CN220110723U - Hazardous waste incineration tail gas treatment fly ash reflux equipment - Google Patents
Hazardous waste incineration tail gas treatment fly ash reflux equipment Download PDFInfo
- Publication number
- CN220110723U CN220110723U CN202321025283.6U CN202321025283U CN220110723U CN 220110723 U CN220110723 U CN 220110723U CN 202321025283 U CN202321025283 U CN 202321025283U CN 220110723 U CN220110723 U CN 220110723U
- Authority
- CN
- China
- Prior art keywords
- water tank
- tail gas
- pipe
- storehouse
- cooling tube
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 238000004056 waste incineration Methods 0.000 title claims abstract description 17
- 239000002920 hazardous waste Substances 0.000 title claims abstract description 16
- 239000010881 fly ash Substances 0.000 title claims abstract description 11
- 238000010992 reflux Methods 0.000 title description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 238000001816 cooling Methods 0.000 claims abstract description 51
- 229910052751 metal Inorganic materials 0.000 claims abstract description 13
- 239000002184 metal Substances 0.000 claims abstract description 13
- 238000000746 purification Methods 0.000 claims abstract description 12
- 239000002956 ash Substances 0.000 claims description 12
- 230000007246 mechanism Effects 0.000 claims description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 7
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 7
- 239000004571 lime Substances 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 239000000428 dust Substances 0.000 claims description 5
- 239000003570 air Substances 0.000 abstract 2
- 239000012080 ambient air Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 32
- 235000019738 Limestone Nutrition 0.000 description 10
- 239000006028 limestone Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 5
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- FGRBYDKOBBBPOI-UHFFFAOYSA-N 10,10-dioxo-2-[4-(N-phenylanilino)phenyl]thioxanthen-9-one Chemical compound O=C1c2ccccc2S(=O)(=O)c2ccc(cc12)-c1ccc(cc1)N(c1ccccc1)c1ccccc1 FGRBYDKOBBBPOI-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000208125 Nicotiana Species 0.000 description 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a fly ash backflow device for treating hazardous waste incineration tail gas, which particularly relates to the technical field of hazardous waste incineration tail gas treatment devices, and comprises a purification bin, wherein the top of the purification bin is communicated with a deacidification bin, a diversion bin is arranged above the deacidification bin, the top of the diversion bin is communicated with a metal cooling pipe, and the top of the metal cooling pipe is connected with an air inlet; through the use of the heat-conducting pipe, the fan and the guide pipe, which are matched with the air duct, the ambient air can be heated and reused by the heat in the water, and part of the heat contained in the tail gas can also be reused, so that the energy is saved.
Description
Technical Field
The utility model relates to the technical field of hazardous waste incineration waste gas treatment equipment, in particular to hazardous waste incineration tail gas treatment fly ash backflow equipment.
Background
When the hazardous waste is incinerated, the tail gas generated by incineration contains acidic substances such as sulfur dioxide gas, and the like, and the sulfur dioxide and the calcium oxide react to generate calcium sulfate to form slag by adopting a lime dry desulfurization method, so that the tail gas can be effectively deacidified, and the lime dry deacidification device has the advantages of simple flow, low investment, low operation cost and the like, and is widely applied to the field of hazardous waste incineration.
The ash backflow device for treating the hazardous waste incineration tail gas comprises a lime bin and a backflow ash bin, a main device dry deacidification tower and a bag-type dust remover, wherein the publication number of the ash backflow device is CN 212309123U; the outlet of lime bin passes through screw feeder and connects the venturi, and the venturi passes through the high-pressure fan of connection and carries fresh slaked lime to in the dry-type deacidification tower, the backward flow ash spout of dry-type deacidification tower passes through the backward flow ash discharge port of pipeline connection backward flow ash bin and the play tobacco pipe backward flow wind gap of sack cleaner to be equipped with backward flow high-pressure fan on the pipeline, the flue gas outlet of dry-type deacidification tower passes through the pipeline connection sack cleaner, and the ash discharge port of sack cleaner bottom passes through pipeline connection backward flow ash bin, discharges the flying dust of collecting to in the backward flow ash bin. According to the utility model, most slaked lime with deacidification efficiency is refluxed, so that the running cost of enterprises is greatly reduced; meanwhile, the wet deacidification system is not required to be started, the tail gas acidity index can reach the standard, no sewage is generated, and the pollution to the environment is reduced.
The equipment for treating fly ash backflow of the hazardous waste incineration tail gas can treat the tail gas by utilizing the deacidification device in the use process; and the lime dry deacidification device for the dangerous waste incineration tail gas is characterized in that when the lime dry deacidification device is used, the tail gas is directly connected into the device, the device cannot cool the tail gas in advance, the temperature of the tail gas is higher, and the damage to internal parts of the device is easily caused, so that the tail gas is cooled generally by introducing cold water into an annular cooling pipe, but the temperature of water in a water tank is gradually increased along with the continuous use of a water cooling mechanism of the device, so that the cooling effect on the tail gas is reduced, and the practicability is poor.
Disclosure of Invention
The utility model aims to provide a fly ash backflow device for treating hazardous waste incineration tail gas, which aims to solve the problems in the background technology.
In order to solve the technical problems, the utility model provides the following technical scheme: the utility model provides a danger waste incineration tail gas treatment flying ash reflow apparatus, includes the purification storehouse, purification storehouse top intercommunication has the deacidification storehouse, deacidification storehouse top is equipped with the reposition of redundant personnel storehouse, reposition of redundant personnel storehouse top intercommunication has the metal cooling tube, metal cooling tube top is connected with the air intake, and is equipped with the dust screen in the air intake, reposition of redundant personnel storehouse bottom intercommunication has a plurality of shunt tubes, and in the shunt tube lower extreme inserts the deacidification storehouse, be equipped with the limestone layer in the deacidification storehouse, be equipped with the active carbon filter plate in the purification storehouse, purification storehouse one side is equipped with water cooling mechanism, water cooling mechanism includes the water tank, the water tank top is equipped with the water pump, water pump input and output are connected with pipe one and pipe two respectively, metal cooling tube outside cover is equipped with circular conducting strip, circular conducting strip outside cover is equipped with the cooling tube that the screw thread distributes and sets up, cooling tube one end and pipe two-phase intercommunication, the cooling tube lower extreme is linked together with the water tank, the pivot is installed in the water tank rotation, pivot outside symmetry is equipped with a plurality of blades, pivot outside blade the place ahead cover is equipped with local gear.
Further, water cooling body still includes the rack, and the rack is located under the local gear in the water tank, the rack bottom is connected with the water tank inner bottom through the support, water tank inner bottom one side is equipped with two extension boards, be equipped with the slide bar between the extension board, slide bar outside cover is equipped with push pedal and spring, and the spring is located and keep away from support one side, the rack is connected with the push pedal through the connecting rod, bottom extension board one side is equipped with the condenser in the water tank, through the water cooling body who is equipped with, makes it can cool down the tail gas of entering device, avoids the higher inside part of device that leads to of temperature to damage, can cool down water treatment simultaneously, makes its temperature distribution even, can continuously cool down the temperature treatment, avoids after the water uses a period to heat up to influence its cooling effect.
Further, blade top is equipped with the baffle in the water tank, and baffle and water tank inner wall fixed connection, fan top is equipped with the heat pipe that the distribution of a plurality of layers roundabout curve form set up in the water tank, and heat pipe one end is linked together with the cooling tube lower extreme, the heat pipe other end passes the baffle and is located pivot and is close to water tank inner wall one side, and the heat pipe lower extreme is relative with the blade, water tank one side is connected with sufficient fan through the wind channel, and the fan is located the baffle top, wind channel one side is kept away from to the fan is connected with wind gathering cover and connecting pipe, the wind channel top is linked together with purifying bin lower part through the pipe III, thereby the active carbon filter plate is located pipe three lower extreme top to thereby utilize the heat of absorption to heat the air, so as to recycle, resources are saved, also can recycle the tail gas that contains the write heat after the deacidification in the device.
Further, a plurality of blades are distributed and arranged in a circumferential equidistant array mode, the blades are fixedly connected with the rotating shaft, and the racks are meshed with the local gears, so that the rotating shaft is driven to rotate by the water pushing moving blades better.
Further, the upper end of the support is provided with a convex groove, two sides of the rack are provided with symmetrical sliding rails, the sliding rails are matched with the upper end of the support, and two ends of the spring are fixedly connected with the push plate and the support plate respectively so as to guide and support the rack.
Further, the limestone layer is located the shunt tubes outside, a plurality of ventholes have been seted up to shunt tubes lower part to make tail gas evenly distributed in the limestone layer, better with the contact reaction of limestone layer.
Compared with the prior art, the utility model has the following beneficial effects:
1. according to the utility model, through the water cooling mechanism, water in the water tank is extracted and guided into the cooling pipe, so that heat is transferred through the circular heat conducting fin, and then the tail gas is cooled, meanwhile, the water after heat absorption is guided into the heat conducting pipe to heat the surrounding air so as to be reused, meanwhile, the water is guided into the lower part of the partition plate to push the blade to drive the rotating shaft to rotate, so that the local gear drives the rack to push the push plate to squeeze the spring, and when the teeth on the local gear are dislocated with the rack, the push plate is reset under the action of the spring, and is reciprocated in such a way that the push plate continuously pushes the water in the water tank to move, so that the water temperature is uniformly distributed by matching with the condenser, the lower temperature is kept, the cooling treatment can be continuously carried out, and the practicability is higher;
2. according to the utility model, the heat-conducting pipe, the fan and the guide pipe are matched with the air duct, so that the air can be heated by heat in water, the air can be reused, and part of heat contained in the tail gas after the tail gas is sucked and treated is reused, so that energy is saved.
Drawings
The accompanying drawings are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate the utility model and together with the embodiments of the utility model, serve to explain the utility model. In the drawings:
FIG. 1 is a schematic diagram of the structure of the present utility model;
FIG. 2 is an enlarged schematic view of the structure of FIG. 1A according to the present utility model;
FIG. 3 is a schematic view of the structure of the stent of the present utility model;
FIG. 4 is a schematic view of the structure between the shaft and the blades of the present utility model;
in the figure: 1. a purifying bin; 2. deacidifying bin; 3. a diversion bin; 4. a shunt; 5. an activated carbon filter plate; 6. a limestone layer; 7. a metal cooling tube; 8. an air inlet; 9. a water tank; 10. a water pump; 11. a first conduit; 12. a second conduit; 13. round heat conducting fin; 14. a cooling tube; 15. a condenser; 16. a rotating shaft; 17. a blade; 18. a partial gear; 19. a rack; 20. a bracket; 21. a support plate; 22. a slide bar; 23. a push plate; 24. a spring; 25. a heat conduction pipe; 26. a partition plate; 27. a blower; 28. and a third conduit.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
The utility model provides a danger useless incineration tail gas treatment flying ash reflow apparatus as shown in fig. 1-4, including purifying bin 1, purifying bin 1 top intercommunication has deacidification storehouse 2, deacidification storehouse 2 top is equipped with reposition of redundant personnel storehouse 3, reposition of redundant personnel storehouse 3 top intercommunication has metal cooling tube 7, metal cooling tube 7 top is connected with air intake 8, and be equipped with the dust screen in air intake 8, reposition of redundant personnel storehouse 3 bottom intercommunication has a plurality of shunt tubes 4, and shunt tube 4 lower extreme inserts in deacidification storehouse 2, be equipped with limestone layer 6 in deacidification storehouse 2, be equipped with active carbon filter plate 5 in purifying bin 1, purifying bin 1 one side is equipped with water cooling mechanism, water cooling mechanism includes water tank 9, water tank 9 top is equipped with water pump 10, water pump 10 input and output are connected with pipe one 11 and pipe two 12 respectively, metal cooling tube 7 outside cover is equipped with circular heat conducting strip 13, circular heat conducting strip 13 outside cover is equipped with cooling tube 14 that is the screw thread distribution setting, cooling tube 14 one end is linked together with pipe two 12, cooling tube 14 lower extreme is linked together with water tank 9, pivot 16 is installed to the rotation 16 in water tank 9, 16 outside symmetry is equipped with a plurality of blades 17, 16 outside blade 17 place ahead of rotation shaft 18 is equipped with local gear 18.
In this example, water cooling mechanism still includes rack 19, and rack 19 is located in the water tank 9 under the local gear 18, rack 19 bottom is connected with the water tank 9 in through support 20, water tank 9 in-bottom one side is equipped with two extension boards 21, be equipped with slide bar 22 between the extension board 21, slide bar 22 outside cover is equipped with push pedal 23 and spring 24, and spring 24 is located and keeps away from support 20 one side, rack 19 is connected with push pedal 23 through the connecting rod, bottom extension board 21 one side is equipped with condenser 15 in the water tank 9, through the water cooling mechanism that is equipped with, make it can cool down the processing to the tail gas that gets into the device, avoid the higher temperature to lead to the device internals damage, can cool down the processing to the water cooling simultaneously, make its temperature distribution even, can continuously cool down the processing, it influences its cooling effect to heat up after avoiding water to use a period. In this example, the blade 17 top is equipped with baffle 26 in the water tank 9, and baffle 26 and water tank 9 inner wall fixed connection, fan 27 top is equipped with the heat pipe 25 that the distribution of a plurality of layers roundabout curve form set up in the water tank 9, and heat pipe 25 one end is linked together with cooling tube 14 lower extreme, the heat pipe 25 other end passes baffle 26 and is located pivot 16 and is close to water tank 9 inner wall one side, and heat pipe 25 lower extreme is relative with blade 17, fan 27 is connected through the wind channel in water tank 9 one side, and fan 27 is located baffle 26 top, fan 27 is kept away from wind channel one side and is connected with wind gathering cover and connecting pipe, the wind channel top is linked together with purification storehouse 1 lower part through pipe three 28, active carbon filter plate 5 is located pipe three 28 lower extreme top, thereby the air heating is used to the heat of heat that absorbs, so as to recycle, resources are saved, also can be with the tail gas that contains the write heat after the deacidification treatment in the device. In this example, a plurality of blades 17 are distributed in a circumferential equidistant array, and the blades 17 are fixedly connected with the rotating shaft 16, and the rack 19 is meshed with the partial gear 18, so that the rotating shaft 16 is driven to rotate by pushing the blades 17 with water. The upper end of the bracket 20 is provided with a convex groove, two sides of the rack 19 are provided with symmetrical sliding rails, the sliding rails are matched with the upper end of the bracket 20, and two ends of the spring 24 are fixedly connected with the push plate 23 and the support plate 21 respectively so as to guide and support the rack 19. The limestone layer 6 is positioned on the outer side of the shunt tube 4, and the lower part of the shunt tube 4 is provided with a plurality of air outlet holes, so that tail gas is uniformly distributed in the limestone layer 6 and better contacts and reacts with the limestone layer 6.
The working principle of the utility model is as follows: when in use, the tail gas is introduced into the air inlet 8 and the metal cooling pipe 7, and then is respectively introduced into the shunt pipe 4 through the shunt bin 3 and is introduced into the deacidification bin 2, so that the tail gas is in contact reaction with the limestone layer 6, the deacidified tail gas is introduced into the purification bin 1 and is filtered by the activated carbon filter plate 5 to remove peculiar smell, the water pump 10 is started while the tail gas is introduced for treatment, the water pump 10 pumps water by the first guide pipe 11 and is introduced into the cooling pipe 14 through the second guide pipe 12, so that the heat is transferred by the circular heat conducting fin 13 to realize cooling of the tail gas, the water after the heat absorption is introduced into the heat conducting pipe 25 through the cooling pipe 14 to heat air above the partition plate 26 in the water tank 9, then the blade 17 is pushed below the guide plate 26, the blade 17 drives the rotating shaft 16 to rotate, the rotating shaft 16 drives the rack 19 to move by the local gear 18, so that rack 19 removes under support 20 auxiliary action to make rack 19 drive the connecting rod drive push pedal 23 slide along slide bar 22 and extrusion spring 24, after tooth on local gear 18 misplaced with rack 19, push pedal 23 resets under spring 24 effect, so reciprocating, thereby make push pedal 23 constantly move about and promote water, and utilize condenser 15 to cool down water, thereby make temperature distribution even, can cool down it, thereby can continuous cooling treatment, the cooling effect is better, the practicality is stronger, simultaneously can take away the air suction after heating in the water tank 9 through fan 27, thereby the air that contains partial heat after the deacidification treatment in the purification storehouse 1 is drawn into the wind channel to the cooperation pipe three 28 simultaneously can be recycled, resources are saved.
Finally, it should be noted that: the foregoing description is only a preferred embodiment of the present utility model, and the present utility model is not limited thereto, but it is to be understood that modifications and equivalents of some of the technical features described in the foregoing embodiments may be made by those skilled in the art, although the present utility model has been described in detail with reference to the foregoing embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (6)
1. The utility model provides a useless incineration tail gas of danger handles flying ash reflow apparatus, includes purification storehouse (1), purification storehouse (1) top intercommunication has deacidification storehouse (2), deacidification storehouse (2) top is equipped with reposition of redundant personnel storehouse (3), reposition of redundant personnel storehouse (3) top intercommunication has metal cooling tube (7), metal cooling tube (7) top is connected with air intake (8), and is equipped with the dust screen in air intake (8), its characterized in that:
the utility model discloses a deacidification storehouse, including deacidification storehouse (2), water cooling mechanism, water tank (9), water pump (10) are equipped with at water tank (9) top, water pump (10) input and output are connected with pipe one (11) and pipe two (12) respectively, metal cooling tube (7) outside cover is equipped with circular conducting strip (13), circular conducting strip (13) outside cover is equipped with cooling tube (14) that are the screw thread distribution setting, cooling tube (14) one end is linked together with pipe two (12), cooling tube (14) lower extreme is linked together with water tank (9), pivot (16) are installed in water tank (9) internal rotation, pivot (16) outside symmetry is equipped with a plurality of blades (17), blade (17) outside of pivot (16) are equipped with local gear (18) in the place ahead of blade (17).
2. The hazardous waste incineration tail gas treatment fly ash reflow device according to claim 1, wherein: the water cooling mechanism further comprises a rack (19), the rack (19) is located under the partial gear (18) in the water tank (9), the bottom of the rack (19) is connected with the inner bottom of the water tank (9) through a support (20), two support plates (21) are arranged on one side of the inner bottom of the water tank (9), a sliding rod (22) is arranged between the support plates (21), a push plate (23) and a spring (24) are sleeved on the outer side of the sliding rod (22), the spring (24) is located on one side far away from the support (20), the rack (19) is connected with the push plate (23) through a connecting rod, and a condenser (15) is arranged on one side of the support plate (21) on the inner bottom of the water tank (9).
3. The hazardous waste incineration tail gas treatment fly ash reflow device according to claim 1, wherein: the utility model discloses a water tank, including fan (27), cooling tube (14), baffle (26) are equipped with in water tank (9) blade (17) top, and baffle (26) and water tank (9) inner wall fixed connection, fan (27) top is equipped with heat pipe (25) that a plurality of layers roundabout curve form distributes and sets up in water tank (9), and heat pipe (25) one end is linked together with cooling tube (14) lower extreme, the heat pipe (25) other end passes baffle (26) and is located pivot (16) and is close to water tank (9) inner wall one side, and heat pipe (25) lower extreme and blade (17) are relative, water tank (9) one side is connected through the wind channel and is enough fan (27), and fan (27) are located baffle (26) top, wind channel one side is kept away from and is connected with wind gathering cover and connecting pipe, the wind channel top is linked together with purification storehouse (1) lower part through pipe three (28), active carbon filter plate (5) are located pipe three (28) lower extreme top.
4. The hazardous waste incineration tail gas treatment fly ash reflow apparatus according to claim 2, wherein: the blades (17) are distributed in a circumferential equidistant array mode, the blades (17) are fixedly connected with the rotating shaft (16), and the racks (19) are meshed with the local gears (18).
5. The hazardous waste incineration tail gas treatment fly ash reflow apparatus according to claim 2, wherein: the upper end of the support (20) is provided with a convex groove, two sides of the rack (19) are provided with symmetrical sliding rails, the sliding rails are matched with the upper end of the support (20), and two ends of the spring (24) are fixedly connected with the push plate (23) and the support plate (21) respectively.
6. The hazardous waste incineration tail gas treatment fly ash reflow device according to claim 1, wherein: the lime layer (6) is positioned at the outer side of the shunt tube (4), and a plurality of air outlet holes are formed in the lower portion of the shunt tube (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321025283.6U CN220110723U (en) | 2023-05-04 | 2023-05-04 | Hazardous waste incineration tail gas treatment fly ash reflux equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321025283.6U CN220110723U (en) | 2023-05-04 | 2023-05-04 | Hazardous waste incineration tail gas treatment fly ash reflux equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220110723U true CN220110723U (en) | 2023-12-01 |
Family
ID=88915181
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321025283.6U Active CN220110723U (en) | 2023-05-04 | 2023-05-04 | Hazardous waste incineration tail gas treatment fly ash reflux equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220110723U (en) |
-
2023
- 2023-05-04 CN CN202321025283.6U patent/CN220110723U/en active Active
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