CN215050695U - Phosphorization deslagging system - Google Patents
Phosphorization deslagging system Download PDFInfo
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- CN215050695U CN215050695U CN202120510972.0U CN202120510972U CN215050695U CN 215050695 U CN215050695 U CN 215050695U CN 202120510972 U CN202120510972 U CN 202120510972U CN 215050695 U CN215050695 U CN 215050695U
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- Prior art keywords
- bonderizing
- groove
- phosphating
- tank
- phosphorization
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- 239000013049 sediment Substances 0.000 claims abstract description 44
- 238000001914 filtration Methods 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims description 45
- 239000002893 slag Substances 0.000 claims description 37
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 4
- 229910052782 aluminium Inorganic materials 0.000 claims description 4
- 238000012423 maintenance Methods 0.000 abstract description 9
- 238000000926 separation method Methods 0.000 description 13
- 239000008187 granular material Substances 0.000 description 6
- 210000005056 cell body Anatomy 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003973 paint Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 239000000383 hazardous chemical Substances 0.000 description 2
- 231100000206 health hazard Toxicity 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a bonderizing slagging-off technical field discloses a bonderizing deslagging system, and it includes bonderizing groove, replacement groove, bonderizing sediment groove and PS bonderizing dross removal mechanism, the upper portion in bonderizing sediment groove is equipped with the phosphating solution entry, the phosphating solution entry with bonderizing groove intercommunication, the lower part in bonderizing sediment groove is equipped with the phosphating solution export, the phosphating solution export with PS bonderizing dross removal mechanism intercommunication, the bonderizing sediment inslot is equipped with the filtration pocket, it is located to filter the pocket the phosphating solution entry with between the phosphating solution export, PS bonderizing dross removal mechanism with replacement groove all with bonderizing groove intercommunication. The utility model discloses a phosphating deslagging system slagging-off is efficient and can reduce artifical the maintenance.
Description
Technical Field
The utility model relates to a bonderizing slagging-off technical field especially relates to a bonderizing deslagging system.
Background
White automobile body forms the phosphating coating through the bonderizing process, and remaining impurity can form the bonderizing sediment in automobile body panel and the bonderizing tank liquid, and through the production of certain time, the bonderizing sediment can deposit in the bonderizing tank bottom and more, so need retrieve the bonderizing sediment of bonderizing tank bottom in order to guarantee that the bonderizing process normally goes on. The prior art uses PS bonderizing dross removal mechanism to carry out the drying and the separation of bonderizing sediment to bonderizing tank bottom tank liquid usually to in getting into the bonderizing inslot with the filtrating recirculation, specifically discharge bonderizing tank top tank liquid to the replacement groove, the tank liquid that the bottom slag content is high passes through PS bonderizing dross removal mechanism and filters out the bonderizing sediment. But at actual filter residue in-process, because of the slag content height of bonderizing tank bottom tank liquor, lead to PS bonderizing dross removal mechanism's filter residue time long, it is inefficient, and can make PS bonderizing dross removal mechanism often appear blocking phenomenon and take place, this leads to the staff to need frequent maintenance, has increased and has dealt with cost and cycle.
SUMMERY OF THE UTILITY MODEL
The utility model aims at: the phosphorization deslagging system has high efficiency and can reduce manual maintenance so as to reduce deslagging cost.
In order to realize the above-mentioned purpose, the utility model provides a bonderizing deslagging system, it includes bonderizing groove, replacement groove, bonderizing sediment groove and PS bonderizing dross removal mechanism, the upper portion in bonderizing sediment groove is equipped with the bonderizing liquid entry, bonderizing liquid entry with bonderizing groove intercommunication, the lower part in bonderizing sediment groove is equipped with the bonderizing liquid export, the bonderizing liquid export with PS bonderizing dross removal mechanism intercommunication, the bonderizing sediment inslot is equipped with the filtration pocket, it is located to filter the pocket bonderizing liquid entry with between the bonderizing liquid export, PS bonderizing dross removal mechanism with replacement groove all with bonderizing groove intercommunication.
Furthermore, the phosphating solution inlet is formed in the top surface of the phosphating slag settling tank, the phosphating solution inlet is communicated with the bottom of the phosphating tank through a pipeline, and the filtering bag is arranged below the phosphating solution inlet.
Furthermore, the phosphating solution outlet is arranged on the side wall of the phosphating slag settling tank and is communicated with the PS phosphating slag removal device through a filter pump.
Further, bonderizing dregs of a decoction groove includes cell body and capping, the open-top of cell body, the capping slides and locates the open-top of cell body, the bonderizing liquid entry is located on the capping.
Further, the capping has a plurality ofly, the open-top department of cell body is equipped with first slide and is located the second slide of first slide below, and is a plurality of the capping is located in turn on first slide and the second slide.
Furthermore, the top opening of the groove body is rectangular, and the groove cover is rectangular.
Further, the slot cover is made of aluminum.
Further, the filtering bag comprises a side wall and a filtering net arranged at the bottom of the side wall.
Above-mentioned technical scheme provides a phosphorization deslagging system, compares with prior art, and its beneficial effect lies in: phosphorization tank bottom phosphorization liquid contains phosphorization sediment height, when clear groove is maintained, extract the phosphorization liquid on phosphorization tank upper portion to the replacement groove, lower part phosphorization liquid discharges to phosphorization sediment groove, the phosphorization liquid can get into phosphorization sediment groove and through filtering the pocket through the phosphorization liquid entry, filter the phosphorization sediment of pocket with large granule and carry out the initial gross separation, the lower tank liquor of separation slag content can get into PS phosphorization dross removal mechanism through the phosphorization liquid export and carry out phosphorization liquid secondary filtration and mummification, then take back the phosphorization liquid to the phosphorization inslot, carry out the useless processing of danger after the separation of phosphorization sediment. Consequently, adopt above-mentioned deslagging system's slagging-off mode, filter the bonderizing sediment of large granule through filtering the pocket earlier, can avoid PS bonderizing dross removal mechanism to appear blockking up, reduce artifical maintenance cost to because filtering the slag content that the pocket filtered the back reduced phosphating solution, and then can improve PS bonderizing dross removal mechanism's efficiency, thereby reduced the cost of slagging-off.
Drawings
FIG. 1 is a schematic structural view of a phosphating and deslagging system of an embodiment of the invention;
fig. 2 is a schematic structural diagram of a phosphorization slag settling tank in an embodiment of the utility model.
The device comprises a 1-phosphating tank, a 2-phosphating slag settling tank, a 21-phosphating solution inlet, a 22-phosphating solution outlet, a 23-filtering bag, a 24-tank body, a 25-tank cover, a 3-PS phosphating slag removal device and a 4-pipeline.
Detailed Description
The following detailed description of the embodiments of the present invention is provided with reference to the accompanying drawings and examples. The following examples are intended to illustrate the invention, but are not intended to limit the scope of the invention.
In the description of the present invention, it should be understood that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like, which indicate the orientation or positional relationship, are used in the present invention as being based on the orientation or positional relationship shown in the drawings, and are used only for convenience of description and simplification of the description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted" and "connected" are to be interpreted broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
As shown in figure 1 and figure 2, the embodiment of the utility model provides a phosphorization deslagging system, it includes phosphorization groove 1, the replacement groove, phosphorization sediment groove 2 and PS phosphorization dross removal mechanism 3, phosphorization sediment groove 2's upper portion is equipped with phosphorization liquid entry 21, phosphorization liquid entry 21 and phosphorization groove 1 intercommunication, phosphorization sediment groove 2's lower part is equipped with phosphorization liquid export 22, phosphorization liquid export 22 and PS phosphorization dross removal mechanism 3 intercommunication, be equipped with in the phosphorization sediment groove 2 and filter pocket 23, filter pocket 23 is located between phosphorization liquid entry 21 and the phosphorization liquid export 22, PS phosphorization dross removal mechanism 3 and replacement groove all communicate with phosphorization groove 1.
Bonderizing deslagging system based on above-mentioned scheme, when the clear groove is maintained, extract the phosphorization liquid on phosphorization groove 1 upper portion to the replacement groove, the lower part contains the high phosphorization liquid of sediment volume and discharges to phosphorization sediment groove 2, the phosphorization liquid can get into phosphorization sediment groove 2 and pass through filtration pocket 23 through phosphorization liquid entry 21, filtration pocket 23 carries out the primary separation with the phosphorization sediment of large granule, the lower tank liquor of separation back sediment volume can get into PS phosphorization dross removal mechanism 3 through phosphorization liquid export 22 and carry out phosphorization liquid secondary filter and mummification, then take the phosphorization liquid back to phosphorization groove 1 in, carry out the useless processing of danger after the separation of phosphorization sediment. Consequently, adopt above-mentioned deslagging system's slagging-off mode, filter the bonderizing sediment of large granule through filtering pocket 23 earlier, can avoid PS bonderizing dross removal mechanism 3 to appear blockking up, reduce the manual maintenance cost to because filtering pocket 23 filters the back and has reduced the slag content of bonderizing liquid, and then can improve PS bonderizing dross removal mechanism 3's efficiency, thereby reduced the cost of slagging-off.
Specifically, as shown in fig. 2, the phosphating solution inlet 21 of the embodiment is arranged on the top surface of the phosphating slag settling tank 2, the phosphating solution inlet 21 is communicated with the bottom of the phosphating tank 1 through a pipeline 4, and the filter bag 23 is arranged below the phosphating solution inlet 21. The phosphating solution at the bottom of the phosphating tank 1 enters the phosphating slag settling tank 2 from a phosphating solution inlet 21 through a pipeline 4, is filtered by a filter bag 23 and then is placed at the lower part of the phosphating slag settling tank 2, so that the water content of the phosphating slag is reduced, and the filtrate is recovered preliminarily.
Wherein, as shown in figure 1, a phosphating solution outlet 22 is arranged on the side wall of the phosphating slag settling tank 2, and the phosphating solution outlet 22 is communicated with the PS phosphating deslagging device 3 through a filter pump. The filtrate passing through the filter bag 23 is pumped to the PS phosphorization slag removal device 3 through the phosphorization liquid outlet 22 by the filter pump for secondary filtration and drying, so that the effect of phosphorization slag drying and separation is achieved, and the water content of the separated phosphorization slag is low; the paint slag separation device can avoid overflow and leakage during paint slag separation, and reduce the risk of environmental pollution; meanwhile, secondary operation can be avoided, the labor work load of workers can be reduced, and occupational health hazards caused by operation in severe environments can be reduced.
As shown in fig. 1 and fig. 2, the phosphorization slag-settling tank 2 of the present embodiment includes a tank body 24 and a tank cover 25, wherein the top end of the tank body 24 is open, the tank cover 25 is slidably disposed at the top end opening of the tank body 24, and the phosphorization liquid inlet 21 is disposed on the tank cover 25. Can open the top end opening of cell body 24 through sliding tray lid 25, realize lid push-and-pull folding effect when bonderizing groove 1 bottom is discharged, conveniently to the maintenance of bonderizing sediment groove 2, alleviate staff's work workload, avoid the occupational health harm that the operation leads to in adverse circumstances (bonderizing groove 1).
Specifically, as shown in fig. 2, the slot covers 25 are provided with a plurality of slot covers 25, a top opening of the slot body 24 is provided with a first slide and a second slide below the first slide, the slot covers 25 are alternately arranged on the first slide and the second slide, a part of the slot covers are provided with phosphating solution inlets 21, outlets of the pipelines 4 are positioned above the phosphating solution inlets 21, the push-pull folding effect of the slot covers 25 can be realized, and the maintenance of the whole phosphating slag settling tank 2 is facilitated.
As shown in fig. 2, the top opening of the trough body 24 is rectangular, the trough cover 25 is also rectangular, and the trough cover slides along the long side of the top opening of the trough body 24. In addition, the slot cover 25 is made of aluminum materials, so that the weight is light, and the installation and the convenient maintenance are facilitated.
In addition, in this embodiment, filter pocket 23 includes the lateral wall and locates the filter screen of lateral wall bottom, and the bonderizing sediment of great granule is filtered on filter pocket 23 filter screen in the bonderizing liquid, makes things convenient for artifical scarfing cinder.
To sum up, the embodiment of the utility model provides a pair of bonderizing deslagging system has following beneficial effect:
1. because the separated phosphatized slag is dried by the PS phosphatized slag removing device 3, the water content of the phosphatized slag is low, the weight of the produced waste is reduced, the total amount of the treated slag is reduced, and the cost is reduced.
2. And the overflow leakage during the separation of paint slag is reduced, and the risk potential danger of environmental pollution is eliminated.
3. Remove the dephosphorization slag to the high-efficient maximize degree, promote automobile body quality, reduce and reprocess work man-hour and material cost.
4. The labor work load of workers is reduced by avoiding multiple operations, and the occupational health hazards caused by the operations in a severe environment (in the phosphating tank 1) are reduced.
5. The process is optimized, and a phosphorization slag settling tank 2 is additionally arranged under the condition that the original process foundation (double swing rods and a skid) is not changed; the phosphating circulating pump is connected with a three-way pipeline to realize switching of inverted groove replacement.
6. The sediment groove 2 is subsided in innovation independent design bonderizing, filters the separation of big granule bonderizing sediment through bonderizing sediment groove 2 and accomplishes bag 23, and the higher bonderizing liquid of slag content passes through the PS device, and the further mummification that filters can reach bonderizing liquid secondary loop filter and returns the groove, and the bonderizing sediment is retrieved simultaneously to the maximize in the separation tank liquid, reduces to take out, reduces bonderizing sediment moisture content, and bonderizing sediment mummification degree is high.
7. Design 2 lid materials in phosphorization sediment groove are the aluminum product, realize lid push-and-pull folding effect when 1 bottom in phosphorization groove discharges, and light easy operation is convenient to the maintenance in phosphorization sediment groove 2.
8. Simple structure, design optimization, have the practicality strong, the wholeness is high, processing is simple, the cost is cheap and the facilitate promotion.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of modifications and replacements can be made without departing from the technical principle of the present invention, and these modifications and replacements should also be regarded as the protection scope of the present invention.
Claims (8)
1. The utility model provides a bonderizing deslagging system, its characterized in that, including bonderizing groove, replacement groove, bonderizing sediment groove and PS bonderizing dross removal mechanism, the upper portion in bonderizing sediment groove is equipped with the bonderizing liquid entry, bonderizing liquid entry with bonderizing groove intercommunication, the lower part in bonderizing sediment groove is equipped with the bonderizing liquid export, the bonderizing liquid export with PS bonderizing dross removal mechanism intercommunication, be equipped with in the bonderizing sediment inslot and filter the pocket, filter the pocket and be located the bonderizing liquid entry with between the bonderizing liquid export, PS bonderizing dross removal mechanism with replacement groove all with bonderizing groove intercommunication.
2. The system of claim 1, wherein the phosphating solution inlet is formed in the top surface of the phosphating slag settling tank, the phosphating solution inlet is communicated with the bottom of the phosphating tank through a pipeline, and the filtering bag is arranged below the phosphating solution inlet.
3. The phosphating slag removal system of claim 1, wherein the phosphating solution outlet is formed in the side wall of the phosphating slag settling tank and is communicated with the PS phosphating slag removal device through a filter pump.
4. The phosphating slag removal system of claim 1, wherein the phosphating slag settling tank comprises a tank body and a tank cover, the tank body is open at the top end, the tank cover is slidably arranged at the opening at the top end of the tank body, and the phosphating solution inlet is arranged on the tank cover.
5. The system of claim 4, wherein the cover is provided with a plurality of covers, a first slide way and a second slide way are arranged at the opening at the top end of the tank body, the second slide way is positioned below the first slide way, and the plurality of covers are alternately arranged on the first slide way and the second slide way.
6. The system of claim 4, wherein the top opening of the trough body is rectangular and the trough cover is rectangular.
7. A phosphatizing slag removal system according to claim 4, 5 or 6, wherein the tank cover is made of aluminum.
8. The system of claim 1, wherein the filter pocket comprises a sidewall and a screen disposed at a bottom of the sidewall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120510972.0U CN215050695U (en) | 2021-03-10 | 2021-03-10 | Phosphorization deslagging system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120510972.0U CN215050695U (en) | 2021-03-10 | 2021-03-10 | Phosphorization deslagging system |
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| Publication Number | Publication Date |
|---|---|
| CN215050695U true CN215050695U (en) | 2021-12-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120510972.0U Active CN215050695U (en) | 2021-03-10 | 2021-03-10 | Phosphorization deslagging system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114525503A (en) * | 2022-03-22 | 2022-05-24 | 上海照潇环保科技有限公司 | External deslagging system of phosphating solution tank |
| CN115287640A (en) * | 2022-07-05 | 2022-11-04 | 岚图汽车科技有限公司 | Coating descaling treatment full-line cleaning system |
-
2021
- 2021-03-10 CN CN202120510972.0U patent/CN215050695U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114525503A (en) * | 2022-03-22 | 2022-05-24 | 上海照潇环保科技有限公司 | External deslagging system of phosphating solution tank |
| CN115287640A (en) * | 2022-07-05 | 2022-11-04 | 岚图汽车科技有限公司 | Coating descaling treatment full-line cleaning system |
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