CN218590241U - Ton bag flying dust dissolves slurrying system - Google Patents
Ton bag flying dust dissolves slurrying system Download PDFInfo
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- CN218590241U CN218590241U CN202221242013.6U CN202221242013U CN218590241U CN 218590241 U CN218590241 U CN 218590241U CN 202221242013 U CN202221242013 U CN 202221242013U CN 218590241 U CN218590241 U CN 218590241U
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Abstract
The utility model provides a be applied to flying dust technical field's ton bag flying dust and dissolve slurrying system, ton bag flying dust dissolve slurrying system include emergent pond (1), flying dust waste liquid supply part (2) intercommunication ton bag flying dust dissolves slurrying part (3), emergent pond (1) intercommunication ton bag flying dust dissolves slurrying part (3), ton bag flying dust supply part (4) intercommunication ton bag flying dust dissolves slurrying jar (3), ton bag flying dust dissolves slurrying part (3) intercommunication flying dust washing dechlorination part (5), filtrate pipeline (7) intercommunication ton bag flying dust of anterior segment flying dust washing dechlorination part (6) dissolve slurrying part (3), ton bag flying dust dissolve slurrying system, simple structure optimizes through equipment and the technology to ton bag flying dust dissolution slurrying, effectively utilizes the production process waste liquid, realizes that ton bag flying dust dissolves slurrying, reduces impurity to dissolving ejection of compact process influence, improves whole efficiency and processing reliability.
Description
Technical Field
The utility model belongs to the technical field of the flying dust, more specifically say, relate to a ton bag flying dust dissolves slurrying system.
Background
In the process of co-processing the fly ash generated by burning the household garbage, one part of the fly ash is ton bags of fly ash, which is accumulated by an ash producing unit, and because the fly ash has high water content, long storage time, agglomeration and more impurities, the problems of low dissolving and pulping speed, bag breaking, blockage of an outlet by the impurities and the like exist in the fly ash washing and dechlorinating process. Ton bag fly ash dissolving and pulping systems are generally based on a complete fly ash disposal production line. In a fly ash disposal workshop, factors such as leakage, flushing, on-site sanitation and the like can generate waste liquid, the waste liquid is gathered in a pit and then pumped into an emergency pool, the concentration of the part of waste water is low in the actual operation process, and finally the waste water is subjected to evaporation salt making treatment after passing through the emergency pool, so that the workload of evaporation salt making is increased invisibly, and the water-cement ratio of fly ash disposal is increased indirectly.
SUMMERY OF THE UTILITY MODEL
The utility model discloses the technical problem that will solve is: aiming at the defects of the prior art, the ton bag fly ash dissolving and pulping system is simple in structure, equipment and process for dissolving and pulping ton bag fly ash are optimized, waste liquid in the production process is effectively utilized, high-efficiency dissolving and pulping of ton bag fly ash is realized, the influence of impurities on the dissolving and discharging process is reduced, and the overall efficiency and the treatment reliability are improved.
To solve the technical problem, the utility model discloses the technical scheme who takes is:
the utility model relates to a ton bag flying dust dissolves slurrying system, ton bag flying dust dissolve slurrying system include emergent pond, flying dust waste liquid supply part intercommunication ton bag flying dust dissolves slurrying part, emergent pond intercommunication ton bag flying dust dissolves slurrying part, ton bag flying dust supply part intercommunication ton bag flying dust dissolves slurrying part, ton bag flying dust dissolves slurrying part intercommunication flying dust washing dechlorination part, the filtrating pipeline intercommunication ton bag flying dust that anterior segment flying dust washed dechlorination part dissolves slurrying part.
The emergency water tank is communicated with the ton bag fly ash dissolving and pulping component through a pipeline II, and the ton bag fly ash dissolving and pulping component is communicated with the fly ash washing and dechlorinating component through a pipeline III.
The fly ash waste liquid supply component is communicated with the emergency pool through a pipeline I.
The ton bag fly ash dissolving and pulping component comprises a ton bag fly ash dissolving and pulping tank, and the ton bag fly ash supply component comprises a ton bag fly ash sealing and bag breaking component and a vibrating screen.
The ton bag fly ash dissolving and pulping tank comprises a dissolving tank body, wherein a stirrer is arranged in the dissolving tank body.
The ton bag fly ash sealed bag breaking component comprises a sealed bag breaking component box body, an electric switch door is arranged on the sealed bag breaking component box body, a ton bag fly ash support is arranged in the sealed bag breaking component box body, a vibrating screen is arranged on the lower portion of the sealed bag breaking component box body, and the sealed bag breaking component box body is communicated with the upper portion of a dissolving tank body through a lower ash funnel.
The lower part of the dissolving tank body is provided with a high-pressure flushing interface.
The lower part of the dissolving tank body is provided with a discharge hole.
And the ash discharging funnel is provided with magnetic separation.
Adopt the technical scheme of the utility model, can obtain following beneficial effect:
ton bag flying dust dissolve slurrying system, to not enough among the prior art, provide brand-new improvement scheme. When the ton bag fly ash dissolving and pulping system operates, on one hand, various waste liquids generated in the fly ash disposal process are collected into an emergency water tank and are conveyed to a ton bag fly ash dissolving and pulping component through the emergency water tank; on the other hand, production filtrate produced in the dechlorination process of the front-section fly ash washing dechlorination component is adopted; when the amount of the production waste liquid is insufficient, the filtrate is used as make-up water. In the pulping and dissolving process of the ton bag fly ash, according to factors such as the water content, the agglomeration degree and the like of the ton bag fly ash, the water-cement ratio is maintained to be 2-5: 1; when the ton bag fly ash dissolving and pulping system works, the water-cement ratio is quantitatively controlled, namely the water amount is added by liquid level control according to the number of ton bag ash dissolved in each tank according to a plan. If 2 tons of ash are planned to be dissolved, the ratio of water to ash is 3:1, dissolving the water in the tank. In the practical process, the water-cement ratio is corrected according to characteristic factors such as water content, bulk density and the like of different ash production unit ton packages. Ton bag flying dust dissolve slurrying system, simple structure optimizes through equipment and the technology to ton bag flying dust dissolve slurrying, effectively utilizes the production process waste liquid, realizes that ton bag flying dust is high-efficient to dissolve slurrying, reduces impurity to dissolving ejection of compact process influence, improves whole efficiency and handles the reliability.
Drawings
The contents of the description and the references in the drawings are briefly described as follows:
FIG. 1 is a schematic structural diagram of a ton bag fly ash dissolving and pulping system according to the present invention;
fig. 2 is a schematic view of a connection structure between a ton bag fly ash dissolving pulping tank and a ton bag fly ash sealing bag breaking component of the ton bag fly ash dissolving pulping system according to the present invention;
fig. 3 is a schematic structural diagram of a ton bag fly ash sealing and bag breaking component of the ton bag fly ash dissolving and pulping system according to the present invention;
in the drawings, the reference numbers are respectively: 1. an emergency pool; 2. a fly ash waste liquid supply part; 3. a ton bag fly ash dissolving and pulping component; 4. a ton bag fly ash supply component; 5. a fly ash washing dechlorination component; 6. a front-section fly ash washing dechlorination component; 7. a filtrate delivery line; 8. a pipeline I; 9. a pipeline II; 10. a pipeline III; 11. a ton bag fly ash dissolving pulping tank; 12. sealing the ton bag fly ash to break the bag; 13. vibrating screen; 14. a dissolving tank body; 15. A stirrer; 16. sealing the bag breaking component box body; 17. electrically opening and closing the door; 18. fly ash support of ton bags; 19. A dust discharging funnel; 20. a high pressure flush port; 21. a discharge port; 22. magnetic separation; 23. a gate valve; 24. an exhaust port; 25. a water inlet; 26. a slope.
Detailed Description
The following description of the embodiments of the present invention, with reference to the accompanying drawings, will be further described in detail, such as the shapes and structures of the components, the mutual positions and connections between the components, the functions and operation principles of the components, etc. according to the embodiments of the present invention:
as shown in the attached drawings 1-3, the utility model relates to a ton bag flying dust dissolves slurrying system, ton bag flying dust dissolve slurrying system include emergent pond 1, flying dust waste liquid supply part 2 communicates ton bag flying dust dissolve slurrying part 3, emergent pond 1 communicates ton bag flying dust dissolve slurrying part 3, ton bag flying dust supply part 4 communicates ton bag flying dust dissolve slurrying part 3, ton bag flying dust dissolve slurrying part 3 communicates flying dust washing dechlorination part 5, anterior segment flying dust washing dechlorination part 6's filtrate conveying line 7 communicates ton bag flying dust dissolve slurrying part 3. The structure provides a brand-new improvement scheme aiming at the defects in the prior art. When the ton bag fly ash dissolving and pulping system operates, on one hand, various waste liquids generated in the fly ash disposal process are collected into an emergency water tank and are conveyed to the ton bag fly ash dissolving and pulping component 3 through the emergency water tank; on the other hand, production filtrate produced in the dechlorination process of the front-section fly ash washing dechlorination component 6 is adopted; when the amount of the production waste liquid is insufficient, the filtrate is used as make-up water. In the pulping and dissolving process of the ton bag fly ash, according to factors such as the water content, the agglomeration degree and the like of the ton bag fly ash, the water-cement ratio is maintained to be 2-5: 1; when the ton bag fly ash dissolving and pulping system works, the water-cement ratio is quantitatively controlled, namely the water amount is added by liquid level control according to the number of ton bag ash dissolved in each tank according to a plan. If 2 tons of ash are planned to be dissolved, the ratio of water to ash is 3:1, dissolving the water in the tank by 6 square. In the practical process, the water-cement ratio is corrected according to the characteristic factors such as water content, bulk density and the like of different ash production unit ton packages. Ton bag flying dust dissolve slurrying system, simple structure optimizes through equipment and the technology to ton bag flying dust dissolve slurrying, utilizes the production process waste liquid, realizes that ton bag flying dust is high-efficient to dissolve slurrying, reduces impurity to dissolving ejection of compact process influence, improves whole efficiency and handles the reliability.
The emergency water tank 1 is communicated with a ton bag fly ash dissolving and pulping component 3 through a pipeline II 9, and the ton bag fly ash dissolving and pulping component 3 is communicated with a fly ash washing and dechlorinating component 5 through a pipeline III 10. The fly ash waste liquid supply component 2 is communicated with the emergency pool 1 through a pipeline I8. Above-mentioned structure through the setting of each pipeline, realizes the reliable transport of corresponding waste liquid etc. and the reliability is high.
The ton bag fly ash dissolving and pulping part 3 comprises a ton bag fly ash dissolving and pulping tank 11, and the ton bag fly ash supply part 4 comprises a ton bag fly ash sealing and breaking part 12 and a vibrating screen 13. The ton bag fly ash dissolving and pulping tank 11 comprises a dissolving tank body 14, and a stirrer 15 is arranged in the dissolving tank body 14. The ton bag fly ash sealed bag breaking component 12 comprises a sealed bag breaking component box body 16, an electric switch door 17 is arranged on the sealed bag breaking component box body 16, a ton bag fly ash support 18 is arranged in the sealed bag breaking component box body 16, a vibrating screen 13 is arranged on the lower portion of the sealed bag breaking component box body 16, and the sealed bag breaking component box body 16 is communicated with the upper portion of a dissolving tank body 14 through a dust discharging funnel 19. According to the structure, during system operation, ton bag ash is conveyed to the ton bag fly ash sealing bag breaking component by a forklift, the fly ash falls onto the vibrating screen to screen large-particle impurities, and meanwhile, larger massive fly ash is broken through the vibration effect; the vibrating screen keeps an inclination angle of 5-15 degrees; magnetically separating the particles to attach to the wall of the funnel, and sorting out the small particles; the tank body of the dissolving tank is provided with an access hole from the bottom, the bottom is made into a slope, one side at a high position is provided with a high-pressure washing interface 20 which is communicated with high-pressure washing water, one side at a low position is provided with a discharge hole, and the connecting pipe part of the discharge hole is also provided with high-pressure washing water; the stirrer is higher than the highest point of the bottom gradient; the high-pressure washing water is not lower than 0.3mpa; the waste gas generated in the operation process of the ton bag fly ash sealing bag breaking component 12 and the dissolving tank body 14 is merged into the tail gas treatment of the fly ash disposal system.
The lower part of the dissolving tank body 14 is provided with a high-pressure flushing interface 20. The lower part of the dissolving tank body 14 is provided with a discharge hole 21. And a magnetic separation 22 is arranged on the ash discharging funnel 19.
Ton bag flying dust dissolve slurrying system, to not enough among the prior art, provide brand-new improvement scheme. When the ton bag fly ash dissolving and pulping system operates, on one hand, various waste liquids generated in the fly ash disposal process are collected into an emergency water tank and are conveyed to a ton bag fly ash dissolving and pulping part through the emergency water tank; on the other hand, production filtrate produced in the dechlorination process of the front-section fly ash washing dechlorination component is adopted; when the amount of the production waste liquid is insufficient, the filtrate is used as make-up water. In the pulping and dissolving process of the ton bag fly ash, according to factors such as the water content, the agglomeration degree and the like of the ton bag fly ash, the water-cement ratio is maintained to be 2-5: 1; when the ton bag fly ash dissolving and pulping system works, the water-cement ratio is quantitatively controlled, namely the water amount is added by liquid level control according to the number of ton bag ash dissolved in each tank according to a plan. If 2 tons of ash are planned to be dissolved, the ratio of water to ash is 3:1, dissolving the water in the tank. In the practical process, the water-cement ratio is corrected according to the characteristic factors such as water content, bulk density and the like of different ash production unit ton packages. Ton bag flying dust dissolve slurrying system, simple structure optimizes through equipment and the technology to ton bag flying dust dissolve slurrying, effectively utilizes the production process waste liquid, realizes that ton bag flying dust is high-efficient to dissolve slurrying, reduces impurity to dissolving ejection of compact process influence, improves whole efficiency and handles the reliability.
The present invention has been described in detail with reference to the accompanying drawings, and it is obvious that the present invention is not limited by the above embodiments, and the present invention can be implemented in various ways without modification, and the present invention is not limited by the above embodiments.
Claims (9)
1. The utility model provides a ton bag flying dust dissolves slurrying system which characterized in that: the ton bag fly ash dissolving and pulping system comprises an emergency water tank (1), a fly ash waste liquid supply part (2) is communicated with a ton bag fly ash dissolving and pulping part (3), the emergency water tank (1) is communicated with the ton bag fly ash dissolving and pulping part (3), a ton bag fly ash supply part (4) is communicated with the ton bag fly ash dissolving and pulping part (3), the ton bag fly ash dissolving and pulping part (3) is communicated with a fly ash washing dechlorinating part (5), and a filtrate conveying pipeline (7) of a front section fly ash washing dechlorinating part (6) is communicated with the ton bag fly ash dissolving and pulping part (3).
2. The ton bag fly ash dissolving and pulping system according to claim 1, characterized in that: the emergency water tank (1) is communicated with the ton bag fly ash dissolving and pulping component (3) through a pipeline II (9), and the ton bag fly ash dissolving and pulping component (3) is communicated with the fly ash washing and dechlorinating component (5) through a pipeline III (10).
3. The ton bag fly ash dissolving and pulping system according to claim 1 or 2, characterized in that: the fly ash waste liquid supply component (2) is communicated with the emergency pool (1) through a pipeline I (8).
4. The ton bag fly ash dissolving and pulping system according to claim 1 or 2, characterized in that: the ton bag fly ash dissolving and pulping component (3) comprises a ton bag fly ash dissolving and pulping tank (11), and the ton bag fly ash supply component (4) comprises a ton bag fly ash sealing and bag breaking component (12) and a vibrating screen (13).
5. The ton bag fly ash dissolving and pulping system according to claim 4, wherein: the ton bag fly ash dissolving pulping tank (11) comprises a dissolving tank body (14), and a stirrer (15) is arranged in the dissolving tank body (14).
6. The ton bag fly ash dissolving and pulping system according to claim 5, wherein: the ton bag fly ash sealed bag breaking component (12) comprises a sealed bag breaking component box body (16), an electric switch door (17) is arranged on the sealed bag breaking component box body (16), a ton bag fly ash support (18) is arranged in the sealed bag breaking component box body (16), a vibrating screen (13) is arranged on the lower portion of the sealed bag breaking component box body (16), and the sealed bag breaking component box body (16) is communicated with the upper portion of a dissolving tank body (14) through a lower ash hopper (19).
7. The ton bag fly ash dissolving and pulping system according to claim 6, characterized in that: the lower part of the dissolving tank body (14) is provided with a high-pressure flushing interface (20).
8. The ton bag fly ash dissolving and pulping system according to claim 5, characterized in that: the lower part of the dissolving tank body (14) is provided with a discharge hole (21).
9. The ton bag fly ash dissolving and pulping system according to claim 6, characterized in that: and the lower ash hopper (19) is provided with a magnetic separation device (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221242013.6U CN218590241U (en) | 2022-05-20 | 2022-05-20 | Ton bag flying dust dissolves slurrying system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221242013.6U CN218590241U (en) | 2022-05-20 | 2022-05-20 | Ton bag flying dust dissolves slurrying system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218590241U true CN218590241U (en) | 2023-03-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221242013.6U Active CN218590241U (en) | 2022-05-20 | 2022-05-20 | Ton bag flying dust dissolves slurrying system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218590241U (en) |
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2022
- 2022-05-20 CN CN202221242013.6U patent/CN218590241U/en active Active
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