CN220239283U - Powder gasification precipitation type slag remover - Google Patents
Powder gasification precipitation type slag remover Download PDFInfo
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- CN220239283U CN220239283U CN202321577339.9U CN202321577339U CN220239283U CN 220239283 U CN220239283 U CN 220239283U CN 202321577339 U CN202321577339 U CN 202321577339U CN 220239283 U CN220239283 U CN 220239283U
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- Prior art keywords
- bin
- powder
- layer
- discharging
- storehouse
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- 239000000843 powder Substances 0.000 title claims abstract description 110
- 238000002309 gasification Methods 0.000 title claims abstract description 28
- 239000002893 slag Substances 0.000 title claims abstract description 22
- 238000001556 precipitation Methods 0.000 title claims abstract description 20
- 238000007599 discharging Methods 0.000 claims abstract description 54
- 238000004062 sedimentation Methods 0.000 claims description 11
- 230000000694 effects Effects 0.000 abstract description 8
- 239000000463 material Substances 0.000 description 10
- 239000006185 dispersion Substances 0.000 description 3
- 239000013049 sediment Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 239000010909 process residue Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
Abstract
The utility model relates to the technical field of powder slag removal and discloses a powder gasification precipitation type slag remover which comprises a precipitation bin, wherein a feed inlet is arranged on the precipitation bin, a first layer of gas bin, a second layer of gas bin and a third layer of gas bin are respectively arranged in the precipitation bin from top to bottom, a powder discharging bin is connected in series with the first layer of gas bin, the second layer of gas bin and the third layer of gas bin, a discharging hopper is arranged at the joint of the powder discharging bin and the first layer of gas bin, the second layer of gas bin and the third layer of gas bin, a first residue bin is arranged at the lower side of the powder discharging bin, a first collecting hopper is arranged in the first residue bin, and a pull handle is connected to the first collecting hopper. According to the utility model, the powder is gasified by layering the first-layer gas bin, the second-layer gas bin and the third-layer gas bin, so that the gasification effect is improved, the gasification channel length is increased, the channel gradient is improved, the gasified powder can be guided to the powder discharge port by matching with the powder discharging bin, and the powder can be intensively and rapidly discharged to the powder discharge bin.
Description
Technical Field
The utility model relates to the technical field of powder slag removal, in particular to a powder gasification precipitation type slag remover.
Background
The granular slag in the powder material not only affects the quality of the powder material, but also has great influence on downstream equipment for conveying and packaging the powder material due to higher hardness of the granular slag (some iron-containing impurities), such as a burning motor and damage equipment, and directly affects the operation rate of the equipment, so that slag removal treatment is required to be carried out on the powder material before the powder material is produced, the quality of subsequent processing and the protection of the equipment are ensured, and a gasification precipitation type slag remover is provided.
The gasification precipitation type slag remover adopted by the existing powder slag removal has the following problems: firstly, the setting of a sediment layer of the residues is less, so that the sufficiency of sediment is extremely easy to be reduced; secondly, the gasification intensity is inconvenient to flexibly adjust, and the deslagging effect on powder materials with different diameters is poor, so that the gasification precipitation type deslagging machine is provided for solving the problems.
Disclosure of Invention
The utility model aims to provide a powder gasification precipitation type slag remover so as to solve the problems in the prior art.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
the utility model provides a powder gasification precipitation type slag remover, its includes deposits the storehouse, the last feed inlet of installing of depositing the storehouse is last to be provided with one deck gas storehouse, two-layer gas storehouse and three-layer gas storehouse respectively from top to bottom in the storehouse that deposits, connect in series the powder down the storehouse on one deck gas storehouse, two-layer gas storehouse and the three-layer gas storehouse, and the powder down the junction of storehouse and one deck gas storehouse, two-layer gas storehouse and three-layer gas storehouse installs down the hopper, the downside of powder down the storehouse is provided with first residue storehouse, install first collection bucket in the first residue storehouse, and be connected with the pull handle on the first collection bucket, the slot has been seted up on the sediment storehouse, and be provided with the second in the slot and collect the bucket, the side of depositing the storehouse is connected with the powder and arrange the storehouse, and the powder discharge port has been seted up to the junction in one deck gas storehouse, two-layer gas storehouse and three-layer gas storehouse, fixed bottom plate is installed to the upper end in powder row storehouse, the fixed bottom plate upside is provided with the pull bar, and the pull bar is installed to the side of powder down the side, just be provided with the pump body on the discharge pump body is installed to the side of the discharge bar.
Preferably, the first-layer gas bin, the second-layer gas bin and the third-layer gas bin are all communicated with the powder discharging bin, and the first-layer gas bin, the second-layer gas bin and the third-layer gas bin are communicated with the powder discharging bin through powder discharging ports.
Preferably, the discharging hopper is in a bucket-loading structure, and the diameter of the upper end of the discharging hopper is larger than that of the lower end of the discharging hopper.
Preferably, the first collecting hopper is connected with the first residue bin in a nested and clamped mode, and the first collecting hopper and the pull handle are integrally designed.
Preferably, the second collecting hopper is connected with the slot in a clamping way, a limiting strip is arranged at the upper end of the second collecting hopper, and a pull handle is connected to the side edge of the second collecting hopper.
Preferably, the drawing lath is in nested clamping connection with the fixed bottom plate, the drawing lath is in welded connection with the pull rod, and the drawing lath is in nested sliding connection with the powder row bin.
Preferably, the powder discharging bin is communicated with the powder discharging bin, the powder discharging bin is connected with the pump body, and the output end of the pump body is communicated with the discharging pipe.
Compared with the prior art, the utility model has the beneficial effects that:
1. according to the utility model, the powder is gasified by layering the first-layer gas bin, the second-layer gas bin and the third-layer gas bin, so that the gasification effect is improved, the gasification channel length is increased, the channel gradient is improved, the gasified powder can be guided to the powder discharge port by matching with the powder discharging bin, and the powder can be intensively and rapidly discharged to the powder discharge bin;
2. according to the utility model, the materials can be subjected to dispersion treatment through the discharging hopper with the upper end diameter larger than the lower end diameter, so that the gasification effect of the powder is improved; can collect heavy residue through first collection fill and second collection fill, and then can avoid the residue to collect the incomplete phenomenon of residue collection that the fill less arouses and produce, promote the collection effect of residue.
Drawings
FIG. 1 is a schematic view of a first perspective of the overall structure of the present utility model;
FIG. 2 is a schematic view of a second perspective of the overall structure of the present utility model;
FIG. 3 is a schematic view of the mounting structure of the collecting hopper of the present utility model;
FIG. 4 is a schematic overall cross-sectional view of the present utility model;
FIG. 5 is a schematic view of the connection structure of the drawing strip plate and the fixed bottom plate of the present utility model;
FIG. 6 is a schematic drawing of the drawer strip panel structure of the present utility model.
In the figure: 1. a sedimentation bin; 2. a feed inlet; 3. a layer of air bin; 4. a two-layer gas bin; 5. three layers of air bins; 6. discharging powder material into a bin; 7. discharging a hopper; 8. a first residue bin; 9. a first collection hopper; 91. a pull handle; 10. a slot; 11. a second collection hopper; 111. a limit bar; 112. a pull handle; 12. discharging powder; 13. a powder discharge port; 14. a fixed bottom plate; 15. drawing the lath; 16. a pull rod; 17. discharging the powder from the bin; 18. a pump body; 19. and a discharge pipe.
Detailed Description
Referring to fig. 1-6, an embodiment of the present utility model is provided:
the utility model provides a powder gasification precipitation formula slag remover, it includes deposits storehouse 1, the last feed inlet 2 of installing of deposit storehouse 1, be provided with one deck gas storehouse 3 from top to bottom respectively in the deposit storehouse 1, two-layer gas storehouse 4 and three-layer gas storehouse 5, connect in series on one deck gas storehouse 3, two-layer gas storehouse 4 and the three-layer gas storehouse 5 and have the powder down feed bin 6, and the powder down feed bin 6 installs down hopper 7 with the junction of one deck gas storehouse 3, two-layer gas storehouse 4 and three-layer gas storehouse 5, down hopper 7 establishes to the fill dress structure, and down hopper 7's upper end diameter is greater than its lower extreme diameter, down hopper 7 that the upper end diameter is greater than its lower extreme diameter can carry out dispersion treatment with the material, promote the gasification effect of powder.
In one embodiment, the downside of the powder discharging bin 6 is provided with a first residue bin 8, a first collecting hopper 9 is arranged in the first residue bin 8, a pull handle 91 is connected to the first collecting hopper 9, the first collecting hopper 9 is connected with the first residue bin 8 in a nested clamping manner, the first collecting hopper 9 and the pull handle 91 are integrally designed, and the first collecting hopper 9 can collect and process residues.
In one embodiment, the sedimentation bin 1 is provided with a slot 10, a second collecting hopper 11 is arranged in the slot 10, the second collecting hopper 11 is connected with the slot 10 in a clamping way, a limiting strip 111 is arranged at the upper end of the second collecting hopper 11, a pull handle 112 is connected to the side edge of the second collecting hopper 11, and the second collecting hopper 11 can collect and process residues in powder again so as to facilitate the lifting of the collecting effect.
In one embodiment, the side of the sedimentation bin 1 is connected with a powder discharge bin 12, a powder discharge outlet 13 is formed in the joint of the first-layer air bin 3, the second-layer air bin 4 and the third-layer air bin 5 and the powder discharge bin 12, a fixed bottom plate 14 is arranged at the upper end of the powder discharge bin 12, a drawing strip plate 15 is arranged on the upper side of the fixed bottom plate 14, a pull rod 16 is arranged on the side of the drawing strip plate 15, the drawing strip plate 15 is in nested clamping connection with the fixed bottom plate 14, the drawing strip plate 15 is in welded connection with the pull rod 16, the drawing strip plate 15 is in nested sliding connection with the powder discharge bin 12, and the air outlet size is adjusted through the staggered arrangement between the drawing strip plate 15 and the fixed bottom plate 14, so that the air pressure can be adjusted.
In one of the preferred embodiments, the upper side of the powder discharging bin 12 is provided with a powder discharging bin 17, a pump body 18 is arranged on the side edge of the powder discharging bin 17, a discharging pipe 19 is connected to the pump body 18, the powder discharging bin 17 is communicated with the powder discharging bin 12, the powder discharging bin 17 is connected with the pump body 18, the output end of the pump body 18 is communicated with the discharging pipe 19, and the pump body 18 operates to guide the powder into the powder discharging bin 17 for centralized discharging, so that the powder is intensively discharged through the discharging pipe 19.
In one preferred embodiment, the first-layer gas bin 3, the second-layer gas bin 4 and the third-layer gas bin 5 are all communicated with the powder discharging bin 6, and the first-layer gas bin 3, the second-layer gas bin 4 and the third-layer gas bin 5 are communicated with the powder discharging bin 12 through the powder discharging outlet 13, and the powder is gasified through layering of the first-layer gas bin 3, the second-layer gas bin 4 and the third-layer gas bin 5, so that the gasification effect is improved, the gasification channel length is increased, the gradient of the channel is improved, the gasified powder can be guided to the powder discharging outlet 13 by matching with the powder discharging bin 6, and the gasified powder is intensively and rapidly discharged to the powder discharging bin 12.
The working principle of the utility model is as follows: firstly, a pump body 18 operates to form negative pressure, a pull rod 16 is pulled according to wind pressure conditions to adjust the size of a staggered air outlet between a pull rod 15 and a fixed bottom plate 14, then powder enters a sedimentation bin 1 through a feed inlet 2, meanwhile, a first-layer air bin 3, a second-layer air bin 4 and a third-layer air bin 5 are used for carrying out gasification treatment on the powder in a layered manner, atomized powder is in the sedimentation bin 1, a discharging hopper 7 with the upper end diameter larger than the lower end diameter of the atomized powder is used for carrying out dispersion treatment on the material, heavy residues fall into a first collecting hopper 9 under the influence of gravity, a second collecting hopper 11 arranged on the first-layer air bin 3, the second-layer air bin 4 and the third-layer air bin 5 is used for carrying out sedimentation concentration on residues on the first-layer air bin 3, the second-layer air bin 4 and the third-layer air bin 5, at the moment, the powder is flushed into a powder discharging bin 12 through a powder discharging outlet 13, the gasified powder is flushed into a pump body 18 through a powder discharging bin 17, and then the powder is discharged through a discharging pipe 19 arranged on the pump body 18.
After the powder gasification is completed, the first collecting hopper 9 and the second collecting hopper 11 are taken out, the pull handle 91 is held to pull the first collecting hopper 9 out of the first residue bin 8 and clean residues in the first collecting hopper 9, then the pull handle 112 is held to pull the second collecting hopper 11 out and clean residues in the second collecting hopper 11, and the cleaned second collecting hopper 11 is installed into the slot 10 again, so that the cleaning treatment of the second collecting hopper 11 is completed.
Claims (7)
1. A powder gasification precipitation slag remover, characterized in that it comprises: sedimentation bin (1), last feed inlet (2) of installing of sedimentation bin (1), be provided with one deck gas storehouse (3), two-layer gas storehouse (4) and three-layer gas storehouse (5) from top to bottom respectively in sedimentation bin (1), connect in series powder lower feed bin (6) on one deck gas storehouse (3), two-layer gas storehouse (4) and three-layer gas storehouse (5), and the junction of powder lower feed bin (6) and one deck gas storehouse (3), two-layer gas storehouse (4) and three-layer gas storehouse (5) installs hopper (7), the downside of powder lower feed bin (6) is provided with first residue storehouse (8), install first collection fill (9) in first residue storehouse (8), and be connected with on first collection fill (9) and draw handle (91), set up slot (10) on sedimentation bin (1), and be provided with second collection fill (11) in slot (10), the side of sedimentation bin (1) is connected with powder row storehouse (12), and one deck gas storehouse (4) and three-layer gas storehouse (5) are connected with bottom plate (13) and are arranged in fixed connection, bottom plate (14) are set up in the bottom plate (13), and pull rod (16) are installed to the side of pull rod board (15), the upside of powder row storehouse (12) is provided with powder discharge bin (17), pump body (18) are installed to the side of powder discharge bin (17), and are connected with discharge pipe (19) on pump body (18).
2. The powder gasification precipitation slag remover according to claim 1, wherein: the first-layer air bin (3), the second-layer air bin (4) and the third-layer air bin (5) are all communicated with the powder discharging bin (6), and the first-layer air bin (3), the second-layer air bin (4) and the third-layer air bin (5) are communicated with the powder discharging bin (12) through the powder discharging outlet (13).
3. The powder gasification precipitation slag remover according to claim 1, wherein: the discharging hopper (7) is of a bucket-loading structure, and the diameter of the upper end of the discharging hopper (7) is larger than that of the lower end of the discharging hopper.
4. The powder gasification precipitation slag remover according to claim 1, wherein: the first collecting hopper (9) is connected with the first residue bin (8) in a nested and clamped mode, and the first collecting hopper (9) and the pull handle (91) are integrally designed.
5. The powder gasification precipitation slag remover according to claim 1, wherein: the second collecting hopper (11) is connected with the slot (10) in a clamping way, a limiting strip (111) is arranged at the upper end of the second collecting hopper (11), and a pull handle (112) is connected to the side edge of the second collecting hopper (11).
6. The powder gasification precipitation slag remover according to claim 1, wherein: the drawing lath (15) is in nested clamping connection with the fixed bottom plate (14), the drawing lath (15) is in welded connection with the pull rod (16), and the drawing lath (15) is in nested sliding connection with the powder row bin (12).
7. The powder gasification precipitation slag remover according to claim 1, wherein: the powder discharging bin (17) is communicated with the powder discharging bin (12), the powder discharging bin (17) is connected with the pump body (18), and the output end of the pump body (18) is communicated with the discharging pipe (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321577339.9U CN220239283U (en) | 2023-06-20 | 2023-06-20 | Powder gasification precipitation type slag remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321577339.9U CN220239283U (en) | 2023-06-20 | 2023-06-20 | Powder gasification precipitation type slag remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220239283U true CN220239283U (en) | 2023-12-26 |
Family
ID=89226697
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321577339.9U Active CN220239283U (en) | 2023-06-20 | 2023-06-20 | Powder gasification precipitation type slag remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220239283U (en) |
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2023
- 2023-06-20 CN CN202321577339.9U patent/CN220239283U/en active Active
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