CN210751662U - Degassing filter tank for recovering aluminum liquid - Google Patents
Degassing filter tank for recovering aluminum liquid Download PDFInfo
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- CN210751662U CN210751662U CN201921593396.XU CN201921593396U CN210751662U CN 210751662 U CN210751662 U CN 210751662U CN 201921593396 U CN201921593396 U CN 201921593396U CN 210751662 U CN210751662 U CN 210751662U
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Abstract
The utility model discloses a degassing and filtering tank for recovering aluminum liquid, which comprises an L-shaped tank body, wherein the L-shaped tank body is respectively provided with a degassing tank, a filtering tank and a sedimentation tank, the filtering tank is arranged at the corner of the L-shaped tank body, the degassing tank and the sedimentation tank are respectively arranged at the two sides of the filtering tank, the depth of the filtering tank is less than that of the degassing tank and the sedimentation tank, a degassing rotor device is arranged in the degassing tank, and independent heating mechanisms are respectively arranged above the degassing tank, the filtering tank and the sedimentation tank; the degassing rotor device removes bubbles in the aluminium liquid through the mode of stirring, improves the quality of aluminium liquid, prevents that the aluminium goods inside of pouring from having the unnecessary gas pocket, filters the aluminium liquid after the degassing through the filtering ponds, gets rid of impurity to outwards carry after a period of time's precipitation, can effectively improve the quality of aluminium liquid, each cell body top all is equipped with heating mechanism, guarantees that aluminium liquid keeps higher temperature basically in the processing procedure.
Description
Technical Field
The utility model relates to a metallic aluminum recycles technical field, more specifically says, it relates to a degassing filtration pond of retrieving aluminium liquid.
Background
The existing metal aluminum is generally recycled through high-temperature melting into aluminum liquid, the aluminum liquid is directly recycled after being simply treated, the aluminum liquid has more impurities, and a large amount of bubbles exist in the aluminum liquid.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects existing in the prior art, the utility model aims to provide a degassing and filtering tank for recovering aluminum liquid, which solves one or more problems.
In order to achieve the above purpose, the utility model provides a following technical scheme:
the utility model provides a retrieve degassing filtration pond of aluminium liquid, includes L type cell body, degassing tank, filtering ponds and sedimentation tank have been seted up on the L type cell body respectively, filtering ponds locate the corner of L type cell body, degassing tank with sedimentation tank locates respectively the both sides of filtering ponds, the degree of depth of filtering ponds is less than degassing tank the degree of depth of sedimentation tank.
Further, a degassing rotor device is arranged in the degassing pool.
Furthermore, a first through groove and a second through groove are formed in the bottom of the filtering tank, the first through groove is communicated with the filtering tank and the degassing tank, and the second through groove is communicated with the filtering tank and the sedimentation tank.
Further, the height of the second through groove is lower than the height of the first through groove.
Furthermore, an installation step is arranged in the filter tank, the installation step is located between the first through groove and the second through groove, and a filtering mechanism is arranged on the installation step.
Furthermore, a treatment pipeline is arranged outside the L-shaped tank body, the treatment pipeline is a T-shaped pipeline, and the degassing tank is connected with the sedimentation tank through the treatment pipeline.
Furthermore, the degassing tank, the filtering tank and the sedimentation tank are respectively provided with an independent heating mechanism above.
Furthermore, a through inlet groove is formed in the degassing tank.
Further, the thickness of the bottom plate of the L-shaped tank body is 14mm, and the wall thickness of the L-shaped tank body is 8 mm.
To sum up, the utility model discloses following beneficial effect has:
1. the degassing rotor device removes bubbles in the aluminum liquid in a stirring mode, so that the quality of the aluminum liquid is improved, and unnecessary air holes are prevented from being formed in a poured aluminum product;
2. the aluminum liquid is conveyed to the filtering tank in an overflow mode without using other conveying equipment;
3. the degassed aluminum liquid is filtered by the filter tank, impurities are removed, and the aluminum liquid is precipitated for a period of time and then is conveyed outwards, so that the quality of the aluminum liquid can be effectively improved;
4. heating mechanisms are arranged above all the tank bodies, so that the aluminum liquid is basically kept at a higher temperature in the treatment process.
Drawings
FIG. 1 is a schematic sectional view of a degassing and filtering tank for recovering aluminum liquid according to an embodiment of the present invention;
FIG. 2 is a front view, cut-away schematic view, of a degassing and filtering tank for recovering aluminum liquid according to an embodiment of the present invention;
FIG. 3 is a schematic sectional view of a left side view of a degassing and filtering tank for recovering aluminum liquid according to an embodiment of the present invention;
in the figure:
1. an L-shaped tank body; 11. processing the pipeline; 2. a degassing pool; 21. a degassing rotor device; 22. an inlet tank; 3. a filtration tank; 31. a first through groove; 32. a second through groove; 33. mounting a step; 34. a filtering mechanism; 4. a sedimentation tank; 5. A heating mechanism.
Detailed Description
Example 1:
the present invention will be described in further detail with reference to the accompanying fig. 1-3.
The utility model provides a retrieve degassing filtration pond of aluminium liquid, as shown in figure 1, including L type cell body 1, degassing pond 2, filtering ponds 3 and sedimentation tank 4 have been seted up on L type cell body 1 respectively, filtering ponds 3 locates the corner of L type cell body 1, and the both sides of filtering ponds 3 are located respectively to degassing pond 2 and sedimentation tank 4, and degassing pond 2 and sedimentation tank 4 are located two limits of L type cell body 1 respectively, and the degree of depth of filtering ponds 3 is less than the degree of depth of degassing pond 2, sedimentation tank 4.
As shown in fig. 2, a degassing rotor device 21 is provided in the degassing tank 2, and the degassing rotor device 21 is a motor-driven device with a stirring function.
As shown in fig. 1-3, a first through groove 31 and a second through groove 32 are formed at the bottom of the filtering tank 3, the first through groove 31 communicates the filtering tank 3 and the degassing tank 2, and the second through groove 32 communicates the filtering tank 3 and the sedimentation tank 4.
As shown in fig. 1 and 2, the second through groove 32 is located at a lower height than the first through groove 31.
As shown in fig. 1, a mounting step 33 is provided in the filtration tank 3, the mounting step 33 is located between the first through groove 31 and the second through groove 32, a filtering mechanism 34 is provided on the mounting step 33, and the filtering mechanism 34 is a high temperature resistant filter net and has a melting point higher than that of metal aluminum.
As shown in figure 1, a treatment pipeline 11 is arranged outside the L-shaped tank body 1, the treatment pipeline 11 is a T-shaped pipeline, the degassing tank 2 is connected with the sedimentation tank 4 through the treatment pipeline 11, and the last pipe orifice of the treatment pipeline 11 is connected with an external pipeline.
As shown in fig. 1, a separate heating mechanism 5 is arranged above the degassing tank 2, the filtering tank 3 and the sedimentation tank 4, and the heating mechanism 5 is preferably a high-temperature spray gun.
As shown in FIG. 1, a through-hole inlet groove 22 is formed in the side surface of the degassing tank 2 opposite to the connection surface with the process line 11.
The thickness of the bottom plate of the L-shaped tank body 1 is 14mm, and the wall thickness of the L-shaped tank body 1 is 8 mm.
All devices in direct contact with the aluminum liquid are made of materials with melting points higher than that of the metal aluminum.
The working principle is as follows: the recovered metal aluminum with impurities enters the degassing tank 2 from the inlet groove 22 after being melted at high temperature, is stirred under the driving of the degassing rotor device 21, bubbles in the high-temperature aluminum liquid are removed, then the process is continuously continued in the degassing tank 2, the deposition height of the aluminum liquid is increased until reaching the height of the first through groove 31, the recovered metal aluminum enters the filtering tank from the first through groove 31, is downwards poured under the action of gravity, passes through the filtering mechanism 34, is removed with redundant impurities, reaches the bottom of the filtering tank 3, enters the sedimentation tank 4 from the second through groove 32, and is discharged from the processing pipeline 11 of the sedimentation tank 4 according to actual conditions.
If pure aluminum liquid enters from the inlet groove 22, the pure aluminum liquid can also be directly discharged from the treatment pipeline 11 of the degassing pool 2 after the degassing treatment of the degassing pool 2.
Example 2:
the present invention will be described in further detail with reference to the accompanying fig. 1-3.
The utility model provides a retrieve degassing filtration pond of aluminium liquid, as shown in figure 1, including L type cell body 1, degassing pond 2, filtering ponds 3 and sedimentation tank 4 have been seted up on L type cell body 1 respectively, filtering ponds 3 locates the corner of L type cell body 1, and the both sides of filtering ponds 3 are located respectively to degassing pond 2 and sedimentation tank 4, and degassing pond 2 and sedimentation tank 4 are located two limits of L type cell body 1 respectively, and the degree of depth of filtering ponds 3 is less than the degree of depth of degassing pond 2, sedimentation tank 4.
As shown in fig. 2, a degassing rotor device 21 is provided in the degassing tank 2, and the degassing rotor device 21 is a motor-driven device with a stirring function.
As shown in fig. 1-3, a first through groove 31 and a second through groove 32 are formed at the bottom of the filtering tank 3, the first through groove 31 communicates the filtering tank 3 and the degassing tank 2, and the second through groove 32 communicates the filtering tank 3 and the sedimentation tank 4.
As shown in fig. 1 and 2, the second through groove 32 is located at a lower height than the first through groove 31.
As shown in fig. 1, a plurality of installation steps 33 are arranged in the filtration tank 3, the installation steps 33 are located between the first through groove 31 and the second through groove 32, the installation steps 33 are arranged at a certain height interval, each installation step 33 is provided with an individual filtration mechanism 34, the filtration mechanism 34 is a high-temperature-resistant filtration net, the melting point of the filtration mechanism is higher than that of the metal aluminum, and the meshes of different filtration mechanisms 34 are different.
As shown in figure 1, a treatment pipeline 11 is arranged outside the L-shaped tank body 1, the treatment pipeline 11 is a T-shaped pipeline, the degassing tank 2 is connected with the sedimentation tank 4 through the treatment pipeline 11, and the last pipe orifice of the treatment pipeline 11 is connected with an external pipeline.
As shown in fig. 1, a separate heating mechanism 5 is arranged above the degassing tank 2, the filtering tank 3 and the sedimentation tank 4, and the heating mechanism 5 is preferably a high-temperature spray gun.
As shown in FIG. 1, a through-hole inlet groove 22 is formed in the side surface of the degassing tank 2 opposite to the connection surface with the process line 11.
The thickness of the bottom plate of the L-shaped tank body 1 is 14mm, and the wall thickness of the L-shaped tank body 1 is 8 mm.
All devices in direct contact with the aluminum liquid are made of materials with melting points higher than that of the metal aluminum.
The difference with embodiment 1 is that the number of the mounting steps 33 is changed, so that the filtering operation of the aluminum liquid in the filtering tank 3 can be further refined, the impurity removal is more detailed, the purpose of deepening the impurity removal is achieved, and the obtained aluminum liquid has higher quality.
Example 3:
the present invention will be described in further detail with reference to fig. 1.
The utility model provides a retrieve degassing filtration pond of aluminium liquid, as shown in figure 1, including L type cell body 1, degassing pond 2, filtering ponds 3 and sedimentation tank 4 have been seted up on L type cell body 1 respectively, filtering ponds 3 locates the corner of L type cell body 1, and the both sides of filtering ponds 3 are located respectively to degassing pond 2 and sedimentation tank 4, and degassing pond 2 and sedimentation tank 4 are located two limits of L type cell body 1 respectively, and the degree of depth of filtering ponds 3 is less than the degree of depth of degassing pond 2, sedimentation tank 4.
As shown in fig. 2, a degassing rotor device 21 is provided in the degassing tank 2, and the degassing rotor device 21 is a motor-driven device with a stirring function.
As shown in fig. 1-3, a first through groove 31 and a second through groove 32 are formed in the bottom of the filtering tank 3, the first through groove 31 communicates the filtering tank 3 and the degassing tank 2, the second through groove 32 communicates the filtering tank 3 and the sedimentation tank 4, and a filtering mechanism 34 is also arranged in the first through groove 31 and the second through groove 32.
As shown in fig. 1 and 2, the second through groove 32 is located at a lower height than the first through groove 31.
As shown in fig. 1, a mounting step 33 is provided in the filtration tank 3, the mounting step 33 is located between the first through groove 31 and the second through groove 32, a filtering mechanism 34 is provided on the mounting step 33, and the filtering mechanism 34 is a high temperature resistant filter net with a melting point higher than that of metal aluminum.
As shown in figure 1, a treatment pipeline 11 is arranged outside the L-shaped tank body 1, the treatment pipeline 11 is a T-shaped pipeline, the degassing tank 2 is connected with the sedimentation tank 4 through the treatment pipeline 11, and the last pipe orifice of the treatment pipeline 11 is connected with an external pipeline.
As shown in fig. 1, a separate heating mechanism 5 is arranged above the degassing tank 2, the filtering tank 3 and the sedimentation tank 4, and the heating mechanism 5 is preferably a high-temperature spray gun.
As shown in FIG. 1, a through-hole inlet groove 22 is formed in the side surface of the degassing tank 2 opposite to the connection surface with the process line 11.
The thickness of the bottom plate of the L-shaped tank body 1 is 14mm, and the wall thickness of the L-shaped tank body 1 is 8 mm.
All devices in direct contact with the aluminum liquid are made of materials with melting points higher than that of the metal aluminum.
The difference from the embodiment 1 is that the first through groove 31 and the second through groove 32 are internally provided with the filtering mechanism 34, and a filtering link is added between different tank bodies, so that the purpose of improving impurity removal efficiency is achieved, and the quality of the obtained aluminum liquid is improved.
It should be noted that all expressions using "first" and "second" in the embodiments of the present invention are used for distinguishing two entities with the same name but different names or different parameters, and it is understood that "first" and "second" are only used for convenience of expression and should not be understood as limitations to the embodiments of the present invention, and the following embodiments do not describe any more.
In the description of the present invention, it is to be understood that the terms "central," "lateral," "longitudinal," "front," "rear," "left," "right," "upper," "lower," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like are used in the orientation or positional relationship indicated in the drawings for convenience in describing the invention and for simplicity in description, and are not intended to indicate or imply that the referenced device or element must have a particular orientation, be constructed and operated in a particular orientation, and are therefore not to be considered limiting of the scope of the invention.
The present embodiment is only for explaining the present invention, and it is not limited to the present invention, and those skilled in the art can make modifications to the present embodiment without inventive contribution as required after reading the present specification, but all of them are protected by patent laws within the scope of the claims of the present invention.
Claims (9)
1. A degassing filter tank for recovering aluminum liquid is characterized in that: including L type cell body (1), degasification pond (2), filtering ponds (3) and sedimentation tank (4) have been seted up on L type cell body (1) respectively, filtering ponds (3) are located the corner of L type cell body (1), degasification pond (2) with sedimentation tank (4) are located respectively the both sides of filtering ponds (3), the degree of depth of filtering ponds (3) is less than degasification pond (2) the degree of depth of sedimentation tank (4).
2. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 1, characterized in that: a degassing rotor device (21) is arranged in the degassing pool (2).
3. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 1, characterized in that: the bottom of the filtering tank (3) is provided with a first through groove (31) and a second through groove (32), the first through groove (31) is communicated with the filtering tank (3) and the degassing tank (2), and the second through groove (32) is communicated with the filtering tank (3) and the sedimentation tank (4).
4. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 3, characterized in that: the height of the second through groove (32) is smaller than that of the first through groove.
5. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 3, characterized in that: and an installation step (33) is arranged in the filter tank (3), the installation step (33) is positioned between the first through groove (31) and the second through groove (32), and a filter mechanism (34) is arranged on the installation step (33).
6. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 1, characterized in that: a treatment pipeline (11) is arranged outside the L-shaped tank body (1), the treatment pipeline (11) is a T-shaped pipeline, and the degassing tank (2) is connected with the sedimentation tank (4) through the treatment pipeline (11).
7. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 1, characterized in that: and an independent heating mechanism (5) is arranged above the degassing tank (2), the filtering tank (3) and the sedimentation tank (4).
8. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 1, characterized in that: a through inlet groove (22) is formed in the degassing pool (2).
9. The degassing and filtering tank for recovering aluminum liquid as claimed in claim 1, characterized in that: the thickness of the bottom plate of the L-shaped tank body (1) is 14mm, and the wall thickness of the L-shaped tank body (1) is 8 mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921593396.XU CN210751662U (en) | 2019-09-24 | 2019-09-24 | Degassing filter tank for recovering aluminum liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921593396.XU CN210751662U (en) | 2019-09-24 | 2019-09-24 | Degassing filter tank for recovering aluminum liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210751662U true CN210751662U (en) | 2020-06-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921593396.XU Active CN210751662U (en) | 2019-09-24 | 2019-09-24 | Degassing filter tank for recovering aluminum liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210751662U (en) |
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2019
- 2019-09-24 CN CN201921593396.XU patent/CN210751662U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230921 Address after: No. 8, Dingsheng Road, Nantong High tech Industrial Development Zone, Jiangsu Province, 226000 Patentee after: Nantong Hongbo Renewable Resources Co.,Ltd. Address before: 226000 Jinqiao Road, Tongzhou Development Zone, Nantong City, Jiangsu Province Patentee before: NANTONG HONGJIN METAL ALUMINUM INDUSTRY CO.,LTD. |
|
| TR01 | Transfer of patent right |