CN106299490B - A kind of lead-acid battery formation method - Google Patents

A kind of lead-acid battery formation method Download PDF

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Publication number
CN106299490B
CN106299490B CN201610708968.9A CN201610708968A CN106299490B CN 106299490 B CN106299490 B CN 106299490B CN 201610708968 A CN201610708968 A CN 201610708968A CN 106299490 B CN106299490 B CN 106299490B
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time
electric current
hour
battery
charges
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CN106299490A (en
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朱溢慧
徐丹
石沫
王新虎
殷粉娥
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Chaowei Power Group Co Ltd
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Chaowei Power Supply Co Ltd
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    • 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
    • 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

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The present invention relates to the present invention provides a kind of lead-acid battery formation methods, including the following steps: 1) dry cell acid adding enters sink, static, pumping negative pressure；2) it charges, electric current 0.2-0.32C2, time 2-3 hour, vacuumize；3) charge 0.25-0.38C2, time 9-10 hour；4) it charges, electric current 0.15-0.28C2, time 6-7 hour；5) it discharges, electric current 0.25C2, until every battery is that 10.0V turns to jump；6) it charges, electric current 0.15-0.26C2, time 8-9 hour；7) it discharges, electric current 0.4C2, until every battery is that 10.0V turns to jump；8) it charges, electric current 0.15-0.26C2, time 7-8 hour；9) 0.5H is stood；10) charge 0.15-0.26C2, time 7-8 hour；11) 1.8C is filled with after electric discharge scale2Electricity simultaneously takes out acid.

Description

A kind of lead-acid battery formation method
Technical field
The present invention relates to a kind of lead-acid battery formation methods.
Background technique
In view of the high-performance that lead-acid battery has been found, low cost, easily recycling and reliable safety, it is at present in the whole world In the range of be widely used.Lead-acid accumulator chemical conversion, which is divided into, to be internalized into and tank formation, because it is few to be internalized into pollution, pole plate The inside is melted into plastic housing, has carried out the popularization of large area.Lead-acid accumulator is 1 in battery forming process, needs fill 4 times or so for entering theoretical total electricity can be only achieved formation effect, and the electricity more being filled with largely causes the waste and temperature of electricity Raising；2, the Battery formation time is long, and chemical conversion takes out acid and needs 6-8 days time altogether.
Summary of the invention
In order to solve the above-mentioned technical problems, the present invention provides a kind of lead-acid battery formation methods, including the following steps: 1) dry cell acid adding enters sink, static, pumping negative pressure；2) it charges, electric current 0.2-0.32C2, time 2-3 hour, vacuumize；3) it fills Electric 0.25-0.38C2, time 9-10 hour；4) it charges, electric current 0.15-0.28C2, time 6-7 hour；5) it discharges, electric current 0.25C2, until every battery is that 10.0V turns to jump；6) it charges, electric current 0.15-0.26C2, time 8-9 hour；7) it discharges, electric current 0.4C2, until every battery is that 10.0V turns to jump；8) it charges, electric current 0.15-0.26C2, time 7-8 hour；9) 0.5H is stood；10) Charge 0.15-0.26C2, time 7-8 hour；11) 1.8C is filled with after electric discharge scale2Electricity simultaneously takes out acid.
Further, in step 1), quiescent time is 10-60 minutes；
Further, negative pressure is taken out more than -0.03MPA, time 0.5-3 minute.
The chemical synthesizing method Battery formation time of the invention is substantially reduced, is melted into electricity reduction.
Specific embodiment
The present invention is further explained in the light of specific embodiments.
Chemical synthesizing method of the present invention is static first by assembled dry cell after adding acid by acid adding machine and entering sink 10-60 minutes, pumping negative pressure is carried out to battery with negative-pressure vacuum pipe, pressure requirements are more than -0.03MPA, and the time is at 0.5-3 points Clock.After exhausting negative pressure, a part of heat is sucked away, after battery is started to be melted into, charge, electric current 0.2-0.32C2, when Between 2-3 hours, vacuumize；Charge 0.25-0.38C2, time 9-10 hour；Charging, electric current 0.15-0.28C2, the time, 6-7 was small When；Electric discharge, electric current 0.25C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.15-0.26C2, time 8-9 hour；It puts Electricity, electric current 0.4C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.15-0.26C2, time 7-8 hour；Stand 0.5H； Charge 0.15-0.26C2, time 7-8 hour；It is filled with 1.8C2Electricity simultaneously carries out taking out acid according to sour technique is taken out.
By taking 12V12AH as an example, charging, electric current 0.25C2, the time 3 hours, vacuumize；Charge 0.3C2, the time 10 hours；It fills Electricity, electric current 0.28C2, the time 6 hours；Electric discharge, electric current 0.25C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.2C2, Time 9 hours；Electric discharge, electric current 0.4C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.25C2, the time 8 hours；It stands 0.5H；Charge 0.15C2, the time 7 hours；1.8C is filled with after electric discharge scale2Electricity simultaneously carries out taking out acid according to sour technique is taken out.Actually make Electricity consumption is 113AH, and the chemical conversion time is 55 hours.
By taking 12V12AH as an example, charging, electric current 0.32C2, the time 3 hours, vacuumize；Charge 0.38C2, the time 10 hours； Charging, electric current 0.28C2, the time 7 hours；Electric discharge, electric current 0.25C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.26C2, the time 8 hours；Electric discharge, electric current 0.4C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.26C2, the time 7 is small When；Stand 0.5H；Charge 0.26C2, the time 7 hours；1.8C is filled with after electric discharge scale2Electricity is simultaneously taken out according to sour technique is taken out Acid.Electricity 120AH is actually used, the chemical conversion time is 55 hours.
By taking 12V12AH as an example, charging, electric current 0.3C2, the time 2.5 hours, vacuumize；Charge 0.3C2, the time 9.5 hours； Charging, electric current 0.2C2, the time 6.5 hours；Electric discharge, electric current 0.25C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.2C2, the time 8.5 hours；Electric discharge, electric current 0.4C2, until every battery is that 10.0V turns to jump；Charging, electric current 0.2C2, the time 8 is small When；Stand 0.5H；Charge 0.26C2, the time 8 hours；1.8C is filled with after electric discharge scale2Electricity is simultaneously taken out according to sour technique is taken out Acid.Electricity 113AH is actually used, the chemical conversion time is 55 hours.
The chemical synthesizing method Battery formation time of the invention is substantially reduced, is melted into electricity reduction.

Claims (3)

1. a kind of lead-acid battery formation method, including the following steps: 1) dry cell acid adding enters sink, static, pumping negative pressure；2) it fills Electricity, electric current 0.2-0.32C2, time 2-3 hour, vacuumize；3) charge 0.25-0.38C2, time 9-10 hour；4) it charges, electricity Flow 0.15-0.28C2, time 6-7 hour；5) it discharges, electric current 0.25C2, until every battery is that 10.0V turns to jump；6) it charges, electric current 0.15-0.26C2, time 8-9 hour；7) it discharges, electric current 0.4C2, until every battery is that 10.0V turns to jump；8) it charges, electric current 0.15-0.26C2, time 7-8 hour；9) 0.5H is stood；10) charge 0.15-0.26C2, time 7-8 hour；11) discharge scale After be filled with 1.8C2Electricity simultaneously takes out acid.
2. a kind of lead-acid battery formation method as described in claim 1, which is characterized in that in step 1), quiescent time is 10-60 minutes.
3. a kind of lead-acid battery formation method as claimed in claim 2, which is characterized in that take out negative pressure -0.03MPA with On, time 0.5-3 minute.
CN201610708968.9A 2016-08-23 2016-08-23 A kind of lead-acid battery formation method Active CN106299490B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109378535B (en) * 2018-08-28 2020-09-08 超威电源集团有限公司 Formation method of tubular gel battery
CN114020060B (en) * 2022-01-10 2022-03-25 深圳市铂纳特斯自动化科技有限公司 Negative pressure vacuum control system for battery formation equipment and automatic control method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101355152A (en) * 2008-05-08 2009-01-28 江苏快乐电源有限公司 Technique for making polar plate of dried-charge tube-type dynamic lead acid battery
CN101853968B (en) * 2010-05-31 2012-05-30 张天任 Container formation charging method for standby lead-acid storage battery
CN103560274A (en) * 2013-10-31 2014-02-05 河南超威电源有限公司 Battery evacuating formation method
CN103943907A (en) * 2014-03-25 2014-07-23 超威电源有限公司 Energy storage lead-acid battery charging technology
JP5659484B2 (en) * 2008-12-09 2015-01-28 新神戸電機株式会社 Battery case formation method for lead acid battery
CN104393323A (en) * 2013-11-16 2015-03-04 广西柳州中嘉知识产权服务有限公司 Storage battery formation method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101355152A (en) * 2008-05-08 2009-01-28 江苏快乐电源有限公司 Technique for making polar plate of dried-charge tube-type dynamic lead acid battery
JP5659484B2 (en) * 2008-12-09 2015-01-28 新神戸電機株式会社 Battery case formation method for lead acid battery
CN101853968B (en) * 2010-05-31 2012-05-30 张天任 Container formation charging method for standby lead-acid storage battery
CN103560274A (en) * 2013-10-31 2014-02-05 河南超威电源有限公司 Battery evacuating formation method
CN104393323A (en) * 2013-11-16 2015-03-04 广西柳州中嘉知识产权服务有限公司 Storage battery formation method
CN103943907A (en) * 2014-03-25 2014-07-23 超威电源有限公司 Energy storage lead-acid battery charging technology

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Address after: 313199 new industrial park, pheasant Town, Huzhou, Zhejiang, Changxing County

Patentee after: Chaowei Power Group Co., Ltd

Address before: 313199 new industrial park, pheasant Town, Huzhou, Zhejiang, Changxing County

Patentee before: Chilwee Power Supply Co., Ltd.