CN101459259A - Production method for colloid accumulator - Google Patents

Production method for colloid accumulator Download PDF

Info

Publication number
CN101459259A
CN101459259A CNA2009100286239A CN200910028623A CN101459259A CN 101459259 A CN101459259 A CN 101459259A CN A2009100286239 A CNA2009100286239 A CN A2009100286239A CN 200910028623 A CN200910028623 A CN 200910028623A CN 101459259 A CN101459259 A CN 101459259A
Authority
CN
China
Prior art keywords
battery
colloid
storage battery
agm
sio
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CNA2009100286239A
Other languages
Chinese (zh)
Inventor
钱学楼
王增海
陆长江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU UDE POWER SUPPLY TECHNOLOGY Co Ltd
Original Assignee
JIANGSU UDE POWER SUPPLY TECHNOLOGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JIANGSU UDE POWER SUPPLY TECHNOLOGY Co Ltd filed Critical JIANGSU UDE POWER SUPPLY TECHNOLOGY Co Ltd
Priority to CNA2009100286239A priority Critical patent/CN101459259A/en
Publication of CN101459259A publication Critical patent/CN101459259A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Abstract

The invention discloses a method of manufacturing a novel colloidal storage battery, which adopts a mircrporous hard rubber separator to substitute an absorptive glass mat separator (AGM), thereby overcoming the difficulty of filling colloid in the AGM-colloidal storage battery, and eliminating liquid leakage resulted from colloid-liquid separation caused by colloid leakage of AGM. The colloid storage amount of the obtained rubber separator colloidal battery is increased, colloid deposition is sufficient and uniform without acid and liquid separation, the battery does not leak liquid, and the battery has long circle life without thermal runaway.

Description

A kind of manufacture method of colloid storage battery
Technical field
The invention belongs to the storage battery field, be specifically related to a kind of manufacture method of colloid electrolyte lead-acid accumulator.
Background technology
Lead acid accumulator is easy to get because of raw material, makes simply, and stable performance, characteristics such as low price and great variety of goods still dominate in various secondary chemical sources of electric energy so far, occupy the maximum market share.Valve controlling sealed battery has appearred in the sixties in 20th century in the world, and its non-leakage acid solution is seldom discharged acid mist during charging, need not add dilute sulfuric acid and pure water in the use, thereby be non-maintaining.Valve controlling sealed battery comprises two types on absorption type battery and colloidal electrolyte battery.The former is adsorbed on dilute sulfuric acid electrolyte wherein with superfine glass fibre partition board (AGM), and the internal resistance of cell is little, and electrolyte content is relatively low, and heavy-current discharge performance is good, is suitable as start type battery and various emergency power supply (UPS).The AGM battery is the lean solution formula, electrolyte stratification can occur in discharging and recharging, and many, the weak heat-dissipating of big, the living heat of floating current is not suitable for deep discharge and recycles, and easily produces bulge and thermal runaway phenomenon, and its service condition is subjected to many restrictions.Colloid storage battery is to add SiO in dilute sulfuric acid 2The gel of class makes electrolyte become gelinite, loses flowability, and the complete no leakage of battery has been eliminated the electrolyte stratification phenomenon.Colloid storage battery is a pregnant solution type, its floating current is little, give birth to heat less, big, the good heat dissipation of specific heat, so be suitable for dark cycle applications, so more safe and reliable than AGM battery, it is long to recycle the life-span.In many conventional batteries and the inapplicable occasion of AGM battery, can use colloid storage battery.But the colloid storage battery internal resistance is high slightly, and its specific energy approximately reduces by 10%, its manufacturing process complexity, and prices of raw and semifnished materials height is so the price of colloid storage battery is more much higher than conventional batteries and AGM battery.At present, be that the countries in the world company of representative makes colloid storage battery and all adopts the U.S. to reach polyester that auspicious Mick (DARAMIC) company produces to apply the micropore PVC SiO that phenolic resins dividing plate or European A Moxier (ARMER-SIL) company produce with German sunlight storage battery company 2Dividing plate, its price is at 40-60 yuan/m 2, be the AGM dividing plate of domestic use and 5-10 times of other dividing plates, and supply is very inconvenient.So it is difficult that China adopts the import dividing plate to prepare colloid storage battery fully.
1993, the inventor changed the can colloidal electrolyte in order to improve the AGM battery with the AGM battery, made AGM colloid hybrid battery.Because electrolyte increases and the influence of gel to battery performance, this improved hybrid battery capacitance obviously increases, and deep discharge cycle life has also prolonged, and has promoted the development of China's electric bicycle industry.But this hybrid colloid storage battery perfusion colloid difficulty is separated because AGM, produces glue to the colloid percolation, and battery still can the seepage acid solution.Because battery structure does not change, in fact it be still lean solution formula battery, still has bulge and thermal runaway phenomenon.These shortcomings are seriously restricting the development of China's colloid storage battery industry [1]
Summary of the invention
The objective of the invention is to improve battery structure, overcome perfusion colloid difficulty, eliminate the percolation of AGM to colloid, become the lean solution formula and be pregnant solution type, solve the low and expensive problem of external colloid storage battery specific energy simultaneously, a kind of method of being made colloid electrolyte lead-acid accumulator by the function admirable that is applicable to colloid storage battery, low-cost dividing plate is provided.
Purpose of the present invention can reach by following measure:
A kind of manufacture method of colloid storage battery comprises positive/negative plate is carried out utmost point group welding, combo, encloses battery case, pour into colloid after, carry out charging process, wherein the dividing plate between the positive/negative plate is a microporous rubber separator.
Described microporous rubber separator is generally by natural rubber and SiO 2Make through sulfuration with sulphur, perhaps by natural rubber and SiO 2Make through electron radiation, its surface is preferably corrugated, so that encapsulating.Deposit the advantage of aspects such as glue amount and battery cycle life in increase in order farthest to bring into play microporous rubber separator, the present invention preferably uses resistivity≤0.003 Ω/dm 2, porosity is 50~70% microporous rubber separator, adopts the microporous rubber separator of Baoding sail dividing plate factory in the embodiments of the invention.
Method of the present invention can be applied in the various gelled lead acid batteries, particularly valve controlling sealed colloid storage battery or conventional open type colloid battery.
The present invention does not have particular requirement to the pole plate of both positive and negative polarity, can use so long as can be applied to the pole plate of lead acid accumulator, all can as tubular plate, pasting plate.The present invention does not have particular requirement to grid yet, general lead acid accumulator all can, but, generally select alloy grids such as Pb-Ca alloy grid, Pb-Sb for use in order more preferably to bring into play the performance of battery.
The present invention does not have particular requirement for colloid, and the colloid of various gelled lead acid batteries all can use, but can bring into play performance better in order to make between colloid and the dividing plate, preferably adds the SiO of 1~6wt% in colloid 2, the SiO of gaseous state especially 2
The present invention there is no particular requirement to the step that changes into of battery or pole plate, adopts internal formation process or change into technology outward all can.
A kind of concrete manufacture method of novel colloidal storage battery of the present invention is as follows:
1. adopt normal pole plate (producer is not limit) to carry out utmost point group welding, combo, insert rubber separator between positive/negative plate, carry out capping again and handle.
2. battery pours into and contains SiO 21~6% colloid can pour into by the mode of vacuumizing in case of necessity.
3. battery carries out charging process.
Wherein in the step 1 micropore hard rubber dividing plate by natural rubber and SiO 2Make through sulfuration with sulphur, perhaps by natural rubber and SiO 2Make through electron radiation.The resistivity of micropore hard rubber dividing plate is smaller or equal to 0.003 Ω/dm 2, porosity is 50~70%.
Contain SiO in the step 2 2Or the material of silicic acid all may be as the gel of colloid storage battery, and the present invention preferably adopts gas phase SiO 2Make gel.If adopt other to contain SiO 2Or the material of silicic acid, as Ludox, and produce colloid storage battery with rubber separator, also should belong to scope of the present invention.In addition, the content of gel (is amounted to into SiO in the colloid storage battery 2) what can not influence claim of the present invention.
Employed rubber separator is than other dividing plate low prices in the method for the present invention, prepared rubber separator battery, and it is deposited the glue amount and increases, and gel is full and uniform, no acid solution layering, the battery no leakage, battery cycle life is long, no thermal runaway.
Embodiment
Embodiment 1
Except AGM, the present invention has selected polyethylene (PE) dividing plate, 10g modification dividing plate, rubber separator to make the colloid storage battery test, and makes comparisons with the polyester coating phenolic resins dividing plate of DARAMIC.Here the rubber separator of usefulness is by natural rubber and SiO 2Reach sulphur and make through sulfuration, or natural rubber and SiO 2Make through electron radiation is crosslinked, its surface is a corrugated, helps pouring into colloid.Its resistivity≤0.003 Ω/dm 2, porosity is about 60%.Rubber separator mechanical strength height can stop antimony to shift between both positive and negative polarity, prevents dendrite short circuit, can make long life accumulator [2]The 10g modification dividing plate here adds the diatomite modification in polyethylene.
The concrete preparation method of 4 test cells is as follows:
1. grid is the Pb-Ca alloy, and degree of oxidation of lead powder is 76%.
2. behind coated plate, curing drying, burst brush sheet, weld utmost point group.
3. insert different dividing plates, welding once more among the utmost point group.For the ease of operation, battery is uncovered
4. encapsulating charges.The prescription of colloid is the gas phase SiO that adds 3.0% weight in the sulfuric acid of proportion 1.28 2With a spot ofly help gel, the agent of lengthening the life, after strong agitation, directly pour in the battery and (need not vacuumize).Every single lattice battery pours into about 400ml colloid.After changing into according to a conventional method, survey battery 5A discharge time, its preceding 5 test capacity see Table 1.
Table 1, different dividing plate 12V, 40Ah colloid storage battery 5A discharge time
Figure A200910028623D00051
Figure A200910028623D00061
Because Pb-Ca alloy pole plate causes battery capacity early ageing, above-mentioned 5A presents significantly downward trend one by one discharge time, and it is no exception that polyester applies the phenolic resins dividing plate.The colloid storage battery capacity that rubber separator is made is comparatively stable, and a little more than polyester dividing plate battery.From the feature of long life that has of rubber separator, its price is also cheaply a lot of than polyester dividing plate.Therefore, rubber separator can be used as the dividing plate of colloid storage battery.
Embodiment 2
Test cell: 2 6-DZMJ-10 battery of electric vehicle, overall dimension are 152 * 98 * 94 (mm), and grid is the Pb-Ca alloy, are internalized into, and use AGM dividing plate and rubber separator respectively, and other technologies are with embodiment 1.
Two kinds of separator glue accumulator body experimental performances are listed in table 2.
Table 2, AGM and rubber separator colloid storage battery experimental performance are relatively
Figure A200910028623D00062
Result of the test shows that rubber separator colloid storage battery initial stage 5A discharge capacity is a little less than the AGM storage battery, but battery capacity can reach technical standard, and all the other every performances all are better than the AGM storage battery.It deposits the many approximately 100g of glue amount, reaches the level of pregnant solution type battery, prolongs very favourable to capacity rising and life-span.When constant current charge, the rubber separator battery temperature is low, and water consumption is few, and the grid corrosion is slow, helps extending battery life and prevents thermal runaway.Find AGM colloid storage battery utmost point group top and abundant gel on every side after dissecting battery, but AGM inside does not almost have gel, substantially all is acid solution, this glue segregation phenomenon becomes the hidden danger of battery leakage.Upper and lower, the inside and outside and gel that all distributing equably on every side of rubber separator colloid storage battery utmost point group does not have the liquefaction phenomenon, and battery can leakage.
Embodiment 2
Test cell is the 6-CN-100 energy-storage battery.
Battery 1 is to use the AGM dividing plate, and pole plate is internalized into, and contains 1.0%SiO in the colloid 2, vacuumize and pour in the battery.
Battery 2 is rubber separators, through outside change into after pole plate be assembled into battery.Contain 2.5% gas phase SiO in the colloid 2, do not vacuumize during encapsulating.
Battery 3 rubber separators, green plate.Change into by common technology after adding sulfuric acid, survey battery capacity with the 10A discharge.
Battery 4 is that the dilute sulfuric acid in the exhausted cell 3 is all poured out, and adds to contain 3.0% SiO in the acid of pouring out 2With help gel.For the sulfuric acid that consumed in the up operation with because of adding gel (SiO 2) may cause that the internal resistance of cell increases and capacity descends, the content of acid is increased to 21.0%, is fed in the battery after the colloid of preparing is fully stirred (need not vacuumize), by common process determining capacity.
Battery 5 is Dryfit A412/100.0A colloid storage batteries of German sunlight, overall dimension: 513 * 189 * 195 (mm), and heavy 40.0Kg, this battery adapts to various application, 10 years useful life of floating charge.
Battery 6 is the two accumulation energy type colloid storage battery that company produces, 100Ah of stepping on.
With above-mentioned 12V, 100Ah energy-storage battery main performance is listed in table 3.
Table 3,12V, 100Ah energy-storage battery performance is relatively
Figure A200910028623D00071
*120h leads and measures with the 1.0A discharge discharge time.
*Specific energy leads discharge capacity with 10h and calculates.
Above-mentioned test shows, replace AGM and special-purpose in the world colloid storage battery dividing plate (battery 5 and 6) with rubber separator, the medium current of prepared accumulation energy type colloid storage battery and the performance of low discharging current can not reduce, and specific energy is apparently higher than the colloid storage battery of domestic (battery 6) and external (battery 5).So, can produce good accumulation energy type colloid storage battery with rubber separator.
Conclusion
The present invention replaces AGM preparing in the colloid storage battery with AGM with rubber separator, has overcome perfusion colloid difficulty, has eliminated AGM the colloid diafiltration is produced the glue separation, causes the battery acid leaking.Rubber separator makes abundant, the even gel of colloid, has exempted electrolyte stratification, and has deposited the glue amount also more than the AGM battery, and this prolongs cycle life and prevent that thermal runaway from all being favourable improving the colloid storage battery capacity.
Embodiments of the invention are minitype motivation type and accumulation energy type colloid storage battery, but this method is equally applicable to other gelled lead acid batteries: alloy grid, pole plates such as valve controlling sealed storage battery, conventional open type battery, tubular plate, pasting plate, Pb-Ca alloy grid, Pb-Sb are with being internalized into and changing into technology outward.

Claims (6)

1, a kind of manufacture method of colloid storage battery comprises positive/negative plate is carried out utmost point group welding, combo, encloses battery case, pour into colloid after, carry out charging process, it is characterized in that the dividing plate between the positive/negative plate is a microporous rubber separator.
2, manufacture method according to claim 1 is characterized in that described microporous rubber separator is by natural rubber and SiO 2Make through sulfuration with sulphur, perhaps by natural rubber and SiO 2Make through electron radiation.
3, manufacture method according to claim 1 and 2 is characterized in that the resistivity≤0.003 Ω/dm of described microporous rubber separator 2, porosity is 50~70%.
4, manufacture method according to claim 1 and 2 is characterized in that described microporous rubber separator has the surface to be corrugated.
5, manufacture method according to claim 1 is characterized in that containing in the described colloid SiO of 1~6wt% 2
6, manufacture method according to claim 1 is characterized in that described colloid storage battery is valve controlling sealed colloid storage battery or conventional open type colloid battery.
CNA2009100286239A 2009-01-06 2009-01-06 Production method for colloid accumulator Pending CN101459259A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2009100286239A CN101459259A (en) 2009-01-06 2009-01-06 Production method for colloid accumulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2009100286239A CN101459259A (en) 2009-01-06 2009-01-06 Production method for colloid accumulator

Publications (1)

Publication Number Publication Date
CN101459259A true CN101459259A (en) 2009-06-17

Family

ID=40769963

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2009100286239A Pending CN101459259A (en) 2009-01-06 2009-01-06 Production method for colloid accumulator

Country Status (1)

Country Link
CN (1) CN101459259A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103000961A (en) * 2012-12-10 2013-03-27 山东圣阳电源股份有限公司 Formation method of colloidal lead-acid storage battery
CN105470437A (en) * 2015-12-15 2016-04-06 程艳青 Manufacturing method for long-life high-capacity tubular storage battery
CN106025167A (en) * 2016-06-24 2016-10-12 张家口保胜新能源科技有限公司 Colloid filling method for start-stop colloid storage battery
CN110943204A (en) * 2019-12-30 2020-03-31 湖南丰日电源电气股份有限公司 Novel storage battery with long service life, low energy consumption, high efficiency and low cost
CN112103569A (en) * 2020-08-21 2020-12-18 风帆有限责任公司 Method for prolonging high-temperature floating charge life of AGM valve-controlled sealed storage battery
US11211612B2 (en) 2014-06-17 2021-12-28 Owens Corning Intellectual Capital, Llc Water loss reducing pasting mats for lead-acid batteries
US11380962B2 (en) 2014-06-17 2022-07-05 Owens Corning Intellectual Capital, Llc Anti-sulphation pasting mats for lead-acid batteries

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103000961A (en) * 2012-12-10 2013-03-27 山东圣阳电源股份有限公司 Formation method of colloidal lead-acid storage battery
CN103000961B (en) * 2012-12-10 2017-09-26 山东圣阳电源股份有限公司 A kind of chemical synthesizing method of gelled lead acid battery
US11211612B2 (en) 2014-06-17 2021-12-28 Owens Corning Intellectual Capital, Llc Water loss reducing pasting mats for lead-acid batteries
US11380962B2 (en) 2014-06-17 2022-07-05 Owens Corning Intellectual Capital, Llc Anti-sulphation pasting mats for lead-acid batteries
CN105470437A (en) * 2015-12-15 2016-04-06 程艳青 Manufacturing method for long-life high-capacity tubular storage battery
CN105470437B (en) * 2015-12-15 2019-02-12 武汉法比特电源有限公司 A kind of manufacturing method of long life high capacity tube type storage battery
CN106025167A (en) * 2016-06-24 2016-10-12 张家口保胜新能源科技有限公司 Colloid filling method for start-stop colloid storage battery
CN110943204A (en) * 2019-12-30 2020-03-31 湖南丰日电源电气股份有限公司 Novel storage battery with long service life, low energy consumption, high efficiency and low cost
CN112103569A (en) * 2020-08-21 2020-12-18 风帆有限责任公司 Method for prolonging high-temperature floating charge life of AGM valve-controlled sealed storage battery

Similar Documents

Publication Publication Date Title
CN100399620C (en) Valve control type lead acid accumulator for metro vehicle
CN101459259A (en) Production method for colloid accumulator
CN102064319B (en) Negative plate of lead acid super battery, production method and lead acid super battery assembled by negative plate
CN100593875C (en) Technique for making polar plate of dried-charge tube-type dynamic lead acid battery
CN103208633A (en) Horizon battery and manufacturing method thereof
CN101764264B (en) Lead-acid ultra-battery
CN107317055A (en) High-performance lead-acid accumulator and its packaging technology
CN105470496A (en) Positive and negative plates for lithium-ion battery and battery employing positive and negative plates
CN102332561B (en) A kind of preparation method of electrodes of lithium-ion batteries
CN102074693A (en) Additive for high-carbon lead-acid storage-battery polar plate
CN108306006A (en) Negative material, negative plate and preparation method thereof, lithium ion battery and preparation method thereof
CN103606705A (en) Lithium ion battery and preparation method thereof
CN110504495A (en) A kind of acid adding chemical synthesizing method of battery
CN202259460U (en) Horizontal battery container
CN201887121U (en) Inhomogeneous electrolyte lead-acid storage battery
CN102945929B (en) Multi-pole-set battery and manufacture method thereof
CN103594748B (en) A kind of container formation method
CN107978800A (en) Single battery is realized the method and preparation and its battery pack preparation method of high pressure
CN112909262A (en) Silicon cathode and preparation method and application thereof
CN111081985B (en) Lead storage battery positive plate suitable for large-current work and lead storage battery
CN105895876A (en) Fast-charge and fast-discharge spirally wound lithium-ion battery and manufacturing method thereof
CN202268440U (en) Horizontal battery
CN102299339A (en) Lithium titanate and lithium vanadium phosphate lithium ion battery and preparation method thereof
CN102263254A (en) Method for producing composite anode of lead acid battery
JP5017746B2 (en) Control valve type lead acid battery

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Open date: 20090617