CN201655559U - Heat energy recycling device for electrode foil chemical device - Google Patents
Heat energy recycling device for electrode foil chemical device Download PDFInfo
- Publication number
- CN201655559U CN201655559U CN2010203021721U CN201020302172U CN201655559U CN 201655559 U CN201655559 U CN 201655559U CN 2010203021721 U CN2010203021721 U CN 2010203021721U CN 201020302172 U CN201020302172 U CN 201020302172U CN 201655559 U CN201655559 U CN 201655559U
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- water pipe
- heat exchanger
- tank liquor
- pipe
- circulating pump
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Abstract
The utility model discloses a heat energy recycling device for an electrode foil chemical device. A primary bath liquor heat exchange system is added on the heat exchange basis of the prior chemical recycling system; a primary heat exchanger and a pipeline are added on a treatment tank recycling system; and the temperature is controlled by a solenoid valve through adjusting a valve. Tank liquor adopts a secondary heat exchange system to not only solve the defect of primary cooling deficiency, but also extract hot water with the temperature of 70-75 DEG C by utilizing both circulating water as a cooling medium and reverse osmosis production water or mixed bed production water as another cyclic cooling medium. The hot water is utilized for thermal insulation of a treatment tank and heating of factories in winter, so that energy sources are recycled, thereby saving resources.
Description
Technical field
The utility model relates to electrode foil formation device circulating cooling system field, a kind of electrode foil formation device heat energy recycling device of more specifically saying so.
Background technology
Electrode foil is the main raw material(s) of aluminium electrolytic capacitor, is used to make the anode and the negative electrode of aluminium electrolytic capacitor.The anode aluminium foil of aluminium electrolytic capacitor (changing into paper tinsel), cathode aluminum foil are aluminum feedstock and process through multiple working procedure.When changing into, electrode foil to generate the oxide-film of aluminium oxide by electrochemical reaction on the corrosive aluminum foil surface, oxide-film plays the effect of capacitor medium, can produce a large amount of heats when in formation process, changing into, the temperature that becomes tank liquor for stabilisation is in technological temperature control, and the method that adopts was referring to as Fig. 1 in the past.
When the electrolytic bath liquid temp was controlled: the tank liquor temperature technological requirement was generally at 85 ± 4 ℃, originally system extracts tank liquor with circulating pump 11 from electrolytic bath 1, deliver to heat exchanger 12 through tank liquor pipe 3, heat exchanger 12 1 sides are being led to heat channel liquid always, logical recirculated water when opposite side is opened water pipe 5 according to recirculated water electromagnetically operated valve 13, by recirculated water the tank liquor heat is taken away, recirculated water electromagnetically operated valve 13 was opened when electrolytic bath 1 temperature was higher than design temperature, recirculated water is taken away the heat that changes into tank liquor by heat exchanger 12, when electrolytic bath 1 temperature is lower than design temperature, recirculated water electromagnetically operated valve 13 cuts out, there is not recirculated water to enter in the heat exchanger 12, change into tank liquor because aluminium foil carries out the electrochemical reaction heat release and progressively raises tank liquor to design temperature in groove, so circulation is gone down always, has guaranteed that tank liquor temperature fluctuates in the technological requirement scope.Sometimes tank liquor temperature is too high, and the first-class heat exchanger cooling does not reach requirement, can not drop to specified requirements to temperature and suffer with regard to having fed electrolytic bath again, so just having caused the cooling failure.The temperature of circulating hot water is generally about in the of 40 ℃ in addition, and a large amount of heats scatter and disappear by cooling tower, can not get reasonable utilization, have wasted ample resources.
The utility model content
The purpose of this utility model is to overcome prior art one-level heat-exchange system cooling and does not reach the deficiency of requirement, provide a kind of simple in structure, be easy to realize can satisfy the electrode foil formation device heat energy recycling device that cooling requires.
Another purpose of the present utility model is to overcome the deficiency that prior art is wasted cycle down warm water resource in a large number, providing a kind of utilizes the cycle down warm water to be incubated with factory with the treatment trough in the formation device to warm oneself the electrode foil formation device heat energy recycling device that the energy is utilized once more winter.
An also purpose of the present utility model is to overcome in the prior art treatment trough for keeping the deficiency that the needed tank liquor temperature of technology need add the heat waster resource in addition, providing a kind of utilizes the cycle down warm water to be incubated for it, Utilizing Energy Sources in Reason, the electrode foil formation device heat energy recycling device of environmental protection and saving resource.、
In order to reach above purpose, the utility model is to be achieved through the following technical solutions: a kind of electrode foil formation device heat energy recycling device, comprise electrolytic bath, treatment trough, circulating pump, heat exchanger, electromagnetically operated valve, tank liquor pipe and water pipe, electrolytic bath connects circulating pump one by the tank liquor pipe, circulating pump is connected back on the electrolytic bath by the tank liquor pipe again and again, the tank liquor pipe is provided with heat exchanger, also leads on the heat exchanger and establishes water pipe, is furnished with electromagnetically operated valve on the water pipe; Treatment trough connects circulating pump two by the tank liquor pipe, circulating pump two is connected back on the treatment trough by the tank liquor pipe again, it is characterized in that, be connected back at circulating pump one on the tank liquor pipe of electrolytic bath section and be sequentially with first-class heat exchanger and secondary heat exchanger, also logically on the first-class heat exchanger be provided with water pipe, be furnished with the one-level electromagnetically operated valve on the entrance point of this water pipe, the also logical water pipe that is provided with on the secondary heat exchanger, then be furnished with the two-stage electromagnetic valve on the entrance point of this water pipe, then be furnished with the sealing valve on the port of export;
Be connected back at circulating pump two on the tank liquor pipe of treatment trough section and be provided with three grades of heat exchangers, the also logical water pipe that is provided with on three grades of heat exchangers, the entrance point of this water pipe are connected on the port of export before the sealing valve on the water pipe on the secondary heat exchanger; Then be furnished with three grades of electromagnetically operated valves on the entrance point of the water pipe on three grades of heat exchangers.
Increase the heat exchange of one-level tank liquor on the circulatory system heat exchange basis in original changing into, on the treatment trough circulatory system, increased first-class heat exchanger and pipeline,, use the solenoid control temperature then by adjusting valve.
When the electrolytic bath liquid temp is controlled, the tank liquor temperature technological requirement is at 85 ± 4 ℃, when tank liquor temperature is raised to 86 ℃, the reverse osmosis of circulation or mixed bed produce a water backwater two-stage electromagnetic valve and open to changing into the tank liquor cooling, by the secondary heat exchanger that increases the water intensification is produced in the reverse osmosis of circulation or mixed bed simultaneously, output hot water, temperature can reach 70 ~ 75 ℃, the reverse osmosis of circulation or a mixed bed product water backwater two-stage electromagnetic valve are closed automatically when temperature is lower than 81 ℃, are heated up by the tank liquor electrochemical reaction.When indivedual tank liquor temperatures were raised to 89 ℃, recirculated water one-level electromagnetically operated valve was opened and is strengthened cooling, and when temperature was lower than 86 ℃, circulating water one-level closed electromagnetic valve guaranteed that the electrolytic bath liquid temp is in the technological requirement scope.
On the treatment trough circulation line, increase by one or three grades of heat exchangers, when tank liquor temperature is lower than processing tank liquor technological requirement temperature, for three grades of electromagnetically operated valves of treatment trough heating open-minded, for treatment trough heats up, when being higher than the technological requirement temperature, three grades of electromagnetically operated valves cut out automatically, reach the purpose of treatment trough temperature in the technological requirement scope.
The hot water of exporting in the secondary heat exchanger is except providing thermal source for the insulation of processing tank liquor, can also provide high-temperature-hot-water for factory's winter heating, promptly can reach in the circulatory system to utilize and change into the purpose of heat energy as long as be linked into heating, save the expense of the heating fire coal etc. in winter for factory's heating.
As preferably, the import and export two ends of the water pipe on described three grades of heat exchangers order respectively are connected on the port of export of the water pipe on the secondary heat exchanger, and a sealing valve is set on the water pipe section of the secondary heat exchanger between these two ends.
Need lower the temperature at electrolytic bath and to open under the two-stage electromagnetic valve condition, when needs heated up to treatment trough, the sealing valve cut out, and three grades of electromagnetically operated valves are open-minded, reverse osmosis of having heated in secondary heat exchanger or mixed bed produce a water backwater, flow into to heat up in three grades of heat exchangers the treatment trough tank liquor.When not needing to heat up, close three grades of electromagnetically operated valves, open the sealing valve.
As preferably, the water pipe current turnover on the secondary heat exchanger flow to first-class heat exchanger on the turnover of water pipe current flow to and be rightabout.
As preferably, the water pipe current turnover on the secondary heat exchanger flow to first-class heat exchanger on the turnover of water pipe current flow to and be equidirectional.
The beneficial effects of the utility model: increase the heat exchange of one-level tank liquor on the circulatory system heat exchange basis in original changing into, on the treatment trough circulatory system, increased first-class heat exchanger and pipeline,, use the solenoid control temperature then by adjusting valve.Tank liquor is taked the secondary heat-exchange system, not only can reach the not enough shortcoming of one-level cooling, and can utilize except recirculated water as the coolant, produce water as another set of circulation cooling medium by reverse osmosis produced water or mixed bed again, extract 70 ~ 75 ℃ of hot water, utilize hot water to warm oneself winter for treatment trough is incubated with factory, the energy is utilized once more, has saved resource.
Description of drawings
Fig. 1 is the structural representation of prior art formation device;
Fig. 2 is a structural representation of the present utility model.
Embodiment
Below in conjunction with accompanying drawing and specific embodiment the utility model is further described.
Embodiment 1: as shown in Figure 2, a kind of electrode foil formation device heat energy recycling device, comprise electrolytic bath 1, treatment trough 2, circulating pump, heat exchanger, electromagnetically operated valve, tank liquor pipe 3 and water pipe 5, electrolytic bath 1 connects circulating pump 1 by tank liquor pipe 3, circulating pump 1 is connected back on the electrolytic bath 1 by tank liquor pipe 3 again, tank liquor pipe 3 is provided with heat exchanger, also leads on the heat exchanger and establishes water pipe 5, is furnished with electromagnetically operated valve on the water pipe 5.Treatment trough 2 connects circulating pump 2 21 by tank liquor pipe 3, and circulating pump 2 21 is connected back on the treatment trough 2 by tank liquor pipe 3 again,
Increase the heat exchange of one-level tank liquor in order to strengthen lowering the temperature on the circulatory system heat exchange basis in original changing into, by being sequentially with first-class heat exchanger 12 and secondary heat exchanger 14 on the tank liquor pipe 3 that is connected back to 1 section of electrolytic bath at circulating pump 1, the also logical water pipe 5 that is provided with on the first-class heat exchanger 12, be furnished with one-level electromagnetically operated valve 13 on the entrance point of this water pipe 5, the also logical water pipe 5 that is provided with on the secondary heat exchanger 14, then be furnished with two-stage electromagnetic valve 13 on the entrance point of this water pipe 5, then be furnished with sealing valve 4 on the port of export.The water pipe 5 current turnover flow direction on the secondary heat exchanger 14 flows to the water pipe 5 current turnover on the first-class heat exchanger 12 and is rightabout.
Utilize the hot water treatment tank liquor insulation of exporting in the secondary heat exchanger in order to save resource saving production cost, by being provided with three grades of heat exchangers 22 on the tank liquor pipe 3 that is connected back to 2 sections of treatment troughs at circulating pump 2 21, the also logical water pipe 5 that is provided with on three grades of heat exchangers 22, the entrance point of this water pipe 5 are connected on the port of export before the sealing valve 4 on the water pipe 5 on the secondary heat exchanger 14; Then be furnished with three grades of electromagnetically operated valves 23 on the entrance point of the water pipe 5 on three grades of heat exchangers 22.
Embodiment 2: as shown in Figure 2, the import and export two ends of the water pipe 5 on three grades of heat exchangers 22 order respectively are connected on the port of export of the water pipe 5 on the secondary heat exchanger 14, on 5 sections in the water pipe of the secondary heat exchanger between these two ends 14 a sealing valve 4 are set.All the other are with embodiment 1.
Embodiment 3: the water pipe 5 current turnover flow direction on the secondary heat exchanger 14 flows to the water pipe 5 current turnover on the first-class heat exchanger 12 and is equidirectional.All the other are with embodiment 2.
In the use: when the electrolytic bath liquid temp is controlled, the tank liquor temperature technological requirement is at 85 ± 4 ℃, when tank liquor temperature is raised to 86 ℃, the reverse osmosis of circulation or mixed bed produce a water backwater two-stage electromagnetic valve and open to changing into the tank liquor cooling, by the secondary heat exchanger that increases the water intensification is produced in the reverse osmosis of circulation or mixed bed simultaneously, output hot water, temperature can reach 70 ~ 75 ℃, the reverse osmosis of circulation or a mixed bed product water backwater two-stage electromagnetic valve are closed automatically when temperature is lower than 81 ℃, are heated up by the tank liquor electrochemical reaction.When indivedual tank liquor temperatures were raised to 89 ℃, recirculated water one-level electromagnetically operated valve was opened and is strengthened cooling, and when temperature was lower than 86 ℃, circulating water one-level closed electromagnetic valve guaranteed that the electrolytic bath liquid temp is in the technological requirement scope.
Need lower the temperature at electrolytic bath and to open under the two-stage electromagnetic valve condition, the treatment trough temperature is generally below 70 ℃ in the formation device, for keeping the needed tank liquor temperature of technology, when needs heat up to treatment trough, the sealing valve cuts out, three grades of electromagnetically operated valves are open-minded, and reverse osmosis of having heated in secondary heat exchanger or mixed bed produce a water backwater, flow into and heat up in three grades of heat exchangers the treatment trough tank liquor.When not needing to heat up, close three grades of electromagnetically operated valves, open the sealing valve.
Claims (2)
1. electrode foil formation device heat energy recycling device, comprise electrolytic bath, treatment trough, circulating pump, heat exchanger, electromagnetically operated valve, tank liquor pipe and water pipe, electrolytic bath connects circulating pump one by the tank liquor pipe, circulating pump is connected back on the electrolytic bath by the tank liquor pipe again and again, the tank liquor pipe is provided with heat exchanger, also lead on the heat exchanger and establish water pipe, be furnished with electromagnetically operated valve on the water pipe; Treatment trough connects circulating pump two by the tank liquor pipe, circulating pump two is connected back on the treatment trough by the tank liquor pipe again, it is characterized in that, be connected back at circulating pump one (11) on the tank liquor pipe (3) of electrolytic bath (1) section and be sequentially with first-class heat exchanger (12) and secondary heat exchanger (14), the also logical water pipe (5) that is provided with on the first-class heat exchanger (12), be furnished with one-level electromagnetically operated valve (13) on the entrance point of this water pipe (5), the also logical water pipe (5) that is provided with on the secondary heat exchanger (14), then be furnished with two-stage electromagnetic valve (13) on the entrance point of this water pipe (5), then be furnished with sealing valve (4) on the port of export;
Be connected back at circulating pump two (21) on the tank liquor pipe (3) of treatment trough (2) section and be provided with three grades of heat exchangers (22), the also logical water pipe (5) that is provided with on three grades of heat exchangers (22), the entrance point of this water pipe (5) are connected on the preceding port of export of sealing valve (4) on the water pipe (5) on the secondary heat exchanger (14); Then be furnished with three grades of electromagnetically operated valves (23) on the entrance point of the water pipe (5) on three grades of heat exchangers (22).
2. electrode foil formation device heat energy recycling device according to claim 1, it is characterized in that, the import and export two ends of the water pipe (5) on described three grades of heat exchangers (22) order respectively are connected on the port of export of the water pipe (5) on the secondary heat exchanger (14), on water pipe (5) section of the secondary heat exchanger between these two ends (14) a sealing valve (4) are set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010203021721U CN201655559U (en) | 2010-02-03 | 2010-02-03 | Heat energy recycling device for electrode foil chemical device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010203021721U CN201655559U (en) | 2010-02-03 | 2010-02-03 | Heat energy recycling device for electrode foil chemical device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201655559U true CN201655559U (en) | 2010-11-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010203021721U Expired - Fee Related CN201655559U (en) | 2010-02-03 | 2010-02-03 | Heat energy recycling device for electrode foil chemical device |
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| CN (1) | CN201655559U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104109890A (en) * | 2014-07-11 | 2014-10-22 | 四川石棉华瑞电子有限公司 | Formation line tank liquor preheating and consumption-reduction system and formation line tank liquor preheating and consumption-reduction method |
| CN104112599A (en) * | 2014-06-27 | 2014-10-22 | 四川石棉华瑞电子有限公司 | Formation system capable of controlling treatment tank liquid to be in constant temperature state |
| CN105977060A (en) * | 2016-06-29 | 2016-09-28 | 宝兴县剑锋制箔电子有限公司 | Device for utilizing heat of electrode foil production line |
| 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 |
-
2010
- 2010-02-03 CN CN2010203021721U patent/CN201655559U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104112599A (en) * | 2014-06-27 | 2014-10-22 | 四川石棉华瑞电子有限公司 | Formation system capable of controlling treatment tank liquid to be in constant temperature state |
| CN104109890A (en) * | 2014-07-11 | 2014-10-22 | 四川石棉华瑞电子有限公司 | Formation line tank liquor preheating and consumption-reduction system and formation line tank liquor preheating and consumption-reduction method |
| CN104109890B (en) * | 2014-07-11 | 2017-04-12 | 四川石棉华瑞电子有限公司 | Formation line tank liquor preheating and consumption-reduction system and formation line tank liquor preheating and consumption-reduction method |
| CN105977060A (en) * | 2016-06-29 | 2016-09-28 | 宝兴县剑锋制箔电子有限公司 | Device for utilizing heat of electrode foil production line |
| 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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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101124 Termination date: 20150203 |
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| EXPY | Termination of patent right or utility model |