Wet incineration quench tower

Abstract

The utility model relates to the field of garbage disposal equipment, concretely relates to a quenching tower for wet incineration, including quenching assembly, deacidification assembly, smoke exhaust component and dust collecting component, quenching assembly and deacidification assembly be equipped with inner tube respectively and the water mist sprayer piece of being placed in inner tube and the outer tube and the medicine mist sprayer piece of being placed in outer tube, inner tube is placed in outer tube, still be equipped with filter screen and high pressure back flushing spare in outer tube. Utilize the water mist sprayer piece in inner tube to spray water mist to high temperature smoke dust and make it quenching cooling, the smoke dust after quenching directly diffuses to outer tube again by the medicine mist sprayer piece in outer tube and sprays alkaline medicine mist to make the acid gas in smoke dust be neutralized and deacidification, utilize filter screen and high pressure back flushing spare in outer tube and smoke exhaust component and dust collecting component can carry out filtration and collection to the dust and particulate matter in smoke dust, and high pressure back flushing cleaning to filter screen when necessary, thereby can improve operation efficiency, reduce cost and avoid secondary pollution risk.

Description

Technical Field

[0001] This utility model relates to the field of waste treatment equipment, specifically to a quench tower for wet incineration. Background Technology

[0002] Wet incineration of waste involves adding water to turn waste into a sludge-like substance, which is then burned at a high temperature of around 800°C to convert the waste into ash and produce high-temperature flue gas and dust. Large-scale waste treatment plants can recover and utilize the high-temperature flue gas produced after incineration through energy conversion equipment, such as power generation. However, due to investment limitations, small-scale treatment plants typically allow the high-temperature flue gas and dust produced after incineration to be cooled and dusted before being naturally discharged. Because waste has a complex composition, the high-temperature flue gas produced after combustion contains acidic gases such as sulfur dioxide and nitrogen oxides. Furthermore, the harmful substance dioxins are highly susceptible to resynthesis in the temperature range of 300°C to 500°C. If the high-temperature flue gas is allowed to cool naturally and be freely discharged, it will cause secondary pollution to the surrounding environment. Therefore, most wet incineration processes currently use quench towers to rapidly cool the high-temperature flue gas to around 200°C to avoid the temperature window for dioxin formation. However, even after quenching, some acidic components remain in the steam, which will still have an environmental impact if not further treated. However, performing multiple separate treatments using multiple facilities not only reduces efficiency and increases processing costs but also poses a risk of secondary pollution. Therefore, it is necessary to improve the quench tower used in wet incineration. The goal is to integrate quenching, acid removal, and dust collection into a single unit, enabling rapid cooling of high-temperature flue gas, neutralization and deacidification of acidic gases in the flue gas, and filtration, separation, and collection of residual dust. This would improve operational efficiency, reduce costs, and avoid the risk of secondary pollution. This is the problem to be solved in this case. Utility Model Content

[0003] To overcome the shortcomings of existing technologies, this utility model discloses a quench tower for wet incineration, comprising a quenching component, a deacidification component, a flue gas exhaust component, and a dust collection component. The quenching component and the deacidification component are each equipped with an inner cylinder and a water mist sprayer placed inside the inner cylinder, and an outer cylinder and a chemical mist sprayer placed inside the outer cylinder. The inner cylinder is placed inside the outer cylinder, which also contains a filter screen and a high-pressure backflushing component. High-temperature flue gas discharged from wet incineration and fed into the inner cylinder of the quenching component can be rapidly cooled by spraying water mist, and the rapidly cooled flue gas can be diffused into the outer cylinder. The deacidification component can neutralize and deacidify the flue gas dispersed in the outer cylinder by spraying alkaline chemical mist. This invention improves upon the quench tower used in wet incineration by using water mist sprayers inside the inner cylinder to spray water mist onto high-temperature flue gas, rapidly cooling it. The cooled flue gas then diffuses directly into the outer cylinder, where alkaline chemical mist is sprayed by chemical mist sprayers to neutralize and deacidify the acidic gases in the flue gas. The filter screen, high-pressure backflushing components, exhaust components, and dust collection components inside the outer cylinder can filter and collect dust and particulate matter in the flue gas, and the filter screen can be cleaned by high-pressure backflushing when necessary. This improves operational efficiency, reduces costs, and avoids the risk of secondary pollution.

[0004] To achieve the above objectives, the technical solution adopted by this utility model is as follows:

[0005] A quench tower for wet incineration is characterized by comprising a quenching component, a deacidification component, a flue gas exhaust component, and a dust collection component. The quenching component has an inner cylinder and a water mist sprayer located at the upper part of the inner cylinder cavity. The deacidification component has an outer cylinder and a chemical mist sprayer, a filter screen, and a high-pressure backflushing component located at the upper part of the outer cylinder cavity. The inner cylinder of the quenching component is placed inside the cavity of the outer cylinder of the deacidification component. The quenching component can spray water mist to rapidly cool the high-temperature flue gas discharged from wet incineration that is fed into the inner cylinder from the outside, and can diffuse the rapidly cooled flue gas into the outer cylinder of the deacidification component. The deacidification component can spray alkaline chemical mist to deacidify the flue gas dispersed in the outer cylinder. The flue gas exhaust component and the dust collection component are respectively connected to the top and bottom of the outer cylinder of the deacidification component. The deacidification component can filter the flue gas in the outer cylinder, and the filtered flue gas and residual dust can be discharged by the flue gas exhaust component and collected by the dust collection component, respectively. The deacidification component can use reverse high-pressure air blowing to clean the residual dust on the filter screen.

[0006] The inner cylinder is a circular cavity formed by a peripheral wall and a conical bottom wall. The bottom of the conical cylinder has a drain port with a valve. The upper part of the peripheral wall has several flow holes for smoke and dust to overflow. The outer cylinder is a circular cavity formed by a peripheral wall and a bottom wall with a bottom hole. The inner cylinder can be inserted into the cavity of the outer cylinder through the bottom hole of the bottom wall of the outer cylinder and is fixed to the bottom wall of the outer cylinder. There is a gap between the peripheral wall of the inner cylinder and the peripheral wall of the outer cylinder.

[0007] The water mist spraying component is provided with a first disc-shaped liquid supply pipe and a first spray nozzle. The first spray nozzle consists of several pieces, which are distributed and connected below the first disc-shaped liquid supply pipe and are connected to the pipe of the first disc-shaped liquid supply pipe. The first disc-shaped liquid supply pipe is a disc-shaped mesh component consisting of several circular pipes connected end to end and interconnected by horizontal pipes. The diameter of the several circular pipes increases sequentially and is arranged in concentric circles from the inside to the outside. An inlet pipe that can be connected to an external water supply network is provided on its periphery. The water mist spraying component is fixed inside the inner cylinder and placed below the flow hole.

[0008] The aerosol spraying device is equipped with a second disc-shaped liquid supply pipe and a second spray nozzle. The second spray nozzle consists of several pieces, which are distributed and connected below the second disc-shaped liquid supply pipe and are connected to the pipe of the second disc-shaped liquid supply pipe. The second disc-shaped liquid supply pipe is a disc-shaped mesh component consisting of several circular pipes connected end to end and interconnected by horizontal pipes. The diameter of the several circular pipes increases sequentially and is arranged in concentric circles from the inside to the outside. An inlet pipe is provided on its periphery that can be connected to an external liquid supply network.

[0009] The quenching assembly is also equipped with an inner top cover and a smoke inlet pipe. The inner top cover is a conical cover that is placed above the inner cylinder and is detachably connected to the inner cylinder. The smoke inlet pipe is located on one side of the middle of the inner cylinder. After passing through the cylinder walls of the outer cylinder and the inner cylinder, the smoke inlet pipe communicates with the cavity of the inner cylinder. The smoke inlet pipe is fixedly connected to both the outer cylinder and the inner cylinder. The smoke inlet pipe is equipped with a valve.

[0010] The deacidification assembly is also provided with an outer top cover, which is spherical and is positioned above the outer cylinder and is detachably and sealed to the outer cylinder.

[0011] The high-pressure backflush component is equipped with an air pipe and an air nozzle. The air pipe is arranged in a serpentine pattern on the back of the outer top cover. There are several air nozzles, which are distributed and connected to the air pipe. The air pipe can be connected to an external compressed air pipeline network.

[0012] The filter screen is placed between the high-pressure backflush component and the aerosol spray component and is detachably connected to the inner wall of the outer cylinder.

[0013] The smoke exhaust assembly is equipped with an adsorption box and an exhaust fan. The adsorption box is filled with activated carbon and is placed on top of the outer cover. Its input end is connected to the outer cylinder by a pipe, and its output end is connected to the exhaust fan by a pipe with a valve.

[0014] The dust collection assembly is equipped with a dust pump and a dust collection box. The dust collection box contains a dust collection bag. The input end of the dust pump is connected to the bottom of the outer cylinder via a pipe with a valve, and the output end of the dust pump is connected to the dust collection bag inside the dust collection box via a pipe.

[0015] As described above, the advantages of the quench tower for wet incineration provided by this utility model are as follows: the inner cylinder of the quenching component equipped with water mist sprayers is placed inside the inner cavity of the outer cylinder of the deacidification component equipped with chemical mist sprayers, a filter screen, and a high-pressure backflushing component. The flue gas exhaust component and the dust collection component are respectively connected to the top and bottom of the outer cylinder. The water mist sprayers in the inner cylinder spray water mist onto the high-temperature flue gas to rapidly cool it down. The rapidly cooled flue gas diffuses directly into the outer cylinder, where the chemical mist sprayers spray alkaline chemical mist to neutralize the acidic gases in the flue gas and remove acid. The filter screen and high-pressure backflushing component in the outer cylinder, as well as the flue gas exhaust component and the dust collection component, can filter and collect dust and particulate matter in the flue gas, and the filter screen can be cleaned by high-pressure backflushing when necessary, thereby improving operating efficiency, reducing costs, and avoiding the risk of secondary pollution. This utility model has a reasonable design, simple structure, low cost, and is easy to promote. Attached Figure Description

[0016] Figure 1 This is a schematic diagram of a quench tower for wet incineration according to the present invention.

[0017] Figure 2 This is an enlarged schematic diagram of the quenching component;

[0018] Figure 3 for Figure 2 Enlarged diagram of direction A in the diagram;

[0019] Figure 4 This is an enlarged schematic diagram of the deacidification component;

[0020] Figure 5 for Figure 4 Enlarged schematic diagram in direction B;

[0021] Figure 6 for Figure 4 Enlarged schematic diagram of part C;

[0022] Figure 7 This is an enlarged schematic diagram of the smoke extraction assembly;

[0023] Figure 8 This is an enlarged schematic diagram of the dust collection component.

[0024] Figure label:

[0025] 1. Rapid cooling assembly; 11. Inner cylinder; 111. Flow hole; 12. Inner top cover; 13. Water mist spraying component; 131. First disc-shaped liquid supply pipe; 132. First spray nozzle; 14. Smoke inlet pipe; 2. Deacidification assembly; 21. Outer cylinder; 22. Outer top cover; 23. Chemical mist spraying component; 231. Second disc-shaped liquid supply pipe; 232. Second spray nozzle; 24. Filter screen; 25. High-pressure backflushing component; 251. Air pipe; 252. Air blowing nozzle; 3. Smoke exhaust assembly; 31. Adsorption box; 32. Exhaust fan; 4. Dust collection assembly; 41. Dust pump; 42. Dust collection box. Detailed Implementation

[0026] The present invention will be further described below through specific embodiments.

[0027] like Figure 1 , Figure 2 and Figure 4 As shown, the present invention discloses a quench tower for wet incineration, comprising a quenching assembly 1, a deacidification assembly 2, a flue gas exhaust assembly 3, and a dust collection assembly 4. The quenching assembly 1 includes an inner cylinder 11, a water mist sprayer 13 positioned at the upper part of the inner cavity of the inner cylinder 11, an inner top cover 12, and a flue gas inlet pipe 14. The deacidification assembly 2 includes an outer cylinder 21, a chemical mist sprayer 23 positioned at the upper part of the inner cavity of the outer cylinder 21, a filter screen 24, a high-pressure backflushing component 25, and an outer top cover 22. The inner cylinder 11 of the quenching assembly 1 is placed inside the cavity of the outer cylinder 21 of the deacidification assembly 2. The quenching assembly 1 can handle externally supplied materials into the inner cylinder 11. The high-temperature flue gas emitted from the wet incineration in component 1 is rapidly cooled by spraying water mist, and the rapidly cooled flue gas can be diffused into the outer cylinder 21 of the deacidification component 2. The deacidification component 2 can spray alkaline chemical mist to deacidify the flue gas dispersed in the outer cylinder 21. The exhaust component 3 and the dust collection component 4 are respectively connected to the top and bottom of the outer cylinder 21 of the deacidification component 2. The deacidification component 2 can filter the flue gas in the outer cylinder 21, and the filtered flue gas and residual dust can be discharged by the exhaust component 3 and collected by the dust collection component 4, respectively. The deacidification component 2 can clean the residual dust on the filter screen 24 by reverse high-pressure blowing.

[0028] like Figures 1 to 4 As shown, the inner cylinder 11 of this utility model is a circular cavity formed by a peripheral wall and a conical bottom wall. The conical bottom is provided with a drain port and a valve on the drain port. The upper part of the peripheral wall is evenly provided with a number of flow holes 111 for smoke and dust to overflow. The water mist spraying component 13 is provided with a first disc-shaped liquid supply pipe 131 and a first spray nozzle 132. There are several first spray nozzles 132, which are distributed and connected below the first disc-shaped liquid supply pipe 131 and connected to the pipe of the first disc-shaped liquid supply pipe 131. The first disc-shaped liquid supply pipe 131 is a disc-shaped mesh component consisting of several circular pipes connected end to end and interconnected by a transverse pipe. The diameter of the several circular pipes increases sequentially and is arranged in concentric circles from the inside to the outside. A water inlet pipe that can be connected to an external water supply network is provided on its periphery. The water mist spraying component 13 is fixed inside the inner cylinder 11 and placed below the flow holes 111. The inner top cover 12 is a conical cover, which is placed above the inner cylinder 11 and is detachably connected to the inner cylinder 11. The smoke inlet pipe 14 is placed on one side of the middle part of the inner cylinder 11. The smoke inlet pipe 14 passes through the cylinder walls of the outer cylinder 21 and the inner cylinder 11 and communicates with the cavity of the inner cylinder 11. The smoke inlet pipe 14 is fixedly connected to both the outer cylinder 21 and the inner cylinder 11. The smoke inlet pipe 14 is equipped with a valve.

[0029] like Figure 1 , Figure 2 , Figures 4 to 6 As shown, the outer cylinder 21 of this utility model is a circular cavity formed by a peripheral wall and a bottom wall with a bottom hole. The inner cylinder 11 can be inserted into the cavity of the outer cylinder 21 through the bottom hole of the bottom wall of the outer cylinder 21 and is fixedly connected to the bottom wall of the outer cylinder 21. There is a gap between the peripheral wall of the inner cylinder 11 and the peripheral wall of the outer cylinder 21. The aerosol spraying component 23 is provided with a second disc-shaped liquid supply pipe 231 and a second spray nozzle 232. There are several second spray nozzles 232, which are distributed and connected below the second disc-shaped liquid supply pipe 231 and connected to the pipe of the second disc-shaped liquid supply pipe 231. The second disc-shaped liquid supply pipe 231 is a disc-shaped mesh component consisting of several circular pipes connected end to end and interconnected by a transverse pipe. The diameter of the several circular pipes increases sequentially and is arranged in concentric circles from the inside to the outside. An inlet pipe that can be connected to an external liquid supply network is provided on its periphery. The outer top cover 22 is spherical in shape, positioned above the outer cylinder 21 and detachably and sealingly connected to it. The high-pressure backflush component 25 includes an air pipe 251 and air nozzles 252. The air pipe 251 is arranged in a serpentine pattern on the back of the outer top cover 22. Several air nozzles 252 are distributed and connected to the air pipe 251, which can be connected to an external compressed air network. The filter screen 24 is positioned between the high-pressure backflush component 25 and the aerosol spray component 23 and detachably connected to the inner wall of the outer cylinder 21.

[0030] like Figure 1 , Figure 4 and Figure 7 As shown, the smoke exhaust assembly 3 of this utility model is provided with an adsorption box 31 and an exhaust fan 32. The adsorption box 31 is filled with activated carbon and is placed on top of the outer top cover 22. Its input end is connected to the outer cylinder 21 by a pipe, and its output end is connected to the exhaust fan 32 by a pipe with a valve.

[0031] like Figure 1 , Figure 4 and Figure 8 As shown, the dust collection assembly 4 of this utility model is provided with a dust pump 41 and a dust collection box 42. The dust collection box 42 is provided with a dust collection bag. The input end of the dust pump 41 is connected to the bottom of the outer cylinder 21 by a pipe with a valve, and the output end of the dust pump 41 is connected to the dust collection bag in the dust collection box 42 by a pipe.

[0032] The wet incineration quench tower described in this utility model can also be equipped with a temperature sensor for temperature detection and a control system for automatic control. Both temperature detection and automatic control are known technologies.

[0033] The usage method of this quench tower for wet incineration is as follows:

[0034] In use, first open the valves on the inlet pipe 14 and the pipes on the exhaust assembly 3; close the valves on the drain port at the bottom of the inner cylinder 11 and the pipes on the dust collection assembly 4; close the external air supply port that supplies compressed air to the high-pressure backflush unit 25. Open the external water supply valve that supplies water to the water mist sprayer 13 and the external chemical supply valve that supplies alkaline chemicals to the chemical mist sprayer 23, so that the water mist sprayer 13 and the chemical mist sprayer 23 begin to spray; turn on the exhaust fan 32. At this time, the high-temperature flue gas discharged from the external wet incineration of waste enters the inner cylinder 11 of the rapid cooling assembly 1 through the inlet pipe 14, and the water mist sprayer 13 sprays water mist to rapidly cool the high-temperature flue gas to a window temperature of about 200°C, which avoids the generation of dioxins. At this time, the solid matter mixed in the smoke and dust settles, while the gaseous smoke and dust rises and diffuses through the flow holes 111 on both sides of the inner cylinder 11 into the outer cylinder 21 of the deacidification component 2. There, the gaseous gas is neutralized by the alkaline mist sprayed by the mist sprayer 23 inside the outer cylinder 21, thus deacidifying and cooling down again. The solid matter formed after the neutralization reaction settles, while the gaseous smoke and dust continues to rise and is filtered by the filter screen 24. At this time, the flue gas passes through the filter screen 24, is adsorbed by the adsorption box 31, and is extracted and discharged by the exhaust fan 32. The residue intercepted by the filter screen 24 settles to the bottom of the outer cylinder 21 or adheres to the filter screen 24.

[0035] If the filter screen 24 becomes clogged and needs cleaning, close the valve on the smoke inlet pipe 14 and the valve on the exhaust assembly 3; stop the water mist sprayer 13 and the chemical mist sprayer 23; open the valve on the dust collection assembly 4; start the dust collection pump 41 of the dust collection assembly 4; open the external air supply port that supplies compressed air to the high-pressure backflush unit 25. At this time, the high-pressure backflush unit 25 can blow air in reverse high pressure onto the filter screen 24 from above, causing the residue attached to the filter screen 24 to fall off and fall into the bottom of the outer cylinder 21; the dust collection pump 41 of the dust collection assembly 4 can suck out the residue and collect it by the dust collection box 42; open the valve on the drain port at the bottom of the inner cylinder 11, and the residue discharged from the drain port at the bottom of the inner cylinder 11 can be collected separately.

[0036] This invention improves the quench tower for wet incineration by placing the inner cylinder 11 of the quenching component 1, equipped with a water mist sprayer 13, inside the outer cylinder 21 of the deacidification component 2, which is equipped with a chemical mist sprayer 23, a filter screen 24, and a high-pressure backflushing component 25. The flue gas exhaust component 3 and the dust collection component 4 are connected to the top and bottom of the outer cylinder 21, respectively. The water mist sprayer 13 in the inner cylinder 11 sprays water mist onto the high-temperature flue gas to rapidly cool it down. The rapidly cooled flue gas diffuses directly into the outer cylinder 21, where the chemical mist sprayer 23 sprays alkaline chemical mist to neutralize the acidic gases in the flue gas and remove acid. The filter screen 24 and the high-pressure backflushing component 25 in the outer cylinder 21, as well as the flue gas exhaust component 3 and the dust collection component 4, can filter and collect dust and particulate matter in the flue gas, and the filter screen 24 can be cleaned by high-pressure backflushing when necessary. This improves operating efficiency, reduces costs, and avoids the risk of secondary pollution.

[0037] The above is only one specific embodiment of the present utility model, but the design concept of the present utility model is not limited thereto. Any non-substantial modifications made to the present utility model using this concept shall be deemed as an infringement of the protection scope of the present utility model.

Claims

1. A quench tower for wet incineration, characterized in that: The assembly includes a quenching component (1), a deacidification component (2), a flue gas exhaust component (3), and a dust collection component (4). The quenching component (1) has an inner cylinder (11) and a water mist sprayer (13) located in the upper part of the inner cavity of the inner cylinder (11). The deacidification component (2) has an outer cylinder (21) and a chemical mist sprayer (23), a filter screen (24), and a high-pressure backflushing component (25) located in the upper part of the inner cavity of the outer cylinder (21). The inner cylinder (11) of the quenching component (1) is placed inside the cavity of the outer cylinder (21) of the deacidification component (2). The quenching component (1) can process the high-temperature flue gas discharged from the wet incineration that is fed into the inner cylinder (11) from the outside. The spray water mist rapidly cools the smoke and dust and diffuses the cooled smoke and dust into the outer cylinder (21) of the deacidification component (2). The deacidification component (2) sprays alkaline chemical mist to deacidify the smoke and dust dispersed in the outer cylinder (21). The exhaust component (3) and the dust collection component (4) are respectively connected to the top and bottom of the outer cylinder (21) of the deacidification component (2). The deacidification component (2) can filter the smoke and dust in the outer cylinder (21), and the filtered smoke and dust can be discharged by the exhaust component (3) and collected by the dust collection component (4). The deacidification component (2) can perform reverse high-pressure air blowing on the filter screen (24) to clean the dust on the filter screen (24).

2. A quench tower for wet incineration according to claim 1, characterized in that: The inner cylinder (11) is a circular cavity formed by a peripheral wall and a conical bottom wall. Several flow holes (111) are evenly distributed on the upper part of the peripheral wall. The outer cylinder (21) is a circular cavity formed by a peripheral wall and a bottom wall with a bottom hole. The inner cylinder (11) can be inserted into the cavity of the outer cylinder (21) through the bottom hole of the bottom wall of the outer cylinder (21) and fixedly connected to the bottom wall of the outer cylinder (21).

3. A quench tower for wet incineration according to claim 2, characterized in that: The water mist spraying component (13) is provided with a first disc-shaped liquid supply pipe (131) and a first spray nozzle (132). The first spray nozzle (132) consists of several pieces, which are distributed and connected below the first disc-shaped liquid supply pipe (131) and connected to the pipe of the first disc-shaped liquid supply pipe (131). The water mist spraying component (13) is fixed inside the inner cylinder (11) and placed below the flow hole (111).

4. A quench tower for wet incineration according to claim 3, characterized in that: The atomizing sprayer (23) is provided with a second disc-shaped liquid supply pipe (231) and a second spray nozzle (232). The second spray nozzle (232) consists of several pieces, which are distributed and connected below the second disc-shaped liquid supply pipe (231) and are connected to the pipe of the second disc-shaped liquid supply pipe (231).

5. A quench tower for wet incineration according to claim 4, characterized in that: The quenching assembly (1) is also provided with an inner top cover (12) and a smoke inlet pipe (14). The inner top cover (12) is a conical cover that is placed above the inner cylinder (11) and connected to the inner cylinder (11). The smoke inlet pipe (14) is placed on one side of the middle part of the inner cylinder (11). The smoke inlet pipe (14) passes through the cylinder walls of the outer cylinder (21) and the inner cylinder (11) and communicates with the cavity of the inner cylinder (11).

6. A quench tower for wet incineration according to claim 5, characterized in that: The deacidification component (2) is also provided with an outer top cover (22), which is placed above the outer cylinder (21) and is sealed to the outer cylinder (21).

7. A quench tower for wet incineration according to claim 6, characterized in that: The high-pressure backflush component (25) is provided with an air pipe (251) and an air nozzle (252). The air pipe (251) is located on the back of the outer top cover (22). There are several air nozzles (252), which are distributed and connected to the air pipe (251).

8. A quench tower for wet incineration according to claim 7, characterized in that: The filter screen (24) is placed between the high-pressure backflush component (25) and the aerosol spray component (23) and connected to the inner wall of the outer cylinder (21).

9. A quench tower for wet incineration according to claim 8, characterized in that: The smoke exhaust assembly (3) is equipped with an adsorption box (31) and an exhaust fan (32). The adsorption box (31) is placed on the top of the outer top cover (22), its input end is connected to the outer cylinder (21), and its output end is connected to the exhaust fan (32).

10. A quench tower for wet incineration according to claim 9, characterized in that: The dust collection assembly (4) is equipped with a dust pump (41) and a dust collection box (42). The input end of the dust pump (41) is connected to the bottom of the outer cylinder (21), and the output end of the dust pump (41) is connected to the dust collection box (42).

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