CN104112599A - Formation system capable of controlling treatment tank liquid to be in constant temperature state - Google Patents
Formation system capable of controlling treatment tank liquid to be in constant temperature state Download PDFInfo
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- CN104112599A CN104112599A CN201410299441.6A CN201410299441A CN104112599A CN 104112599 A CN104112599 A CN 104112599A CN 201410299441 A CN201410299441 A CN 201410299441A CN 104112599 A CN104112599 A CN 104112599A
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- Prior art keywords
- heat exchanger
- liquid
- treatment
- trough
- operated valve
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- 239000007788 liquid Substances 0.000 title claims abstract description 50
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000000498 cooling water Substances 0.000 claims abstract description 19
- 238000005868 electrolysis reaction Methods 0.000 claims description 13
- 230000008676 import Effects 0.000 claims description 11
- 238000000034 method Methods 0.000 abstract description 12
- 239000011888 foil Substances 0.000 abstract description 5
- 239000002253 acid Substances 0.000 description 4
- 238000005485 electric heating Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 239000005030 aluminium foil Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 210000005056 cell body Anatomy 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052593 corundum Inorganic materials 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 229910001845 yogo sapphire Inorganic materials 0.000 description 1
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The invention relates to formation of a formed foil, and the technical problem to be solved is to provide a formation system capable of controlling a treatment tank liquid to be in a constant temperature state. The invention provides a formation system capable of controlling a treatment tank liquid to be in a constant temperature state. The formation system includes an electrolytic tank, a treatment tank, a water return pool, a first heat exchanger, a second heat exchanger, a second circulating pump, a first solenoid valve and a second solenoid valve, an outlet of the first heat exchanger for cooling water after heat exchange is connected with a hot water inlet of the second heat exchanger through the first solenoid valve, a heat exchanger liquid inlet of the second heat exchanger is connected with one end of the second circulating pump, and the other end of the second circulation pump is connected with a liquid outlet of the treatment through; the outlet of the first heat exchanger for the cooling water after heat exchange is also connected with one end of the second solenoid pump, the other end of the second solenoid pump is connected with the water return pool, an outlet of the second heat exchanger for water after heat exchange is connected with the water return pool, and the heat exchanger liquid outlet of the second heat exchanger is connected with an liquid inlet of the treatment tank; and the formation system is suitable for a formation process of a formed foil.
Description
Technical field
The present invention relates to Waste Acid From Hua Cheng Foil and change into field, especially relate to and a kind ofly can control the formation system for the treatment of trough liquid in temperature constant state.
Background technology
Waste Acid From Hua Cheng Foil is mainly the anode foils being used in aluminium electrolytic capacitor.Its whole formation process be by special high-purity aluminum foil in the tank liquor of uniform temperature, concentration, through certain reaction time, aluminium foil is applied to set voltage one by one, thus aluminium foil surface form one deck densification, there is certain thickness alundum (Al2O3) product.Whole process is exothermic reaction.The production procedure that changes into line critical piece has: put paper tinsel machine-charging roller-electrolysis tank-liquid to electric groove-electrolysis tank-treatment trough-roasting furnace-foil closing machine; Auxiliary facility structure has: liquid-supplying system, cooling recirculation system, water manufacturing system, electric power system, sewage disposal system and ventilating system etc.Be positioned at treatment trough electrolysis tank before, its concrete connected mode is: the liquid-inlet of electrolysis tank is directly connected with the heat exchanger liquid outlet of heat exchanger, the liquid outlet of electrolysis tank is connected with the first circulating pump, the first circulating pump is connected with the import of the heat exchanger liquid of First Heat Exchanger again, the import of the cooling water of heat exchanger is connected with cooling water pipe by electromagnetically operated valve, and the outlet after the cooling water heat exchange of First Heat Exchanger is connected with back pool.And when changing into line and normally move, treatment trough is mainly that aluminium foil surface is cleaned and eliminate flaw, so its temperature is lower than the required temperature of other cell bodies, yet it also has concrete temperature requirement.Because the liquid for the treatment of trough is not to be exothermic reaction as electrolytic bath in production process, therefore need to carry out constant temperature method to the liquid for the treatment of trough, guarantee fluid temperature reaches technology controlling and process requirement.The method of using is at present that the electric heating tube that some, certain load are installed in the bottom for the treatment of trough heats liquid, and connected mode is that flange connects, then by temperature controller, keeps the temperature constant process of liquid in treatment trough.And this process is power consumption energy process, and the material for the treatment of trough cell body is mainly plastic material, once operating personnel's improper use electric heating tube or carry out misoperation, all easily cause potential safety hazard, cause any property loss, incur loss through delay and produce, or even threaten staff's personal safety.
Summary of the invention
Technical problem to be solved by this invention is to overcome in the formation system of existing Waste Acid From Hua Cheng Foil, by electric heating tube, treatment trough liquid is carried out to thermostatic control, and energy consumption is large and fail safe is low, provides a kind of and can control the formation system for the treatment of trough liquid in temperature constant state.
The technical solution adopted for the present invention to solve the technical problems is: can control the formation system for the treatment of trough liquid in temperature constant state, comprise electrolysis tank, treatment trough, back pool, First Heat Exchanger, the second heat exchanger, the second circulating pump, the first electromagnetically operated valve and the second electromagnetically operated valve, outlet after the cooling water heat exchange of described First Heat Exchanger is connected with the hot water inlet of the second heat exchanger by the first electromagnetically operated valve, the heat exchanger liquid import of the second heat exchanger is connected with one end of the second circulating pump, and the other end of the second circulating pump is connected with the liquid outlet for the treatment of trough; Outlet after the cooling water heat exchange of First Heat Exchanger is also connected with one end of the second electromagnetically operated valve, the other end of the second electromagnetically operated valve is connected with back pool, water out after the second heat exchanger heat exchange is also connected with back pool, and the heat exchanger liquid outlet of the second heat exchanger is connected with the liquid-inlet for the treatment of trough.
Concrete, described the first electromagnetically operated valve and the second electromagnetically operated valve are direct-acting electromagnetic valve.Concrete, described the second heat exchanger is dividing wall type heat exchanger.
Preferably, described the second heat exchanger is tube heat exchanger.
As the preferred version of technique scheme, described the second heat exchanger is mixed heat exchanger.
The invention has the beneficial effects as follows: simple in structure, easy operating, can realize the temperature of efficient treatment trough liquid and control, and reduces energy resource consumption, improves fail safe, effectively improves the operating efficiency that changes into line.The present invention is applicable to Waste Acid From Hua Cheng Foil formation process.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Wherein, 1 is electrolysis tank, and 2 is treatment trough, and 3 is back pool, and 41 is First Heat Exchanger, and 42 is the second heat exchanger, and 51 is the first circulating pump, and 52 is the second circulating pump, and 60 is electromagnetically operated valve, and 61 is the first electromagnetically operated valve, and 62 is the second electromagnetically operated valve, and 7 is cooling water pipe.
Embodiment
Below in conjunction with accompanying drawing, describe technical scheme of the present invention in detail.
As shown in Figure 1, of the present inventionly can control the formation system for the treatment of trough liquid in temperature constant state, comprise electrolysis tank 1, treatment trough 2, back pool 3, First Heat Exchanger 41, the second heat exchanger 42, the second circulating pump 52, the first electromagnetically operated valve 61 and the second electromagnetically operated valve 62, outlet after the cooling water heat exchange of described First Heat Exchanger 41 is connected with the hot water inlet of the second heat exchanger 42 by the first electromagnetically operated valve 61, the heat exchanger liquid import of the second heat exchanger 42 is connected with one end of the second circulating pump 52, and the other end of the second circulating pump 52 is connected with the liquid outlet for the treatment of trough 2; Outlet after the cooling water heat exchange of First Heat Exchanger 41 is also connected with one end of the second electromagnetically operated valve 62, the other end of the second electromagnetically operated valve 62 is connected with back pool 3, after the heat exchange of the second heat exchanger 42, water out is also connected with back pool 3, and the heat exchanger liquid outlet of the second heat exchanger 42 is connected with the liquid-inlet for the treatment of trough 2.
In figure, treatment trough 2 upper port are liquid-inlet, and its lower port is liquid outlet; The left side upper port of First Heat Exchanger 41 is the outlet of heat exchanger liquid, and its left side lower port is the import of heat exchanger liquid, the import that its right side upper port is cooling water, and its right side lower port is the outlet after cooling water heat exchange; The left side upper port of the second heat exchanger 42 is water out after heat exchange, and its left side lower port is hot water inlet, and its right side upper port is the outlet of heat exchanger liquid, and its right side lower port is the import of heat exchanger liquid.
Cold water in the rear cooling water pipe 7 of opens solenoid valve 60 can be entered in First Heat Exchanger 41 by the import of the cooling water of First Heat Exchanger 41, and after heat-shift, the outlet from the cooling water heat exchange of First Heat Exchanger 41 is flowed out again; The first circulating pump 51 is extracted out from the liquid outlet of electrolysis tank 1 carrying out the later tank liquor of exothermic reaction in electrolysis tank 1, the import of the direct heat exchanger liquid by First Heat Exchanger 41 enters in heat exchanger, with after cooling water heat-shift again the outlet from the heat exchanger liquid of First Heat Exchanger 41 flow out, then the liquid-inlet by electrolysis tank 1 flows in electrolysis tank 1.
The temperature of the water that the outlet after the cooling water heat exchange of First Heat Exchanger 41 is flowed out can reach 70 degree, when the first electromagnetically operated valve 61 is opened, and in the second electromagnetically operated valve 62 closures, these current can enter by the hot water inlet of the second heat exchanger 42 in the second heat exchanger 42, the second circulating pump 52 pumps the liquid in treatment trough 2 from its liquid outlet, the then heat exchanger liquid import by the second heat exchanger 42 enters into the second heat exchanger 42, carry out after exchange heat the liquid-inlet by treatment trough 2 from the heat exchanger liquid outlet of the second heat exchanger 42 with hot water in the second heat exchanger 42 and enter into treatment trough 2, thereby realize the effective heating to treatment trough 2, simultaneously, water after heat exchange enters back pool 3 from the water out of the second heat exchanger 42.When the temperature for the treatment of trough 2 interior liquid reaches to fixed temperature, close the first electromagnetically operated valve 61, open the second electromagnetically operated valve 62 simultaneously, now the water after First Heat Exchanger 41 heat exchange directly enters back pool 3.So design, utilizes backwater waste heat to keep in treatment trough 2 liquid in temperature constant state., without using electrically heated parts to heat treatment trough, reduce power consumption, reduced electric cost, reduce electric heating and bring potential safety hazard.
The first electromagnetically operated valve 61 and the second electromagnetically operated valve 62 are direct-acting electromagnetic valve.Such electromagnetically operated valve can both normally be worked under condition when vacuum, negative pressure, zero-pressure etc.
Based on cost and realize effect and consider, the second heat exchanger 42 be dividing wall type heat exchanger, and the type heat exchanger shape is various, with low cost, uses extensive.For example, can be tube heat exchanger, such heat exchanger, for helical bundle designs, can increase turbulence effects to greatest extent, strengthens heat exchange efficiency.The asymmetrical design of inner shell and pipe layer, can enhance productivity greatly, cost-saving.In addition, the second heat exchanger 42 can be also mixed heat exchanger, and the rate of heat transfer of such heat exchanger is larger, and operating efficiency is fast.
Claims (5)
1. can control the formation system for the treatment of trough liquid in temperature constant state, it is characterized in that, comprise electrolysis tank (1), treatment trough (2), back pool (3), First Heat Exchanger (41), the second heat exchanger (42), the second circulating pump (52), the first electromagnetically operated valve (61) and the second electromagnetically operated valve (62), outlet after the cooling water heat exchange of described First Heat Exchanger (41) is connected with the hot water inlet of the second heat exchanger (42) by the first electromagnetically operated valve (61), the heat exchanger liquid import of the second heat exchanger (42) is connected with one end of the second circulating pump (52), the other end of the second circulating pump (52) is connected with the liquid outlet for the treatment of trough (2), outlet after the cooling water heat exchange of First Heat Exchanger (41) is also connected with one end of the second electromagnetically operated valve (62), the other end of the second electromagnetically operated valve (62) is connected with back pool (3), after the heat exchange of the second heat exchanger (42), water out is also connected with back pool (3), and the heat exchanger liquid outlet of the second heat exchanger (42) is connected with the liquid-inlet for the treatment of trough (2).
2. as claimed in claim 1ly can control the formation system for the treatment of trough liquid in temperature constant state, it is characterized in that, described the first electromagnetically operated valve (61) and the second electromagnetically operated valve (62) are direct-acting electromagnetic valve.
3. as claimed in claim 1ly can control the formation system for the treatment of trough liquid in temperature constant state, it is characterized in that, described the second heat exchanger (42) is dividing wall type heat exchanger.
4. as claimed in claim 3ly can control the formation system for the treatment of trough liquid in temperature constant state, it is characterized in that, described the second heat exchanger (42) is tube heat exchanger.
5. as claimed in claim 1ly can control the formation system for the treatment of trough liquid in temperature constant state, it is characterized in that, described the second heat exchanger (42) is mixed heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410299441.6A CN104112599A (en) | 2014-06-27 | 2014-06-27 | Formation system capable of controlling treatment tank liquid to be in constant temperature state |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410299441.6A CN104112599A (en) | 2014-06-27 | 2014-06-27 | Formation system capable of controlling treatment tank liquid to be in constant temperature state |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104112599A true CN104112599A (en) | 2014-10-22 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410299441.6A Pending CN104112599A (en) | 2014-06-27 | 2014-06-27 | Formation system capable of controlling treatment tank liquid to be in constant temperature state |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109004290A (en) * | 2018-08-10 | 2018-12-14 | 江苏海宝电池科技有限公司 | A kind of heavy-duty battery constant temperature formation system and its use technique |
| CN109518248A (en) * | 2019-01-07 | 2019-03-26 | 广西贺州市桂东电子科技有限责任公司 | A kind of cooling system and its working method of the power supply slot electrolyte of aluminum electrolysis capacitor anode aluminium foil chemical conversion |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05289756A (en) * | 1992-04-14 | 1993-11-05 | Canon Inc | Thermostatic heater |
| CN1978974A (en) * | 2005-11-29 | 2007-06-13 | 天津渤天化工有限责任公司 | Circulation ulitizing recovering pipe |
| CN201655559U (en) * | 2010-02-03 | 2010-11-24 | 横店集团东磁有限公司 | Thermal Energy Recycling Device for Electrode Foil Formation Equipment |
| CN202643915U (en) * | 2012-03-19 | 2013-01-02 | 苏州晶洲装备科技有限公司 | High precision groove body heat exchange system |
| CN203966840U (en) * | 2014-06-27 | 2014-11-26 | 四川石棉华瑞电子有限公司 | Formation system |
-
2014
- 2014-06-27 CN CN201410299441.6A patent/CN104112599A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05289756A (en) * | 1992-04-14 | 1993-11-05 | Canon Inc | Thermostatic heater |
| CN1978974A (en) * | 2005-11-29 | 2007-06-13 | 天津渤天化工有限责任公司 | Circulation ulitizing recovering pipe |
| CN201655559U (en) * | 2010-02-03 | 2010-11-24 | 横店集团东磁有限公司 | Thermal Energy Recycling Device for Electrode Foil Formation Equipment |
| CN202643915U (en) * | 2012-03-19 | 2013-01-02 | 苏州晶洲装备科技有限公司 | High precision groove body heat exchange system |
| CN203966840U (en) * | 2014-06-27 | 2014-11-26 | 四川石棉华瑞电子有限公司 | Formation system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109004290A (en) * | 2018-08-10 | 2018-12-14 | 江苏海宝电池科技有限公司 | A kind of heavy-duty battery constant temperature formation system and its use technique |
| CN109518248A (en) * | 2019-01-07 | 2019-03-26 | 广西贺州市桂东电子科技有限责任公司 | A kind of cooling system and its working method of the power supply slot electrolyte of aluminum electrolysis capacitor anode aluminium foil chemical conversion |
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| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB03 | Change of inventor or designer information |
Inventor after: Wang Weiguo Inventor after: Cha Hongfeng Inventor after: Gu Donghui Inventor before: Yan Qixu Inventor before: Chen Huachang Inventor before: Gu Donghui |
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| COR | Change of bibliographic data | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20141022 |