CN106299490A - 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
CN106299490A
CN106299490A CN201610708968.9A CN201610708968A CN106299490A CN 106299490 A CN106299490 A CN 106299490A CN 201610708968 A CN201610708968 A CN 201610708968A CN 106299490 A CN106299490 A CN 106299490A
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China
Prior art keywords
electric current
charging
time
battery
acid
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CN201610708968.9A
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Chinese (zh)
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CN106299490B (en
Inventor
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 invention provides a kind of lead-acid battery formation method, comprise the following steps: 1) aneroid battery acid adding enters tank, static, take out negative pressure；2) charging, electric current 0.2 0.32C2, 23 hours time, evacuation；3) charge 0.25 0.38C2, 9 10 hours time；4) charging, electric current 0.15 0.28C2, 67 hours time；5) electric discharge, electric current 0.25C2, it is that 10.0V turns jumping to every battery；6) charging, electric current 0.15 0.26C2, 89 hours time；7) electric discharge, electric current 0.4C2, it is that 10.0V turns jumping to every battery；8) charging, electric current 0.15 0.26C2, 78 hours time；9) 0.5H is stood；10) charge 0.15 0.26C2, 78 hours time；11) it is filled with 1.8C after electric discharge scale2Electricity also 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 method.
Background technology
The high-performance having been found in view of lead-acid battery, low cost, easily to reclaim and reliable safety, it is at present in the whole world In the range of be widely used.Lead-acid accumulator is melted into be divided into and is internalized into and tank formation, because it is few to be internalized into pollution, and pole plate In moulding shell, the inside is melted into, and has carried out large-area popularization.Lead-acid accumulator in battery forming process 1, need to fill About 4 times that enter theoretical total electricity can be only achieved formation effect, and the electricity major part being filled with causes waste and the temperature of electricity more Rising；2, the Battery formation time is long, and acid is taken out in chemical conversion needs 6-8 days time altogether.
Summary of the invention
In order to solve above-mentioned technical problem, the invention provides a kind of lead-acid battery formation method, comprise the following steps: 1) aneroid battery acid adding enters tank, static, take out negative pressure；2) charging, electric current 0.2-0.32C2, 2-3 hour time, evacuation；3) fill Electricity 0.25-0.38C2, 9-10 hour time；4) charging, electric current 0.15-0.28C2, 6-7 hour time；5) electric discharge, electric current 0.25C2, it is that 10.0V turns jumping to every battery；6) charging, electric current 0.15-0.26C2, 8-9 hour time；7) electric discharge, electric current 0.4C2, it is that 10.0V turns jumping to every battery；8) charging, electric current 0.15-0.26C2, 7-8 hour time；9) 0.5H is stood；10) Charging 0.15-0.26C2, 7-8 hour time；11) it is filled with 1.8C after electric discharge scale2Electricity also takes out acid.
Further, step 1) in, quiescent time is 10-60 minute；
Further, negative pressure is taken out more than-0.03MPA, 0.5-3 minute time.
The chemical synthesizing method Battery formation time of the present invention is substantially reduced, is melted into electricity minimizing.
Detailed description of the invention
Below in conjunction with specific embodiment, the invention will be further described.
First the aneroid battery assembled is entered after tank being added acid by acid adding machine by chemical synthesizing method of the present invention, static 10-60 minute, with negative-pressure vacuum pipe, battery being taken out negative pressure, pressure requirements divided at 0.5-3 in more than-0.03MPA, time Clock.After exhausting negative pressure, a part heat be sucked away, after battery is proceeded by chemical conversion, charging, electric current 0.2-0.32C2, time Between 2-3 hour, evacuation；Charging 0.25-0.38C2, 9-10 hour time；Charging, electric current 0.15-0.28C2, the time, 6-7 was little Time；Electric discharge, electric current 0.25C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.15-0.26C2, 8-9 hour time；Put Electricity, electric current 0.4C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.15-0.26C2, 7-8 hour time；Stand 0.5H； Charging 0.15-0.26C2, 7-8 hour time；It is filled with 1.8C2Electricity also carries out taking out acid according to taking out acid technique.
As a example by 12V12AH, charging, electric current 0.25C2, 3 hours time, evacuation；Charging 0.3C2, 10 hours time；Fill Electricity, electric current 0.28C2, 6 hours time；Electric discharge, electric current 0.25C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.2C2, 9 hours time；Electric discharge, electric current 0.4C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.25C2, 8 hours time；Stand 0.5H；Charging 0.15C2, 7 hours time；It is filled with 1.8C after electric discharge scale2Electricity also carries out taking out acid according to taking out acid technique.Actual make Power consumption is 113AH, and the chemical conversion time is 55 hours.
As a example by 12V12AH, charging, electric current 0.32C2, 3 hours time, evacuation；Charging 0.38C2, 10 hours time； Charging, electric current 0.28C2, 7 hours time；Electric discharge, electric current 0.25C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.26C2, 8 hours time；Electric discharge, electric current 0.4C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.26C2, the time 7 is little Time；Stand 0.5H；Charging 0.26C2, 7 hours time；It is filled with 1.8C after electric discharge scale2Electricity is also taken out according to taking out acid technique Acid.Actually used electricity 120AH, the chemical conversion time is 55 hours.
As a example by 12V12AH, charging, electric current 0.3C2, 2.5 hours time, evacuation；Charging 0.3C2, 9.5 hours time； Charging, electric current 0.2C2, 6.5 hours time；Electric discharge, electric current 0.25C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.2C2, 8.5 hours time；Electric discharge, electric current 0.4C2, it is that 10.0V turns jumping to every battery；Charging, electric current 0.2C2, the time 8 is little Time；Stand 0.5H；Charging 0.26C2, 8 hours time；It is filled with 1.8C after electric discharge scale2Electricity is also taken out according to taking out acid technique Acid.Actually used electricity 113AH, the chemical conversion time is 55 hours.
The chemical synthesizing method Battery formation time of the present invention is substantially reduced, is melted into electricity minimizing.

Claims (3)

1. a lead-acid battery formation method, comprises the following steps: 1) aneroid battery acid adding enters tank, static, take out negative pressure；2) fill Electricity, electric current 0.2-0.32C2, 2-3 hour time, evacuation；3) charging 0.25-0.38C2, 9-10 hour time；4) charging, electricity Stream 0.15-0.28C2, 6-7 hour time；5) electric discharge, electric current 0.25C2, it is that 10.0V turns jumping to every battery；6) charging, electric current 0.15-0.26C2, 8-9 hour time；7) electric discharge, electric current 0.4C2, it is that 10.0V turns jumping to every battery；8) charging, electric current 0.15-0.26C2, 7-8 hour time；9) 0.5H is stood；10) charging 0.15-0.26C2, 7-8 hour time；11) electric discharge scale After be filled with 1.8C2Electricity also takes out acid.
2. lead-acid battery formation method as claimed in claim 1 a kind of, it is characterised in that step 1) in, quiescent time is 10-60 minute.
3. lead-acid battery formation method as claimed in claim 2 a kind of, it is characterised in that take out negative pressure-0.03MPA with On, 0.5-3 minute time.
CN201610708968.9A 2016-08-23 2016-08-23 A kind of lead-acid battery formation method Active CN106299490B (en)

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CN106299490B CN106299490B (en) 2019-03-12

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109378535A (en) * 2018-08-28 2019-02-22 超威电源有限公司 A kind of chemical synthesizing method of tubular colloidal battery
CN114020060A (en) * 2022-01-10 2022-02-08 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

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109378535A (en) * 2018-08-28 2019-02-22 超威电源有限公司 A kind of chemical synthesizing method of tubular colloidal battery
CN114020060A (en) * 2022-01-10 2022-02-08 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
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

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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.