Movable sludge drying incineration equipment

By designing a movable sludge drying incineration equipment and using biomass waste as fuel, the problem of the existing sludge incineration equipment being too large and unable to move is solved, and efficient and flexible sludge treatment is achieved, reducing treatment costs.

CN222597745UActive Publication Date: 2025-03-11CENT SOUTHERN CHINA ELECTRIC POWER DESIGN INST CHINA POWER ENG CONSULTING GROUP CORP
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Patent Information

Application Number
CN202323326979.5
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2023-12-07
Publication Date
2025-03-11
Estimated Expiration
2033-12-07

AI Technical Summary

Technical Problem

The existing sludge incineration equipment is too large to move, resulting in high cost of sludge treatment and the inability to dispose of sludge at different locations.

Method used

A movable sludge drying incineration equipment is designed, including drying modules, incineration modules and environmentally friendly modules. It is connected by bolts and pipes to facilitate disassembly and assembly, and uses biomass waste as fuel to improve sludge treatment efficiency.

Benefits of technology

It realizes efficient drying incineration of sludge, reduces the cost of sludge treatment, solves the problem of biomass waste treatment, and the equipment can be quickly disassembled and assembled at different locations, improving the flexibility and efficiency of sludge disposal.

✦ Generated by Eureka AI based on patent content.

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Patent Text Reader

Abstract

The utility model discloses movable sludge drying and incinerating equipment which comprises a drying module, an incinerating module and an environment-friendly module, the drying module, the incineration module and the environmental protection module are connected through bolts and pipelines, the drying module is connected with the environmental protection module, the incineration module is connected with the drying module, and the environmental protection module is connected with the incineration module; the device is high in integration level, and the three modules are small in size, can be transported by a van truck, are relatively independent and are convenient to disassemble, so that the drying incineration device can be used back and forth at different agricultural sludge treatment points; biomass waste such as straw generated in the agricultural production process of villages, towns and villages serves as biomass fuel and is conveyed into the incinerator together with granular sludge to be combusted, and the problem of treatment of the biomass waste generated in the agricultural production process of the villages, towns and villages is solved while the problem of sludge treatment is solved.
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Description

Technical Field

[0001] The utility model belongs to the technical field of sludge treatment, and in particular relates to a movable sludge drying and incineration device. Background Art

[0002] With the improvement of urban sewage treatment plants, the technology in the field of sludge disposal is becoming more and more mature. The sludge treatment market is sinking to towns and villages, but the sludge production in small towns and villages is small and not concentrated. Centralized sludge disposal consumes a lot of transportation costs, so mobile sludge treatment is the development trend of the sludge disposal market in towns and villages. Utility Model Content

[0003] The utility model aims to provide a mobile sludge drying and incineration equipment. Biomass waste can be used as fuel for sludge incineration in the mobile sludge drying and incineration equipment to improve sludge treatment efficiency and solve the problem of biomass waste treatment.

[0004] In order to achieve the above objectives, the technical solution of the utility model is:

[0005] A movable sludge drying and incineration equipment comprises a drying module, an incineration module and an environmental protection module; the drying module, the incineration module and the environmental protection module are connected by bolts and pipelines, the drying module is connected to the environmental protection module, the incineration module is connected to the drying module, and the environmental protection module is connected to the incineration module.

[0006] Furthermore, the drying module includes a sludge dryer, a first cyclone separator, a dust collector, a dry sludge bin and a mixing bin; the sludge dryer is connected to the inlet of the first cyclone separator, the solid particle discharge port of the first cyclone separator is connected to the feed port of the dry sludge bin, the discharge port of the dry sludge bin is connected to the feed port of the mixing bin, and the discharge port of the mixing bin is connected to the incineration module; the gas discharge port of the first cyclone separator is connected to the air inlet of the dust collector.

[0007] Furthermore, an external wet sludge feed port is provided on one surface of the sludge dryer, the wet sludge feed port is connected with one end of a spiral conveying device, the other end of the spiral conveying device is connected with an external sludge bin, and the wet sludge in the external sludge bin enters the sludge dryer through the wet sludge feed port through the spiral conveying device; a dry gas inlet is provided on the sludge dryer, the wet sludge feed port is arranged on the top surface of the sludge dryer, the dry gas inlet is arranged on the bottom surface or the side surface of the sludge dryer, the dry gas inlet is lower than the wet sludge feed port, and the dry gas inlet is located close to the wet sludge feed port.

[0008] Furthermore, the discharge port of the sludge dryer is connected to the inlet of the first cyclone separator, and the sludge that becomes granular in the sludge dryer enters the first cyclone separator together with the air, and the first cyclone separator separates the air and the solid particles.

[0009] Furthermore, the outlet of the first cyclone separator includes a gas outlet and a solid particle outlet. The solid particle outlet of the first cyclone separator is connected to the feed inlet of the dry sludge bin, the discharge port of the dry sludge bin is connected to the feed inlet of the mixing bin, and the discharge port of the mixing bin is connected to the incineration module, specifically, to the fuel feed inlet of the incinerator included in the incineration module.

[0010] Furthermore, the gas outlet of the first cyclone separator is connected to the air inlet of the dust collector, the gas separated from the first cyclone separator enters the dust collector for purification, and the exhaust port of the dust collector is connected to the environmental protection module.

[0011] Furthermore, the incineration module includes an incinerator, a second cyclone separator, and a fan. The incinerator is provided with a fuel feed port and a smoke exhaust pipe. The mixing bin outlet is connected to the fuel feed port, and the smoke exhaust pipe is connected to the inlet of the second cyclone separator; the second cyclone separator includes a gas outlet and a solid particle outlet. The gas outlet of the second cyclone separator is connected to the dry gas inlet on the sludge dryer; the solid particle outlet of the second cyclone separator is connected to the slag bin at the bottom of the incinerator furnace through a pipeline.

[0012] Furthermore, the fan is connected to the incinerator through a connecting pipe and bolts, and air for combustion is transported into the incinerator through the fan.

[0013] Furthermore, the environmental protection module includes an alkali washing tower, an oxidation tower, a UV photolysis tower, a tail exhaust fan, and a discharge tower. The exhaust port of the dust collector is connected to the air inlet of the alkali washing tower, the air outlet of the alkali washing tower is connected to the air inlet of the oxidation tower, the air outlet of the oxidation tower is connected to the air inlet of the UV photolysis tower, the air outlet of the UV photolysis tower is connected to the air inlet of the tail exhaust fan, and the air outlet of the tail exhaust fan is respectively connected to the inner cavity of the incinerator and the discharge tower. Specifically, a three-way pipe with one outlet and two inlets is set at the air outlet of the tail exhaust fan, so that the air outlet of the tail exhaust fan is connected to the inner cavity of the incinerator and the discharge tower.

[0014] Furthermore, the sludge drying and incineration equipment also includes a power distribution control area, and the power distribution cabinet of the power distribution control area is installed on the upper left side of the tail exhaust fan inside the environmental protection module. The power distribution control area is electrically connected to the drying module, incineration module and environmental protection module.

[0015] The beneficial effects of the utility model are:

[0016] 1. The utility model modularizes the three parts of the sludge drying and incineration equipment, namely, drying, incineration and environmental protection, and manufactures each module to a size that can be transported by a box truck. The pipes between the modules are connected by bolts for easy disassembly, thereby effectively solving the problem that the existing sludge incineration equipment is too large and can only be fixedly installed in the factory building, and the working location cannot be changed. The sludge needs to be transported to the site, and the sludge treatment production cost is high. The three modules of the utility model are connected by bolts and pipes, which can ensure the convenience of module assembly and disassembly, and improve the efficiency of sludge disposal at different locations.

[0017] 2. The equipment of the utility model has high integration, and the three modules are small in size and can be transported by a van. The three modules are relatively independent and easy to disassemble, and can be used back and forth at different agricultural sludge treatment points.

[0018] 3. In the utility model, biomass wastes such as straw, rice husk and bark generated in the agricultural production process in towns and villages are used as biomass fuels and transported to the incinerator together with granular sludge for combustion. On the one hand, the problem of handling biomass wastes generated in the agricultural production process in towns and villages is solved while solving the sludge problem. On the other hand, the biomass wastes are used as fuel for sludge combustion treatment, which makes the sludge combustion treatment more complete. At the same time, the flue gas generated by the combustion of the biomass waste enters the sludge dryer and is used as fluidizing air for drying and fluidizing the wet sludge, thereby realizing the recycling of biomass wastes, making the treatment of biomass wastes more environmentally friendly, and saving the cost of separately disposing of biomass wastes.

[0019] 4. In the utility model, the discharge end of the sludge dryer is connected to the feed end of the incinerator, and the granular sludge output from the sludge dryer is fed into the incinerator for combustion, so that the sludge treatment is more complete; the smoke exhaust pipe of the incinerator is connected to the inner cavity of the sludge dryer, and the combustion flue gas is used to provide heat for the dryer. The gas outlet end of the emission tower is connected to the furnace cavity of the incinerator, and combustion-supporting gas can be transported to the incinerator, thereby realizing the recycling of the exhaust gas during the sludge drying and incineration process, making the sludge treatment method of the utility model environmentally friendly and energy-saving. BRIEF DESCRIPTION OF THE DRAWINGS

[0020] Figure 1 It is an overall schematic diagram of the utility model.

[0021] Figure 2 It is a schematic diagram of the drying module of the utility model.

[0022] Figure 3 It is a schematic diagram of the incineration module of the utility model.

[0023] Figure 4 It is a schematic diagram of the environmental protection module of the utility model.

[0024] Among them: drying module 1; sludge dryer 11; wet sludge feed port 111; dry gas inlet 112; first cyclone separator 12; dust collector 13; dry sludge bin 14; mixing bin 15; incineration module 2; environmental protection module 3; incineration module 2; incinerator 21; second cyclone separator 22; fan 23; fuel feed port 211; exhaust pipe 212; slag bin 213; environmental protection module 3; alkali washing tower 31; alkali liquid tank 311; alkali washing tower dosing pump 312; oxidation tower 32; reagent box 321; oxidation tower dosing pump 322; UV photolysis tower 33; circulating water tank 331; circulating water pump 332; tail exhaust fan 34; discharge tower 35; external sludge bin 4; power distribution control area 5; screw conveyor 6. DETAILED DESCRIPTION

[0025] In order to make the purpose, technical solution and advantages of the utility model clearer, the utility model is further described below with reference to the accompanying drawings.

[0026] like Figure 1 As shown, the utility model movable sludge drying and incineration equipment includes a drying module 1, an incineration module 2 and an environmental protection module 3. The drying module 1 is connected to the environmental protection module 3, the incineration module 2 is connected to the drying module 1, and the environmental protection module 3 is connected to the incineration module 2; the connection between the three modules and the connection of each component inside each module are all connected by bolts and pipes to ensure the convenience of module assembly and disassembly, and improve the efficiency of sludge drying and incineration equipment in disposing of agricultural solid waste at different locations; the specifications of each module are within 3*3*13m, which is convenient for transportation by van.

[0027] like Figure 1 , Figure 2 and Figure 3 As shown, the drying module 1 includes a sludge dryer 11 , a first cyclone separator 12 , a dust collector 13 , a dry sludge bin 14 and a mixing bin 15 .

[0028] An external wet sludge feed port 111 is provided on one surface of the sludge dryer 11, and the wet sludge feed port 111 is connected to one end of the screw conveying device 6, and the other end of the screw conveying device 6 is connected to the external sludge bin 4. Through the screw conveying device 6, the wet sludge in the external sludge bin 4 enters the sludge dryer 11 through the wet sludge feed port 111.

[0029] The sludge dryer 11 is provided with a drying gas inlet 112. If the wet sludge feed port 111 is provided on the top surface of the sludge dryer 11, the drying gas inlet 112 may be provided on the bottom surface or the side surface of the sludge dryer 11, so that the drying gas inlet 112 is lower than the wet sludge feed port 111, and the drying gas inlet 112 is as close to the wet sludge feed port 111 as possible, so that the drying gas is blown toward the wet sludge entering from the wet sludge feed port 111, so that the wet sludge is fluidized and dried. After the wet sludge enters the dryer, it is quickly dried and broken into particles by the fluidizing air with a temperature of 400-500°C within 3-5 seconds.

[0030] The discharge port of the sludge dryer 11 is connected to the inlet of the first cyclone separator 12. The sludge that has become granular in the sludge dryer 11 enters the first cyclone separator 12 together with the air. The cyclone separator can separate the air and the solid particles.

[0031] The outlet of the first cyclone separator 12 includes a gas outlet and a solid particle outlet. The solid particle outlet of the first cyclone separator 12 is connected to the feed port of the dry sludge bin 14. The discharge port of the dry sludge bin 14 is connected to the feed port of the mixing bin 15. The discharge port of the mixing bin 15 is connected to the incineration module 2, specifically, the discharge port of the mixing bin 15 is connected to the fuel feed port 211 of the incinerator 21 included in the incineration module 2.

[0032] The gas outlet of the first cyclone separator 12 is connected to the air inlet of the dust collector 13, and the gas separated from the first cyclone separator 12 enters the dust collector 13 for purification. The exhaust port of the dust collector 13 is connected to the environmental protection module 3, specifically, the alkali washing tower 31 included in the environmental protection module 3.

[0033] like Figure 3 As shown, the incineration module 2 includes an incinerator 21, a second cyclone separator 22, and a fan 23. The incinerator 21 is provided with a fuel feed port 211 and a smoke exhaust pipe 212. The discharge port of the mixing bin 15 is connected to the fuel feed port 211, and the smoke exhaust pipe 212 is connected to the inlet of the second cyclone separator 22; the second cyclone separator 22 includes a gas discharge port and a solid particle discharge port. The second cyclone separator 22 can separate the gas and the solid particles. The gas discharge port of the second cyclone separator 22 is connected to the sludge dryer 11. The drying gas inlet 112 is connected through a connecting pipe. As a preferred embodiment, a flue gas circulation fan can be set on the connecting pipe between the gas outlet of the second cyclone separator 22 and the drying gas inlet 112 on the sludge dryer 11. The flue gas circulation fan can increase the speed of the gas entering the dryer 11 to 40m / s to improve the fluidization efficiency of the sludge in the dryer 11; the solid particle outlet of the second cyclone separator 22 is connected to the slag bin 213 at the bottom of the furnace of the incinerator 21 through a pipeline.

[0034] The environmental protection module 3 includes an alkali washing tower 31, an oxidation tower 32, a UV photolysis tower 33, a tail exhaust fan 34, and a discharge tower 35. The exhaust port of the dust collector 13 is connected to the air inlet of the alkali washing tower 31, the air outlet of the alkali washing tower 31 is connected to the air inlet of the oxidation tower 32, the air outlet of the oxidation tower 32 is connected to the air inlet of the UV photolysis tower 33, the air outlet of the UV photolysis tower 33 is connected to the air inlet of the tail exhaust fan 34, and the air outlet of the tail exhaust fan 34 is respectively connected to the inner cavity of the incinerator 21 and the discharge tower 35. Specifically, a three-way pipe with one outlet and two inlets can be set at the air outlet of the tail exhaust fan 34, so that the air outlet of the tail exhaust fan 34 is connected to the inner cavity of the incinerator 21 and the discharge tower 35.

[0035] The alkali washing tower 31 includes an alkali liquid tank 311 and an alkali washing tower dosing pump 312 for supporting use; the oxidation tower 32 includes an agent box 321 and an oxidation tower dosing pump 322 for supporting use; the UV photolysis tower 33 includes a circulating water tank 331 and a circulating water pump 332 for supporting use.

[0036] The working process of the mobile sludge drying and incineration equipment of the utility model is as follows:

[0037] The wet sludge in the external sludge bin 4 is transported by a screw conveyor and enters the sludge dryer 11 from the external sludge bin 4 along the external wet sludge feed port 111. The high-temperature gas transported from the drying gas inlet 112 serves as a fluidized drying medium for the wet sludge. Under the action of the high-temperature gas, the wet sludge is quickly dried and broken into granules by the fluidizing wind during the process of falling in the sludge dryer 11. The granular sludge enters the first cyclone separator 12 under the action of the fluidizing wind, and the first cyclone separator 12 separates the granular sludge and the gas.

[0038] The solid particles separated by the first cyclone separator 12 enter the dry sludge bin 14 through the screw conveying device, and then the solid particles enter the mixing bin 15 through the screw conveying device, and the solid particles are mixed with the biomass particle fuel in the mixing bin 15. The solid particles and the biomass particle fuel are discharged from the discharge port of the mixing bin 15 together, and then enter the incinerator 21 through the fuel feed port 211 through the screw conveying device for combustion. The sludge is fully burned in the incinerator 21 to generate high-temperature flue gas containing solid particles. The high-temperature flue gas containing solid particles enters the second cyclone separator 22 along the exhaust pipe 212. The second cyclone separator 22 separates the high-temperature flue gas containing solid particles into solid particles and high-temperature flue gas. The solid particles enter the slag bin 213 at the bottom of the furnace of the incinerator 21 along the pipeline from the solid particle discharge port of the second cyclone separator 22. The slag in the slag bin 213 can be collected regularly, and the slag can be used as a construction resource such as road construction. The high-temperature flue gas discharged from the exhaust port of the second cyclone separator 22 enters the sludge dryer 11 from the dry gas inlet 112. The high-temperature flue gas separated by the second cyclone separator 22 can provide a drying heat source for the fluidized drying of wet sludge in the sludge dryer 11, so that the temperature in the sludge dryer 11 is maintained at 400-500℃.

[0039] The gas separated by the first cyclone separator 12 is discharged from the gas outlet of the first cyclone separator 12 and first enters the dust collector 13. The dust collector 13 is connected to the alkali washing tower 31. The gas discharged from the dust collector 13 flows into the alkali washing tower 31, the oxidation tower 32, and the UV photolysis tower 33 in sequence for further purification. The purified gas enters the tail exhaust fan 34 from the UV photolysis tower 33. Part of the gas discharged from the tail exhaust fan 34 enters the incinerator 21 to be used as the combustion air required for combustion, and part of the gas enters the emission tower 35 and then is discharged from the emission tower 35 into the atmosphere.

[0040] The utility model also provides a power distribution control area 5, and the power distribution cabinet of the power distribution control area 5 can be installed inside the environmental protection module 3. The power distribution control area 5 is electrically connected to the drying module 1, the incineration module 2 and the environmental protection module 3 to provide power for the drying module 1, the incineration module 2 and the environmental protection module 3.

[0041] As a preferred embodiment of the utility model, a fan 23 can be provided, which is connected to the incinerator 21 through a connecting pipe and bolts, and the fan 23 delivers combustion-supporting air into the incinerator 21 to make the fuel in the incinerator 21 burn more fully.

[0042] In addition to the granular sludge, the mixing bin 15 also contains biomass fuel, which may be straw, rice husk and bark, and may be cut into small pieces or crushed into granules for use. As a preferred embodiment, a screw conveyor may be provided between the solid particle outlet of the first cyclone separator 12 and the inlet of the dry sludge bin 14, between the outlet of the dry sludge bin 14 and the inlet of the mixing bin 15, and between the outlet of the mixing bin 15 and the fuel feed port 211. The screw conveyor is used to realize the connection between the solid particle outlet of the first cyclone separator 12 and the inlet of the dry sludge bin 14, the connection between the outlet of the dry sludge bin 14 and the inlet of the mixing bin 15, and the connection between the outlet of the mixing bin 15 and the fuel feed port 211, so as to facilitate the delivery of solid sludge particles and biomass fuel into the incinerator 21 for combustion.

[0043] As a preferred embodiment of the present invention, a separate feed port for external biomass fuels such as straw, rice husk and bark can be provided on the incinerator 21 for the input of external biomass sources.

[0044] In the utility model, the drying module 1, the incineration module 2 and the environmental protection module 3 are all reserved for solid waste feed ports and waste gas and wastewater discharge ports. Each module is connected to a fixing bracket for the installation module and the modules are connected with bolts to facilitate disassembly and reassembly.

[0045] Finally, it should be noted that the contents not described in detail in this specification belong to the prior art known to professional and technical personnel in this field. The above description is only the preferred embodiment of the utility model and is not used to limit the utility model. Although the utility model is described in detail with reference to the above embodiments, for those skilled in the art, they can still modify the technical solutions recorded in the above embodiments, or replace some of the technical features therein with equivalents. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the utility model shall be included in the protection scope of the utility model.

Claims

1. A movable sludge drying and incineration equipment, characterized in that: The invention comprises a drying module (1), an incineration module (2) and an environmental protection module (3); the drying module (1), the incineration module (2) and the environmental protection module (3) are connected via bolts and pipes; the drying module (1) is connected to the environmental protection module, the incineration module (2) is connected to the drying module (1), and the environmental protection module (3) is connected to the incineration module (2).

2. The movable sludge drying and incineration equipment according to claim 1 is characterized in that: The drying module (1) comprises a sludge dryer (11), a first cyclone separator (12), a dust collector (13), a dry sludge bin (14) and a mixing bin (15); the sludge dryer (11) is connected to the inlet of the first cyclone separator (12), the solid particle discharge port of the first cyclone separator (12) is connected to the feed port of the dry sludge bin (14), the discharge port of the dry sludge bin (14) is connected to the feed port of the mixing bin (15), and the discharge port of the mixing bin (15) is connected to the incineration module (2); the gas discharge port of the first cyclone separator (12) is connected to the gas inlet of the dust collector (13).

3. The movable sludge drying and incineration equipment according to claim 2 is characterized in that: The sludge dryer (11) is provided with an external wet sludge feed port (111) on one surface thereof, the wet sludge feed port (111) is communicated with one end of a screw conveying device (6), the other end of the screw conveying device (6) is communicated with an external sludge bin (4), and through the screw conveying device (6), wet sludge in the external sludge bin (4) enters the sludge dryer (11) through the wet sludge feed port (111); the sludge dryer (11) is provided with a dry gas inlet (112), the wet sludge feed port (111) is arranged on the top surface of the sludge dryer (11), the dry gas inlet (112) is arranged on the bottom surface or the side surface of the sludge dryer (11), the dry gas inlet (112) is lower than the wet sludge feed port (111), and the dry gas inlet (112) is located close to the wet sludge feed port (111).

4. The movable sludge drying and incineration equipment according to claim 2 is characterized in that: The discharge port of the sludge dryer (11) is connected to the inlet of the first cyclone separator (12), and the sludge that becomes granular in the sludge dryer (11) enters the first cyclone separator (12) together with the air, and the first cyclone separator (12) separates the air and the solid particles.

5. The movable sludge drying and incineration equipment according to claim 2 is characterized in that: The outlet of the first cyclone separator (12) comprises a gas outlet and a solid particle outlet, the solid particle outlet of the first cyclone separator (12) is connected to the feed inlet of the dry sludge bin (14), the outlet of the dry sludge bin (14) is connected to the feed inlet of the mixing bin (15), and the outlet of the mixing bin (15) is connected to the incineration module (2), specifically, to the fuel feed inlet (211) of the incinerator (21) included in the incineration module (2).

6. The movable sludge drying and incineration equipment according to claim 2 is characterized in that: The gas outlet of the first cyclone separator (12) is connected to the air inlet of the dust collector (13), the gas separated from the first cyclone separator (12) enters the dust collector (13) for purification, and the exhaust port of the dust collector (13) is connected to the environmental protection module (3).

7. The movable sludge drying and incineration equipment according to claim 1 is characterized in that: The incineration module (2) comprises an incinerator (21), a second cyclone separator (22), and a fan (23); the incinerator (21) is provided with a fuel feed port (211) and a smoke exhaust pipe (212); the discharge port of the mixing bin (15) is connected to the fuel feed port (211); the smoke exhaust pipe (212) is connected to the inlet of the second cyclone separator (22); the second cyclone separator (22) comprises a gas discharge port and a solid particle discharge port; the gas discharge port of the second cyclone separator (22) is connected to the dry gas inlet (112) on the sludge dryer (11); the solid particle discharge port of the second cyclone separator (22) is connected to the slag bin (213) at the bottom of the furnace of the incinerator (21) through a pipeline.

8. The movable sludge drying and incineration equipment according to claim 7 is characterized in that: The fan (23) is connected to the incinerator (21) through a connecting pipe and bolts, and air for combustion support is transported into the incinerator (21) through the fan (23).

9. The movable sludge drying and incineration equipment according to claim 1 is characterized in that: The environmental protection module (3) comprises an alkali washing tower (31), an oxidation tower (32), a UV photolysis tower (33), a tail exhaust fan (34), and a discharge tower (35); the exhaust port of the dust collector (13) is connected to the air inlet of the alkali washing tower (31); the air outlet of the alkali washing tower (31) is connected to the air inlet of the oxidation tower (32); the air outlet of the oxidation tower (32) is connected to the air inlet of the UV photolysis tower (33); the air outlet of the UV photolysis tower (33) is connected to the air inlet of the tail exhaust fan (34); the air outlet of the tail exhaust fan (34) is respectively connected to the inner cavity of the incinerator (21) and the discharge tower (35); specifically, a three-way pipeline with one outlet and two inlets is arranged at the air outlet of the tail exhaust fan (34), so that the air outlet of the tail exhaust fan (34) is connected to the inner cavity of the incinerator (21) and the discharge tower (35).