Agglomerated composite agent and desulfurization wastewater mixed liquid supply system
By installing a premixing device and a static mixer on the inlet pipe of the mixing unit, the problem of insufficient mixing between the agglomerating compound agent and the desulfurization wastewater was solved, the purification effect of chloride ions was improved, and flue corrosion and air preheater blockage were prevented.
Patent Information
- Application Number
- CN202520010123.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-01-03
- Publication Date
- 2026-02-03
- Estimated Expiration
- 2035-01-03
AI Technical Summary
In the existing technology, the agglomerating composite agent and desulfurization wastewater mixed liquid supply system is not fully mixed with the desulfurization wastewater, resulting in poor chloride ion purification effect in the desulfurization wastewater.
A premixing device is installed on the inlet pipe of the mixing unit. The water is initially mixed by a static mixer and then further mixed in the mixing unit to ensure that the agglomerating compound agent and the desulfurization wastewater are fully mixed.
By setting up a premixing device, the agglomerating compound agent and desulfurization wastewater are fully mixed, which improves the purification effect of chloride ions, avoids corrosion of flue gas, and reduces clogging of air preheater.
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Figure CN223861733U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of supply technology of high-temperature flue gas agglomeration composite agent and desulfurization wastewater mixture in desulfurization wastewater treatment system of coal-fired power plant, and particularly to a supply system of agglomeration composite agent and desulfurization wastewater mixture. Background Technology
[0002] Currently, the wastewater discharge requirement is no external discharge of wastewater. Specifically, industrial wastewater, after treatment to meet standards, is entirely reused in the plant's production system and not discharged externally. Desulfurization wastewater, a type of end-of-pipe high-salt wastewater with chloride ion levels as high as 31,000 ppm, is a key and challenging aspect of wastewater treatment. Currently, desulfurization wastewater is directly used as makeup water for the wet slag system, which is not conducive to comprehensive utilization. Specifically, after entering the slag water system, the desulfurization wastewater undergoes high-temperature evaporation, causing chloride ions to enter the boiler, affecting pipeline safety. Simultaneously, the slag removal system suffers severe corrosion, seriously threatening its reliability. Therefore, it is necessary to purify the chloride ions in the desulfurization wastewater to reduce its corrosive effect on the boiler.
[0003] The process involves injecting a mixture of atomized agglomerating compound agent and desulfurization wastewater into the high-temperature flue of a coal-fired power plant to purify the chloride ions in the desulfurization wastewater. The basic procedure is to add the agglomerating compound agent to the desulfurization wastewater; the main purpose of the agglomerating compound agent is to reduce the chloride ions in the wastewater. - The diluted agglomerating compound agent solution is atomized and sprayed into the high-temperature flue gas before the air preheater via a spray pump. The atomized solution mixes thoroughly with the hot flue gas, undergoing heat exchange and evaporation. Various ions in the wastewater form various salt solids in the flue gas, which are then removed by a dust collector and collected in dry ash, achieving "zero discharge" of wastewater. Simultaneously, spraying the agglomerating compound agent solution into the high-temperature flue gas before the air preheater significantly removes SO3 from the flue gas, preventing it from reacting with ammonia (NH3) to form NH4HSO4, thus reducing air preheater blockage.
[0004] However, in existing technologies, the atomized high-temperature flue gas injected into the high-temperature flue gas duct before the air preheater is supplied by a mixture of agglomerating compound agent and desulfurization wastewater. This system first dilutes and emulsifies the agglomerating compound agent, then mixes the diluted and emulsified agent with the desulfurization wastewater, and finally atomizes the mixture and injects it into the high-temperature flue gas duct before the air preheater. However, this existing system suffers from insufficient mixing of the emulsified agglomerating compound agent and the desulfurization wastewater, resulting in poor chloride ion purification in the wastewater.
[0005] Therefore, it is necessary to improve the existing supply system of agglomerating compound agent and desulfurization wastewater mixture to ensure that the agglomerating compound agent and desulfurization wastewater are fully mixed. Utility Model Content
[0006] The purpose of this invention is to provide a mixed liquid supply system for agglomerating compound agents and desulfurization wastewater, so as to solve the problem of insufficient mixing of agglomerating compound agents and desulfurization wastewater in existing mixed liquid supply systems.
[0007] To solve the above-mentioned technical problems, this utility model provides a supply system for agglomerating compound agent and desulfurization wastewater mixture, including an emulsification device, a mixing device, and a spraying device, and also includes a premixing device. The inlet pipe of the premixing device is connected to the wastewater inlet pipe and the outlet pipe of the emulsification device, respectively. The outlet pipe of the premixing device is connected to the inlet pipe of the mixing device, and the outlet pipe of the mixing device is connected to the inlet pipe of the spraying device.
[0008] Optionally, the premixing device is a static mixer.
[0009] Optionally, it also includes a premixed branch pipe, the inlet of which is connected to the inlet pipe of the mixing device and located upstream of the premixed device, and the outlet of which is connected to the inlet pipe of the mixing device and located downstream of the premixed device.
[0010] Optionally, a premixed branch pipe valve is provided on the premixed branch pipe.
[0011] Optionally, the mixing device includes a mixing tank, the inlet pipe of which is connected to a wastewater inlet pipe and the outlet pipe of the emulsification device, the inlet pipe of the spraying device is connected to the outlet pipe of the mixing tank, and the premixing device is installed on the inlet pipe of the mixing tank.
[0012] Optionally, the inlet of the premixed branch pipe is connected to the inlet pipe of the mixing tank and is located upstream of the premixing device, and the outlet of the premixed branch pipe is connected to the inlet pipe of the mixing tank and is located downstream of the premixing device.
[0013] Optionally, the mixing device further includes an agitator disposed on the mixing tank, the agitator's impeller extending downward into the mixing tank.
[0014] Optionally, the water inlet pipe of the mixing tank is located at the top of the mixing tank, and the water outlet pipe of the mixing tank is located at the bottom of the mixing tank.
[0015] Optionally, the system also includes a main drain pipe, and the mixing device further includes an overflow pipe, the inlet of which is connected to the top of the mixing tank, and the outlet of which is connected to the main drain pipe.
[0016] Optionally, the mixing device further includes a tank drain pipe, the inlet of which is connected to the bottom of the mixing tank, and the outlet of which is connected to the main drain pipe.
[0017] The present invention provides a mixed liquid supply system for agglomerating composite agents and desulfurization wastewater, which has the following beneficial effects:
[0018] By installing a premixing device on the inlet pipe of the mixing device, the wastewater and the emulsified agglomerating compound agent can be premixed before entering the mixing device for further mixing. Compared with the method of directly entering the mixing device for mixing, the wastewater and the emulsified agglomerating compound agent can be fully mixed. Attached Figure Description
[0019] Figure 1 This is an isometric view of the supply system for the agglomeration composite agent and desulfurization wastewater mixture in an embodiment of this utility model;
[0020] Figure 2 This is a partial schematic diagram of the supply system for the agglomeration composite agent and the desulfurization wastewater mixture in an embodiment of this utility model;
[0021] Figure 3 This is a right view of the supply system for the agglomeration composite agent and desulfurization wastewater mixture in an embodiment of this utility model;
[0022] Figure 4 This is a left view of the supply system for the agglomeration compound agent and desulfurization wastewater mixture in an embodiment of this utility model.
[0023] Explanation of reference numerals in the attached figures:
[0024] 100 - Emulsification unit; 110 - Chemical storage tank; 120 - Emulsification tank; 130 - Emulsification pump set;
[0025] 200 - Mixing device; 210 - Mixing tank; 220 - Overflow pipe; 230 - Tank drain pipe; 240 - Tank cleaning pipe;
[0026] 300 - Spraying device; 310 - Spray pump; 320 - Pump cleaning pipe; 330 - Pump drain pipe;
[0027] 410 - Premixing unit; 420 - Premixing branch pipe;
[0028] 520 - Escalator; 530 - Work platform. Detailed Implementation
[0029] To make the objectives, technical solutions, and advantages of the embodiments of this utility model clearer, the technical solutions of the embodiments of this utility model will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some embodiments of this utility model, and not all embodiments. The components of the embodiments of this utility model described and shown in the accompanying drawings can generally be arranged and designed in various different configurations.
[0030] Therefore, the following detailed description of the embodiments of the present invention provided in the accompanying drawings is not intended to limit the scope of the claimed invention, but merely to illustrate selected embodiments of the invention. All other embodiments obtained by those skilled in the art based on the embodiments of the present invention without inventive effort are within the scope of protection of the present invention.
[0031] It should be noted that similar labels and letters in the following figures indicate similar items. Therefore, once an item is defined in one figure, it does not need to be further defined and explained in subsequent figures.
[0032] In the description of this utility model, it should be noted that the terms "center," "upper," "lower," "left," "right," "vertical," "horizontal," "inner," and "outer," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings, or the orientation or positional relationship commonly used when the product of this utility model is in use. They are only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this utility model. In addition, the terms "first," "second," and "third," etc., are only used to distinguish descriptions and should not be construed as indicating or implying relative importance.
[0033] Furthermore, terms such as "horizontal" and "vertical" do not imply that components must be absolutely horizontal or suspended, but rather that they can be slightly tilted. For example, "horizontal" simply means that its direction is more horizontal than "vertical," and does not mean that the structure must be completely horizontal, but can be slightly tilted.
[0034] In the description of this utility model, it should also be noted that, unless otherwise explicitly specified and limited, the terms "set," "install," "connect," and "link" should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral connection; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; and they can refer to a connection within two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model based on the specific circumstances.
[0035] refer to Figure 1 , Figure 2 , Figure 3 and Figure 4 , Figure 1 This is an isometric view of the supply system for the agglomeration composite agent and desulfurization wastewater mixture in an embodiment of this utility model. Figure 2 This is a partial schematic diagram of the supply system for the agglomeration composite agent and the desulfurization wastewater mixture in an embodiment of this utility model. Figure 3 This is a right view of the supply system for the agglomeration composite agent and desulfurization wastewater mixture in an embodiment of this utility model. Figure 4 This is a left view of the agglomeration compound agent and desulfurization wastewater mixture supply system in this embodiment of the present invention. This embodiment provides an agglomeration compound agent and desulfurization wastewater mixture supply system, including an emulsification device 100, a mixing device 200, and a spraying device 300, and also includes a premixing device 410. The inlet pipe of the premixing device 410 is connected to the wastewater inlet pipe and the outlet pipe of the emulsification device 100, respectively. The outlet pipe of the premixing device 410 is connected to the inlet pipe of the mixing device 200, and the outlet pipe of the mixing device 200 is connected to the inlet pipe of the spraying device 300.
[0036] By installing a premixing device 410 on the inlet pipe of the mixing device 200, the wastewater and the emulsified agglomerating compound agent can be premixed before entering the mixing device 200 for mixing. Compared with the method of directly entering the mixing device 200 for mixing, the wastewater and the emulsified agglomerating compound agent can be fully mixed.
[0037] Specifically, the premixing device 410 is a static mixer.
[0038] The agglomeration compound agent and desulfurization wastewater mixture supply system also includes a premixed branch pipe 420. The inlet of the premixed branch pipe 420 is connected to the inlet pipe of the mixing device 200 and is located upstream of the premixing device 410. The outlet of the premixed branch pipe 420 is connected to the inlet pipe of the mixing device 200 and is located downstream of the premixing device 410. The premixed branch pipe 420 facilitates the maintenance of the premixing device 410.
[0039] The premixed branch pipe 420 is equipped with a premixed branch pipe valve, which is closed during normal operation of the premixed device 410 and open when the premixed device 410 is under maintenance.
[0040] The mixing device 200 includes a mixing tank 210, the inlet pipe of the mixing tank 210 is connected to the wastewater inlet pipe and the outlet pipe of the emulsifying device 100 respectively, the inlet pipe of the spraying device 300 is connected to the outlet pipe of the mixing tank 210, and the premixing device 410 is installed on the inlet pipe of the mixing tank 210.
[0041] The inlet of the premixing branch pipe 420 is connected to the inlet pipe of the mixing tank 210 and is located upstream of the premixing device 410, while the outlet of the premixing branch pipe 420 is connected to the inlet pipe of the mixing tank 210 and is located downstream of the premixing device 410.
[0042] The mixing device 200 also includes a stirrer disposed on the mixing tank 210, wherein the stirring paddle of the stirrer extends into the mixing tank 210 from top to bottom.
[0043] Preferably, the inlet pipe of the mixing tank 210 is located at the top of the mixing tank 210, and the outlet pipe of the mixing tank 210 is located at the bottom of the mixing tank 210, so as to facilitate the thorough mixing of wastewater and emulsified agglomerating compound agent.
[0044] Preferably, the agglomeration composite agent and desulfurization wastewater mixture supply system further includes a main sewage pipe, and the mixing device 200 further includes an overflow pipe 220, the inlet of the overflow pipe 220 is connected to the top of the mixing tank 210, and the outlet of the overflow pipe 220 is connected to the main sewage pipe.
[0045] Furthermore, the mixing device 200 also includes a tank drain pipe 230, the inlet of which is connected to the bottom of the mixing tank 210, and the outlet of which is connected to the main drain pipe.
[0046] The agglomeration compound agent and desulfurization wastewater mixture supply system also includes a clean water main pipe, and the mixing device 200 also includes a tank cleaning pipe 240. The clean water main pipe and the inlet end of the tank cleaning pipe 240 are connected, and the outlet end of the tank cleaning pipe 240 is connected to the mixing tank 210.
[0047] Preferably, the outlet end of the tank cleaning pipe 240 is connected to the top of the mixing tank 210. This facilitates cleaning the mixing tank 210.
[0048] The spraying device 300 includes a spray pump 310 and a nozzle. The input pipe of the spray pump 310 is connected to the water outlet pipe of the mixing device 200, and the output pipe of the spray pump 310 is connected to the nozzle.
[0049] The spraying device 300 further includes a pump cleaning pipe 320, a pump drain pipe 330, a pump cleaning valve, and a pump drain valve. The input pipe of the spray pump 310 is connected to the outlet pipe of the mixing device 200, the output pipe of the spray pump 310 is connected to the nozzle, and the nozzle is connected to the flue. The pump cleaning pipe 320 is connected to the output pipe of the spray pump 310, and the pump drain pipe 330 is connected to the input pipe of the spray pump 310. The pump cleaning valve is installed on the pump cleaning pipe 320, the pump drain valve is installed on the pump drain pipe 330, and the pump inlet valve is installed on the outlet pipe of the mixing device 200. This allows for both reverse and forward cleaning of the spray pump 310. During reverse cleaning, clean water enters the spray pump 310 from the pump cleaning pipe 320 in reverse, while wastewater flows from the input pipe of the spray pump 310 into the pump drain pipe 330. During forward cleaning, clean water enters the output pipe of the spray pump 310 from the pump cleaning pipe 320, preventing the agglomerating compound from depositing in the pipe after prolonged operation. By performing forward and reverse cleaning on the spray pump 310, clogging of the spray pump 310 can be avoided.
[0050] The pump cleaning pipe 320 is connected to the clean water main pipe, and the pump drain pipe 330 is connected to the drain main pipe.
[0051] The emulsification device 100 includes a reagent storage tank 110, an emulsification tank 120, and an emulsification pump set 130. The reagent storage tank 110 is connected to the emulsification tank 120. The input pipe of the emulsification pump set 130 is connected to the output pipe of the emulsification tank 120. The output end of the emulsification pump set 130 is connected to the premixing device 410.
[0052] The emulsifying pump assembly 130 includes a shear pump and a delivery pump. The input pipe of the shear pump is connected to the output pipe of the emulsifying tank 120, the output pipe of the shear pump is connected to the input pipe of the delivery pump, and the output pipe of the delivery pump is connected to the premixing device 410.
[0053] The emulsification device 100 also includes a pharmaceutical delivery component, the input end of which is connected to the pharmaceutical storage tank, and the output end of which is connected to the emulsification tank 120.
[0054] The emulsification device 100 also includes a level gauge, which is disposed inside the emulsification tank 120.
[0055] The emulsification device 100 also includes a pharmaceutical metering device for measuring the dosage of the pharmaceutical agent flowing into the emulsification tank 120.
[0056] The mixing device 200, the spraying device, and the premixing device 410 are located in the first region, and the emulsifying device 100 is located in the second region. A maintenance channel is provided between the first region and the second region, and the output pipe of the emulsifying device 100 is connected to the premixing device 410 through the maintenance channel.
[0057] The maintenance channel is equipped with a pedal, and the output pipe of the emulsifying device 100 passes through the bottom of the pedal.
[0058] The agglomeration compound agent and desulfurization wastewater mixture supply system also includes a ladder 520 and a work platform 530. The ladder 520 is located on the side of the emulsification device 100 away from the maintenance passage and is connected to the work platform 530. The work platform 530 is connected to the emulsification tank 120 and the mixing tank 210.
[0059] The above description is only a description of the preferred embodiment of the present utility model and is not intended to limit the scope of the present utility model in any way. Any changes or modifications made by those skilled in the art based on the above disclosure shall fall within the protection scope of the claims.
Claims
1. A system for supplying a mixture of agglomerating compound agent and desulfurization wastewater, comprising an emulsification device, a mixing device, and a spraying device, characterized in that, It also includes a premixing device, the water inlet pipe of which is connected to the wastewater inlet pipe and the water outlet pipe of the emulsification device, the water outlet pipe of which is connected to the water inlet pipe of the mixing device, and the water outlet pipe of the mixing device is connected to the water inlet pipe of the spraying device.
2. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 1, characterized in that, The premixing device is a static mixer.
3. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 2, characterized in that, It also includes a premixed branch pipe, the inlet of which is connected to the inlet pipe of the mixing device and located upstream of the premixed device, and the outlet of which is connected to the inlet pipe of the mixing device and located downstream of the premixed device.
4. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 3, characterized in that, The premixed branch pipe is equipped with a premixed branch pipe valve.
5. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 3, characterized in that, The mixing device includes a mixing tank, the inlet pipe of which is connected to a wastewater inlet pipe and the outlet pipe of the emulsification device, the inlet pipe of the spraying device is connected to the outlet pipe of the mixing tank, and the premixing device is installed on the inlet pipe of the mixing tank.
6. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 5, characterized in that, The inlet of the premixed branch pipe is connected to the inlet pipe of the mixing tank and is located upstream of the premixing device, while the outlet of the premixed branch pipe is connected to the inlet pipe of the mixing tank and is located downstream of the premixing device.
7. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 5, characterized in that, The mixing device also includes a stirrer disposed on the mixing tank, the stirring paddle of the stirrer extending from top to bottom into the mixing tank.
8. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 5, characterized in that, The inlet pipe of the mixing tank is located at the top of the mixing tank, and the outlet pipe of the mixing tank is located at the bottom of the mixing tank.
9. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 5, characterized in that, It also includes a main drain pipe, and the mixing device also includes an overflow pipe, the inlet of which is connected to the top of the mixing tank, and the outlet of which is connected to the main drain pipe.
10. The agglomeration composite agent and desulfurization wastewater mixture supply system as described in claim 9, characterized in that, The mixing device also includes a tank drain pipe, the inlet of which is connected to the bottom of the mixing tank, and the outlet of which is connected to the main drain pipe.