CN108598609A - A kind of colloid power container formation process for lead acid storage battery - Google Patents
A kind of colloid power container formation process for lead acid storage battery Download PDFInfo
- Publication number
- CN108598609A CN108598609A CN201810264825.2A CN201810264825A CN108598609A CN 108598609 A CN108598609 A CN 108598609A CN 201810264825 A CN201810264825 A CN 201810264825A CN 108598609 A CN108598609 A CN 108598609A
- Authority
- CN
- China
- Prior art keywords
- stage
- fill
- electric currents
- battery
- charging
- 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.)
- Granted
Links
- 239000002253 acid Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 35
- 239000000084 colloidal system Substances 0.000 title claims abstract description 30
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 28
- 230000005611 electricity Effects 0.000 claims abstract description 17
- 239000000126 substance Substances 0.000 claims abstract description 16
- 239000003792 electrolyte Substances 0.000 claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 12
- 239000011149 active material Substances 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 5
- 238000001514 detection method Methods 0.000 abstract description 4
- 230000002708 enhancing effect Effects 0.000 abstract description 3
- 238000009738 saturating Methods 0.000 abstract description 3
- 208000028659 discharge Diseases 0.000 description 49
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 7
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000010287 polarization Effects 0.000 description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 description 2
- 235000011152 sodium sulphate Nutrition 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 229910002012 Aerosil® Inorganic materials 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000028161 membrane depolarization Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000037452 priming Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- RCIVOBGSMSSVTR-UHFFFAOYSA-L stannous sulfate Chemical compound [SnH2+2].[O-]S([O-])(=O)=O RCIVOBGSMSSVTR-UHFFFAOYSA-L 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 229910000375 tin(II) sulfate Inorganic materials 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- 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
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M10/44—Methods for charging or discharging
- H01M10/446—Initial charging measures
-
- 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
- H01M10/121—Valve regulated lead acid batteries [VRLA]
-
- 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
Landscapes
- 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 battery technology fields, more particularly to a kind of colloid power container formation process for lead acid storage battery, colloidal electrolyte is added in accumulator, stands 0.5~1h, chemical conversion program fills stage, alternate nine discharge regimes including ten successively and stands the stage and take out acid phase.Present invention efficiently solves the saturating problem of power type being difficult to of colloid battery, it can guarantee that the chemical conversion of colloid battery positive plate is uniform, active material conversion is abundant, improves colloid battery and is internalized into quality.The technique is always melted into the time as 27~51h before the detection of the 9th discharge capacity and combo electric discharge simultaneously, total net charge volume is 3.4~8.75 times of rated capacity, reduce battery charge and chemical conversion time, enhancing battery is effectively filled with electricity, it improves power colloid battery and produces production capacity, it reduces battery production cost and improves production efficiency, improve battery competitiveness in the market.
Description
Technical field
The present invention relates to battery technology field more particularly to a kind of colloid power container formation process for lead acid storage battery.
Background technology
The chemical conversion of lead-acid accumulator is a very crucial procedure in lead-acid accumulator manufacture, the quality of formation process
Directly influence the performance and service life of lead-acid accumulator.Even with formula, same to technique, the lead-acid accumulator with batch,
Also result in the granular size and arrangement shape of active material from the different chemical conversion time using different electric currents in formation process
The variation of formula.
Lead-acid accumulator chemical synthesis technology be generally divided to be internalized into two kinds of tank formation, be internalized into and tank formation (channelization at) phase
Than haing the following advantages：Technological process simplifies pole plate washing, the load of dry and battery supplement electricity and slot type chemical conversion, weldering
It connects, take the processes such as piece, save a large amount of energy (energy such as pure water, acid and electricity), working hour, floor space is small, without purchasing
Grooving equipment and acid-mist equipment, battery obtain certain reduction at instinct.Pole plate is not easy to be polluted by impurity, can reduce battery
Self discharge improves battery with two side terminals, extends battery life.
Existing power type AGM valve-regulated lead-acid batteries generally use three is filled two and is put, and four fill three internal formation process put, the work
Artistic skill enough ensures that the positive plate chemical conversion of AGM battery is uniform, and active material is fully converted.But the presence of colloidal electrolyte can prolong
The diffusion velocity of slow electrolyte, the internal resistance for increasing battery play negative effect, therefore colloid power plumbic acid to the effect being internalized into
Container formation using above-mentioned three fill two put technique, four fill three and put internal formation process when, being difficult to of positive plate is saturating, and surface occurs very
More hickies, internal resistance is big in formation process, and anode polarization increases, and big volume and electricity is used for the electrolysis of water in formation process, causes a large amount of
Energy loss increases battery production cost, increases the moisture loss in formation process, to influence battery performance.
Invention content
The present invention in order to overcome in existing colloid power type container formation process for lead acid storage battery there is being difficult to thoroughly, energy consumption
It is high, internal resistance is big, influences the problem of battery performance, provide that a kind of battery positive plate chemical conversion is uniform, and active material conversion is sufficient
Colloid power container formation process for lead acid storage battery.
To achieve the goals above, the present invention uses following technical scheme：
Colloidal electrolyte is added in a kind of colloid power container formation process for lead acid storage battery in accumulator, stands 0.5~1h, changes
Include the following steps successively at program：
(1) one fills the stage：First with 0.1~0.15C electric currents, 3~5h of charging, then with 0.15~0.2C electric currents charging, 3~5h；
(2) one put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(3) two fill the stage：With 0.15~0.2C electric currents charging, 3~5h；
(4) two put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(5) three fill the stage：With 0.2~0.25C electric currents charging, 2~4h；
(6) three put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(7) four fill the stage：With 0.25~0.3C electric currents charging, 2~4h；
(8) four put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(9) five fill the stage：With 0.3~0.35C electric currents charging, 2~4h；
(10) five put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(11) six fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(12) six put the stage：With 0.5~1h of 0.2C current discharges；
(13) seven fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(14) seven put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(15) eight fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(16) eight put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(17) nine fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(18) nine put the stage：With 0.5C current discharges to 1.75V/ single lattices；
(19) ten fill the stage：First with 0.25~0.35C electric currents, 3~5h of charging, then with 0.1~0.15C electric currents charging, 1~2h；
(20) stage is stood：Stand 0.5~1h；
(21) acid phase is taken out：To carry out taking out acid after 0.02~0.04C constant-current charges, 2~3h.
Preferably, in formation process, the temperature of accumulator is controlled at 25~50 DEG C.
Colloid power container formation process for lead acid storage battery of the present invention fills 9 using 10 puts charge technology, stringent in formation process
Between controlling 25 to 50 DEG C of battery temperature, while the charging current in each charge and discharge stage, charging time are optimized,
In, C indicates the rated capacity of battery.
Preferably, in step (1), a stage of filling is filled with 0.75~1.75 times that electricity is rated capacity, it is ensured that early period
Grid corrosion layer generate, enhance grid and active material binding force, then carry out 0.5~1h low discharging current go electrification
Learn polarization.
Preferably, step (2) is to (10), two fill that stage to five stages of putting are filled with that electricity is specified electric quantity 1.25~
3.8 again.
Two, which fill the stage, puts stage gradually slow raising charging current to five, while low current being used alternatingly in charging process
Discharge depolarization, the utilization ratio of intensified charging electric current allow most active materials to convert completely, and two, which fill the stage, puts rank to five
Section is filled with 1.25~3.8 times of net charge volume specified electric quantity.Six to nine charge and discharge stages passed through continuous charge and discharge pulse formation solution
The hickie phenomenon for positive plate surface of having determined improves battery performance and cycle life.Nine put the stage as battery capacity detection and electricity
Pond combo discharge regime, ten fill the stage to supplement capacitance Restoration stage after battery discharge.
Therefore, the present invention has the advantages that：Solve the problems, such as that power type being difficult to of colloid battery is saturating,
It can guarantee that the chemical conversion of colloid battery positive plate is uniform, active material conversion is abundant, improves colloid battery and is internalized into quality.The work simultaneously
Skill is always melted into the time as 27~55h before the detection of the 9th discharge capacity and combo electric discharge, and total net charge volume is rated capacity
3.4~8.75 times, battery charge and chemical conversion time are reduced, enhancing battery is effectively filled with electricity, improves power colloid battery
Production capacity is produced, battery production cost is reduced and improves production efficiency, improve battery competitiveness in the market.
Specific implementation mode
Below by specific embodiment, the technical solutions of the present invention will be further described.
In the present invention, if not refering in particular to, all devices and raw material is commercially available or the industry is common are following
Method in embodiment is unless otherwise instructed this field conventional method.
The embodiment of the present invention uses 6-DZM-20, and (rated capacity is the electric boosted automobile-used power colloid lead acid storage battery of 20Ah
For pond.
Embodiment 1
Colloidal electrolyte is added in accumulator：First use the concentrated sulfuric acid, pure water (conductivity is less than 2 μ S/cm), sodium sulphate, sulfuric acid sub-
Tin is configured to sulfuric acid mass fraction 37.5%, sodium sulphate 1.5%, the electrolyte of stannous sulfate 0.5%, then side sheared edge addition
Aerosil is configured to colloid concentration 2.5%, and the colloidal electrolyte of 1.250~1.260g/ml of sulfuric acid electrolyte density is matched
The colloidal electrolyte set is added to by priming by vacuum mode in battery, and 0.5h is stood, and the temperature of accumulator is controlled at 25 DEG C,
Chemical conversion program includes the following steps successively：
(1) one fills the stage：First with 0.1C electric currents charging 5h, then with 0.15C electric currents charging 5h；It is specified that one stage of filling, which was filled with electricity,
1.25 times of capacity；
(2) one put the stage：With 0.1C current discharges 1h；
(3) two fill the stage：With 0.15C electric currents charging 5h；
(4) two put the stage：With 0.1C current discharges 1h；
(5) three fill the stage：With 0.2C electric currents charging 4h；
(6) three put the stage：With 0.1C current discharges 1h；
(7) four fill the stage：With 0.25C electric currents charging 4h；
(8) four put the stage：With 0.1C current discharges 1h；
(9) five fill the stage：With 0.3C electric currents charging 4h；
(10) five put the stage：With 0.1C current discharges 1h；Two fill stage to five stages of putting be filled with electricity be specified electric quantity 3.35
Times；
(11) six fill the stage：With 0.15C electric currents charging 4h；
(12) six put the stage：With 0.2C current discharges 0.5h；
(13) seven fill the stage：With 0.15C electric currents charging 4h；
(14) seven put the stage：With 0.1C current discharges 1h；
(15) eight fill the stage：With 0.15C electric currents charging 4h；
(16) eight put the stage：With 0.1C current discharges 1h；
(17) nine fill the stage：With 0.15C electric currents charging 4h；
(18) nine put the stage：With 0.5C current discharges to 1.75V/ single lattices；
(19) ten fill the stage：First with 0.25C electric currents charging 5h, then with 0.1C electric currents charging 2h；
(20) stage is stood：Stand 0.5h；
(21) acid phase is taken out：To carry out taking out acid after 0.02C constant-current charges 3h.
Embodiment 2
Be added colloidal electrolyte in accumulator, stand 1h, the temperature of accumulator is controlled at 30 DEG C, chemical conversion program include successively with
Lower step：
(1) one fills the stage：First with 0.15C electric currents charging 3h, then with 0.2C electric currents charging 3h；It is specified that one stage of filling, which was filled with electricity,
1.05 times of capacity；
(2) one put the stage：With 0.2C current discharges 0.5h；
(3) two fill the stage：With 0.2C electric currents charging 3h；
(4) two put the stage：With 0.2C current discharges 0.5h；
(5) three fill the stage：With 0.25C electric currents charging 2h；
(6) three put the stage：With 0.2C current discharges 0.5h；
(7) four fill the stage：With 0.3C electric currents charging 2h；
(8) four put the stage：With 0.2C current discharges 0.5h；
(9) five fill the stage：With 0.35C electric currents charging 2h；
(10) five put the stage：With 0.2C current discharges 0.5h；Two fill stage to five stages of putting be filled with electricity be specified electric quantity 2
Times；
(11) six fill the stage：With 0.25C electric currents charging 2h；
(12) six put the stage：With 0.2C current discharges 0.5h；
(13) seven fill the stage：With 0.25C electric currents charging 2h；
(14) seven put the stage：With 0.2C current discharges 0.5h；
(15) eight fill the stage：With 0.25C electric currents charging 2h；
(16) eight put the stage：With 0.2C current discharges 0.5h；
(17) nine fill the stage：With 0.25C electric currents charging 2h；
(18) nine put the stage：With 0.5C current discharges to 1.75V/ single lattices；
(19) ten fill the stage：First with 0.35C electric currents charging 3h, then with 0.15C electric currents charging 1h；
(20) stage is stood：Stand 1h；
(21) acid phase is taken out：To carry out taking out acid after 2~3h of 0.04C constant-current charges.
Embodiment 3
Colloidal electrolyte is added in accumulator, stands 0.75h, the temperature of accumulator is controlled at 45 DEG C, and chemical conversion program is wrapped successively
Include following steps：
(1) one fills the stage：First with 0.125C electric currents charging 4h, then with 0.15C electric currents charging 3h；It is volume that one stage of filling, which was filled with electricity,
0.95 times of constant volume；
(2) one put the stage：With 0.1C current discharges 0.75h；
(3) two fill the stage：With 0.175 electric current charging 3h；
(4) two put the stage：With 0.15C current discharges 0.5h；
(5) three fill the stage：With 0.2C electric currents charging 4h；
(6) three put the stage：With 0.15C current discharges 0.5h；
(7) four fill the stage：With 0.25C electric currents charging 4h；
(8) four put the stage：With 0.15C current discharges 0.5h；
(9) five fill the stage：With 0.35C electric currents charging 4h；
(10) five put the stage：With 0.15C current discharges 0.5h；Two fill stage to five stages of putting, and to be filled with electricity be specified electric quantity
3.425 again；
(11) six fill the stage：With 0.175C electric currents charging 3h；
(12) six put the stage：With 0.2C current discharges 0.5h；
(13) seven fill the stage：With 0.175C electric currents charging 3h；
(14) seven put the stage：With 0.2C current discharges 0.5h；
(15) eight fill the stage：With 0.175C electric currents charging 3h；
(16) eight put the stage：With 0.2C current discharges 0.5h；
(17) nine fill the stage：With 0.175C electric currents charging 3h；
(18) nine put the stage：With 0.5C current discharges to 1.75V/ single lattices；
(19) ten fill the stage：First with 0.35C electric currents charging 4h, then with 0.15C electric currents charging 2h；
(20) stage is stood：Stand 0.5h；
(21) acid phase is taken out：To carry out taking out acid after 0.03C constant-current charges 2h.
Comparative example
Comparative example is melted into using workshop common process：
Colloidal electrolyte is added in accumulator, stands 1.5h, the temperature of accumulator is controlled at 50 DEG C, and chemical conversion program includes successively
Following steps：
(1) one fills the stage：First with 0.075C electric currents charging 2h；
(2) two fill the stage：With 0.185C electric currents charging 35h；
(3) three fill the stage：With 0.14C electric currents charging 15h；
(4) one put the stage：With 0.25C current discharges 3h；
(5) four fill the stage：With 0.175C electric currents charging 20h；
(6) five fill the stage：With 0.125C current discharges 20h；
(7) two put the stage：With 0.25C current discharges 5h；
(8) two put the stage：Then with 0.5C current discharges to 1.75v/ single lattices；
(9) six fill the stage：With 0.175C electric currents charging 8h；
(10) seven fill the stage：With 0.125C electric currents charging 10h；
(11) it stands：2h；
(12) acid is taken out：With 0.1C electric currents, pressure limiting 2.5v/ single lattices charging 2h；.
The colloid storage battery and comparative example obtained to embodiment 1-3 colloid power container formation process for lead acid storage battery is internalized into
Technique obtains colloid storage battery, by GB/T 22199-2008《Sealing lead acid storage battery for electric vehicle》And other countries' mark
Standard carries out performance detection, and the results are shown in Table 1：
1. testing result of table
As can be seen from Table 1, the colloid storage battery that colloid power container formation process for lead acid storage battery through the invention obtains
Performance indicator meets national standard, and the performance of the colloid being melted into the method in other respects is melted into also superior to conventional method
Battery reduces battery charge and chemical conversion time, and enhancing battery is effectively filled with electricity, improves the production production of power colloid battery
Can, it reduces battery production cost and improves production efficiency, improve battery competitiveness in the market.
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the present invention in any form, and is not surpassing
There are other variations and modifications under the premise of going out the technical solution recorded in claim.
Claims (4)
1. a kind of colloid power container formation process for lead acid storage battery, which is characterized in that colloidal electrolyte is added in accumulator, it is quiet
.5~1h is set to 0, chemical conversion program includes the following steps successively：
(1) one fills the stage：First with 0.1~0.15C electric currents, 3~5h of charging, then with 0.15~0.2C electric currents charging, 3~5h；
(2) one put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(3) two fill the stage：With 0.15~0.2C electric currents charging, 3~5h；
(4) two put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(5) three fill the stage：With 0.2~0.25C electric currents charging, 2~4h；
(6) three put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(7) four fill the stage：With 0.25~0.3C electric currents charging, 2~4h；
(8) four put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(9) five fill the stage：With 0.3~0.35C electric currents charging, 2~4h；
(10) five put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(11) six fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(12) six put the stage：With 0.5~1h of 0.2C current discharges；
(13) seven fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(14) seven put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(15) eight fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(16) eight put the stage：With 0.1~0.2C current discharges, 0.5~1h；
(17) nine fill the stage：With 0.15~0.25C electric currents charging, 2~4h；
(18) nine put the stage：With 0.5C current discharges to 1.75V/ single lattices；
(19) ten fill the stage：First with 0.25~0.35C electric currents, 3~5h of charging, then with 0.1~0.15C electric currents charging, 1~2h；
(20) stage is stood：Stand 0.5~1h；
(21) acid phase is taken out：To carry out taking out acid after 0.02~0.04C constant-current charges, 2~3h.
2. a kind of colloid power container formation process for lead acid storage battery according to claim 1, which is characterized in that formation process
In, the temperature of accumulator is controlled at 25~50 DEG C.
3. a kind of colloid power container formation process for lead acid storage battery according to claim 1 or 2, which is characterized in that step
(1) in, a stage of filling is filled with 0.75~1.75 times that electricity is rated capacity.
4. a kind of colloid power container formation process for lead acid storage battery according to claim 1 or 2, which is characterized in that step
(2) to (10), two fill stage to five stages of putting, and to be filled with electricity be 1.25~3.8 times of specified electric quantity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810264825.2A CN108598609B (en) | 2018-03-28 | 2018-03-28 | Internal formation process of colloid power lead-acid storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810264825.2A CN108598609B (en) | 2018-03-28 | 2018-03-28 | Internal formation process of colloid power lead-acid storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108598609A true CN108598609A (en) | 2018-09-28 |
| CN108598609B CN108598609B (en) | 2020-09-01 |
Family
ID=63624918
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810264825.2A Active CN108598609B (en) | 2018-03-28 | 2018-03-28 | Internal formation process of colloid power lead-acid storage battery |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108598609B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109148992A (en) * | 2018-11-29 | 2019-01-04 | 湖南丰日电源电气股份有限公司 | Tubular colloidal battery rapid internalization is at technique |
| CN109659638A (en) * | 2018-12-18 | 2019-04-19 | 超威电源有限公司 | A kind of power type lead storage battery high current chemical synthesis technology |
| CN110085933A (en) * | 2019-03-26 | 2019-08-02 | 天能电池集团股份有限公司 | A kind of lead storage battery method for group matching |
| CN111477982A (en) * | 2020-04-15 | 2020-07-31 | 天能电池(芜湖)有限公司 | Formation process of low-charging-rate CNF battery for energy storage |
| CN113471560A (en) * | 2021-06-29 | 2021-10-01 | 浙江巨江电源制造有限公司 | Formation method of horizontal lead-acid storage battery |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101901935A (en) * | 2010-07-02 | 2010-12-01 | 超威电源有限公司 | Internal formation process for high-capacity gel battery |
| CN102244301B (en) * | 2011-05-26 | 2013-08-28 | 江苏永达电源股份有限公司 | Container formation process for lead acid storage battery |
| CN104218263A (en) * | 2014-08-14 | 2014-12-17 | 超威电源有限公司 | Power gel battery container formation technology |
| CN104617325A (en) * | 2015-01-28 | 2015-05-13 | 衡阳瑞达电源有限公司 | Tube-type accumulator container formation process |
| CN106450502A (en) * | 2016-08-30 | 2017-02-22 | 天能电池集团有限公司 | Container formation charging technology of lead storage battery |
-
2018
- 2018-03-28 CN CN201810264825.2A patent/CN108598609B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101901935A (en) * | 2010-07-02 | 2010-12-01 | 超威电源有限公司 | Internal formation process for high-capacity gel battery |
| CN102244301B (en) * | 2011-05-26 | 2013-08-28 | 江苏永达电源股份有限公司 | Container formation process for lead acid storage battery |
| CN104218263A (en) * | 2014-08-14 | 2014-12-17 | 超威电源有限公司 | Power gel battery container formation technology |
| CN104617325A (en) * | 2015-01-28 | 2015-05-13 | 衡阳瑞达电源有限公司 | Tube-type accumulator container formation process |
| CN106450502A (en) * | 2016-08-30 | 2017-02-22 | 天能电池集团有限公司 | Container formation charging technology of lead storage battery |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109148992A (en) * | 2018-11-29 | 2019-01-04 | 湖南丰日电源电气股份有限公司 | Tubular colloidal battery rapid internalization is at technique |
| CN109148992B (en) * | 2018-11-29 | 2019-04-02 | 湖南丰日电源电气股份有限公司 | Tubular colloidal battery rapid internalization is at technique |
| CN109659638A (en) * | 2018-12-18 | 2019-04-19 | 超威电源有限公司 | A kind of power type lead storage battery high current chemical synthesis technology |
| CN109659638B (en) * | 2018-12-18 | 2021-08-17 | 超威电源集团有限公司 | Heavy-current formation process for power type lead storage battery |
| CN110085933A (en) * | 2019-03-26 | 2019-08-02 | 天能电池集团股份有限公司 | A kind of lead storage battery method for group matching |
| CN111477982A (en) * | 2020-04-15 | 2020-07-31 | 天能电池(芜湖)有限公司 | Formation process of low-charging-rate CNF battery for energy storage |
| CN113471560A (en) * | 2021-06-29 | 2021-10-01 | 浙江巨江电源制造有限公司 | Formation method of horizontal lead-acid storage battery |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108598609B (en) | 2020-09-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108598609A (en) | A kind of colloid power container formation process for lead acid storage battery | |
| CN105226338B (en) | A kind of lead-acid accumulator rapid internalization is into charging method | |
| CN102437380A (en) | Method for internal chemical reaction in battery via charging five times and discharging four times | |
| CN107331902B (en) | A kind of lead-acid accumulator pulse container formation technique | |
| EP2960978B1 (en) | Flooded lead-acid battery | |
| CN106450502B (en) | A kind of lead storage battery is internalized into charge technology | |
| CN110931892A (en) | Acid injection and formation method for 12V 20-150 Ah lead-acid storage battery | |
| CN104466190B (en) | Optimize thin type electrode tubular type sealed motive force lead-acid accumulator and its manufacture method | |
| CN104300179A (en) | Container formation process for valve-regulated lead storage battery | |
| CN205081170U (en) | Improved storage battery | |
| CN107579255A (en) | A kind of positive electrode grid of lead storage battery alloy and preparation method thereof | |
| CN100394633C (en) | Lead-acid accumulator negative pole lead paste for electric booster vehicle and preparing method | |
| CN108963367A (en) | Colloid power lead-acid accumulator chemical synthesis technology | |
| CN106684391A (en) | Rare earth grid alloy for lead-acid storage batteries and production method thereof | |
| CN106099209B (en) | A kind of power lead-acid storage battery electrolysis additive and preparation method thereof | |
| CN1482696A (en) | Formula and curing process of anode lead plaster of long and narrow valve-controlled sealed lead-acid storage battery | |
| CN105591163B (en) | A kind of valve-control sealed lead acid battery production technology | |
| CN105186047B (en) | A kind of high-performance lead-acid battery colloidal electrolyte and preparation method thereof | |
| CN107681162A (en) | A kind of positive grid of lead-acid accumulator low antimony alloy | |
| CN102945948B (en) | Novel rare earth lead-acid power cell | |
| CN105428605B (en) | The technique that a kind of lead-acid battery negative pole plate reduces hardening time | |
| CN103199307A (en) | Container formation lead-acid battery technology | |
| CN104103827A (en) | Lead paste composition of lead-acid battery anode | |
| CN108417840A (en) | A kind of valve-regulated rare earth energy storing battery | |
| CN100446328C (en) | Highly conductive natrium salt electrolysis and its making method and accumulator using the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 313100 Zhejiang city of Huzhou province Changxing County pheasant emerging urban industrial park Applicant after: Chaowei Power Group Co.,Ltd. Address before: 313100 Zhejiang city of Huzhou province Changxing County pheasant emerging urban industrial park Applicant before: CHILWEE POWER Co.,Ltd. |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: An internalization process for colloidal power lead acid battery Effective date of registration: 20210630 Granted publication date: 20200901 Pledgee: Agricultural Bank of China Limited by Share Ltd. Changxing County branch Pledgor: Chaowei Power Group Co.,Ltd. Registration number: Y2021330000727 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20231016 Granted publication date: 20200901 Pledgee: Agricultural Bank of China Limited by Share Ltd. Changxing County branch Pledgor: Chaowei Power Group Co.,Ltd. Registration number: Y2021330000727 |