CN203999895U - Change into line electrolytic bath fluid circulation - Google Patents
Change into line electrolytic bath fluid circulation Download PDFInfo
- Publication number
- CN203999895U CN203999895U CN201420415325.1U CN201420415325U CN203999895U CN 203999895 U CN203999895 U CN 203999895U CN 201420415325 U CN201420415325 U CN 201420415325U CN 203999895 U CN203999895 U CN 203999895U
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- CN
- China
- Prior art keywords
- tank liquor
- mixing vessel
- liquor mixing
- cell body
- electrolytic bath
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model discloses one and change into line electrolytic bath fluid circulation, especially a kind ofly change into line electrolytic bath fluid circulation for Waste Acid From Hua Cheng Foil production field.The utility model provides one can make electrolytic bath liquid after refrigeration cycle, keep concentration, temperature even, and that improves the stability of producing and conforming product rate changes into line electrolytic bath fluid circulation, comprises cell body and two cover circulation devices; Described cell body is communicated with the import of pump, the outlet of strainer is communicated with cell body, also comprise tank liquor mixing vessel, on described tank liquor mixing vessel, be provided with outlet and two imports, the strainer of described two cover circulation devices is connected with two imports of tank liquor mixing vessel respectively, and the outlet of described tank liquor mixing vessel is communicated with cell body.Between strainer and cell body, set up tank liquor mixing vessel, make the tank liquor of two-way after refrigeration cycle in tank liquor mixing vessel after fully mixed, then enter in electrolytic cell body.
Description
Technical field
The utility model relates to one and changes into line electrolytic bath fluid circulation, especially a kind ofly changes into line electrolytic bath fluid circulation for Waste Acid From Hua Cheng Foil production field.
Background technology
Waste Acid From Hua Cheng Foil is mainly the anode foils being used in aluminium electrolutic capacitor, and the whole process changing into is in certain density tank liquor, certain temperature, certain reaction times, aluminium foil is applied to set voltage one by one, thereby form one deck densification, certain thickness Al2O3 at aluminium foil surface.Its process is also thermopositive reaction.The structure that changes into the whole Production Flow Chart of line is: put paper tinsel machine-charging roller-electrolyzer-liquid to electric groove-electrolyzer-treatment trough-roasting furnace-foil closing machine etc., electrolyzer wherein, liquid have to electric groove, auxiliary facility structure: liquid-supplying system, cooling recirculation system, water manufacturing system, power supply system, Sewage treatment systems, ventilation system etc.
The electrochemical reaction changing in process of production in line electrolyzer is all thermopositive reaction, and keeps constant temperature according to processing requirement groove planted agent, therefore must carry out heat exchange by heat exchanger to take away the waste heat producing in thermopositive reaction guarantee homo(io)thermism.In prior art in order to increase the heat in the same time, ensure that the waste heat in electrolyzer can be taken away in time, adopt two interchanger to carry out heat exchange simultaneously, being tank liquor divides two-way to enter respectively in two interchanger from cell body out, and tank liquor is directly got back in electrolyzer after interchanger heat exchange.Because being divided into two-way, tank liquor carries out refrigeration cycle, its refrigeration cycle finishes the temperature of rear two-way tank liquor concentration inconsistent, even go out now larger concentration difference and the temperature difference, after existing the two-way tank liquor of concentration difference and the temperature difference to get back in cell body, can cause the phenomenon of concentration and non-uniform temperature in electrolyzer, can affect the stability of final product quality, reduce the qualification rate of product.Therefore in prior art, also do not have one can make electrolytic bath liquid after refrigeration cycle, keep concentration, temperature even, reduce partial points temperature head and concentration difference in cell body, ensure the consistence of product, that improves the stability of producing and conforming product rate changes into line electrolytic bath fluid circulation.
Utility model content
Technical problem to be solved in the utility model is to provide one can make electrolytic bath liquid after refrigeration cycle, keep concentration, temperature even, reduce partial points temperature head and concentration difference in cell body, ensure the consistence of product, that improves the stability of producing and conforming product rate changes into line electrolytic bath fluid circulation.
What the utility model solved that its technical problem adopts changes into line electrolytic bath fluid circulation, comprises cell body and two cover circulation devices; Every cover circulation device comprises pump, interchanger and strainer, and pump outlet is communicated with the import of interchanger, and the outlet of interchanger is communicated with the import of strainer; Described cell body is communicated with the import of pump, the outlet of strainer is communicated with cell body, also comprise tank liquor mixing vessel, on described tank liquor mixing vessel, be provided with outlet and two imports, the strainer of described two cover circulation devices is connected with two imports of tank liquor mixing vessel respectively, and the outlet of described tank liquor mixing vessel is communicated with cell body.
Be further, two imports of described tank liquor mixing vessel are separately positioned on the two ends of tank liquor mixing vessel, draw at least one honeycomb duct from each import one end, the honeycomb duct of drawing from two imports is staggered in tank liquor mixing vessel, every sluice way is made up of two flow deflectors, and flow deflector can rotate relative to tank liquor mixing vessel.
Further, described import is arranged on the top of tank liquor mixing vessel, and ingress is provided with shower nozzle with holes.
Further, also comprise stirring rake, described stirring rake is arranged on the inside of tank liquor mixing vessel.
The beneficial effects of the utility model are: owing to having set up tank liquor mixing vessel between strainer and cell body, the tank liquor of the two-way that makes to exist concentration difference and temperature head after refrigeration cycle after fully mixed, then enters in electrolytic cell body in tank liquor mixing vessel.In tank liquor mixing vessel, two-way tank liquor concentration difference and temperature head in well-mixed process reduces gradually, after finally reaching unanimously, enter again in electrolytic cell body, avoided because the interior partial points temperature of cell body and the underproof phenomenon of concentration product inconsistent and that cause.Adopt flow deflector to be combined to form the form of honeycomb duct, can make the interlaced mixing of two-way tank liquor, mixed tank liquor is more even.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of the tank liquor mixing vessel of the utility model band flow deflector;
Fig. 3 is the structural representation of the tank liquor mixing vessel of the utility model band shower nozzle;
Fig. 4 is the structural representation of the tank liquor mixing vessel of the utility model band stirring rake;
Component, position and numbering in figure: cell body 1, pump 2, interchanger 3, strainer 4, import 5, shower nozzle 6, flow deflector 7, tank liquor mixing vessel 8, stirring rake 9.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, the line electrolytic bath fluid circulation that changes into of the present utility model, comprises cell body 1 and two cover circulation devices; Every cover circulation device comprises pump 2, interchanger 3 and strainer 4, and the outlet of pump 2 is communicated with the import of interchanger 3, and the outlet of interchanger 3 is communicated with the import of strainer 4; Described cell body 1 is communicated with the import of pump 2, the outlet of strainer 4 is communicated with cell body 1, also comprise tank liquor mixing vessel 8, on described tank liquor mixing vessel 8, be provided with outlet and two imports 5, the strainer 4 of described two cover circulation devices is connected with two imports 5 of tank liquor mixing vessel respectively, and the outlet of described tank liquor mixing vessel 8 is communicated with cell body 1.Prior art change into line electrolytic bath fluid circulation, tank liquor is introduced in interchanger 3 cooling after being extracted out by pump 2, then through filtering in strainer 4, in above process, the concentration of two-way tank liquor and temperature there will be larger difference.Owing to having set up tank liquor mixing vessel 8 between strainer 4 and cell body 1, the tank liquor of the two-way that makes to exist concentration difference and temperature head after refrigeration cycle after fully mixed, then enters in electrolytic cell body 1 in tank liquor mixing vessel 8.In tank liquor mixing vessel 8, two-way tank liquor concentration difference and temperature head in well-mixed process reduces gradually, after finally reaching unanimously, enter again in electrolytic cell body 1, avoided because the interior partial points temperature of cell body 1 and the underproof phenomenon of concentration product inconsistent and that cause.
As shown in Figure 2, two imports 5 of described tank liquor mixing vessel 8 are separately positioned on the two ends of tank liquor mixing vessel 8, draw at least one honeycomb duct from each import 5 one end, the honeycomb duct of drawing from two imports 5 is staggered in tank liquor mixing vessel 8, every sluice way is made up of two flow deflectors 7, and flow deflector 7 can rotate relative to tank liquor mixing vessel 8.Can flow deflector 7 is hinged near one end and the tank liquor mixing vessel 8 of tank liquor mixing vessel 8 diapires when concrete enforcement, realize the rotation of flow deflector 7, the hinged one end of flow deflector 7 and tank liquor mixing vessel 8 can arrange a jointed shaft, jointed shaft is extended outside tank liquor mixing vessel 8, can facilitate the rotation of flow deflector 7.If directly two-way tank liquor is passed in tank liquor mixing vessel 8, the contact area of tank liquor is less, owing to first passing into stopping of tank liquor, after the part tank liquor that passes into be difficult to mutual mixing, or need the long period to mix.And set up after honeycomb duct, flow at tank liquor that tank liquor mixing vessel 8 is front turns to plumb position by flow deflector 7, form honeycomb duct in the inside of tank liquor mixing vessel 8.At this moment, two-way tank liquor, under the guiding of honeycomb duct, in the staggered influent mixing vessel of ingress, then rotates 90 degree by flow deflector 7 to same direction, removes the obstruct to tank liquor, and two-way tank liquor just can mix mutually.Due to the guiding of honeycomb duct, when two-way tank liquor is mixed, contact interface area is larger, also more even after mixing.
As shown in Figure 3, described import 5 is arranged on the top of tank liquor mixing vessel 8, and import 5 places are provided with shower nozzle with holes 6.Tank liquor enters into after shower nozzle 6 by import, under the pressure-acting of pump, from the hole of shower nozzle 6, sprays out, and is distributed to each position of tank liquor mixing vessel 8, and remix after two-way tank liquor Monodispersed makes the mixing of tank liquor more abundant.In order to make tank liquor spray area larger, preferably shower nozzle 6 is arranged on to the top of tank liquor mixing vessel 8.
As shown in Figure 4, also comprise stirring rake 9, described stirring rake 9 is arranged on the inside of tank liquor mixing vessel 8.For tank liquor is mixed, can also adopt stirring rake 9, stirring rake 9 is arranged on the inside of tank liquor mixing vessel 8.In tank liquor mixing process, rotate stirring rake 9, can make the mixing of two-way tank liquor more even.When concrete enforcement, can draw a rotating shaft from the end of stirring rake 9, a part for rotating shaft is positioned at the outside of tank liquor mixing vessel 8, is convenient to rotate from external drive rotating shaft.The mode of drive shaft both can adopt the method for artificial rotation, also can adopt the mechanical means of motor, hydraulic pressure or air pressure to drive.
Claims (4)
1. change into line electrolytic bath fluid circulation, comprise cell body (1) and two cover circulation devices; Every cover circulation device comprises pump (2), interchanger (3) and strainer (4), and the outlet of pump (2) is communicated with the import of interchanger (3), the outlet of interchanger (3) is communicated with the import of strainer (4); Described cell body (1) is communicated with the import of pump (2), the outlet of strainer (4) is communicated with cell body (1), it is characterized in that: also comprise tank liquor mixing vessel (8), on described tank liquor mixing vessel (8), be provided with outlet and two imports (5), the strainer (4) of described two cover circulation devices is connected with two imports (5) of tank liquor mixing vessel respectively, and the outlet of described tank liquor mixing vessel (8) is communicated with cell body (1).
2. the line electrolytic bath fluid circulation that changes into as claimed in claim 1, it is characterized in that: two imports (5) of described tank liquor mixing vessel (8) are separately positioned on the two ends of tank liquor mixing vessel (8), draw at least one honeycomb duct from each import (5) one end, the honeycomb duct of drawing from two imports (5) is staggered in tank liquor mixing vessel (8), every sluice way is made up of two flow deflectors (7), and flow deflector (7) can rotate relative to tank liquor mixing vessel (8).
3. the line electrolytic bath fluid circulation that changes into as claimed in claim 1, it is characterized in that: described import (5) is arranged on the top of tank liquor mixing vessel (8), import (5) locates to be provided with shower nozzle with holes (6).
4. the line electrolytic bath fluid circulation that changes into as claimed in claim 1, is characterized in that: also comprise stirring rake (9), described stirring rake (9) is arranged on the inside of tank liquor mixing vessel (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420415325.1U CN203999895U (en) | 2014-07-25 | 2014-07-25 | Change into line electrolytic bath fluid circulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420415325.1U CN203999895U (en) | 2014-07-25 | 2014-07-25 | Change into line electrolytic bath fluid circulation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203999895U true CN203999895U (en) | 2014-12-10 |
Family
ID=52039923
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420415325.1U Expired - Fee Related CN203999895U (en) | 2014-07-25 | 2014-07-25 | Change into line electrolytic bath fluid circulation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203999895U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104975317A (en) * | 2015-06-09 | 2015-10-14 | 新疆众和股份有限公司 | Automatic-control liquid distribution and supply system for formation process liquid |
-
2014
- 2014-07-25 CN CN201420415325.1U patent/CN203999895U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104975317A (en) * | 2015-06-09 | 2015-10-14 | 新疆众和股份有限公司 | Automatic-control liquid distribution and supply system for formation process liquid |
| CN104975317B (en) * | 2015-06-09 | 2018-04-10 | 新疆众和股份有限公司 | Liquid and liquid-supplying system are matched somebody with somebody in the automatic control of chemical synthesis technology liquid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Wang Weiguo Inventor after: Zha Hongfeng Inventor after: Gu Donghui Inventor before: Yan Qixu Inventor before: Chen Huachang Inventor before: Gu Donghui |
|
| COR | Change of bibliographic data | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141210 Termination date: 20210725 |