Novel efficient equipment for groundwater pollution treatment

By optimizing the injection control and mixing design of coagulant and coagulant in underground sewage treatment equipment, the problem of poor auxiliary role in the existing technology is solved, and more efficient sewage treatment and treatment effects are achieved, and underground and The quality of surface water.

CN119143330APending Publication Date: 2024-12-17YUNNAN HANENG ENVIRONMENTAL PROTECTION TECH CO LTD
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Patent Information

Application Number
CN202411568708.7
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2024-11-05
Publication Date
2024-12-17

AI Technical Summary

Technical Problem

During the existing underground sewage treatment process, the auxiliary effects of coagulants and coagulants are not effectively realized, resulting in poor treatment results.

Method used

A new high-efficiency equipment was designed to ensure effective mixing of coagulant and coagulant through the injection control of coagulant and coagulant and the design of the internal mixing flow channel, and improve the processing performance. The equipment includes an inclined screen well, a sand sedimentation tank, a regulation tank, a reaction tank, a medicine tank and a dosing pump. The controller is used to adjust the working power of the dosing pump to optimize the mixing effect of the coagulant and coagulant.

Benefits of technology

The mixing effect of coagulant and coagulant is improved, the treatment and treatment performance of underground sewage is enhanced, the efficient filtration and precipitation of sewage is ensured, the emission of pollutants is reduced, and the quality of groundwater and surface water is protected.

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Abstract

The invention discloses novel efficient equipment for underground water pollution treatment, which is characterized in that underground sewage liquid flow is conveyed into an inclined screen well to be filtered by a screen plate, silt is settled and filtered by a grit chamber and then conveyed outwards by a silt pump, and then the liquid flow enters an adjusting tank to be treated; then the liquid flow is conveyed into a reaction tank, a coagulant and a coagulant aid are injected into the reaction tank, a first partition plate, a second partition plate and a flow distribution plate are arranged in the reaction tank, and under the arrangement of the first partition plate and the flow distribution plate, the coagulant conveyed by a first dosing pump can be conveyed under the guidance of the first partition plate and the flow distribution plate; a guide plate is arranged at the top of the splitter plate to guide the coagulant, so that the mixing effect of the coagulant and the coagulant aid is improved, and the working power of a second dosing pump is adjusted according to the working power of a first dosing pump, so that the mixing effect of the coagulant and the coagulant aid is improved; further, the fusion performance of the coagulant aid and the coagulant is improved, so that the underground sewage treatment and treatment performance is improved.
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Description

Technical Field

[0001] The present application relates to the field of underground sewage treatment control technology, and in particular to a new type of high-efficiency equipment for groundwater pollution control. Background Art

[0002] Underground sewage may contain various harmful substances, such as organic matter, heavy metals, pathogens, etc. If it is discharged directly without treatment, it will pollute the soil and groundwater, affect the balance of the surrounding ecosystem, and at the same time, avoid polluting the surrounding water bodies and protect the quality of surface water. If underground sewage seeps into rivers, lakes and other water bodies, it will cause eutrophication and deterioration of water quality, affecting the survival of aquatic organisms and the sustainable use of water resources. Furthermore, underground sewage may contain pathogens such as bacteria, viruses, and parasites. If it is not treated, it may cause various diseases and pose a threat to public health. At the same time, untreated underground sewage will produce odors and harmful gases, such as hydrogen sulfide, which will affect the living environment and health of surrounding residents.

[0003] At present, the existing underground sewage treatment methods include physical treatment, chemical treatment and biological treatment. When using chemical treatment to treat underground sewage, coagulants and coagulant aids are usually added to domestic sewage. Coagulants can destabilize colloids and fine suspended matter in water and aggregate to form larger particles through mechanisms such as compression of double electrical layers, adsorption and electrical neutralization, adsorption bridging, and sediment capture. Coagulant aids mainly play the role of auxiliary coagulants to help improve the coagulation effect, such as adjusting the pH value, increasing the strength and density of flocs, and accelerating the sedimentation rate. However, in the current treatment process, coagulants and coagulant aids are usually added directly to the treatment tank, which cannot effectively achieve the auxiliary coagulation effect of coagulants on coagulants. Summary of the invention

[0004] In an exemplary embodiment of the present application, a new type of high-efficiency equipment for groundwater pollution control is provided, which achieves an efficient mixed treatment effect of coagulants and coagulant aids through injection control of coagulants and coagulant aids and design of internal mixed flow channels, thereby improving the treatment performance of domestic sewage.

[0005] The present application provides a novel and efficient device for groundwater pollution control, comprising an inclined screen well, a sand settling tank, a regulating tank, a reaction tank, a first medicine tank, a second medicine tank, a first dosing pump, a second dosing pump and a controller;

[0006] The inclined screen well is connected to the grit chamber, a screen plate is arranged in the inclined screen well, and the screen plate is arranged obliquely along the vertical direction, and the liquid flows to the grit chamber after being filtered by the screen plate;

[0007] A sediment pump is arranged in the sedimentation tank, and the sediment pump is used to transport the sediment in the sedimentation tank to the outside of the sedimentation tank, and the sedimentation tank is connected to the regulating tank;

[0008] A sewage lifting pump is arranged in the regulating tank, and the sewage lifting pump is used to transport the liquid flow in the regulating tank to the reaction tank;

[0009] The first medicine tank stores a coagulant, the first medicine tank is connected to the input end of the first dosing pump through a pipeline, the output end of the first dosing pump is connected to the top of the reaction tank through a pipeline, and the first dosing pump transports the coagulant stored in the first medicine tank to the reaction tank.

[0010] The second medicine tank stores a coagulant aid, the second medicine tank is connected to the input end of the second dosing pump through a pipeline, the output end of the second dosing pump is connected to the top of the reaction tank through a pipeline, and the second dosing pump transports the coagulant stored in the second medicine tank to the reaction tank;

[0011] A first baffle, a second baffle and a diverter plate are arranged in the reaction pool, wherein the first baffle and the second baffle are arranged at the top of the reaction pool in a vertical direction, wherein the connection position between the output end of the first dosing pump and the top of the reaction pool is located between the side wall of the reaction pool and the first baffle plate, and the connection position between the output end of the second dosing pump and the top of the reaction pool is located between the first baffle plate and the second baffle plate, the diverter plate is arranged at the bottom of the reaction pool in a vertical direction and between the first baffle plate and the second baffle plate, a guide plate is arranged on the top of the diverter plate, the guide plate comprises a first plate body and a second plate body, the first plate body and the second plate body are connected together to the top of the diverter plate, and the angle between the first plate body and the second plate body is an obtuse angle;

[0012] The controller is connected to the first dosing pump and the second dosing pump, and the controller adjusts the working power of the first dosing pump and the second dosing pump, wherein the controller is configured to adjust the working power of the second dosing pump according to the working power of the first dosing pump.

[0013] Further, the controller is configured to: if the working power of the first dosing pump is greater than or equal to the first preset power, drive the second dosing pump to operate at the first power; otherwise, drive the second dosing pump to operate at the second power.

[0014] Furthermore, the first power is 50% of the maximum power of the second dosing pump, and the second power is 80% of the maximum power of the second dosing pump.

[0015] Furthermore, the reaction pool is connected to a delivery pump through a pipeline, and the delivery pump delivers the liquid in the reaction pool to the outside.

[0016] Furthermore, a ventilation pipeline is also provided in the regulating tank, and the ventilation pipeline is used to transport the airflow outside the regulating tank to the inside of the regulating tank.

[0017] Furthermore, a stirrer is provided on the first medicine tank and the second medicine tank respectively, and an output end of the stirrer is connected to a stirring shaft, and the stirring shaft rotates inside the first medicine tank or the second medicine tank under the drive of the stirrer.

[0018] Furthermore, the connection position between the output end of the second dosing pump and the top of the reaction tank is located between the diverter plate and the second partition plate.

[0019] Furthermore, a gap is formed between the bottom of the first partition plate and the second partition plate and the bottom of the reaction tank in the vertical direction, and a gap is formed between the top of the diverter plate and the top of the reaction tank in the vertical direction.

[0020] Furthermore, an angle between the first plate body or the second plate body and the diverter plate is an obtuse angle.

[0021] The embodiments of the present application have the following beneficial effects: the underground sewage liquid flow is transported to the inclined screen well and filtered by the screen plate, the sediment is precipitated and filtered in the grit chamber and then transported outward by the sediment pump, and then the liquid flow enters the regulating tank for treatment, and then the liquid flow is transported to the reaction tank and the coagulant and the coagulant aid are injected into the reaction tank, a first partition, a second partition and a diverter plate are respectively arranged in the reaction tank, and under the arrangement of the first partition and the diverter plate, the coagulant transported by the first dosing pump can be transported under the guidance of the first partition and the diverter plate, and a guide plate is arranged on the top of the diverter plate to realize the diversion of the coagulant, so as to improve the mixing effect of the coagulant and the coagulant aid, and the working power of the second dosing pump is adjusted according to the working power of the first dosing pump to improve the mixing effect of the coagulant and the coagulant aid, thereby improving the fusion performance of the coagulant aid and the coagulant to improve the treatment and governance performance of the underground sewage. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] In order to more clearly illustrate the technical solutions in the embodiments of the present application, the drawings required for use in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present application. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying creative labor.

[0023] Figure 1The schematic diagram of the structure of a new type of efficient equipment for groundwater pollution control provided by an embodiment of the present application is exemplarily shown;

[0024] Figure 2 A system schematic diagram of a new type of efficient equipment for groundwater pollution control provided in an embodiment of the present application is exemplified. DETAILED DESCRIPTION

[0025] In order to make the purpose, technical solutions and advantages of the embodiments of the present application clearer, the technical solutions in the embodiments of the present application will be clearly and completely described below in conjunction with the drawings in the embodiments of the present application.

[0026] To further illustrate the technical solution provided by the embodiment of the present application, this is described in detail below in conjunction with the accompanying drawings and specific implementation methods. Although the embodiment of the present application provides the method operation steps shown in the following embodiments or drawings, more or fewer operation steps may be included in the method based on routine or no creative labor. In the steps where there is no necessary causal relationship logically, the execution order of these steps is not limited to the execution order provided in the embodiment of the present application.

[0027] refer to Figure 1-2 As shown, the present application provides a new type of high-efficiency equipment for groundwater pollution control, including an inclined screen well 11, a sand settling tank 12, a regulating tank 13, a reaction tank 14, a first medicine tank 21, a second medicine tank 22, a first dosing pump 31, a second dosing pump 32 and a controller 33.

[0028] The inclined screen well 11 is connected to the grit chamber 12. A screen plate 111 is arranged in the inclined screen well 11. The screen plate 111 is inclined in the vertical direction. After the liquid is filtered by the screen plate 111, it flows to the grit chamber 12. The screen plate 111 performs preliminary screening of the liquid to remove larger particles of sediment.

[0029] A sediment pump 121 is provided in the sedimentation tank 12 , and the sediment pump 121 is used to transport the sediment in the sedimentation tank 12 to the outside of the sedimentation tank 12 . The sedimentation tank 12 is connected to the regulating tank 13 , and the liquid flow in the sedimentation tank 12 is transported to the regulating tank 13 .

[0030] A sewage lifting pump 131 is provided in the regulating tank 13, and the sewage lifting pump 131 is used to transport the liquid flow in the regulating tank 13 to the reaction tank 14. A ventilation pipeline is also provided in the regulating tank 13, and the ventilation pipeline is used to transport the air flow outside the regulating tank 13 to the inside of the regulating tank 13. The reaction tank 14 is connected to the delivery pump through a pipeline, and the delivery pump transports the liquid flow in the reaction tank 14 to the outside.

[0031] The first medicine tank 21 stores coagulant, and the first medicine tank 21 is connected to the input end of the first dosing pump 31 through a pipeline. The output end of the first dosing pump 31 is connected to the top of the reaction tank 14 through a pipeline. The first dosing pump 31 transports the coagulant stored in the first medicine tank 21 to the reaction tank 14.

[0032] The second medicine tank 22 stores a coagulant aid, and the second medicine tank 22 is connected to the input end of the second dosing pump 32 through a pipeline. The output end of the second dosing pump 32 is connected to the top of the reaction tank 14 through a pipeline. The second dosing pump 32 transports the coagulant stored in the second medicine tank 22 to the reaction tank 14.

[0033] Agitators are respectively arranged on the first medicine tank 21 and the second medicine tank 22, and the output end of the agitator is connected to a stirring shaft. The stirring shaft is driven by the agitator to rotate inside the first medicine tank 21 or the second medicine tank 22, thereby preventing the coagulant and the coagulant aid from being deposited in the first medicine tank 21 and the second medicine tank 22 respectively.

[0034] A first partition 41, a second partition 42 and a diverter plate 43 are arranged in the reaction tank 14, wherein the first partition 41 and the second partition 42 are arranged at the top of the reaction tank 14 in the vertical direction, wherein the connection position between the output end of the first dosing pump 31 and the top of the reaction tank 14 is located between the side wall of the reaction tank 14 and the first partition 41, and the connection position between the output end of the second dosing pump 32 and the top of the reaction tank 14 is located between the first partition 41 and the second partition 42, specifically, the connection position between the output end of the second dosing pump 32 and the top of the reaction tank 14 is located between the diverter plate 43 and the second partition 42.

[0035] The diverter plate 43 is arranged at the bottom of the reaction tank 14 along the vertical direction and between the first baffle plate 41 and the second baffle plate 42. A guide plate is arranged on the top of the diverter plate 43. The guide plate includes a first plate body 431 and a second plate body 432. The first plate body 431 and the second plate body 432 are connected to the top of the diverter plate 43, and the angle between the first plate body 431 and the second plate body 432 is an obtuse angle. The angle between the first plate body 431 or the second plate body 432 and the diverter plate 43 is an obtuse angle.

[0036] Specifically, the bottoms of the first partition plate 41 and the second partition plate 42 form a gap with the bottom of the reaction tank 14 in the vertical direction, and the top of the diverter plate 43 forms a gap with the top of the reaction tank 14 in the vertical direction.

[0037] Therefore, the coagulant delivered by the first dosing pump 31 is guided and a delivery channel is formed through the first partition 41 and the diverter plate 43. When the coagulant is delivered to the upper part of the diverter plate 43, it is diffused and diverted by the guide plate, and the direction of the diffused diversion is toward both sides of the delivery direction of the coagulant, so as to achieve better mixing of the coagulant and the coagulant aid delivered subsequently.

[0038] The obtuse structure formed between the first plate body 431 and the second plate body 432 changes the flow cross-sectional shape of the entire diverter plate. Compared with a straight plate structure, this obtuse structure makes the flow path of the coagulant relatively tortuous when it flows through here. The flow direction of the coagulant needs to change when passing through the connection between the first plate body 431 and the second plate body 432, thereby reducing the flow rate of the coagulant. This can make the transportation of the coagulant more stable, reduce unstable phenomena such as turbulence and splashing that may be caused by excessive flow rate, and facilitate the accurate and uniform transportation of the coagulant to the target location.

[0039] A slower flow rate also allows the coagulant more time to mix and react during the transportation process. For coagulants that need to be fully mixed, it can improve their mixing effect and reaction efficiency, thereby better playing the role of the coagulant.

[0040] The obtuse angle structure of the first plate 431 and the second plate 432 can guide the flow of the coagulant to a certain extent. When the coagulant flows into the diverter plate from one direction, the first plate 431 and the second plate 432 can divide it into two or more directions of flow, and due to the existence of the obtuse angle, this diversion will be more uniform. For example, in some application scenarios where the coagulant needs to be transported to multiple different locations at the same time, this uniform diversion feature can ensure that each location can receive an appropriate amount of coagulant, ensuring the normal operation of the entire system.

[0041] Uniform diversion can also reduce the situation where there is too much or too little coagulant in some local areas, and avoid problems such as poor treatment effect in some areas or equipment blockage due to uneven distribution of coagulant.

[0042] During the transportation of coagulants, instantaneous pressure shocks may be generated due to the start and stop of the pump, the opening and closing of the valve, and other operations. Compared with the straight plate structure, the obtuse-angled diverter plate can support each other on both sides, thereby enhancing the overall structural strength. When encountering a pressure shock, the first plate 431 and the second plate 432 can jointly withstand the impact force, reduce the deformation and damage of the diverter plate, and thus ensure that the transportation of the coagulant is not affected. This enhanced impact resistance also helps to extend the service life of the diverter plate and reduce the maintenance cost of the equipment.

[0043] The obtuse angle structure design of the first plate body 431 and the second plate body 432 may make the corners inside the diverter plate relatively small, reducing the possibility of coagulant accumulation in the corners. After the equipment has been running for a period of time, when the diverter plate needs to be cleaned and maintained, this structure can make the cleaning work easier and improve the efficiency and effect of cleaning.

[0044] The controller 33 is connected to the first dosing pump 31 and the second dosing pump 32 , and is used to adjust the working power of the first dosing pump 31 and the second dosing pump 32 , wherein the controller 33 is configured to adjust the working power of the second dosing pump 32 according to the working power of the first dosing pump 31 .

[0045] Specifically, the controller 33 is configured to: if the working power of the first dosing pump 31 is greater than or equal to the first preset power, drive the second dosing pump 32 to operate at the first power; otherwise, drive the second dosing pump 32 to operate at the second power, wherein the first preset power is a preset value and can be set to 60% of the maximum power of the first dosing pump 31.

[0046] The first power is 50% of the maximum power of the second dosing pump 32 , and the second power is 80% of the maximum power of the second dosing pump 32 .

[0047] When the working power of the first dosing pump 31 is greater than or equal to the first preset power, the second dosing pump 32 is driven to operate at a lower working power, so that the output end of the second dosing pump 32 can be connected to the top of the reaction tank 14 through a pipeline, and when the first dosing pump 31 operates at a higher power, it is avoided that the second dosing pump 32 still operates at a higher working power, thereby causing a greater interference effect on the mixing of the coagulant and the coagulant aid at the diverter plate 43 or the guide plate, thereby generating a larger turbulence or mixing inside, thereby reducing the liquid flow delivery efficiency.

[0048] When the first dosing pump 31 is running at a relatively low power, that is, when the working power of the first dosing pump 31 is less than the first preset power, the working power of the second dosing pump 32 can be increased so that the coagulant delivered by the second dosing pump 32 can be better mixed, and when the coagulant is delivered at a relatively low flow rate, the flow rate of the coagulant can be appropriately increased so that better mixing can be achieved through the increased flow rate of the coagulant. Therefore, by adjusting the working power of the second dosing pump 32 according to the working power of the first dosing pump 31, the mixing performance can be achieved when the liquid flow at the diverter plate 43 is in a variety of flow states such as mixing and diversion.

[0049] The underground sewage liquid flow is transported to the inclined screen well 11 and filtered by the screen plate 111. The sediment is precipitated and filtered in the sand settling tank 12 and then transported outward by the sediment pump 121. The liquid flow then enters the regulating tank 13 for treatment, and then the liquid flow is transported to the reaction tank 14 and the coagulant and coagulant aid are injected into the reaction tank 14. The first partition 41, the second partition 42 and the diverter plate 43 are respectively arranged in the reaction tank 14. Under the arrangement of the first partition 41 and the diverter plate 43, the first dosing The coagulant delivered by the pump 31 is transported under the guidance of the first partition 41 and the diverter plate 43, and a guide plate is set on the top of the diverter plate 43 to realize the diversion of the coagulant, so as to improve the mixing effect of the coagulant and the coagulant aid. The controller 33 adjusts the working power of the second dosing pump 32 according to the working power of the first dosing pump 31 to improve the mixing effect of the coagulant and the coagulant aid, thereby improving the fusion performance of the coagulant aid and the coagulant to improve the treatment and governance performance of underground sewage.

[0050] Those skilled in the art will appreciate that the embodiments of the present application may be provided as methods, systems, or computer program products. Therefore, the present application may adopt the form of a complete hardware embodiment, a complete software embodiment, or an embodiment in combination with software and hardware. Moreover, the present application may adopt the form of a computer program product implemented in one or more computer-usable storage media (including but not limited to disk storage, CD-ROM, optical storage, etc.) that contain computer-usable program code.

[0051] The present application is described with reference to the flowcharts and / or block diagrams of the methods, devices (systems), and computer program products according to the present application. It should be understood that each process and / or box in the flowchart and / or block diagram, as well as the combination of the processes and / or boxes in the flowchart and / or block diagram, can be implemented by computer program instructions. These computer program instructions can be provided to a processor of a general-purpose computer, a special-purpose computer, an embedded processor, or other programmable data processing device to produce a machine, so that the instructions executed by the processor of the computer or other programmable data processing device generate instructions for implementing the processes in the flowchart and / or block diagram. Figure 1 A process or multiple processes and / or boxes Figure 1 A device that provides the functions specified in a block or multiple blocks.

[0052] These computer program instructions may also be stored in a computer-readable memory capable of directing a computer or other programmable data processing device to operate in a specific manner, so that the instructions stored in the computer-readable memory produce an article of manufacture comprising an instruction device, which implements the process Figure 1 A process or multiple processes and / or boxes Figure 1 A function specified in one or more boxes.

[0053] These computer program instructions can also be loaded onto a computer or other programmable data processing device so that a series of operating steps are executed on the computer or other programmable device to produce a computer-implemented process, thereby providing instructions for implementing the process. Figure 1 A process or multiple processes and / or boxes Figure 1 The steps for the functions specified in one or more boxes.

[0054] Obviously, those skilled in the art can make various changes and modifications to the present application without departing from the scope of the present application. Thus, if these modifications and variations of the present application fall within the scope of the claims of the present application and their equivalents, the present application is also intended to include these modifications and variations.

Claims

1. A new and efficient equipment for groundwater pollution control, It is characterized in that It includes an inclined screen well, a sand settling tank, a regulating tank, a reaction tank, a first medicine tank, a second medicine tank, a first dosing pump, a second dosing pump and a controller; The inclined screen well is connected to the grit chamber, a screen plate is arranged in the inclined screen well, and the screen plate is arranged obliquely along the vertical direction, and the liquid flows to the grit chamber after being filtered by the screen plate; A sediment pump is arranged in the sedimentation tank, and the sediment pump is used to transport the sediment in the sedimentation tank to the outside of the sedimentation tank, and the sedimentation tank is connected to the regulating tank; A sewage lifting pump is arranged in the regulating tank, and the sewage lifting pump is used to transport the liquid flow in the regulating tank to the reaction tank; The first medicine tank stores a coagulant, the first medicine tank is connected to the input end of the first dosing pump through a pipeline, the output end of the first dosing pump is connected to the top of the reaction tank through a pipeline, and the first dosing pump transports the coagulant stored in the first medicine tank to the reaction tank. The second medicine tank stores a coagulant aid, the second medicine tank is connected to the input end of the second dosing pump through a pipeline, the output end of the second dosing pump is connected to the top of the reaction tank through a pipeline, and the second dosing pump transports the coagulant stored in the second medicine tank to the reaction tank; A first baffle, a second baffle and a diverter plate are arranged in the reaction pool, wherein the first baffle and the second baffle are arranged at the top of the reaction pool in a vertical direction, wherein the connection position between the output end of the first dosing pump and the top of the reaction pool is located between the side wall of the reaction pool and the first baffle plate, and the connection position between the output end of the second dosing pump and the top of the reaction pool is located between the first baffle plate and the second baffle plate, the diverter plate is arranged at the bottom of the reaction pool in a vertical direction and between the first baffle plate and the second baffle plate, a guide plate is arranged on the top of the diverter plate, the guide plate comprises a first plate body and a second plate body, the first plate body and the second plate body are connected together to the top of the diverter plate, and the angle between the first plate body and the second plate body is an obtuse angle; The controller is connected to the first dosing pump and the second dosing pump, and the controller adjusts the working power of the first dosing pump and the second dosing pump, wherein the controller is configured to adjust the working power of the second dosing pump according to the working power of the first dosing pump.

2. The novel and efficient equipment according to claim 1, It is characterized in that The controller is configured to: if the working power of the first dosing pump is greater than or equal to the first preset power, drive the second dosing pump to operate at the first power; otherwise, drive the second dosing pump to operate at the second power.

3. The novel high-efficiency device according to claim 2, It is characterized in that The first power is 50% of the maximum power of the second dosing pump, and the second power is 80% of the maximum power of the second dosing pump.

4. The novel high-efficiency device according to claim 3, It is characterized in that The reaction pool is connected to a delivery pump through a pipeline, and the delivery pump delivers the liquid flow in the reaction pool to the outside.

5. The novel and efficient equipment according to claim 1, It is characterized in that A ventilation pipeline is also provided in the regulating pool, and the ventilation pipeline is used to transport the airflow outside the regulating pool to the inside of the regulating pool.

6. The novel and efficient equipment according to claim 1, It is characterized in that A stirrer is disposed on the first medicine tank and the second medicine tank, respectively. The output end of the stirrer is connected to a stirring shaft. The stirring shaft rotates inside the first medicine tank or the second medicine tank under the drive of the stirrer.

7. The novel and efficient equipment according to claim 1, It is characterized in that The connection position between the output end of the second dosing pump and the top of the reaction tank is located between the diverter plate and the second partition plate.

8. The novel and highly efficient device according to claim 1, It is characterized in that A gap is formed between the bottom of the first partition plate and the second partition plate and the bottom of the reaction tank in the vertical direction, and a gap is formed between the top of the diverter plate and the top of the reaction tank in the vertical direction.

9. The novel and efficient device according to claim 1, It is characterized in that The included angle between the first plate body or the second plate body and the diverter plate is an obtuse angle.

Citation Information

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