward along the inclined tube, the separated sludge slides downward along the inclined tube to the bottom of the tank under the action of gravity, and then is discharged centrally, so that the sedimentation efficiency can be improved by 50-60%, and the treatment capacity can be improved by 3-5 times on the same area.

[0029] High-efficiency air floatation ultrafiltration tank: the high-efficiency air floatation ultrafiltration tank mainly comprises a dissolved air module and an ultrafiltration module, the sedimentation water is formed into dissolved air water through a releaser, and the air in the water is released at a reduced pressure in the high-efficiency air floatation ultrafiltration tank to form precipitation in the form of 20-30 um air bubbles, has very high surface area and adsorption capacity, and can better remove suspended matter, part of the backflow water after treatment is pressurized into a water dissolved air tank through a dissolved air pump and mixed with air, the air is dissolved in the water, and the efficiency of the container reaches more than 80%. The air dissolved in the water is released from the water to form micro-bubbles with a particle size of 20-50 um, the micro-bubbles combine with the suspended matter in the water to make the specific gravity of the suspended matter in the sewage small, and the suspended matter floats to the surface of the water body; a large amount of dregs is formed, and the dregs is removed by a dreg scraper, the algae pollution of the water body is effectively reduced, and the damage to the ultrafiltration membrane in the tank is reduced, the water in the tank is filtered through the membrane separation technology of the ultrafiltration membrane pressure difference to remove harmful substances such as iron rust, colloid, bacteria and macromolecular organic matter in the water, and some beneficial mineral elements to the human body can be retained, and the microorganism safety of drinking water is ensured.

[0030] The working process of the utility model is as follows: raw water enters into pipeline mixer 25 through water inlet pipe 22 by raw water pump 21, polyaluminum chloride and sodium hypochlorite are added into the raw water through pretreatment dosing module 23 and pretreatment dosing pipe 24, after being fully mixed by pipeline mixer 25, the water flows through the grid of grid flocculation tank 1, the water flow path is forced to zoom and turn, and then complex turbulence and vortex phenomenon are generated, by increasing the collision frequency, the micro-particles with flocculation performance are gradually gathered into larger flocculation bodies, the water treated by flocculation enters into inclined tube sedimentation tank 2 through the water inlet on the lower tank wall, and the suspended impurities in the water are deposited in the inclined tube filler 26, the water flows upward along the inclined tube filler 26, the separated sludge slides downward along the inclined tube filler 26 to the tank bottom under the action of gravity, and is then discharged. The water treated by sedimentation enters into high-efficiency air floatation ultrafiltration tank 3 through flow guide pipe 27, forms dissolved air water through releaser 40, is released under reduced pressure in high-efficiency air floatation ultrafiltration tank 3, the air in the water forms air bubbles with a diameter of 20-30 um, has a very high surface area and adsorption capacity, and can better remove the suspended matter, part of the backflow water after treatment, pressure air generated by air compressor 37 mixes in dissolved air tank 38 through backflow water pipe 34, dissolved air pump 35 and air pipe 36, and the air is dissolved in the water, at this time, the efficiency of the container is more than 80%. The air dissolved in the water is released from high-efficiency air floatation ultrafiltration tank 3 by releaser 40 through dissolved air water pipe 39, and forms micro-bubbles with a particle size of 20-50 um, the micro-bubbles combine with the suspended matter in the water, so that the specific gravity of the suspended matter in the water becomes smaller, and the suspended matter floats to the surface of the water body, a large amount of dregs are formed, the dregs are removed by dregs scraping machine 28, are discharged through blowdown pipe 41, the water in the tank is filtered to remove harmful substances such as iron rust, silt, suspended matter, colloid, bacteria and macromolecular organic matter in the water by the membrane separation technology of the hollow fiber ultrafiltration membrane tube of ultrafiltration membrane 29, and some mineral elements beneficial to human body are retained, sodium hypochlorite is added into the filtered liquid through water outlet pipe 30 by disinfection dosing module 31, disinfection dosing pump 32 and disinfection dosing pipe 33 to disinfect, and finally the water is transported to the user through the pipe network for use, so as to ensure the safety of drinking water.

[0031] The contents not described in detail in the specification belong to the prior art known by the person skilled in the art, the standard parts used can be purchased from the market, the special-shaped parts can be ordered according to the description and the drawings, the specific connection modes of the parts adopt the conventional means such as bolts, rivets and welding in the prior art, the machinery, parts and equipment adopt the conventional types in the prior art, the circuit connection adopts the conventional connection mode in the prior art, and the details are not described herein.

[0032] The utility model is not limited by the above-mentioned embodiments, any change, modification, replacement, combination, simplification made without departing from the spirit and principle of the utility model should be equivalent replacement mode, and all are included in the protection scope of the utility model.

Claims

1. A highly efficient algae-removing drinking water treatment device, characterized in that: The application relates to a water purification device, which comprises a grid flocculation tank (1), an inclined tube sedimentation tank (2) and a high-efficiency air floatation ultrafiltration tank (3), the water inlet of the grid flocculation tank (1) is connected with a raw water pump (21) through a water inlet pipe (22), raw water enters the grid flocculation tank (1) through the raw water pump (21), the outlet end of the grid flocculation tank (1) is connected with the water inlet of the inclined tube sedimentation tank (2), the outlet end of the inclined tube sedimentation tank (2) is connected with the water inlet of the high-efficiency air floatation ultrafiltration tank (3) through a flow guide pipe (27), the high-efficiency air floatation ultrafiltration tank (3) is internally provided with an ultrafiltration membrane (29), the water outlet of the ultrafiltration membrane (29) is respectively connected with a backflow water pipe (34) and a water production pipe (30) through pipes, the other end of the backflow water pipe (34) is connected with the water inlet of a dissolved air pump (35), the water outlet of the dissolved air pump (35) is connected with the water inlet of a dissolved air tank (38) through a pipe, the air inlet of the dissolved air tank (38) is connected with an air pipe (36), the other end of the air pipe (36) is connected with an air compressor (37), the outlet at the bottom end of the dissolved air tank (38) is connected with a dissolved air water pipe (39), and the other end of the dissolved air water pipe (39) is connected with a releaser (40) at the bottom of the high-efficiency air floatation ultrafiltration tank (3).

2. The high-efficiency algae-removing drinking water treatment device according to claim 1, characterized in that: A pipe mixer (25) is arranged on the pipe between the raw water pump (21) and the grid flocculation tank (1), raw water enters the pipe mixer (25) through the water inlet pipe (22) and the raw water pump (21), and the pipe mixer (25) is connected with a pretreatment dosing module (23) through a pretreatment dosing pipe (24).

3. The high-efficiency algae-removing drinking water treatment device according to claim 1, characterized in that: A grid grille is arranged in the grid flocculation tank (1), and an inclined tube filler (26) is arranged in the inclined tube sedimentation tank (2), raw water enters the inclined tube sedimentation tank (2) through the water inlet at the lower tank wall after flowing through the grid grille of the grid flocculation tank (1), and suspended impurities in the water are precipitated in the inclined tube filler (26), and the water flowing upwards along the inclined tube filler (26) enters the high-efficiency air floatation ultrafiltration tank (3) through the flow guide pipe (27).

4. The high-efficient algae-removing drinking water treatment device according to claim 1, characterized in that: The inclined tube sedimentation tank (2) comprises a water inlet area, an inclined tube filler area and a water outlet area, which are sequentially arranged from bottom to top, the inclined tube filler (26) is arranged in the inclined tube filler area, and the bottom of the inclined tube sedimentation tank (2) is provided with a sludge discharge outlet for discharging the separated sludge.

5. The high-efficiency algae-removing drinking water treatment device according to any one of claims 1 to 4, characterized in that: A disinfection dosing pipe (33) is connected with the water production pipe (30), the other end of the disinfection dosing pipe (33) is connected with a disinfection dosing pump (32), and the other end of the disinfection dosing pump (32) is connected with a disinfection dosing module (31).

6. The high-efficiency algae-removing drinking water treatment device according to any one of claims 1 to 4, characterized in that: A sludge scraper (28) is arranged above the high-efficiency air floatation ultrafiltration tank (3), the sludge scraper (28) is used for removing floating sludge, a sewage outlet is arranged at one side and the top of the high-efficiency air floatation ultrafiltration tank (3), and the sewage outlet is connected with a sewage pipe (41).

7. The high-efficient algae-removing drinking water treatment device according to claim 1, characterized in that: The ultrafiltration membrane (29) is arranged in the middle of the high-efficiency air floatation ultrafiltration tank (3), and spaces are reserved between the ultrafiltration membrane (29) and the inner wall of the high-efficiency air floatation ultrafiltration tank (3) around the ultrafiltration membrane (29), and the hollow fiber ultrafiltration membrane tube is used for membrane separation in the ultrafiltration membrane (29).