CN102723532A - Rapid forming process used for internal formation of lead-acid storage batteries - Google Patents
Rapid forming process used for internal formation of lead-acid storage batteries Download PDFInfo
- Publication number
- CN102723532A CN102723532A CN2012101777013A CN201210177701A CN102723532A CN 102723532 A CN102723532 A CN 102723532A CN 2012101777013 A CN2012101777013 A CN 2012101777013A CN 201210177701 A CN201210177701 A CN 201210177701A CN 102723532 A CN102723532 A CN 102723532A
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- Prior art keywords
- lead
- acid storage
- formation
- lead acid
- storage 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
- 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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- Battery Electrode And Active Subsutance (AREA)
Abstract
A rapid forming process used for internal formation of lead-acid storage batteries relates to a lead-acid storage battery. At present, the forming processes for lead-acid storage batteries include the following methods: 1, external forming method which causes greater pollution and is more energy consumption; and 2, conventional internal forming method which takes too long time for formation and is low in production efficiency. The rapid forming process for internal formation of lead-acid storage batteries is characterized in that a lead-acid storage battery is filled with an electrolytic solution, stands for 2-3 hours, and then is subjected to charge/discharge formation; the whole process allows the current deviation within plus or minus 15% as well as the voltage deviation within plus or minus 1.0%; the internal temperature of the lead-acid storage battery is controlled in range from 25 to 65 DEG C; and during the charge process, the first four stages take charge voltage as the conversion condition, and the fifth stage takes charge duration as the conversion condition. The invention has the benefit that the rapid forming process used for internal formation of lead-acid storage batteries has the advantages of relatively short formation duration, high production efficiency, cleanness, environmental protection and low energy consumption.
Description
Technical field
The present invention relates to lead acid accumulator, is a kind of quick chemical synthesis technology that lead acid accumulator is internalized into that is used for more specifically.
Background technology
At present; In the lead acid accumulator industry; The method for chemically synthesizing of lead acid accumulator has: 1, adopting to change into method (claiming that also pole plate changes into) outward, is the pole plate that lead acid accumulator is assembled usefulness to be placed in the electrolytic bath that has electrolyte discharge and recharge, and the polar plate of lead acid storage battery that will change into then is placed in the deionization and cleans; And handle through process procedures such as anti-oxidation, dryings, when lead acid accumulator is assembled, pole plate is encased in the lead acid accumulator housing then and goes.But this process is polluted big, big energy-consuming; 2, adopting conventional formation method (claiming that also battery changes into), is not go there being active polar plate of lead acid storage battery directly to be encased in the battery container, irritates then to add electrolyte; Carry out static and discharge and recharge changing into processing; Thereby do not need links such as washing, anti-oxidation, drying, but conventional internal formation process method requires technical standard higher, changes into overlong time; Production efficiency is low, and is wayward.
Summary of the invention
The purpose of this invention is to provide a kind of quick chemical synthesis technology that lead acid accumulator is internalized into that is used for, have the time of changing into relatively short, production efficiency is high, clean environment firendly, characteristics that power consumption is few.
The present invention realizes through following mode: a kind ofly be used for the quick chemical synthesis technology that lead acid accumulator is internalized into, it is characterized in that, after the lead acid storage battery basin irrigation powers up and separates liquid, at first left standstill 2～3 hours, change into then and discharge and recharge.Whole formation process allows ± 15% with interior current deviation, and ± 1.0% to be internalized into voltage deviation; The lead acid accumulator internal temperature should be controlled between 25～65 ℃, and water bath heat preservation is adopted in suggestion, when interior temperature surpasses 65 ℃, should stop charging, treats to recover charging again after temperature drops to 50 ℃; In the whole charging process, the switch condition in preceding 4 stages calculates (battery pack can be calculated with total voltage) with charging voltage, the 5th stage with the charging interval as switch condition; The whole formation process cycle of using the lead acid accumulator that this technology is internalized into is no more than 36 hours.
The invention has the beneficial effects as follows: the present invention is a kind of to be used for the quick chemical synthesis technology that lead acid accumulator is internalized into, exist the time that changes into relatively short, production efficiency is high, clean environment firendly, advantage that power consumption is few.
Embodiment
Carry out lead acid accumulator when being internalized into, at first the lead acid storage battery basin irrigation is powered up and separate liquid, left standstill then 2～3 hours, change into and discharge and recharge.Change into and be divided into five stages: the 1st stage, with the current charges of 5 times of battery capacities, represent with 5CA, after voltage reaches the 2.45V/ monomer, discharged for 10 seconds with 1CA; In the 2nd stage,, after charging voltage reaches the 2.60V/ monomer, discharged for 10 seconds with 1CA with the current charges of 2.5 times of battery capacities; In the 3rd stage,, after charging voltage reaches the 2.80V/ monomer, discharged for 10 seconds with 1CA with the current charges of 1.0 times of battery capacities; In the 4th stage,, after charging voltage reaches the 2.80V/ monomer, discharged for 10 seconds with 1CA with the current charges of 0.5 times of battery capacity; The 5th stage, with the current charges of 0.15 times of battery capacity, trickle charge 10 hours, last static rolling off the production line.
Claims (2)
1. one kind is used for the quick chemical synthesis technology that lead acid accumulator is internalized into, and it is characterized in that, after the lead acid storage battery basin irrigation powers up and separates liquid, at first leaves standstill 2～3 hours, changes into then to discharge and recharge.
2. as claimed in claim 1 changing into discharges and recharges, and it is characterized in that whole formation process allows ± 15% with interior current deviation, and ± 1.0% to be internalized into voltage deviation; The lead acid accumulator internal temperature should be controlled between 25～65 ℃, and water bath heat preservation is adopted in suggestion, when interior temperature surpasses 65 ℃, should stop charging, treats to recover charging again after temperature drops to 50 ℃; In the whole charging process, the switch condition in preceding 4 stages calculates (battery pack can be calculated with total voltage) with charging voltage, the 5th stage with the charging interval as switch condition; The whole formation process cycle of using the lead acid accumulator that this technology is internalized into is no more than 36 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101777013A CN102723532A (en) | 2012-05-27 | 2012-05-27 | Rapid forming process used for internal formation of lead-acid storage batteries |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012101777013A CN102723532A (en) | 2012-05-27 | 2012-05-27 | Rapid forming process used for internal formation of lead-acid storage batteries |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102723532A true CN102723532A (en) | 2012-10-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012101777013A Pending CN102723532A (en) | 2012-05-27 | 2012-05-27 | Rapid forming process used for internal formation of lead-acid storage batteries |
Country Status (1)
| Country | Link |
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| CN (1) | CN102723532A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103579686A (en) * | 2013-11-01 | 2014-02-12 | 湖北润阳新能源有限公司 | Formation method of lead-acid storage battery |
| CN103943888A (en) * | 2014-02-26 | 2014-07-23 | 超威电源有限公司 | Valve-regulated lead acid battery inner formation technology capable of controlling battery separator saturation |
| CN107658430A (en) * | 2017-10-11 | 2018-02-02 | 超威电源有限公司 | A kind of power lead acid battery high temperature formation method |
| CN110797585A (en) * | 2018-08-02 | 2020-02-14 | 肇庆理士电源技术有限公司 | Container formation method for lead-acid storage battery |
| CN113675397A (en) * | 2021-08-23 | 2021-11-19 | 浙江巨江电源制造有限公司 | Deep-cycle long-life lead-acid storage battery lead paste for parking, battery thereof and manufacturing process method of battery |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101673844A (en) * | 2009-10-21 | 2010-03-17 | 风帆股份有限公司 | Container formation method of valve-regulated lead-acid battery |
| CN102324576A (en) * | 2011-09-28 | 2012-01-18 | 江苏富思特电源有限公司 | Gel battery manufacturing method |
| CN102347516A (en) * | 2011-10-26 | 2012-02-08 | 浙江天能电池江苏新能源有限公司 | Inner forming process of tubular lead-acid storage battery |
| CN102354771A (en) * | 2011-10-26 | 2012-02-15 | 浙江天能电池江苏新能源有限公司 | Quick charging device for lead-acid storage battery and quick charging method |
| CN102368567A (en) * | 2011-10-13 | 2012-03-07 | 超威电源有限公司 | Formation method for dynamic lead-acid cell jar formation |
-
2012
- 2012-05-27 CN CN2012101777013A patent/CN102723532A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101673844A (en) * | 2009-10-21 | 2010-03-17 | 风帆股份有限公司 | Container formation method of valve-regulated lead-acid battery |
| CN102324576A (en) * | 2011-09-28 | 2012-01-18 | 江苏富思特电源有限公司 | Gel battery manufacturing method |
| CN102368567A (en) * | 2011-10-13 | 2012-03-07 | 超威电源有限公司 | Formation method for dynamic lead-acid cell jar formation |
| CN102347516A (en) * | 2011-10-26 | 2012-02-08 | 浙江天能电池江苏新能源有限公司 | Inner forming process of tubular lead-acid storage battery |
| CN102354771A (en) * | 2011-10-26 | 2012-02-15 | 浙江天能电池江苏新能源有限公司 | Quick charging device for lead-acid storage battery and quick charging method |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103579686A (en) * | 2013-11-01 | 2014-02-12 | 湖北润阳新能源有限公司 | Formation method of lead-acid storage battery |
| CN103943888A (en) * | 2014-02-26 | 2014-07-23 | 超威电源有限公司 | Valve-regulated lead acid battery inner formation technology capable of controlling battery separator saturation |
| CN103943888B (en) * | 2014-02-26 | 2016-04-06 | 超威电源有限公司 | A kind of valve-regulated sealed storage battery internal formation process controlling dividing plate saturation |
| CN107658430A (en) * | 2017-10-11 | 2018-02-02 | 超威电源有限公司 | A kind of power lead acid battery high temperature formation method |
| CN107658430B (en) * | 2017-10-11 | 2020-06-30 | 超威电源集团有限公司 | High-temperature container formation method for power type lead-acid storage battery |
| CN110797585A (en) * | 2018-08-02 | 2020-02-14 | 肇庆理士电源技术有限公司 | Container formation method for lead-acid storage battery |
| CN110797585B (en) * | 2018-08-02 | 2022-07-26 | 肇庆理士电源技术有限公司 | Container formation method for lead-acid storage battery |
| CN113675397A (en) * | 2021-08-23 | 2021-11-19 | 浙江巨江电源制造有限公司 | Deep-cycle long-life lead-acid storage battery lead paste for parking, battery thereof and manufacturing process method of battery |
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| C06 | Publication | ||
| PB01 | Publication | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20140214 Address after: 273100 Shandong province Qufu Shengyang Road No. 1 Applicant after: Shandong Sacred Sun Power Sources Co., Ltd. Address before: 273100 No. 6, customs East Road, Qufu, Shandong Applicant before: Shandong Sacred Sun Power Supply Technology Co., Ltd. |
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| TA01 | Transfer of patent application right | ||
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| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121010 |
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| WD01 | Invention patent application deemed withdrawn after publication |