CN109509926A - Sour cycle battery formation device and method - Google Patents
Sour cycle battery formation device and method Download PDFInfo
- Publication number
- CN109509926A CN109509926A CN201811552124.5A CN201811552124A CN109509926A CN 109509926 A CN109509926 A CN 109509926A CN 201811552124 A CN201811552124 A CN 201811552124A CN 109509926 A CN109509926 A CN 109509926A
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- acid
- acid solution
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- tank
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- 238000000034 method Methods 0.000 title claims abstract description 21
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 16
- 239000002253 acid Substances 0.000 claims abstract description 372
- 238000001816 cooling Methods 0.000 claims abstract description 52
- 238000001514 detection method Methods 0.000 claims abstract description 18
- 238000011897 real-time detection Methods 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 10
- 238000009423 ventilation Methods 0.000 claims description 6
- 125000004122 cyclic group Chemical group 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 230000002194 synthesizing effect Effects 0.000 claims description 3
- 238000011017 operating method Methods 0.000 claims 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/44—Methods for charging or discharging
- H01M10/446—Initial charging measures
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/12—Construction or manufacture
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/4214—Arrangements for moving electrodes or electrolyte
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Abstract
The invention discloses sour cycle battery formation device and method, which includes acid solution storage device, the acid solution conveying circulatory system, acid solution cooling system, acid solution detection system, charging system and electric control system；Storage of the acid solution storage device for complex acid and acid solution；Acid solution detection system is arranged in acid solution storage device, is used for real-time detection acid solution；The acid solution cooling system is arranged in acid solution transportation system, for reducing the temperature of acid solution；The acid solution conveying circulatory system is used to the acid solution in acid solution storage device being transported to charging system；Several motor-driven valves are provided in the acid solution conveying circulatory system, the switch and flow of motor-driven valve are controlled by electric control system；The charging system is connect by connector with battery to be charged.This method includes preparing low-density acid, low-density acid circulation, switching to high-density acid, charging and shutdown.The present invention, system pipes are short out, and modulation acid solution is quick, and charging is stablized.
Description
Technical field
The present invention relates to sour cycle battery formation device and methods, belong to battery charging equipment technical field.
Background technique
Lead-acid accumulator is liked, still, lead acid battery charge process is skill extensively because its is competitively priced by market
Art core, traditional lead-acid accumulator in charging, need to expend a large amount of water and acid solution to be allocated as individual workshop complete
At deployed to be pipelined to charging system again, pipeline is long, and it is technical problem that the parameter of acid solution, which cannot accurately control,.
Summary of the invention
To solve the above problems, the invention discloses a kind of sour cycle battery formation device and method, tools
Body technique scheme is as follows:
Sour cycle battery formation device, including acid solution storage device, acid solution the conveying circulatory system, acid solution cooling system, acid solution inspection
Examining system, charging system and electric control system；
Storage of the acid solution storage device for complex acid and acid solution；
The acid solution detection system is arranged in acid solution storage device, is used for real-time detection acid solution；
The acid solution cooling system is arranged in acid solution transportation system, for reducing the temperature of acid solution；
The acid solution conveying circulatory system is used to the acid solution in acid solution storage device being transported to charging system；
Several motor-driven valves are provided in the acid solution conveying circulatory system, the switch of motor-driven valve is controlled by electric control system
And flow；
The charging system is connect by connector with battery to be charged.
It further include filter；
The acid solution storage device includes low-density acid tank and high density acid tank, and the low-density acid tank and high density acid tank connect
It is connected to pure water water inlet pipe and concentrated acid inlet tube, pure water water inlet pipe and concentrated acid inlet tube are provided with hand-operated valve, the low-density acid
Slot and high density acid tank are connect with time acid tube road, for being received back acid；The low-density acid tank and high density acid tank with into
Acid tube road connection, for prepared acid solution to be conveyed to acid inlet tube, the effluent conduit and filter of the low-density acid tank
The connection of downstream pipeline, the upstream end pipeline of the effluent conduit of high density acid tank and filter connects, and final and into acid
Pipeline connection.
The acid solution cooling system includes blower and cooling tower, and the blower is dried towards cooling tower, and cooling tower is under
Portion offers ventilation opening；
It is connected with tee tube after the effluent conduit of the low-density acid tank and the effluent conduit confluence of high density acid tank, tee tube
One end is connect with acid inlet tube, and the pipeline that the other end connects out is connect with cooling tower, and the bottom of cooling tower is arrived by pipeline shunt
Low-density acid tank and high density acid tank, and be respectively arranged in the connecting pipe of low-density acid tank and high density acid tank it is electronic
Valve.
The acid solution detection system includes that low-density acid tank and the temperature-detecting device in high density acid tank, density is arranged in
Detection device and liquid level detection device.
Acid fog removing device is additionally provided in the low-density acid tank and high density acid tank.
Acid-proof pump is provided on pipeline between the filter and high density acid tank.
Sour cycle battery chemical synthesizing method, this method are walked based on above-mentioned sour cycle battery formation device, including following operation
It is rapid:
Step 1: preparing low-density acid: opening blower, cooling tower is in ventilation operation state, pure water valve is opened, towards low-density
Pure water is injected in acid tank, after water filling, closes pure water valve, opens low sour acid return valve, goes back to acid tube road towards in low-density acid tank
Acid solution is conveyed, acid pump is opened, the liquid circulation in acid tube road and low-density acid tank is flowed, reaches dynamic equilibrium, then open
Concentrated acid valve, towards injecting concentrated acid in low-density acid tank, in modulated process, dynamic between the liquid and cooling tower in low-density acid tank
Flowing, when acid solution is modulated to scheduled concentration and temperature, closing concentrated acid valve, and the pipeline connecting with cooling tower；
Step 2: low acid circulation: after acid solution prepares, closing all go back to acid tube roads being connected to low-density acid tank, open low-density acid
The low acid of slot goes out sour valve, conveys prepared acid solution towards acid inlet tube；
Step 3: low-density acid cyclic switching high-density acid circulation: closing the pump in the acid solution conveying circulatory system, close low-density
Acid tank goes out sour valve, after the acid solution conveying circulatory system is stablized, closes the acid return valve of low-density acid tank, opens high density acid tank
Acid return valve and go out sour valve, open the pump in the acid solution conveying circulatory system, recycle acid solution in high-density acid's system, and with it is cold
But tower is connected, and is closed after high-density acid reaches estimated concentration and temperature according to the preparation of the completion high-density acid of step 1
All towards the valve being infused in high-density acid, that opens high density acid tank goes out sour valve, conveys towards acid inlet tube prepared
Acid solution；
Step 4: charging: high-density acid for acid, realizes dynamic equilibrium to charger dynamic, charger by connector be plugged on to
On rechargeable battery；
Step 5: shut down: after battery is fully charged, charger is shut down, and closes the pump and highly dense in the acid solution conveying circulatory system
That spends acid tank goes out sour valve, if the acid solution conveying circulatory system is connected to cooling tower, the liquid valve of cooling tower is closed at this time, so that acid solution
The conveying circulatory system is in close state and high density acid tank is in close state.
The working principle of the invention is:
The present invention realizes the modulation and conveying of acid solution, charges to lead-acid battery, in acid solution modulated process and acid solution is defeated
It send in cyclic process, lowers the temperature of acid solution by acid solution cooling system.
The beneficial effects of the present invention are:
The present invention, pipeline connection relationship is clearly brief, realizes that low-density acid is prepared and high-density acid prepares public same set of acid solution
The conveying circulatory system and acid solution cooling system, pipeline and equipment are more saved, and occupied area and hall space are saved.
Detailed description of the invention
Fig. 1 is connection status figure of the invention,
Appended drawing reference: 1-- blower, 2-filters, 3-acid-proof pumps.
Specific embodiment
With reference to the accompanying drawings and detailed description, the present invention is furture elucidated.It should be understood that following specific embodiments are only
For illustrating the present invention rather than limiting the scope of the invention.
This acid cycle battery formation device, including acid solution storage device, acid solution conveying the circulatory system, acid solution cooling system,
Acid solution detection system, charging system and electric control system；Storage of the acid solution storage device for complex acid and acid solution；
The acid solution detection system is arranged in acid solution storage device, is used for real-time detection acid solution；The acid solution cooling system setting exists
In acid solution transportation system, for reducing the temperature of acid solution；The acid solution conveying circulatory system is used for will be in acid solution storage device
Acid solution is transported to charging system；Several motor-driven valves are provided in the acid solution conveying circulatory system, pass through electric control system
Control the switch and flow of motor-driven valve；The charging system is connect by connector with battery to be charged.
Fig. 1 is connection status figure of the invention, in conjunction with attached drawing as it can be seen that the invention also includes filters 2；Filter 2 is used for
High-density acid's filtration cycle will be come from.
The acid solution storage device includes low-density acid tank and high density acid tank, the low-density acid tank and high density acid tank
It is respectively connected with pure water water inlet pipe and concentrated acid inlet tube, pure water water inlet pipe and concentrated acid inlet tube are provided with hand-operated valve, described low close
Degree acid tank and high density acid tank are connect with time acid tube road, for being received back acid；The low-density acid tank and high density acid tank are equal
It is connect with acid inlet tube, for prepared acid solution to be conveyed to acid inlet tube, the effluent conduit and mistake of the low-density acid tank
The downstream pipeline of filter 2 connects, and the effluent conduit of high density acid tank is connect with the upstream end pipeline of filter 2, and final equal
It is connect with acid inlet tube.
The acid solution cooling system includes blower 1 and cooling tower, and the blower 1 is dried towards cooling tower, and cooling tower is close
Lower part offers ventilation opening.Blower 1 realizes air cooling towards drying in cooling tower.
Tee tube, threeway are connected with after the effluent conduit of the low-density acid tank and the effluent conduit confluence of high density acid tank
One end of pipe is connect with acid inlet tube, and the pipeline that the other end connects out is connect with cooling tower, and the bottom of cooling tower passes through pipeline point
Flow to low-density acid tank and high density acid tank, and be respectively arranged in the connecting pipe of low-density acid tank and high density acid tank
Electrically operated valve.
The acid solution detection system includes that low-density acid tank and the temperature-detecting device in high density acid tank, density is arranged in
Detection device and liquid level detection device.As specific embodiment, temperature-detecting device can be acidproof thermometer, be inserted in correspondence
Low-density acid tank and high density acid tank in, device for detecting density be acidproof sour Density Detection meter, liquid level detection device be peace
Mounted in corresponding low-density acid tank and high density acid tank close to the liquidometer of bottom, liquidometer is detected by pressure value apart from liquid
The height in face.And temperature-detecting device, device for detecting density and liquid level detection device are by being wiredly connected to computer or operation
The mode of system or wireless transmission is sent to corresponding operation interface in computer or operating system, related with corresponding software
Connection, is arranged its parameter area in software.
Acid fog removing device is additionally provided in the low-density acid tank and high density acid tank.Acid fog removing device can be existing
The acid fog removing device of any one acid corrosion-resistant, or Patent No.: the disclosed acid mist dress out of CN201610625340.2
It sets.
Acid-proof pump 3 is provided on pipeline between the filter 2 and high density acid tank.It will be of the invention by acid-proof pump 3
Acid solution in pipeline quickly circulates.
In conjunction with attached drawing as it can be seen that providing a specific embodiment of the invention, the specific connection relationship of the embodiment are as follows:
Low-density acid tank is connected with pure water water inlet pipe and concentrated acid inlet tube, is provided with valve NV4 on the pure water water inlet pipe, the concentrated acid
Valve NV3 is provided on inlet tube.There are twice to go back to acid tube road to connect with low-density acid tank, one of them returns on acid tube road and is provided with
Valve PV8 is provided with valve PV6 on another time acid tube road, and low-density acid tank is equipped with two liquid outlet pipes, wherein a connection
To the downstream of filter, it is provided with valve PV10 on the pipeline, another is connected to the liquid outlet pipe of high density acid tank, is located at
The upstream end of filter is provided with valve PV1 on the pipeline, is provided with by the part that the pipeline of filter is connected to cooling tower
Valve PV3, or it is directly connected to input duct.
High density acid tank is connected with pure water water inlet pipe and concentrated acid inlet tube, is provided with valve NV1 on the pure water water inlet pipe, should
Valve NV2 is provided on concentrated acid inlet tube.There are twice to go back to acid tube road to connect with high density acid tank, one of them returns on acid tube road and sets
It is equipped with valve PV7, is provided with valve PV9 on another time acid tube road.High density acid tank has an output channel, the output channel
It is provided with valve PV2, which is connected to acid-proof pump, and the downstream of acid-proof pump is connected to filter.
Acid solution is from the inlet close to cooling tower top towards cooling tower internal spray, and blower is dried towards cooling tower, wind
Side wall from cooling tower close to lower part is gone out, and acid solution after cooling is picked out from cooling tower bottom by pipeline, passes through pipeline respectively
It is connected to bottom density acid tank and high density acid tank, is connected on the pipeline of bottom density acid tank and is provided with valve PV5, is connected to highly dense
It spends on the pipeline of acid tank and is provided with valve PV4.
Valve PV1 ~ equal the motor-driven valve of valve PV10, valve NV1 ~ valve NV4 is hand-operated valve.Motor-driven valve is by electrical control system
System control, hand-operated valve are opened or closed manually by operator.
Sour cycle battery chemical synthesizing method, this method are walked based on above-mentioned sour cycle battery formation device, including following operation
It is rapid:
Step 1: preparing low-density acid: opening blower, cooling tower is in ventilation operation state, pure water valve is opened, towards low-density
Pure water is injected in acid tank, after water filling, closes pure water valve, opens low sour acid return valve, goes back to acid tube road towards in low-density acid tank
Acid solution is conveyed, acid pump is opened, the liquid circulation in acid tube road and low-density acid tank is flowed, reaches dynamic equilibrium, then open
Concentrated acid valve, towards injecting concentrated acid in low-density acid tank, in modulated process, dynamic between the liquid and cooling tower in low-density acid tank
Flowing, when acid solution is modulated to scheduled concentration and temperature, closing concentrated acid valve, and the pipeline connecting with cooling tower；
Step 2: low acid circulation: after acid solution prepares, closing all go back to acid tube roads being connected to low-density acid tank, open low-density acid
The low acid of slot goes out sour valve, conveys prepared acid solution towards acid inlet tube；
Step 3: low-density acid cyclic switching high-density acid circulation: closing the pump in the acid solution conveying circulatory system, close low-density
Acid tank goes out sour valve, after the acid solution conveying circulatory system is stablized, closes the acid return valve of low-density acid tank, opens high density acid tank
Acid return valve and go out sour valve, open the pump in the acid solution conveying circulatory system, recycle acid solution in high-density acid's system, and with it is cold
But tower is connected, and is closed after high-density acid reaches estimated concentration and temperature according to the preparation of the completion high-density acid of step 1
All towards the valve being infused in high-density acid, that opens high density acid tank goes out sour valve, conveys towards acid inlet tube prepared
Acid solution；
Step 4: charging: high-density acid for acid, realizes dynamic equilibrium to charger dynamic, charger by connector be plugged on to
On rechargeable battery；
Step 5: shut down: after battery is fully charged, charger is shut down, and closes the pump and highly dense in the acid solution conveying circulatory system
That spends acid tank goes out sour valve, if the acid solution conveying circulatory system is connected to cooling tower, the liquid valve of cooling tower is closed at this time, so that acid solution
The conveying circulatory system is in close state and high density acid tank is in close state.
This method charges applied to battery, realizes safety and stability quick charge.Pipeline connection is simple, avoids workshop pipeline mistake
In redundancy, maintenance difficult is caused, increases operating cost.
The technical means disclosed in the embodiments of the present invention is not limited to the technical means disclosed in the above technical means, and further includes
Technical solution consisting of any combination of the above technical features.
Taking the above-mentioned ideal embodiment according to the present invention as inspiration, through the above description, relevant staff is complete
Various changes and amendments can be carried out without departing from the scope of the technological thought of the present invention' entirely.The technology of this invention
Property range is not limited to the contents of the specification, it is necessary to which the technical scope thereof is determined according to the scope of the claim.
Claims (7)
1. sour cycle battery formation device, it is characterised in that including acid solution storage device, the acid solution conveying circulatory system, acid solution cooling
System, acid solution detection system, charging system and electric control system；
Storage of the acid solution storage device for complex acid and acid solution；
The acid solution detection system is arranged in acid solution storage device, is used for real-time detection acid solution；
The acid solution cooling system is arranged in acid solution transportation system, for reducing the temperature of acid solution；
The acid solution conveying circulatory system is used to the acid solution in acid solution storage device being transported to charging system；
Several motor-driven valves are provided in the acid solution conveying circulatory system, the switch of motor-driven valve is controlled by electric control system
And flow；
The charging system is connect by connector with battery to be charged.
2. acid cycle battery formation device according to claim 1, it is characterised in that further include filter；
The acid solution storage device includes low-density acid tank and high density acid tank, and the low-density acid tank and high density acid tank connect
It is connected to pure water water inlet pipe and concentrated acid inlet tube, pure water water inlet pipe and concentrated acid inlet tube are provided with hand-operated valve, the low-density acid
Slot and high density acid tank are connect with time acid tube road, for being received back acid；The low-density acid tank and high density acid tank with into
Acid tube road connection, for prepared acid solution to be conveyed to acid inlet tube, the effluent conduit and filter of the low-density acid tank
The connection of downstream pipeline, the upstream end pipeline of the effluent conduit of high density acid tank and filter connects, and final and into acid
Pipeline connection.
3. acid cycle battery formation device according to claim 1, it is characterised in that the acid solution cooling system includes wind
Machine and cooling tower, the blower are dried towards cooling tower, and cooling tower offers ventilation opening close to lower part；
It is connected with tee tube after the effluent conduit of the low-density acid tank and the effluent conduit confluence of high density acid tank, tee tube
One end is connect with acid inlet tube, and the pipeline that the other end connects out is connect with cooling tower, and the bottom of cooling tower is arrived by pipeline shunt
Low-density acid tank and high density acid tank, and be respectively arranged in the connecting pipe of low-density acid tank and high density acid tank it is electronic
Valve.
4. acid cycle battery formation device according to claim 1, it is characterised in that the acid solution detection system includes setting
Set temperature-detecting device, device for detecting density and liquid level detection device in low-density acid tank and high density acid tank.
5. acid cycle battery formation device according to claim 1, it is characterised in that the low-density acid tank and high density
Acid fog removing device is additionally provided in acid tank.
6. acid cycle battery formation device according to claim 1, it is characterised in that the filter and high density acid tank
Between pipeline on be provided with acid-proof pump.
7. sour cycle battery chemical synthesizing method, it is characterised in that this method is based on sour cycle battery described in any of the above-described claim
Formation device, including following operating procedure:
Step 1: preparing low-density acid: opening blower, cooling tower is in ventilation operation state, pure water valve is opened, towards low-density
Pure water is injected in acid tank, after water filling, closes pure water valve, opens low sour acid return valve, goes back to acid tube road towards in low-density acid tank
Acid solution is conveyed, acid pump is opened, the liquid circulation in acid tube road and low-density acid tank is flowed, reaches dynamic equilibrium, then open
Concentrated acid valve, towards injecting concentrated acid in low-density acid tank, in modulated process, dynamic between the liquid and cooling tower in low-density acid tank
Flowing, when acid solution is modulated to scheduled concentration and temperature, closing concentrated acid valve, and the pipeline connecting with cooling tower；
Step 2: low acid circulation: after acid solution prepares, closing all go back to acid tube roads being connected to low-density acid tank, open low-density acid
The low acid of slot goes out sour valve, conveys prepared acid solution towards acid inlet tube；
Step 3: low-density acid cyclic switching high-density acid circulation: closing the pump in the acid solution conveying circulatory system, close low-density
Acid tank goes out sour valve, after the acid solution conveying circulatory system is stablized, closes the acid return valve of low-density acid tank, opens high density acid tank
Acid return valve and go out sour valve, open the pump in the acid solution conveying circulatory system, recycle acid solution in high-density acid's system, and with it is cold
But tower is connected, and is closed after high-density acid reaches estimated concentration and temperature according to the preparation of the completion high-density acid of step 1
All towards the valve being infused in high-density acid, that opens high density acid tank goes out sour valve, conveys towards acid inlet tube prepared
Acid solution；
Step 4: charging: high-density acid for acid, realizes dynamic equilibrium to charger dynamic, charger by connector be plugged on to
On rechargeable battery；
Step 5: shut down: after battery is fully charged, charger is shut down, and closes the pump and highly dense in the acid solution conveying circulatory system
That spends acid tank goes out sour valve, if the acid solution conveying circulatory system is connected to cooling tower, the liquid valve of cooling tower is closed at this time, so that acid solution
The conveying circulatory system is in close state and high density acid tank is in close state.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811552124.5A CN109509926A (en) | 2018-12-19 | 2018-12-19 | Sour cycle battery formation device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811552124.5A CN109509926A (en) | 2018-12-19 | 2018-12-19 | Sour cycle battery formation device and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109509926A true CN109509926A (en) | 2019-03-22 |
Family
ID=65753570
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811552124.5A Pending CN109509926A (en) | 2018-12-19 | 2018-12-19 | Sour cycle battery formation device and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109509926A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203339267U (en) * | 2013-06-03 | 2013-12-11 | 淄博火炬能源有限责任公司 | Full-automatic acid circulating equipment for inner formation of pregnant solution type lead-acid storage battery |
| CN103972593A (en) * | 2014-05-23 | 2014-08-06 | 江苏三环实业股份有限公司 | Acid mixing box for lead-acid storage battery formation system |
| CN105140555A (en) * | 2015-08-31 | 2015-12-09 | 山东圣阳电源股份有限公司 | Container formation system for storage battery acid circulation |
| CN106611883A (en) * | 2015-10-26 | 2017-05-03 | 张家港市益成机械有限公司 | Acid circulation device for lead-acid storage battery internal formation |
| CN209344267U (en) * | 2018-12-19 | 2019-09-03 | 扬州金快乐电源有限公司 | Sour cycle battery formation device |
-
2018
- 2018-12-19 CN CN201811552124.5A patent/CN109509926A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203339267U (en) * | 2013-06-03 | 2013-12-11 | 淄博火炬能源有限责任公司 | Full-automatic acid circulating equipment for inner formation of pregnant solution type lead-acid storage battery |
| CN103972593A (en) * | 2014-05-23 | 2014-08-06 | 江苏三环实业股份有限公司 | Acid mixing box for lead-acid storage battery formation system |
| CN105140555A (en) * | 2015-08-31 | 2015-12-09 | 山东圣阳电源股份有限公司 | Container formation system for storage battery acid circulation |
| CN106611883A (en) * | 2015-10-26 | 2017-05-03 | 张家港市益成机械有限公司 | Acid circulation device for lead-acid storage battery internal formation |
| CN209344267U (en) * | 2018-12-19 | 2019-09-03 | 扬州金快乐电源有限公司 | Sour cycle battery formation device |
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