Circulating treatment device for incineration fly ash

Abstract

The utility model relates to the technical field of fly ash circulating treatment, in particular to an incineration fly ash circulating treatment device which comprises a drying assembly and a desulfurization assembly on the right side of the drying assembly, a collecting assembly is arranged on the left side, close to the lower portion, of the desulfurization assembly, and the drying assembly comprises a drying box and drying sponge arranged in the drying box. An air outlet pipeline is arranged at the top of the drying box, the desulfurization assembly comprises a desulfurization box and a spraying pipe in the desulfurization box, the collecting assembly comprises a fly ash cabin and a first pipeline arranged at the upper end of the fly ash cabin, and an air blower is arranged below the right side of the first pipeline; by arranging the drying box, water vapor in gas is absorbed, residual water vapor is prevented from being fed into the incineration tower again, the incineration efficiency is prevented from being affected, the air blower is arranged to push fly ash to be circularly treated, and the fly ash is prevented from flowing back to the incineration tower due to insufficient wind power, and the fly ash is prevented from being circularly treated; purified gas can be discharged through the air outlet pipeline, and safety risks caused by the fact that the incineration tower is in a continuous pressurization state are avoided.

Description

Technical Field

[0001] The utility model relates to the technical field of fly ash circulation treatment, in particular to a device for circulating treatment of incineration fly ash. Background Art

[0002] The incineration of hazardous waste, domestic garbage, and medical waste produces a large amount of fly ash. Fly ash is a hazardous solid waste that contains volatile organic compounds such as chlorobenzenes and dioxins, and heavy metals. Its particles are extremely small and light, making it easy to escape and float in the atmosphere, causing serious pollution to the areas surrounding the waste incineration site. In addition, since fly ash is enriched with toxic substances such as dioxins, which are carcinogenic to humans, it causes great harm to people living near the incineration site. Therefore, it is particularly important to remove the organic matter in the fly ash.

[0003] The utility model with announcement number CN206112955U discloses a sludge incineration fly ash recycling system, including an incinerator, a desulfurization tower, a fly ash collector and a fly ash bin. The fly ash collector includes a smoke pipe, a first 100-blade group and a second 100-blade group. The smoke pipe includes an upper L-shaped pipe and a lower L-shaped pipe that are interconnected. The first 100-blade group is arranged at the bend of the upper L-shaped pipe, and the second 100-blade group is arranged at the bend of the lower L-shaped pipe. The first 100-blade group and the second 100-blade group are respectively provided with a first ash outlet and a second ash outlet at the bottom of the bend of the first L-shaped pipe and the lower L-shaped pipe;

[0004] The above technical solution can collect, treat and recycle sludge incineration fly ash, with good resource utilization effect, reducing the pollution of dioxins and heavy metals in sludge incineration fly ash to the environment, and has good economic value; however, in actual use, after the gas in the device passes through the desulfurization tower for desulfurization, the gas contains water vapor, and the fly ash is easy to stick to the inner wall of the fly ash collector and is not easy to clean. After the fly ash is separated, there is still moisture inside the gas, which is re-sent to the incinerator, affecting the incineration treatment efficiency. At the same time, the device relies on the reaction of the reactor to provide power to promote the fly ash recycling treatment, which is prone to fly ash backflow, affecting the normal progress of the fly ash recycling treatment, and there is no ventilation port inside the device. The incinerator is in a continuously pressurized state, which is prone to explosion, causing safety risks. Utility Model Content

[0005] The purpose of the present utility model is to provide a ventilation and heat dissipation device in a prefabricated cabin to solve the problem of a sludge incineration fly ash recycling system with the authorization announcement number CN206112955U proposed in the above background technology. However, in actual use, after the gas in the device passes through the desulfurization tower for desulfurization, the gas contains water vapor, and the fly ash is easily adhered to the inner wall of the fly ash collector and is not easy to clean. After the fly ash is separated, there is still residual moisture in the gas, which is re-sent into the incinerator, affecting the incineration treatment efficiency. At the same time, the device relies on the reaction of the reactor to provide power to promote the fly ash recycling treatment, and fly ash backflow is likely to occur, affecting the normal progress of the fly ash recycling treatment. In addition, there is no ventilation port inside the device, and the incinerator is in a continuously pressurized state, which is prone to explosion, causing safety risks.

[0006] To achieve the above objectives, the present invention provides the following technical solutions:

[0007] A circulating treatment device for incineration fly ash includes a drying component and a desulfurization component on the right side of the drying component. The desulfurization component is provided with a collecting component near the lower left side. The drying component includes a drying box and a drying sponge inside the drying box. A flap is provided on the top of the drying box, and an air outlet duct is provided at the center of the top of the flap. The desulfurization component includes a desulfurization box and a spray pipe inside the desulfurization box. A demister is provided above the spray pipe. The collecting component includes a fly ash chamber and a first pipe provided at the upper end of the fly ash chamber. A blower is provided at the lower right side of the first pipe.

[0008] Preferably, an air inlet duct is provided on the left side of the drying component, an air inlet valve is provided above the air inlet duct, an incineration tower is provided on the left side of the air inlet duct, a feed pipe is provided at the top center of the incineration tower, and a feed valve is provided on the left side of the feed pipe.

[0009] In the utility model, the air inlet duct is welded and fixed to the drying component, the air inlet valve is threadedly connected to the air inlet duct, the air inlet duct is welded and fixed to the incineration tower, the bottom end of the feed pipe is welded and fixed to the top end of the incineration tower, and the feed valve is threadedly connected to the feed pipe. By setting the air inlet duct, the gas dried by the drying component is sent back into the incineration tower. By setting the air inlet valve, the user can manually adjust the air outlet of the air inlet duct by twisting the air inlet valve, thereby increasing the use scenarios of the device. By setting the feed pipe, it is convenient to add materials to the incineration tower. By setting the feed valve, the size of the feed pipe opening can be adjusted, thereby reducing heat loss during incineration in the incineration tower and reducing waste of resources.

[0010] Preferably, a second pipe is provided on the right side of the drying box, a wind wheel is provided on the right side of the inner wall of the second pipe, the wind wheel is rotatably connected to the second pipe, a drive motor is provided at the front end of the second pipe corresponding to the wind wheel axon, and the output shaft of the drive motor is coaxially connected to the front end axon of the wind wheel.

[0011] In the utility model, the drying box is welded and fixed to the second pipeline, and the driving motor is fixed to the second pipeline by screws. By setting the second pipeline, the gas treated by the desulfurization component is transported to the drying box for drying. The wind wheel rotates counterclockwise. By manually adjusting the wind wheel speed, the circulation speed of the gas in the second pipeline moving to the left is adjusted to increase the circulation efficiency of the device. By setting the driving motor, the wind wheel is provided with rotational power.

[0012] Preferably, the flap is rotatably connected to the top of the drying box via a hinge, a sealing gasket is provided at the bottom of the flap, the sealing gasket is bonded and fixed to the top and the bottom of the flap, and the inner wall of the sealing gasket fits tightly, and an air outlet valve is provided on the left side of the air outlet duct.

[0013] In the utility model, the air outlet valve is threadedly connected to the air outlet duct. By arranging a flip cover, the drying sponge in the drying box can be easily replaced, thereby avoiding the drying sponge working for a long time and reducing the drying effect of the gas. By arranging a sealing gasket, the gas sealing inside the drying box is increased. By arranging an air outlet duct, the completely treated gas is discharged from the device, thereby avoiding continuous pressurization of the incineration tower and the occurrence of safety hazards. By adjusting the air outlet valve, the air outlet volume of the air outlet duct can be adjusted.

[0014] Preferably, an observation window is provided at the front end of the desulfurization box, a top cover is provided at the top of the desulfurization box, the top cover is rotatably connected to the desulfurization box through a hinge, a liquid inlet pipe is provided near the upper end on the right side of the desulfurization box, and a drain faucet is provided near the bottom end on the right side of the desulfurization box.

[0015] In the present invention, the liquid inlet pipe is welded and fixed to the desulfurization box, and the liquid discharge tap is welded and fixed to the desulfurization box. By setting an observation window, the reaction of the desulfurization liquid in the desulfurization box can be observed in real time, and the desulfurization liquid in the desulfurization box can be replaced in time to avoid affecting the removal effect of sulfur dioxide in the gas. By setting the liquid inlet pipe, new desulfurization liquid can be input into the desulfurization box in time, and by setting the liquid discharge tap, the desulfurization liquid after the reaction can be discharged from the desulfurization box, and the desulfurization liquid in the desulfurization box can be replaced.

[0016] Preferably, the desulfurization box is filled with desulfurization liquid, the spray pipe is fixedly connected to the inner wall of the desulfurization box by screws, and a plurality of nozzles are provided at the bottom of the spray pipe.

[0017] In the present invention, the top end of the nozzle is bonded and fixed to the bottom end of the spray pipe, and the desulfurization liquid is made by mixing chemical agents such as ammonia water. The ammonia water in the desulfurization liquid can react with sulfur dioxide to generate compounds such as ammonium sulfate or ammonium sulfite, thereby removing sulfur dioxide in the gas and avoiding sulfur dioxide discharge from the device to damage the environment. By setting the nozzle, the desulfurization liquid in the spray pipe is evenly sprayed, increasing the contact area between the desulfurization liquid and the gas, and accelerating the reaction efficiency of sulfur dioxide in the gas.

[0018] Preferably, a circulation pump is provided at the water inlet of the spray pipe, and a connecting pipe is provided at the water inlet end of the circulation pump. The connecting pipe passes through the outer wall of the desulfurization box and extends into the desulfurization liquid. A plurality of corrugated plates are provided in the demister, and the corrugated plates are distributed at equal intervals, and the corrugated plates and the demister are an integrally formed structure.

[0019] In the present invention, the water outlet of the circulation pump is welded and fixed to the water inlet of the spray pipe, the water outlet of the connecting pipe is welded and fixed to the water inlet of the circulation pump, and the connecting pipe is welded and fixed to the desulfurization box. By arranging the circulation pump and the spray pipe, the desulfurization liquid filled in the desulfurization box is transported to the top of the desulfurization box. By arranging the demister, when the gas containing mist flows through the demister at a certain speed, due to the inertial impact of the gas, the mist collides with the corrugated plate and the gathered droplets are so large that the gravity generated by itself exceeds the combined force of the rising force of the gas and the surface tension of the liquid. The droplets are separated from the surface of the corrugated plate in the demister, and the multi-fold structure of the corrugated plate increases the chance of mist being captured. The mist that is not removed is captured at the next turn through the same action. This repeated action greatly improves the demisting efficiency, pre-demists the gas flowing into the drying component, facilitates the drying of the drying component in the later stage, and increases the service life of the drying sponge in the drying component.

[0020] Preferably, a side cover is provided on the right side of the fly ash cabin, the side cover is rotatably connected to the fly ash cabin via a hinge, a fly ash window is provided at the front end of the fly ash cabin, a fly ash trough is provided inside the fly ash cabin, and the fly ash trough is plugged into the fly ash cabin.

[0021] In the utility model, by providing a side cover, it is convenient to take the fly ash trough out of the fly ash cabin, and by providing a fly ash window, it is convenient to observe the fly ash collection situation in the fly ash trough in real time and clean the fly ash in the fly ash trough in time. The fly ash trough and the fly ash cabin are plugged together, which makes it easy to take the fly ash trough. The outer wall of the fly ash trough fits tightly with the inner wall of the fly ash cabin, preventing fly ash from falling into the gap between the fly ash trough and the fly ash cabin, which increases labor costs.

[0022] Preferably, a partition is provided in the center of the Y-shape inside the first pipe, and a number of baffles are provided on both sides of the inverted V-shape on the right side of the first pipe, and the baffle welded and fixed to the top of the inner wall of the first pipe forms a 90-degree angle with the bottom surface, and the baffle welded and fixed to the bottom end of the inner wall of the first pipe is horizontal and inclined 15 degrees toward the ground, and barrier nets are provided at the connections between the first pipe, the air inlet pipe and the incineration tower.

[0023] In the present invention, the top of the partition is welded and fixed to the top of the inner wall of the first pipe, the baffle is welded and fixed to the inner wall of the first pipe, the blower is fixed to the right end of the first pipe by screws, and the left end of the first pipe is welded and fixed to the bottom of the incinerator. By setting the partition to block the fly ash in the gas flowing out of the incinerator, under the action of gravity, large particles of fly ash fall into the fly ash cabin below the first pipe, and by setting the baffle, the fly ash in the gas that further passes over the partition is removed.

[0024] Compared with the prior art, the beneficial effects of the present invention are:

[0025] 1. The utility model provides a demister to condense the water vapor inside the gas and flow into the desulfurization liquid. The drying box is provided to further absorb the water vapor in the gas, preventing the residual water vapor from being re-sent into the incineration tower and affecting the incineration efficiency. The blower is provided to promote the circulation of fly ash, avoiding insufficient wind force causing fly ash to flow back into the incineration tower and affecting the circulation of fly ash. The air outlet duct is provided and the air outlet valve is adjusted to discharge the purified gas through the air outlet duct, avoiding the incineration tower being in a continuously pressurized state, causing explosion and posing a safety risk.

[0026] 2. The utility model provides a fly ash trough in the fly ash chamber to facilitate users to quickly clean the collected fly ash; provides a barrier net at the left end of the first pipe and the air inlet pipe to prevent large particles of impurities from entering the device, causing blockage of the device and affecting the fly ash circulation treatment; and provides a wind wheel in the second pipe to accelerate the rotation speed of the wind wheel, thereby adjusting the gas circulation speed inside the device and accelerating the fly ash circulation treatment efficiency. BRIEF DESCRIPTION OF THE DRAWINGS

[0027] Figure 1 It is a schematic diagram of the overall structure of the utility model;

[0028] Figure 2 It is a side view schematic diagram of the overall structure of the utility model;

[0029] Figure 3 This is a schematic cross-sectional view of the first pipeline of the present invention;

[0030] Figure 4 This is a schematic diagram of the outer structure of the desulfurization component of the utility model;

[0031] Figure 5 This is a schematic diagram of the cross-sectional structure of the desulfurization component of the present utility model;

[0032] Figure 6 This is a schematic diagram of the cross-sectional structure of the drying component of the present invention.

[0033] The meaning of each number in the figure is:

[0034] 1. Incineration tower; 10. Feed pipe; 100. Feed valve;

[0035] 2. Collection assembly; 20. Fly ash chamber; 200. Fly ash window; 201. Side cover; 203. Fly ash chute; 21. First duct; 210. Partition; 211. Baffle; 212. Barrier net; 22. Blower;

[0036] 3. Desulfurization components; 30. Desulfurization box; 300. Observation window; 301. Top cover; 302. Liquid inlet pipe; 303. Drain faucet; 304. Demister; 3040. Corrugated plate; 305. Spray pipe; 3050. Nozzle; 306. Circulation pump; 3060. Connecting pipe; 307. Desulfurization liquid;

[0037] 4. Drying assembly; 40. Drying box; 400. Flip cover; 4000. Sealing gasket; 401. Drying sponge; 41. Second pipe; 410. Wind wheel; 411. Drive motor; 42. Air outlet pipe; 420. Air outlet valve; 43. Air inlet pipe; 430. Air inlet valve. DETAILED DESCRIPTION

[0038] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the embodiments described are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative efforts are within the scope of protection of the present invention.

[0039] See also Figures 1-6 , this embodiment provides a technical solution:

[0040] A circulating treatment device for incineration fly ash includes a drying component 4 and a desulfurization component 3 on the right side of the drying component 4. The desulfurization component 3 is provided with a collecting component 2 near the lower left side. The drying component 4 includes a drying box 40 and a drying sponge 401 provided inside the drying box 40. An air inlet duct 43 is provided on the left side of the drying component 4, an air inlet valve 430 is provided above the air inlet duct 43, an incineration tower 1 is provided on the left side of the air inlet duct 43, a feed pipe 10 is provided at the center of the top of the incineration tower 1, and a feed valve 100 is provided on the left side of the feed pipe 10.

[0041] In the present invention, the air inlet duct 43 is welded and fixed to the drying component 4, the air inlet valve 430 is threadedly connected to the air inlet duct 43, the air inlet duct 43 is welded and fixed to the incineration tower 1, the bottom end of the feed pipe 10 is welded and fixed to the top end of the incineration tower 1, and the feed valve 100 is threadedly connected to the feed pipe 10. By setting the air inlet duct 43, the gas dried by the drying component 4 is re-sent into the incineration tower 1. By setting the air inlet valve 430, the user can manually adjust the gas outlet of the air inlet duct 43 by twisting the air inlet valve 430, thereby increasing the use scenarios of the device. By setting the feed pipe 10, it is convenient to add materials to the incineration tower 1. By setting the feed valve 100, the opening size of the feed pipe 10 can be adjusted to reduce heat loss during incineration of the incineration tower 1 and reduce waste of resources.

[0042] Furthermore, a second pipe 41 is provided on the right side of the drying box 40, and a wind wheel 410 is provided on the right side of the inner wall of the second pipe 41. The wind wheel 410 is rotatably connected to the second pipe 41. A drive motor 411 is provided at the front end of the second pipe 41 corresponding to the axon of the wind wheel 410, and the output shaft of the drive motor 411 is coaxially connected to the front end axon of the wind wheel 410.

[0043] In the present invention, the drying box 40 is welded and fixed to the second pipe 41, and the drive motor 411 is fixed to the second pipe 41 by screws. By setting the second pipe 41, the gas treated by the desulfurization component 3 is transported to the drying box 40 for drying. The wind wheel 410 rotates counterclockwise. By manually adjusting the speed of the wind wheel 410, the circulation speed of the gas in the second pipe 41 is adjusted to the left, thereby increasing the circulation efficiency of the device. By setting the drive motor 411, the wind wheel 410 is provided with rotational power.

[0044] It should be noted that a flap 400 is provided on the top of the drying box 40, and an air outlet duct 42 is provided at the center of the top of the flap 400. The flap 400 is rotatably connected to the top of the drying box 40 through a hinge. A sealing gasket 4000 is provided at the bottom of the flap 400. The sealing gasket 4000 is bonded and fixed to the top and the bottom of the flap 400, and the outer wall of the sealing gasket 4000 is tightly fitted with the inner wall of the drying box 40. An air outlet valve 420 is provided on the left side of the air outlet duct 42.

[0045] In the present invention, the air outlet valve 420 is threadedly connected to the air outlet duct 42. By providing a flip cover 400, the drying sponge 401 in the drying box 40 can be easily replaced to avoid the drying sponge 401 working for a long time and reducing the drying effect of the gas. By providing a sealing gasket 4000, the gas sealing inside the drying box 40 is increased. By providing the air outlet duct 42, the completely treated gas is discharged from the device to avoid continuous pressurization of the incineration tower 1 and the occurrence of safety hazards. By adjusting the air outlet valve 420, the air outlet volume of the air outlet duct 42 can be adjusted.

[0046] Specifically, the desulfurization assembly 3 includes a desulfurization box 30 and a spray pipe 305 inside the desulfurization box 30. An observation window 300 is provided at the front end of the desulfurization box 30, and a top cover 301 is provided at the top of the desulfurization box 30. The top cover 301 is rotatably connected to the desulfurization box 30 through a hinge. A liquid inlet pipe 302 is provided near the upper end on the right side of the desulfurization box 30, and a drainage faucet 303 is provided near the bottom end on the right side of the desulfurization box 30.

[0047] In the present utility model, the liquid inlet pipe 302 is welded and fixed to the desulfurization box 30, and the liquid discharge tap 303 is welded and fixed to the desulfurization box 30. By setting the observation window 300, the reaction of the desulfurization liquid 307 in the desulfurization box 30 can be observed in real time, and the desulfurization liquid 307 in the desulfurization box 30 can be replaced in time to avoid affecting the removal effect of sulfur dioxide in the gas. By setting the liquid inlet pipe 302, new desulfurization liquid 307 can be input into the desulfurization box 30 in time, and by setting the liquid discharge tap 303, the reacted desulfurization liquid 307 can be discharged from the desulfurization box 30, and the desulfurization liquid 307 in the desulfurization box 30 can be replaced.

[0048] In addition, a demister 304 is provided above the spray pipe 305 , the desulfurization box 30 is filled with desulfurization liquid 307 , the spray pipe 305 is fixedly connected to the inner wall of the desulfurization box 30 by screws, and a plurality of nozzles 3050 are provided at the bottom of the spray pipe 305 .

[0049] In the present utility model, the top end of the nozzle 3050 is bonded and fixed to the bottom end of the spray pipe 305, and the desulfurization liquid 307 is made by mixing chemical agents such as ammonia water. The ammonia water in the desulfurization liquid 307 can react with sulfur dioxide to generate compounds such as ammonium sulfate or ammonium sulfite, thereby removing sulfur dioxide in the gas and avoiding sulfur dioxide discharge from the device to damage the environment. By setting the nozzle 3050, the desulfurization liquid 307 in the spray pipe 305 is evenly sprayed, increasing the contact area between the desulfurization liquid 307 and the gas, and accelerating the reaction efficiency of sulfur dioxide in the gas.

[0050] In particular, a circulating pump 306 is provided at the water inlet of the spray pipe 305, and a connecting pipe 3060 is provided at the water inlet end of the circulating pump 306. The connecting pipe 3060 passes through the outer wall of the desulfurization box 30 and extends into the desulfurization liquid 307. A plurality of corrugated plates 3040 are provided in the demister 304. The corrugated plates 3040 are distributed at equal intervals, and the corrugated plates 3040 and the demister 304 are an integrally formed structure.

[0051] In the present invention, the outlet of the circulation pump 306 is welded and fixed to the water inlet of the spray pipe 305, the outlet of the connecting pipe 3060 is welded and fixed to the water inlet of the circulation pump 306, and the connecting pipe 3060 is welded and fixed to the desulfurization box 30. By arranging the circulation pump 306 and the spray pipe 305, the desulfurization liquid 307 filled in the desulfurization box 30 is transported to the top of the desulfurization box 30. By arranging the demister 304, when the gas containing the mist flows through the demister 304 at a certain speed, the mist collides with the corrugated plate 3040 due to the inertial impact of the gas and is When the gathered droplets are so large that the gravity generated by themselves exceeds the combined force of the rising force of the gas and the surface tension of the liquid, the droplets are separated from the surface of the corrugated plate 3040 in the demister 304, and the multi-fold structure of the corrugated plate 3040 increases the chance of the mist being captured. The mist that is not removed is captured at the next turn through the same action. This repeated action greatly improves the demisting efficiency, pre-demists the gas flowing into the drying component 4, facilitates the subsequent drying of the drying component 4, and increases the service life of the drying sponge 401 in the drying component 4.

[0052] It should be noted that the collection assembly 2 includes a fly ash bin 20 and a first pipe 21 provided at the upper end of the fly ash bin 20. A side cover 201 is provided on the right side of the fly ash bin 20. The side cover 201 is rotatably connected to the fly ash bin 20 through a hinge. A fly ash window 200 is provided at the front end of the fly ash bin 20. A fly ash trough 203 is provided inside the fly ash bin 20, and the fly ash trough 203 is plugged into the fly ash bin 20.

[0053] In the present invention, by providing a side cover 201, it is convenient to take out the fly ash trough 203 from the fly ash cabin 20, and by providing a fly ash window 200, it is convenient to observe the fly ash collection situation in the fly ash trough 203 in real time, and clean the fly ash in the fly ash trough 203 in time, and the fly ash trough 203 is plugged into the fly ash cabin 20, which makes it easy to take out the fly ash trough 203, and the outer wall of the fly ash trough 203 fits tightly with the inner wall of the fly ash cabin 20, preventing fly ash from falling into the gap between the fly ash trough 203 and the fly ash cabin 20, which increases labor costs.

[0054] More importantly, a partition 210 is provided in the center of the Y-shape inside the first pipe 21, and a number of baffles 211 are provided on both sides of the inverted V-shape on the right side of the first pipe 21. The baffle 211 welded and fixed to the top of the inner wall of the first pipe 21 forms a 90-degree angle with the bottom surface, and the baffle 211 welded and fixed to the bottom end of the inner wall of the first pipe 21 is horizontal and inclined 15 degrees toward the ground. A barrier net 212 is provided at the connection between the first pipe 21, the air inlet pipe 43 and the incineration tower 1.

[0055] Finally, it should be mentioned that a hair dryer 22 is provided at the lower right side of the first pipe 21 .

[0056] In the present invention, the top of the partition 210 is welded and fixed to the top of the inner wall of the first pipe 21, the baffle 211 is welded and fixed to the inner wall of the first pipe 21, the blower 22 is fixed to the right end of the first pipe 21 by screws, and the left end of the first pipe 21 is welded and fixed to the incineration tower 1 near the bottom. The partition 210 is set to block the fly ash in the gas flowing out of the incineration tower 1. Under the action of gravity, large particles of fly ash fall into the fly ash compartment 20 below the first pipe 21, and by setting the baffle 211, the fly ash in the gas further passes over the partition 210.

[0057] When using the incineration fly ash circulation treatment device of this embodiment, the user first welds the bottom end of the feed pipe 10 to the top of the incineration tower 1, screws the feed valve 100 to the feed pipe 10, rotates the fly ash chamber 20 to the side cover 201 through a hinge, plugs the fly ash trough 203 into the fly ash chamber 20, welds the top of the partition 210 to the top of the Y-shaped center of the first pipe 21, welds the baffle 211 to the two sides of the inverted V-shaped first pipe 21, and screws the barrier net 212 to the left side of the first pipe 21. Fixed connection, fix the blower 22 to the first pipe 21 near the bottom opening with screws, weld the bottom end of the first pipe 21 to the top of the fly ash cabin 20, rotate the top cover 301 to the top of the desulfurization box 30 through a hinge, weld the liquid inlet pipe 302 to the right side of the desulfurization box 30 near the middle, weld the drain tap 303 to the right side of the desulfurization box 30 near the bottom, weld the nozzle 3050 to the bottom end of the spray pipe 305, weld the bottom end of the spray pipe 305 to the water outlet of the circulation pump 306, and connect the connecting pipe 303. The front end of 060 is welded and fixed to the water inlet of the circulation pump 306, the rear end of the connecting pipe 3060 is welded and fixed to the front end of the desulfurization box 30, the outer wall of the demister 304 is fixed to the inner wall of the desulfurization box 30 near the top by screws, the desulfurization liquid 307 is filled into the desulfurization box 30, the top of the sealing gasket 4000 is glued and fixed to the bottom of the flip cover 400, the top of the drying box 40 is connected to the flip cover 400 by hinge rotation, the drying sponge 401 is filled into the drying box 40, the wind wheel 410 is connected to the second pipe 41, and the driving motor is connected. The output shaft of the blower 411 is coaxially connected to the front axle of the wind wheel 410. The left side of the second pipe 41 is welded to the right side of the drying box 40. The right side of the second pipe 41 is welded to the left side of the desulfurization box 30. The right side of the air inlet pipe 43 is welded to the left side of the drying box 40. The left side of the air inlet pipe 43 is welded to the right side of the incineration tower 1. The barrier net 212 is fixed to the left end of the air inlet pipe 43 with screws. The bottom end of the air outlet pipe 42 is welded to the top of the drying box 40. The air outlet valve 420 is threadedly connected to the air outlet pipe 42.

[0058] When it is necessary to use the incineration fly ash circulation treatment device, the user first linearly connects the circulation pump 306, the drive motor 411, and the blower 22 to the external power supply, respectively, and turns on the power switches of the circulation pump 306, the drive motor 411, and the blower 22. The circulation pump 306, the drive motor 411, and the blower 22 are powered on and start working, tighten the air outlet valve 420, close the air outlet duct 42, unscrew the air inlet valve 430, and open the air inlet duct 43 to prevent untreated gas from flowing into the outside through the air outlet duct 42 and causing damage to the external environment. Adjust the feed valve 100 according to the size of the material, and adjust The feed pipe 10 is large and small, and the material is fed into the incineration tower 1 through the feed pipe 10 and incinerated by the incineration tower 1. The fly ash generated after the material is incinerated is filtered through the barrier net 212, and impurities are blocked. The fly ash enters the first pipe 21 through the barrier net 212 to prevent impurities from clogging the first pipe 21. The fly ash entering the first pipe 21 is blocked by the partition 210, and large particles of fly ash enter the fly ash cabin 20 through the pipe at the bottom of the first pipe 21 and are collected by the fly ash trough 203. The remaining fine fly ash is blocked by the baffle 211 and falls into the fly ash cabin 20 under the action of gravity. The residual gas enters the desulfurization box 30 through the first pipe 21;

[0059] The circulation pump 306 draws the desulfurization liquid 307 at the bottom of the desulfurization box 30 out to the spray pipe 305. The spray pipe 305 atomizes the desulfurization liquid 307 through the nozzle 3050 at the bottom. The atomized desulfurization liquid 307 reacts with volatile organic substances such as sulfur dioxide in the residual gas entering the desulfurization box 30 to generate compounds such as ammonium sulfate or ammonium sulfite, thereby removing harmful substances in the residual gas. The residual gas passes through the demister 304, and the residual water vapor in the gas passes through the corrugated plate 3040 and condenses and flows back into the desulfurization liquid 307 to be reused. The gas enters the drying box 40 through the second pipe 41. By adjusting the speed of the wind wheel 410 in the second pipe 41, the circulation speed of the gas in the second pipe 41 is adjusted, and the fly ash circulation filtration efficiency is adjusted. The filtered gas is filtered by the drying sponge 401 to further dry the gas. The dried gas passes through the air inlet pipe 43 and flows back into the incineration tower 1 for recycling.

[0060] When the fly ash trough 203 is filled with fly ash, open the side cover 201, remove the filled fly ash trough 203 from the fly ash cabin 20, pour the fly ash in the fly ash trough 203 into the fly ash collection container, reinsert the fly ash trough 203 into the fly ash cabin 20, close the side cover 201, and when the drying sponge 401 is full of water, tighten the air inlet valve 430, close the air inlet duct 43, open the flip cover 400, take out the drying sponge 401 from the drying box 40, put a new drying sponge 401 into the drying box 40, and close the flip cover 401. 00, unscrew the air inlet valve 430, and the air inlet pipe 43 is reopened. When the air pressure in the incineration tower 1 is too high and needs to be reduced, tighten the air inlet valve 430, close the air inlet pipe 43, unscrew the air outlet valve 420, and open the air outlet pipe 42. The treated gas is discharged from the air outlet pipe 42, and the pressure in the incineration tower 1 is reduced. When the pressure is discharged, tighten the air outlet valve 420, close the air outlet pipe 42, unscrew the air inlet valve 430, and open the air inlet pipe 43. The treated gas flows back into the incineration tower 1 for recycling.

Claims

1. A circulating treatment device for incineration fly ash, comprising a drying component (4) and a desulfurization component (3) on the right side of the drying component (4), wherein a collecting component (2) is provided on the left side near the bottom of the desulfurization component (3), characterized in that: The drying assembly (4) includes a drying box (40) and a drying sponge (401) provided inside the drying box (40); a flap (400) is provided on the top of the drying box (40); an air outlet duct (42) is provided at the center of the top of the flap (400); the desulfurization assembly (3) includes a desulfurization box (30) and a spray pipe (305) inside the desulfurization box (30); a demister (304) is provided above the spray pipe (305); the collecting assembly (2) includes a fly ash chamber (20) and a first pipe (21) provided at the upper end of the fly ash chamber (20); a blower (22) is provided below the right side of the first pipe (21).

2. The incineration fly ash circulation treatment device according to claim 1, characterized in that: An air inlet duct (43) is provided on the left side of the drying component (4), an air inlet valve (430) is provided above the air inlet duct (43), an incineration tower (1) is provided on the left side of the air inlet duct (43), a feed pipe (10) is provided at the center of the top of the incineration tower (1), and a feed valve (100) is provided on the left side of the feed pipe (10).

3. The incineration fly ash circulation treatment device according to claim 2, characterized in that: A second pipe (41) is provided on the right side of the drying box (40), a wind wheel (410) is provided on the right side of the inner wall of the second pipe (41), the wind wheel (410) is rotatably connected to the second pipe (41), a driving motor (411) is provided at a position corresponding to the axon of the wind wheel (410) at the front end of the second pipe (41), and an output shaft of the driving motor (411) is coaxially connected to the axon of the front end of the wind wheel (410).

4. The incineration fly ash circulation treatment device according to claim 1, characterized in that: The flip cover (400) is rotatably connected to the top of the drying box (40) via a hinge. A sealing gasket (4000) is provided at the bottom of the flip cover (400). The sealing gasket (4000) is bonded and fixed to the top and the bottom of the flip cover (400), and the outer wall of the sealing gasket (4000) is tightly fitted to the inner wall of the drying box (40). An air outlet valve (420) is provided on the left side of the air outlet duct (42).

5. The incineration fly ash circulation treatment device according to claim 1, characterized in that: An observation window (300) is provided at the front end of the desulfurization box (30), a top cover (301) is provided at the top end of the desulfurization box (30), and the top cover (301) is rotatably connected to the desulfurization box (30) through a hinge. A liquid inlet pipe (302) is provided at the right side of the desulfurization box (30) near the upper end, and a liquid drain tap (303) is provided at the right side of the desulfurization box (30) near the bottom end.

6. The incineration fly ash circulation treatment device according to claim 1, characterized in that: The desulfurization box (30) is filled with desulfurization liquid (307), the spray pipe (305) is fixedly connected to the inner wall of the desulfurization box (30) by screws, and a plurality of nozzles (3050) are provided at the bottom of the spray pipe (305).

7. The incineration fly ash circulation treatment device according to claim 1, characterized in that: A circulating pump (306) is provided at the water inlet of the spray pipe (305), and a connecting pipe (3060) is provided at the water inlet end of the circulating pump (306). The connecting pipe (3060) penetrates the outer wall of the desulfurization box (30) and extends into the desulfurization liquid (307). A plurality of corrugated plates (3040) are provided in the demister (304), and the corrugated plates (3040) are distributed at equal intervals, and the corrugated plates (3040) and the demister (304) are an integrally formed structure.

8. The incineration fly ash circulation treatment device according to claim 1, characterized in that: A side cover (201) is provided on the right side of the fly ash chamber (20), and the side cover (201) is rotatably connected to the fly ash chamber (20) via a hinge. A fly ash window (200) is provided at the front end of the fly ash chamber (20), and a fly ash trough (203) is provided inside the fly ash chamber (20), and the fly ash trough (203) is plugged into and matched with the fly ash chamber (20).

9. The incineration fly ash circulation treatment device according to claim 1, characterized in that: A partition (210) is provided at the center of the Y-shape inside the first pipe (21), and a plurality of baffles (211) are provided on both sides of the inverted V-shape on the right side of the first pipe (21), and the baffle (211) welded and fixed to the top end of the inner wall of the first pipe (21) forms an angle of 90 degrees with the bottom surface, and the baffle (211) welded and fixed to the bottom end of the inner wall of the first pipe (21) is horizontal and inclined 15 degrees toward the ground, and a barrier net (212) is provided at the connection between the first pipe (21), the air inlet pipe (43) and the incineration tower (1).

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