CN204265879U - A kind of plating tank air stirrer - Google Patents
A kind of plating tank air stirrer Download PDFInfo
- Publication number
- CN204265879U CN204265879U CN201420746140.9U CN201420746140U CN204265879U CN 204265879 U CN204265879 U CN 204265879U CN 201420746140 U CN201420746140 U CN 201420746140U CN 204265879 U CN204265879 U CN 204265879U
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- blast main
- inlet pipe
- plating tank
- cell body
- tank air
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Abstract
The utility model relates to copper and covers steel electroplating technology field, disclose a kind of plating tank air stirrer, it comprises cell body, blast main and inlet pipe, described blast main is horizontally set on the bottom of described cell body, described inlet pipe is horizontally set on the top of described cell body, and the inlet end of described blast main is connected with described inlet pipe by connecting pipeline, and the length direction of described blast main is provided with the staggered production well of two rows.The utility model occurs when can eliminate shutdown that siphonage solution flows backwards and corrodes the problem of blower fan, can solve blast main on-line maintenance problem.
Description
Technical field
The utility model relates to copper and covers steel electroplating technology field, particularly relates to a kind of plating tank air stirrer covered for copper in steel continuous electroplating process for copper.
Background technology
For electroplating process, every mode causing electrolytic solution to do various flowing, is all called stirring.In electroplating process, stir except accelerate the mixing of solution consistent with making temperature, even concentration except, mainly promote the transmittance process of material.Owing to being stirred in the remarkable effect eliminated concentration polarization and improve current density aspect, therefore, most of electroplating technology all have employed stirring technique.
Alr mode comprises movable cathode, pneumatic blending, plating solution circulation, magnetic agitation, negative electrode round rotation, ultrasonic stirring, propeller agitation etc.But copper covers steel continuous plating process, and to determine cell body undersized, plating solution can only be stirred by pneumatic blending and plating solution circulation.
Copper plating solution concentration of copper sulfate is higher, copper sulfate easy Crystallization Plugging pneumatic blending production well, must shutdown maintenance.High cost is shut down, so pneumatic blending inconvenient maintenance because copper covers in steel continuous electroplating production process.
Conventional air whipping appts Inlet Position, bottom cell body, there will be siphonage when the agitation is stopped, and solution blows back in blower fan, and blower fan is corroded.
Utility model content
(1) technical problem that will solve
The purpose of this utility model be to provide a kind ofly be convenient to keep in repair, sky stir respond well, do not affect the normal plating tank air stirrer produced.
(2) technical scheme
In order to solve the problems of the technologies described above, the utility model provides a kind of plating tank air stirrer, it comprises cell body, blast main and inlet pipe, described blast main is horizontally set on the bottom of described cell body, described inlet pipe is horizontally set on the top of described cell body, and the inlet end of described blast main is connected with described inlet pipe by connecting pipeline, and the length direction of described blast main is provided with the staggered production well of two rows.
Wherein, the inlet end of described blast main is connected by elbow transition with one end of connecting pipeline, and the other end of described connecting pipeline is connected by elbow transition with described inlet pipe.
Preferably, described elbow is one eighth bend.
Wherein, described inlet pipe is also connected by union with between connecting pipeline.
Wherein, described inlet pipe is provided with the ball valve controlling charge flow rate.
Preferably, be provided with blast main described in two groups side by side in described cell body, described in two groups, blast main is connected with described inlet pipe respectively.
Wherein, the caliber of described blast main is 8-12cm.
Wherein, the aperture of described production well is 2-4mm.
(3) beneficial effect
Compared with prior art, the utility model has the following advantages:
A kind of plating tank air stirrer that the utility model provides; blast main is utilized to be horizontally set on the bottom of cell body; inlet pipe is horizontally set on the top of described cell body; the inlet end of described blast main is connected with described inlet pipe by connecting pipeline; because Inlet Position is above cell body, siphonage when therefore shutting down, is there will not be to corrode blower fan.
Accompanying drawing explanation
Fig. 1 is the one-piece construction schematic diagram of a kind of plating tank air stirrer of the utility model;
Fig. 2 is the vertical view of Fig. 1.
In figure: 1: blast main; 2: production well; 3: union; 4: ball valve; 5: cell body; 6: elbow; 7: inlet pipe; 8: connecting pipeline.
Embodiment
Below in conjunction with drawings and Examples, embodiment of the present utility model is described in further detail.Following instance for illustration of the utility model, but is not used for limiting scope of the present utility model.
In description of the present utility model, it should be noted that, term " " center ", " longitudinal direction ", " transverse direction ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end " " interior ", orientation or the position relationship of the instruction such as " outward " are based on orientation shown in the drawings or position relationship, only the utility model and simplified characterization for convenience of description, instead of indicate or imply that the device of indication or element must have specific orientation, with specific azimuth configuration and operation, therefore can not be interpreted as restriction of the present utility model.
In description of the present utility model, it should be noted that, unless otherwise clearly defined and limited, term " installation ", " being connected ", " connection " should be interpreted broadly, and such as, can be fixedly connected with, also can be removably connect, or connect integratedly; Can be mechanical connection, also can be electrical connection; Can be directly be connected, also indirectly can be connected by intermediary, can be the connection of two element internals.For the ordinary skill in the art, particular case the concrete meaning of above-mentioned term in the utility model can be understood.
As shown in Figure 1, for a kind of plating tank air stirrer that the utility model provides, it comprises cell body 5, blast main 1 and inlet pipe 7, described blast main 1 is horizontally set on the bottom of described cell body 5, and described inlet pipe 7 is horizontally set on the top of described cell body 5, and the inlet end of described blast main 1 is connected with described inlet pipe 7 by connecting pipeline 8, because Inlet Position is above cell body 5, siphonage solution refluence corrosion blower fan therefore effectively can be prevented when shutting down; The length direction of described blast main 1 is provided with the production well 2 of two row's staggered parallel arrangements, and cell body 5 bottom gas is stirred.
Conveniently change the closure of pipeline, preferably, the inlet end of described blast main 1 is connected by elbow 6 transition with one end of connecting pipeline 8, and the other end of described connecting pipeline 8 is connected by elbow 6 transition with described inlet pipe 7.Preferably, described elbow 6 is one eighth bend 6.
Described inlet pipe 7 is also connected by union 3 with between connecting pipeline 8, when the production well 2 on blast main 1 blocks serious, can unload blast main 1, conveniently keep in repair from union 3.
For the ease of regulating charge flow rate according to need of production, described inlet pipe 7 is provided with the ball valve 4 controlling charge flow rate, and when blocking appears in production well 2, large ball valve 4 can be opened, wash production well 2 open with atm number.
As shown in Figure 2, preferably, blast main 1 described in two groups is provided with side by side in described cell body 5, blast main 1 described in two groups is connected with described inlet pipe 7 respectively, to accomplish a preparation and a use, when wherein a set of blast main 1 production well 2 needs repairing because of blocking, another set of blast main 1 still can play the effect of stirring, can not affect production.
According to test of many times, the caliber of described blast main 1 can be 8-12cm, is preferably 10cm.
In order to reach effect of giving vent to anger preferably, the aperture of described production well 2 can be 2-4mm, is preferably 3mm.
As can be seen from the above embodiments, the utility model reasonable in design, occurs when eliminating shutdown that siphonage solution flows backwards and corrodes the problem of blower fan, solve blast main 1 on-line maintenance problem.
The foregoing is only preferred embodiment of the present utility model; not in order to limit the utility model; all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (8)
1. a plating tank air stirrer, it comprises cell body, it is characterized in that, also comprise blast main and inlet pipe, described blast main is horizontally set on the bottom of described cell body, described inlet pipe is horizontally set on the top of described cell body, and the inlet end of described blast main is connected with described inlet pipe by connecting pipeline, and the length direction of described blast main is provided with the staggered production well of two rows.
2. plating tank air stirrer as claimed in claim 1, it is characterized in that, the inlet end of described blast main is connected by elbow transition with one end of connecting pipeline, and the other end of described connecting pipeline is connected by elbow transition with described inlet pipe.
3. plating tank air stirrer as claimed in claim 2, it is characterized in that, described elbow is one eighth bend.
4. plating tank air stirrer as claimed in claim 3, it is characterized in that, described inlet pipe is also connected by union with between connecting pipeline.
5. plating tank air stirrer as claimed in claim 1, is characterized in that, described inlet pipe is provided with the ball valve controlling charge flow rate.
6. plating tank air stirrer as claimed in claim 1, it is characterized in that, be provided with blast main described in two groups side by side in described cell body, described in two groups, blast main is connected with described inlet pipe respectively.
7. plating tank air stirrer as claimed in claim 1, it is characterized in that, the caliber of described blast main is 8-12cm.
8. plating tank air stirrer as claimed in claim 1, it is characterized in that, the aperture of described production well is 2-4mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420746140.9U CN204265879U (en) | 2014-12-02 | 2014-12-02 | A kind of plating tank air stirrer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420746140.9U CN204265879U (en) | 2014-12-02 | 2014-12-02 | A kind of plating tank air stirrer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204265879U true CN204265879U (en) | 2015-04-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420746140.9U Active CN204265879U (en) | 2014-12-02 | 2014-12-02 | A kind of plating tank air stirrer |
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| CN (1) | CN204265879U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106757254A (en) * | 2015-11-20 | 2017-05-31 | 比亚迪股份有限公司 | Anodic oxidation device |
| CN109680325A (en) * | 2018-11-16 | 2019-04-26 | 中国航发西安动力控制科技有限公司 | For being surface-treated the compressed air micropore agitating device of tank liquor |
| TWI663293B (en) * | 2018-06-22 | 2019-06-21 | 先豐通訊股份有限公司 | Gaseous agitating device of electroplating system |
| CN110714221A (en) * | 2019-11-29 | 2020-01-21 | 无锡星亿智能环保装备股份有限公司 | Electroplating solution air stirring pipeline |
-
2014
- 2014-12-02 CN CN201420746140.9U patent/CN204265879U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106757254A (en) * | 2015-11-20 | 2017-05-31 | 比亚迪股份有限公司 | Anodic oxidation device |
| CN106757254B (en) * | 2015-11-20 | 2019-07-26 | 比亚迪股份有限公司 | Anodic oxidation device |
| TWI663293B (en) * | 2018-06-22 | 2019-06-21 | 先豐通訊股份有限公司 | Gaseous agitating device of electroplating system |
| CN109680325A (en) * | 2018-11-16 | 2019-04-26 | 中国航发西安动力控制科技有限公司 | For being surface-treated the compressed air micropore agitating device of tank liquor |
| CN110714221A (en) * | 2019-11-29 | 2020-01-21 | 无锡星亿智能环保装备股份有限公司 | Electroplating solution air stirring pipeline |
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