CN102136607A - Forming system in lead-acid accumulator - Google Patents
Forming system in lead-acid accumulator Download PDFInfo
- Publication number
- CN102136607A CN102136607A CN2011100353739A CN201110035373A CN102136607A CN 102136607 A CN102136607 A CN 102136607A CN 2011100353739 A CN2011100353739 A CN 2011100353739A CN 201110035373 A CN201110035373 A CN 201110035373A CN 102136607 A CN102136607 A CN 102136607A
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- China
- Prior art keywords
- acid
- diluted acid
- peracid
- jar
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- 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
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- 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
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- Filling, Topping-Up Batteries (AREA)
- Secondary Cells (AREA)
Abstract
The invention belongs to the production field of lead-acid accumulators, in particular to a forming system in a lead-acid accumulator. The forming system in the lead-acid accumulator is characterized by comprising a high-level diluted acid tank, a high-level peracid tank, a low-level diluted acid tank and a low-level peracid tank, wherein the low-level diluted acid tank is connected with the high-level diluted acid tank through a low-level diluted acid pump; the low-level peracid tank is connected with the high-level peracid tank through a low-level peracid pump; the high-level diluted acid tank is connected with an acid feeding device, an acid returning device is connected with the low-level diluted acid tank, the acid feeding device and the diluted acid device are arranged on a bracket, a diluted acid discharging pipeline is provided with a circuit converter and an diluted acid converter valve, and a concentrated acid converter valve is arranged on a diluted acid feeding pipeline. A one-unit-two-path mode is adopted in the invention, and the forming system has the advantages of high efficiency and short time of the accumulator, good battery pack consistency and improved battery performance in the forming process.
Description
Technical field
The invention belongs to lead acid accumulator production field, be specifically related to a kind of lead acid accumulator and be internalized into system.
Background technology
At present, domestic lead acid accumulator tradition forming technology is to adopt common slot type to change into, and the battery case that slot type changes into is open, battery acid mist and hydrogen in formation process constantly overflow, the perverse nose of acid mist in the whole worker-house, environmental pollution is big, and it is healthy to have a strong impact on the operator.Simultaneously the density of electrolyte in each battery case is inconsistent in formation process, and it is inconsistent to cause pole plate in each groove to change into the degree of depth, makes the consistency of battery bad.
In addition, abroad, European market especially, because the environmental requirement strictness, most of battery that adopts is internalized into technology.But external battery is internalized into the equipment price costliness, and production technology can not satisfy the ordinary production requirement in this territory, the battery performance of the bigger domestic storage battery of influence.
Summary of the invention
Technical problem to be solved by this invention is to improve the problem of environmental pollution that former slot type changes into, by adjusting chemical synthesis technology, improved the operating efficiency that storage battery is produced, simultaneously because the electrolyte temperature of acid circulation is consistent with density, improve the consistency of battery, improved battery performance.
The following technical scheme of the concrete employing of the present invention:
A kind of lead acid accumulator is internalized into system, it is characterized in that, comprise high-order diluted acid jar, high-order peracid jar, low level diluted acid jar, low level peracid jar, low level diluted acid jar is connected with high-order diluted acid jar by low level diluted acid pump, and low level peracid jar is connected with high-order peracid jar by low level peracid pump; High-order diluted acid jar with advance sour device and be connected, time sour device is connected with low level diluted acid jar, advances sour device and the diluted acid device is arranged on the support; Diluted acid goes out the acid tube road and is provided with circuit converter and diluted acid switching valve, is provided with the concentrated acid switching valve on peracid acid inlet tube road.
In order to collect and eliminate the acid mist that produces in the formation process, on support, also be provided with the acid mist gatherer.
Also be provided with recooling tower and be connected, play the cooling effect with high and low position peracid jar.
The present invention in use, by acid solution conveying device and automatic control equipment, cold acid is transported in the batteries, hot acid in the batteries cools off by heat exchanger, guaranteed battery in the process of being internalized into, the temperature in the battery is consistent, has guaranteed that battery is in the process of being internalized into, density of electrolyte in the battery is consistent, and the battery initial performance has 2%-5% to improve on year-on-year basis; Simultaneously owing to adopted new chemical synthesis technology, make whole process of production shorten 2-3 days time, improved the production efficiency that storage battery is produced greatly, the present invention in process of production, adopt all-sealed, be internalized in the process, the acid mist of generation and hydrogen can carry out processing up to standard by acid mist gatherer and processor, have avoided environmental pollution.
Description of drawings
Fig. 1 is a schematic top plan view of the present invention;
Fig. 2 is a cross-sectional schematic of the present invention;
Among the figure, the high-order diluted acid jar of 1-, the high-order peracid jar of 2-, 3-low level diluted acid jar, 4-low level peracid jar, 5-low level diluted acid pump, 6-low level peracid pump, 7-recooling tower, 8-advance sour device, 9-returns sour device, 10-acid mist gatherer, 11-electric circuit shifter, 12-diluted acid switching valve, 13-concentrated acid switching valve, 14-support.
Embodiment
As Fig. 1, shown in 2, the present invention rotates by PLC control low level diluted acid pump 5, low-density acid in the low level diluted acid jar 3 is transported in the high-order diluted acid jar 1 by the diluted acid recooling tower, under the situation that two concentrated acid switching valves 13 cut out fully, press the start-up control knob, two diluted acid switching valves 12 are opened fully, diluted acid in the high-order diluted acid jar 1 slowly is transported in the battery pack by advancing sour device 8, after treating that acid solution is full of fully in the battery of battery pack, acid solution turns back in the low level diluted acid jar 3 by returning sour device 9, and the acid mist gatherer is worked simultaneously, eliminates acid mist, go round and begin again and finish a circulation, and then enter the stage of changing into according to battery charging and discharging technology.After the end to be changed, two diluted acid switching valves 12 of system closing, high, two electric circuit shifters of diluted acid two concentrated acid switching valves 13 that automatically switch are simultaneously opened, the peracid of high-order peracid jar 2 slowly is transported in the battery pack by advancing sour device 8 in the system, passes through back sour device 9 again, low level peracid pump, the peracid recooling tower turns back in the low level peracid jar 4, after a period of time, after the diluted acid in the battery pack was replaced fully and finished, whole process finished.
This equipment level is put anticorrosion and is changed in the factory building, and high-order diluted acid jar 1 and high-order peracid jar 2 are placed on the two-layer platform, and low level diluted acid jar 3 and low level peracid jar 4 are placed in the underground tank, the operation of whole piece circuit sealing.
PLC controls concrete action and constitutes: detect liquid level, and--------the diluted acid valve is opened automatically, and-----------------------------------automatic closing system--is changed acid and finishes the back--in the peracid conversion to electrolyte injection battery pack to open the peracid valve automatically to cut off the diluted acid valve automatically to change into the end back in the circulation cooling to start 2# diluted acid pump automatically to detect liquid level to start 1# diluted acid pump automatically to detect liquid level to press the start-up control knob.Whenever finish a circulation, change into and finish a Battery pack.
The present invention is applied to the automation equipment that battery in the lead acid accumulator production field is internalized into production process, being internalized into particularly to the pregnant solution type battery of pine assembling, after adopt giving birth to the plate assembling, directly enter activation and curing that this equipment carries out active material, can realize continuous automatic production.
Claims (3)
1. a lead acid accumulator is internalized into system, it is characterized in that, comprise high-order diluted acid jar, high-order peracid jar, low level diluted acid jar, low level peracid jar, low level diluted acid jar is connected with high-order diluted acid jar by low level diluted acid pump, and low level peracid jar is connected with high-order peracid jar by low level peracid pump; High-order diluted acid jar with advance sour device and be connected, time sour device is connected with low level diluted acid jar, advances sour device and the diluted acid device is arranged on the support; Diluted acid goes out the acid tube road and is provided with circuit converter and diluted acid switching valve, is provided with the concentrated acid switching valve on peracid acid inlet tube road.
2. lead acid accumulator according to claim 1 is internalized into system, it is characterized in that, also is provided with the acid mist gatherer on support.
3. lead acid accumulator according to claim 1 is internalized into system, it is characterized in that, recooling tower is connected with high and low position peracid jar.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100353739A CN102136607A (en) | 2011-02-10 | 2011-02-10 | Forming system in lead-acid accumulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100353739A CN102136607A (en) | 2011-02-10 | 2011-02-10 | Forming system in lead-acid accumulator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102136607A true CN102136607A (en) | 2011-07-27 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011100353739A Pending CN102136607A (en) | 2011-02-10 | 2011-02-10 | Forming system in lead-acid accumulator |
Country Status (1)
| Country | Link |
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| CN (1) | CN102136607A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013159556A1 (en) * | 2012-04-27 | 2013-10-31 | 淄博鑫旭电源科技有限公司 | Automatic internal formation device for 12v lead-acid storage battery |
| CN107611498A (en) * | 2017-09-13 | 2018-01-19 | 淄博火炬能源有限责任公司 | Electrokinetic cell acid circulation rapid forming method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101308922A (en) * | 2007-06-19 | 2008-11-19 | 淄博蓄电池厂 | Battery formed acid loop method of lead acid battery |
| CN201936963U (en) * | 2011-02-10 | 2011-08-17 | 淄博鑫旭机电设备有限公司 | Container formation system in lead-acid storage battery |
-
2011
- 2011-02-10 CN CN2011100353739A patent/CN102136607A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101308922A (en) * | 2007-06-19 | 2008-11-19 | 淄博蓄电池厂 | Battery formed acid loop method of lead acid battery |
| CN201936963U (en) * | 2011-02-10 | 2011-08-17 | 淄博鑫旭机电设备有限公司 | Container formation system in lead-acid storage battery |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013159556A1 (en) * | 2012-04-27 | 2013-10-31 | 淄博鑫旭电源科技有限公司 | Automatic internal formation device for 12v lead-acid storage battery |
| CN107611498A (en) * | 2017-09-13 | 2018-01-19 | 淄博火炬能源有限责任公司 | Electrokinetic cell acid circulation rapid forming method |
| CN107611498B (en) * | 2017-09-13 | 2020-07-17 | 淄博火炬能源有限责任公司 | Acid circulation rapid formation method for power battery |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| ASS | Succession or assignment of patent right |
Owner name: ZIBO XINXU POWER TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: ZIBO XINXU MECHANICAL + ELECTRICAL CO., LTD. Effective date: 20121127 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Wei Zhonglian Inventor after: Liu Jiangang Inventor before: Wang Fuquan Inventor before: Wang Shoubao Inventor before: Li Cuicui |
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| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 255000 ZIBO, SHANDONG PROVINCE TO: 255086 ZIBO, SHANDONG PROVINCE Free format text: CORRECT: INVENTOR; FROM: WANG FUQUAN WANG SHOUBAO LI CUICUI TO: WEI ZHONGLIAN LIU JIANGANG |
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| TA01 | Transfer of patent application right |
Effective date of registration: 20121127 Address after: 255086 Zibo high tech Zone, Shandong Road, No. 135 High-tech Venture Park, block C, room 602 Applicant after: Zibo Xinxu Power Supply Technology Co., Ltd. Address before: 255000 Shandong city of Zibo province high tech Zone Wanjie Road No. 87 Applicant before: Zibo Xinxu Mechanical & Electrical Co., Ltd. |
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| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20110727 |