WO2022174585A1 - Method for preparing positive plate and lead storage battery - Google Patents
Method for preparing positive plate and lead storage battery Download PDFInfo
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- WO2022174585A1 WO2022174585A1 PCT/CN2021/119491 CN2021119491W WO2022174585A1 WO 2022174585 A1 WO2022174585 A1 WO 2022174585A1 CN 2021119491 W CN2021119491 W CN 2021119491W WO 2022174585 A1 WO2022174585 A1 WO 2022174585A1
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- WIPO (PCT)
- Prior art keywords
- lead
- positive
- grid
- paste
- mass
- Prior art date
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- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000003860 storage Methods 0.000 title claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 238000001035 drying Methods 0.000 claims abstract description 34
- 229910000152 cobalt phosphate Inorganic materials 0.000 claims abstract description 33
- ZBDSFTZNNQNSQM-UHFFFAOYSA-H cobalt(2+);diphosphate Chemical compound [Co+2].[Co+2].[Co+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O ZBDSFTZNNQNSQM-UHFFFAOYSA-H 0.000 claims abstract description 33
- 239000000725 suspension Substances 0.000 claims abstract description 18
- 239000011248 coating agent Substances 0.000 claims abstract description 7
- 238000000576 coating method Methods 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 42
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 claims description 39
- 230000005484 gravity Effects 0.000 claims description 31
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 claims description 20
- 239000000835 fiber Substances 0.000 claims description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000006230 acetylene black Substances 0.000 claims description 10
- 229920005610 lignin Polymers 0.000 claims description 10
- 238000002360 preparation method Methods 0.000 claims description 9
- 229910045601 alloy Inorganic materials 0.000 claims description 7
- 239000000956 alloy Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims description 2
- 239000006072 paste Substances 0.000 claims description 2
- 238000005096 rolling process Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims 1
- 239000000843 powder Substances 0.000 claims 1
- 238000005260 corrosion Methods 0.000 abstract description 10
- 230000007797 corrosion Effects 0.000 abstract description 10
- 238000002791 soaking Methods 0.000 abstract description 6
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 239000002253 acid Substances 0.000 description 58
- 239000000203 mixture Substances 0.000 description 19
- 238000003756 stirring Methods 0.000 description 19
- 238000012360 testing method Methods 0.000 description 18
- 238000001723 curing Methods 0.000 description 14
- 238000000227 grinding Methods 0.000 description 12
- 238000002386 leaching Methods 0.000 description 11
- 229910000978 Pb alloy Inorganic materials 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000004080 punching Methods 0.000 description 4
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000007598 dipping method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004146 energy storage Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910052761 rare earth metal Inorganic materials 0.000 description 3
- 208000032953 Device battery issue Diseases 0.000 description 2
- 239000011149 active material Substances 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000006056 electrooxidation reaction Methods 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009749 continuous casting Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 230000002431 foraging effect Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
Classifications
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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
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/70—Carriers or collectors characterised by shape or form
- H01M4/72—Grids
- H01M4/73—Grids for lead-acid accumulators, e.g. frame plates
-
- 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
-
- 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
- H01M10/4235—Safety or regulating additives or arrangements in electrodes, separators or electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/14—Electrodes for lead-acid accumulators
- H01M4/16—Processes of manufacture
- H01M4/20—Processes of manufacture of pasted electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/14—Electrodes for lead-acid accumulators
- H01M4/16—Processes of manufacture
- H01M4/22—Forming of electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
- H01M2004/028—Positive electrodes
-
- 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
Definitions
- the application relates to the technical field of lead storage batteries, in particular to a method for preparing a positive plate and a lead storage battery.
- Lead-acid batteries can be classified into lead-acid batteries for starting, backup-use lead-acid batteries, lead-acid batteries for energy storage, and lead-acid batteries for power use, etc., according to their uses.
- lead-acid batteries due to the different use conditions and occasions of various lead-acid batteries, the reasons for battery failure are also different. Even the same type of battery failure mode is the same for each part.
- the lead-acid battery used for starting motorcycles is used for a long time.
- the failure modes of the battery during the daytime are mostly water loss and corrosion of the positive grid. When driving at night, the lighting battery is added. Most of the failure modes are insufficient charging, negative electrode vulcanization, etc.
- backup batteries are charging throughout their entire life cycle.
- the time in the high voltage area is 4 to 7 hours, and many users can ride for many days on a single charge.
- the backup battery is generally charged by the mains power supply through the transformer device, and is only used in emergencies such as power failure, equipment maintenance, etc., so the battery is charged during the life cycle.
- the positive electrode of the battery has a high charging potential, and the positive electrode grid is prone to electrochemical corrosion.
- the general measures of the battery factory are to use thick plates to increase the floating life of the lead-acid battery.
- Patent document CN109921022A discloses a method for improving the bonding force between the positive electrode grid of a lead-acid battery and the lead paste and the firmness of the lead paste itself.
- the main step is to dry the conventional positive grid at a certain temperature for a period of time.
- the lead-acid battery positive plate obtained by the invention has no obvious peeling and peeling phenomenon under the same use conditions, has good cycle stability, and can significantly improve the service life of the lead-acid battery.
- the lead-acid battery prepared in this patent document is only aimed at the fact that the positive plate does not fall off under normal use conditions.
- Patent document CN101841031B discloses a method for making a positive grid of a lead battery, which belongs to the technical field of electrode material preparation.
- Lead alloy is used as a raw material, and a lead alloy positive grid formed by melting and casting is used as an anode.
- the anode electrochemical oxidation method is used for surface modification, and rare earth is used to improve the performance of the surface of the lead alloy positive grid.
- the invention avoids the difficulty of preparing lead-rare earth alloys, and it is easy to uniformly and quantitatively mix some trace rare earth elements on the surface of the lead alloy positive electrode grid, so as to realize the regulation of electrode surface properties, and the electrochemical preparation of rare earth oxides has the operating conditions of rare earth oxides.
- the invention enables the lead alloy positive grid electrode to have good electrical and chemical properties and long service life, and is also beneficial to the production of the positive grid of the low-cost lead storage battery.
- the grid produced in this patent document needs to be electrochemically modified, the actual operation process is complicated, and the fabrication cost is high.
- the present application discloses a preparation method of a positive plate and a lead storage battery.
- a preparation method of a positive plate comprising the following steps:
- every 100 parts of pure water and 3 to 5 parts of cobalt phosphate are prepared into a cobalt phosphate suspension, and the positive grid is placed in the cobalt phosphate suspension to soak;
- the immersed positive grid is first kept for 3h to 5h under the conditions of relative humidity of 70% to 80% and temperature of 50 to 60°C, and then placed under the conditions of relative humidity of 30% to 40% and temperature of 50 to 60°C. Under the condition of standing for 5 to 8 hours, a corrosion layer is formed on the surface of the grid, and the cobalt phosphate particles are attached to the outside of the corrosion layer. Finally, the temperature is lowered to room temperature within 2 hours under the condition of relative humidity of 30% to 40%;
- step (1) the alloy lead is first melted and then made into a lead strip, which is then rolled, punched, and knurled to obtain a positive grid.
- the thickness of the lead strip after rolling is 2.2-3.2 mm, and the depth of the knurling is 0.1-0.15 mm.
- step (2) after heating to raise the temperature of the cobalt phosphate suspension to 45-55°C, the positive grid is immersed in the cobalt phosphate suspension, and heated to raise the water temperature to 45-55°C.
- the purpose of heating is to improve the solubility of cobalt phosphate, but the effect is not obvious and has a certain effect.
- the purpose of soaking the cobalt phosphate on the positive grid is to attach cobalt phosphate particles on the surface of the grid, and the amount of cobalt phosphate attached has nothing to do with the soaking time.
- Coating was carried out within 8 hours after drying and cooling was completed.
- the mixing process of the positive lead paste is as follows: firstly mix and stir lead powder and fibers that account for 0.08% to 0.10% of the mass of the lead powder, and then add water that accounts for 11.5% of the mass of the lead powder and 8.2% to 9.2% of the mass of the lead powder. 1.40g/mL of sulfuric acid was carried out and paste.
- negative lead paste lead powder, barium sulfate accounting for 0.8%-1% by mass of lead powder, lignin accounting for 0.1%-0.3% by mass of lead powder, acetylene black accounting for 0.2%-0.4% by mass of lead powder,
- the fibers accounting for 0.07%-0.1% of the mass of the lead powder are mixed and stirred, and then water, which accounts for 11.3% of the mass of the lead powder, and sulfuric acid and paste, which accounts for 7.6%-8.6% of the mass of the lead powder and has a specific gravity of 1.4g/mL, are added to obtain the negative lead paste.
- the negative lead paste is coated on both sides of the negative grid to obtain a negative plate.
- the continuous casting positive grid is first soaked in the cobalt phosphate suspension, and then the soaked positive grid is first placed in an environment with a relative humidity of 70% to 80% and a temperature of 50 to 60°C. For 3 to 5 hours, put it in an environment with a relative humidity of 30% to 40% and a temperature of 50 to 60°C for 5 to 8 hours.
- a corrosion layer is formed on the surface of the grid, and the cobalt phosphate particles are attached to the outside of the corrosion layer.
- the grid The temperature was lowered to room temperature within 2 hours in an environment with a relative humidity of 30% to 40%.
- cobalt phosphate penetrates into the grid corrosion layer, which increases the density of the grid corrosion film, enhances the bonding force between the positive grid and the active material, and reduces the positive electrode activity.
- the material softens the risk of falling off and improves the battery's resistance to overcharging.
- the positive alloy lead is made into a lead tape with a thickness of 2.5mm, and the 6-GF-100 positive grid with a size of 151mm ⁇ 151mm is made after punching, and then knurled with a size of 0.5 ⁇ 0.5mm and a depth of 0.12mm deal with.
- negative lead powder 10Kg of barium sulfate, 3Kg of lignin, 4Kg of acetylene black and 1Kg of fiber, then add 113Kg of pure water, and then add 86Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the apparent specific gravity is 4.40g. /cm3 of negative lead paste.
- the negative electrode lead paste is coated on the cast negative grid, and the negative electrode green plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
- 6-GF-100 long-life lead-acid battery for floating charge was prepared by wrapping, assembling, adding acid, charging, and grouping the prepared positive green plate and negative green plate.
- the positive alloy lead is made into a lead tape with a thickness of 3.2mm, and the 6-GF-300 positive grid with a size of 237mm ⁇ 151mm is made after punching the net, and then knurled with a size of 0.5 ⁇ 0.5mm and a depth of 0.15mm deal with.
- the positive electrode lead paste is coated on the treated positive electrode grid, and the positive electrode green plate is obtained after acid dipping, surface drying, curing, drying and slice grinding.
- 6-GF-300 long-life lead-acid battery for floating charge is prepared by wrapping the prepared positive electrode green plate and negative electrode green plate, assembling, adding acid, charging, and grouping.
- the positive alloy lead is made into a lead tape with a thickness of 2.2mm, and the 6-FM-38 positive grid with a size of 150mm ⁇ 122mm is made after punching the net, and then knurled with a size of 0.5 ⁇ 0.5mm and a depth of 0.10mm deal with.
- negative lead paste Mix and stir 1T of negative lead powder, 9Kg of barium sulfate, 2Kg of lignin, 3Kg of acetylene black and 0.8Kg of fiber, then add 113Kg of pure water, and then add 81Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the specific gravity is 4.41g /cm3 of negative lead paste.
- the negative electrode lead paste is coated on the cast negative grid, and the negative electrode green plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
- the prepared positive electrode green plate and negative electrode green plate are packaged, assembled, acidified, charged, assembled and arranged to obtain 6-MF-38 long-life lead-acid battery for floating charge.
- the 6-GF-100 positive electrode green plate is prepared by coating the positive electrode lead paste on the cast positive electrode grid, leaching acid, surface drying, curing, drying, and slicing polishing.
- 6-GF-100 lead-acid battery is prepared by wrapping, assembling, adding acid, charging, and arranging the prepared positive electrode plate and negative electrode plate.
- the 6-GF-100 positive electrode green plate is prepared by coating the positive electrode lead paste on the cast positive electrode grid, leaching acid, surface drying, curing, drying, and slicing polishing.
- negative lead powder 8Kg of barium sulfate, 1Kg of lignin, 2Kg of acetylene black and 0.7Kg of fiber, then add 113Kg of pure water, and then add 76Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the apparent specific gravity is 4.42. g/cm3 negative lead paste.
- the negative electrode lead paste is coated on the casted 6-GF-300 negative electrode grid, and the negative electrode plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
- 6-GF-300 lead-acid battery is prepared by wrapping, assembling, adding acid, charging, and arranging the prepared positive electrode plate and negative electrode plate.
- the 6-MF-38 positive electrode green plate is prepared by coating the positive electrode lead paste on the positive electrode grid made by casting, and after acid leaching, surface drying, curing, drying, and slice grinding.
- negative lead powder 9Kg of barium sulfate, 2Kg of lignin, 3Kg of acetylene black and 0.8Kg of fiber, then add 113Kg of pure water, and then add 81Kg of sulfuric acid with a specific gravity of 1.40g/mL to mix the paste, and the specific specific gravity is 4.41. g/cm3 negative lead paste.
- the negative electrode lead paste is coated on the casted 6-MF-38 negative electrode grid, and the negative electrode plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
- a 6-MF-38 lead-acid battery is prepared by wrapping, assembling, adding acid, charging, and arranging the prepared positive electrode plate and negative electrode plate.
- the positive alloy lead is made into a lead tape with a thickness of 2.5mm, and the 6-GF-100 positive grid with a size of 151mm ⁇ 151mm is made after punching, and then knurled with a size of 0.5 ⁇ 0.5mm and a depth of 0.12mm deal with.
- the positive grid Take out the positive grid and put it in an environment with a relative humidity of 80% and a temperature of 60 °C for 4 hours, then put the positive grid in an environment with a relative humidity of 40% and a temperature of 60 °C for 6.5 hours, and finally put the positive electrode
- the grid is placed in an environment with a relative humidity of 40% for 2 hours, and the temperature is lowered to room temperature to obtain a treated positive grid.
- negative lead powder 10Kg of barium sulfate, 3Kg of lignin, 4Kg of acetylene black and 1Kg of fiber, then add 113Kg of pure water, and then add 86Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the apparent specific gravity is 4.40g. /cm3 of negative lead paste.
- the negative electrode lead paste is coated on the cast negative grid, and the negative electrode green plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
- 6-GF-100 long-life lead-acid battery for floating charge was prepared by wrapping, assembling, adding acid, charging, and grouping the prepared positive green plate and negative green plate.
- the 10-hour rate capacity of the lead storage battery prepared by the method in the present application is no different from that of the control group.
- the positive electrode grid after soaking and aging in the cobalt phosphate suspension in this application is more corrosion-resistant, and the corrosion resistance of the positive grid after soaking in the cobalt phosphate aqueous solution is slightly stronger than that of the non-immersed positive electrode plate grid; the positive electrode grid is soaked in cobalt phosphate suspension for aging, and the bonding force with the active material is enhanced, and the discharge cycle period of the lead battery prepared by using the positive grid in the solution of the present application is increased by more than 33.3%.
- modules in the device in the implementation scenario may be distributed in the device in the implementation scenario according to the description of the implementation scenario, or may be located in one or more devices different from the implementation scenario with corresponding changes.
- the modules of the above implementation scenarios may be combined into one module, or may be further split into multiple sub-modules.
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- Manufacturing & Machinery (AREA)
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- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
The present application relates to the technical field of lead storage batteries and discloses a method for preparing a positive plate and a lead storage battery. The method for preparing a positive plate comprises the following steps: (1) preparing a positive plate grid; (2) soaking of the positive plate grid: soaking the positive plate grid in a cobalt phosphate suspension containing 100 parts of pure water and 3-5 parts of cobalt phosphate; (3) drying and cooling of the positive plate grid: first putting the soaked positive plate grid in an environment having a relative humidity of 70%-80% and a temperature of 50-60°C for standing for 3-5 h, then putting same in an environment having a relative humidity of 30%-40% and a temperature of 50-60°C for standing for 5-8 h, and finally putting same in an environment having a relative humidity of 30%-40% for lowering the temperature to room temperature within 2 h; (4) preparing a paste; and (5) coating. The positive plate grid prepared in the present application is more corrosion-resistant, and the discharge cycle service life of the prepared lead storage battery is prolonged.
Description
本申请涉及铅蓄电池技术领域,具体涉及一种正极板的制备方法、铅蓄电池。The application relates to the technical field of lead storage batteries, in particular to a method for preparing a positive plate and a lead storage battery.
普兰特(G.Plante)于1859年发明铅蓄电池,已经历了近160年的发展历程,铅蓄电池在理论研究、产品种类及产品电气性能等方面都得到了长足的进步。铅蓄电池根据其用途可以分为起动用铅蓄电池、备用铅蓄电池、储能用铅蓄电池、动力用铅蓄电池等。但是由于各种铅蓄电池的使用条件和场合不同,造成电池失效的原因也不同。即使是同类型的电池失效模式也各部相同,例如摩托车起动用的铅蓄电池长时间使用,车辆在白天行驶电池的失效模式多为失水、正极板栅腐蚀,在夜间行驶因增加了照明电池的失效模式多为充电不足,负极硫化等。G. Plante invented the lead-acid battery in 1859, and has experienced nearly 160 years of development. The lead-acid battery has made great progress in theoretical research, product types and product electrical performance. Lead-acid batteries can be classified into lead-acid batteries for starting, backup-use lead-acid batteries, lead-acid batteries for energy storage, and lead-acid batteries for power use, etc., according to their uses. However, due to the different use conditions and occasions of various lead-acid batteries, the reasons for battery failure are also different. Even the same type of battery failure mode is the same for each part. For example, the lead-acid battery used for starting motorcycles is used for a long time. The failure modes of the battery during the daytime are mostly water loss and corrosion of the positive grid. When driving at night, the lighting battery is added. Most of the failure modes are insufficient charging, negative electrode vulcanization, etc.
备用电池与起动用蓄电池、储能用电池、动力用电池相比,其整个寿命周期电池都在充电中。而作为摩托车、汽车起动用蓄电池只有在车辆工作时才充电;储能用电池受太阳光照时间、角度,风力大小的影响,电池多数情况下欠充;动力电池充电与放电分开进行,正常充电时在高电压区的时间为4~7h,许多用户充一次电可骑行很多天。Compared with starting batteries, energy storage batteries, and power batteries, backup batteries are charging throughout their entire life cycle. As a starting battery for motorcycles and automobiles, it is only charged when the vehicle is working; the battery for energy storage is affected by the time, angle, and wind power of the sun, and the battery is undercharged in most cases; the charging and discharging of the power battery are carried out separately, and normal charging The time in the high voltage area is 4 to 7 hours, and many users can ride for many days on a single charge.
备用电池一般由市电供电通过变压装置进行充电,只有在突发事如停电、设备检修等状况下使用,所以电池在使用生命周期内均在充电。电池在充电中,电池正极充电电位高,正极板栅易发生电化学腐蚀。为使备用电池获得足够的寿命,电池厂一般的措施为采用厚极板来增加铅蓄电池的浮充寿命。The backup battery is generally charged by the mains power supply through the transformer device, and is only used in emergencies such as power failure, equipment maintenance, etc., so the battery is charged during the life cycle. When the battery is charging, the positive electrode of the battery has a high charging potential, and the positive electrode grid is prone to electrochemical corrosion. In order to obtain sufficient life of the backup battery, the general measures of the battery factory are to use thick plates to increase the floating life of the lead-acid battery.
专利文献CN109921022A公开了一种提高铅酸电池正极板栅与铅膏结合力以及铅膏自身牢固程度的方法,其主要步骤为,将常规正极板栅在一定温度下烘干一段时间。与此同时,向体积为5~8毫升的蒸馏水中加入0.025~0.125克添加剂,充分搅拌后形成溶液A,随后,将溶液A就加入到经充分研磨的铅粉中,之后缓慢加入稀硫酸,经搅拌后,即制得正极铅膏。取出经热处理过的正极板栅,将得到的铅膏均匀地涂抹其上,之后,经自然烘干后,制成正极生板,最后,进行化成5小时后,即得到制备好的正极熟板。该发明得到的铅蓄电池正极板在相同的使用条件下,未出现明显的脱落起皮等现象,具有较好的循环稳定性,可显著提高铅酸电池的使用寿命。该专利文献制备的铅蓄电池仅针对正常使用条件下正极板没有出现脱落现象。Patent document CN109921022A discloses a method for improving the bonding force between the positive electrode grid of a lead-acid battery and the lead paste and the firmness of the lead paste itself. The main step is to dry the conventional positive grid at a certain temperature for a period of time. At the same time, add 0.025-0.125 g of additives to distilled water with a volume of 5-8 ml, and stir to form solution A. Then, add solution A to the fully ground lead powder, and then slowly add dilute sulfuric acid. After stirring, the positive lead paste is prepared. Take out the heat-treated positive electrode grid, apply the obtained lead paste evenly on it, then, after natural drying, make a positive electrode green plate, and finally, after forming it for 5 hours, the prepared positive electrode cooked plate is obtained. . The lead-acid battery positive plate obtained by the invention has no obvious peeling and peeling phenomenon under the same use conditions, has good cycle stability, and can significantly improve the service life of the lead-acid battery. The lead-acid battery prepared in this patent document is only aimed at the fact that the positive plate does not fall off under normal use conditions.
专利文献CN101841031B公开了一种铅蓄电池正极板栅的制作方法,属于电极材料的制备技术领域,以铅合金为原料,经熔融浇铸成型的铅合金正极板栅为阳极,在稀土硫酸盐和硫酸水溶液中应用阳极电化学氧化方法进行表面修饰,采用稀土改善铅合金正极板栅表面的性能。发明避免了铅-稀土合金制备的困难,容易在铅合金正极板栅表面均匀定量的掺入一些微量稀土元素,实现电极表面性能的调控,电化学法制备稀土氧化物具备稀土氧化物具有操作条件 温和、简单、制备成本低以及制得的稀土氧化物纯度高、稀土氧化物的微区结构可调控等优点。该发明使铅合金正极板栅电极具有电和化学性能好、使用寿命长,还利于低成本铅蓄电池正极板栅的生产。该专利文献制作的板栅需要经过电化学修饰,实际操作过程比较复杂,造作成本高。Patent document CN101841031B discloses a method for making a positive grid of a lead battery, which belongs to the technical field of electrode material preparation. Lead alloy is used as a raw material, and a lead alloy positive grid formed by melting and casting is used as an anode. The anode electrochemical oxidation method is used for surface modification, and rare earth is used to improve the performance of the surface of the lead alloy positive grid. The invention avoids the difficulty of preparing lead-rare earth alloys, and it is easy to uniformly and quantitatively mix some trace rare earth elements on the surface of the lead alloy positive electrode grid, so as to realize the regulation of electrode surface properties, and the electrochemical preparation of rare earth oxides has the operating conditions of rare earth oxides. It has the advantages of mildness, simplicity, low preparation cost, high purity of the prepared rare earth oxide, and adjustable microdomain structure of the rare earth oxide. The invention enables the lead alloy positive grid electrode to have good electrical and chemical properties and long service life, and is also beneficial to the production of the positive grid of the low-cost lead storage battery. The grid produced in this patent document needs to be electrochemically modified, the actual operation process is complicated, and the fabrication cost is high.
发明内容SUMMARY OF THE INVENTION
为解决在长期浮充条件下的铅蓄电池寿命问题,本申请公开了一种正极板的制备方法、铅蓄电池。In order to solve the problem of the lifespan of a lead storage battery under long-term floating charging conditions, the present application discloses a preparation method of a positive plate and a lead storage battery.
一种正极板的制备方法,包括以下步骤:A preparation method of a positive plate, comprising the following steps:
(1)制备正极板栅;(1) Preparation of positive grid;
(2)正极板栅的浸泡,(2) Immersion of the positive grid,
按质量比计,每100份纯水和3~5份磷酸钴配置成磷酸钴悬浊液,将正极板栅放入磷酸钴悬浊液中浸泡;According to the mass ratio, every 100 parts of pure water and 3 to 5 parts of cobalt phosphate are prepared into a cobalt phosphate suspension, and the positive grid is placed in the cobalt phosphate suspension to soak;
(3)正极板栅的干燥降温,(3) Drying and cooling of the positive grid,
浸泡后的正极板栅先在相对湿度为70%~80%、温度为50~60℃的条件下静置3h~5h,再在相对湿度为30%~40%、温度为50~60℃的条件下静置5~8h,此时板栅表面产生腐蚀层,磷酸钴颗粒附于腐蚀层外侧,最后在相对湿度为30%~40%的条件下2小时内将温度降至室温;The immersed positive grid is first kept for 3h to 5h under the conditions of relative humidity of 70% to 80% and temperature of 50 to 60°C, and then placed under the conditions of relative humidity of 30% to 40% and temperature of 50 to 60°C. Under the condition of standing for 5 to 8 hours, a corrosion layer is formed on the surface of the grid, and the cobalt phosphate particles are attached to the outside of the corrosion layer. Finally, the temperature is lowered to room temperature within 2 hours under the condition of relative humidity of 30% to 40%;
(4)和膏,制备正极铅膏;(4) and paste to prepare positive lead paste;
(5)涂板,将正极铅膏涂板到正极板栅。(5) Coating, apply the positive lead paste to the positive grid.
步骤(1)中先将合金铅熔化后制成铅带,再经过辊压、冲网、滚花,得正极板栅。In step (1), the alloy lead is first melted and then made into a lead strip, which is then rolled, punched, and knurled to obtain a positive grid.
辊压后铅带的厚度为2.2~3.2mm,滚花的深度为0.1~0.15mm。The thickness of the lead strip after rolling is 2.2-3.2 mm, and the depth of the knurling is 0.1-0.15 mm.
步骤(2)中加热使磷酸钴悬浊液的温度上升到45~55℃后,再把正极板栅浸泡入磷酸钴悬浊液中,加热使水温回升到45~55℃。In step (2), after heating to raise the temperature of the cobalt phosphate suspension to 45-55°C, the positive grid is immersed in the cobalt phosphate suspension, and heated to raise the water temperature to 45-55°C.
加温目的是提高磷酸钴的溶解度,但是效果不是很明显,具有一定的效果。正极板栅浸泡磷酸钴的目的是为了在板栅表面附着磷酸钴颗粒,磷酸钴的附着量与浸泡时间无关。The purpose of heating is to improve the solubility of cobalt phosphate, but the effect is not obvious and has a certain effect. The purpose of soaking the cobalt phosphate on the positive grid is to attach cobalt phosphate particles on the surface of the grid, and the amount of cobalt phosphate attached has nothing to do with the soaking time.
干燥降温完成后8h内进行涂板。Coating was carried out within 8 hours after drying and cooling was completed.
正极铅膏的和膏过程如下:先将铅粉和占铅粉质量0.08%~0.10%纤维混合搅拌,再加入占铅粉质量11.5%的水和占铅粉质量8.2%~9.2%、比重为1.40g/mL的硫酸进行和膏。The mixing process of the positive lead paste is as follows: firstly mix and stir lead powder and fibers that account for 0.08% to 0.10% of the mass of the lead powder, and then add water that accounts for 11.5% of the mass of the lead powder and 8.2% to 9.2% of the mass of the lead powder. 1.40g/mL of sulfuric acid was carried out and paste.
负极铅膏的制作过程:将铅粉、占铅粉质量0.8%~1%的硫酸钡、占铅粉质量0.1%~0.3%的木素、占铅粉质量0.2%~0.4%的乙炔黑、占铅粉质量0.07%~0.1%的纤维混合搅拌,再加入占铅粉质量11.3%的水和占铅粉质量7.6%~8.6%、比重为1.4g/mL的硫酸和膏,得负极铅膏,将负极铅膏涂覆在负极板栅两侧,得负极板。The production process of negative lead paste: lead powder, barium sulfate accounting for 0.8%-1% by mass of lead powder, lignin accounting for 0.1%-0.3% by mass of lead powder, acetylene black accounting for 0.2%-0.4% by mass of lead powder, The fibers accounting for 0.07%-0.1% of the mass of the lead powder are mixed and stirred, and then water, which accounts for 11.3% of the mass of the lead powder, and sulfuric acid and paste, which accounts for 7.6%-8.6% of the mass of the lead powder and has a specific gravity of 1.4g/mL, are added to obtain the negative lead paste. , the negative lead paste is coated on both sides of the negative grid to obtain a negative plate.
本申请具有以下优点:This application has the following advantages:
本申请通过先将连铸正极板栅放在磷酸钴悬浊液中浸泡,再将浸泡后的正极板栅先放入相对湿度为70%~80%、温度为50~60℃环境中静置3~5h,再 放入相对湿度为30%~40%、温度为50~60℃环境中静置5~8h,板栅表面产生腐蚀层,磷酸钴颗粒附于腐蚀层外侧,最后将板栅在相对湿度为30%~40%的环境中2小时内将温度降至室温。处理后的正极板栅再经涂板、固化、组装充电后,磷酸钴渗透至板栅腐蚀层中,使板栅腐蚀膜密度增大,正极板栅与活性物质的结合力增强,降低正极活性物质软化脱落的风险,并提升了电池的耐过充电能力。In the present application, the continuous casting positive grid is first soaked in the cobalt phosphate suspension, and then the soaked positive grid is first placed in an environment with a relative humidity of 70% to 80% and a temperature of 50 to 60°C. For 3 to 5 hours, put it in an environment with a relative humidity of 30% to 40% and a temperature of 50 to 60°C for 5 to 8 hours. A corrosion layer is formed on the surface of the grid, and the cobalt phosphate particles are attached to the outside of the corrosion layer. Finally, the grid The temperature was lowered to room temperature within 2 hours in an environment with a relative humidity of 30% to 40%. After the treated positive grid is coated, cured, assembled and charged, cobalt phosphate penetrates into the grid corrosion layer, which increases the density of the grid corrosion film, enhances the bonding force between the positive grid and the active material, and reduces the positive electrode activity. The material softens the risk of falling off and improves the battery's resistance to overcharging.
实施例1Example 1
将正极合金铅制成厚度为2.5mm的铅带,冲网后制得尺寸为151mm×151mm的6-GF-100正板栅,再用尺寸为0.5×0.5mm,深度为0.12mm的滚花处理。The positive alloy lead is made into a lead tape with a thickness of 2.5mm, and the 6-GF-100 positive grid with a size of 151mm×151mm is made after punching, and then knurled with a size of 0.5×0.5mm and a depth of 0.12mm deal with.
以质量百分比计,将100份纯水和4份磷酸钴混合,加热使悬浊液温度上升到55℃后把正极板栅放入搅拌中的磷酸钴悬浊液中,加热使水温回升至55℃后,取出正极板栅放入相对湿度为80%、温度为60℃环境中静置4h,然后再将正极板栅放入相对湿度为40%、温度为60℃环境中静置6.5h,最后将正极板栅放入相对湿度为40%的环境中2小时将温度降至室温,得处理后的正极板栅。In terms of mass percentage, mix 100 parts of pure water and 4 parts of cobalt phosphate, heat to raise the temperature of the suspension to 55°C, put the positive grid into the stirring cobalt phosphate suspension, and heat to make the water temperature rise to 55°C. After ℃, take out the positive grid and put it in an environment with a relative humidity of 80% and a temperature of 60 ℃ for 4 hours, and then put the positive grid in an environment with a relative humidity of 40% and a temperature of 60 ℃ for 6.5 hours. Finally, the positive electrode grid is placed in an environment with a relative humidity of 40% for 2 hours, and the temperature is lowered to room temperature to obtain a treated positive electrode grid.
将正极铅粉1T与纤维1Kg混合搅拌,再加入115Kg的纯水,然后加入比重为1.40g/mL硫酸92Kg进行和膏,得视比重为4.30g/cm3的正极铅膏。将正 极铅膏涂覆在处理后的正极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得正极生板。Mix and stir 1T of positive lead powder and 1Kg of fiber, then add 115Kg of pure water, and then add 92Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, depending on the positive lead paste with a specific gravity of 4.30g/cm3. The positive electrode lead paste is coated on the treated positive electrode grid, and the positive electrode green plate is obtained after acid leaching, surface drying, curing, drying, and slice grinding.
将负极铅粉1T、硫酸钡10Kg、木素3Kg、乙炔黑4Kg和纤维1Kg混合搅拌,再加入113Kg纯水,然后加入比重为1.40g/mL硫酸86Kg进行和膏,制得视比重为4.40g/cm3的负极铅膏。将负极铅膏涂覆在浇铸制得的负板栅上,经淋酸、表干、固化、干燥、分片打磨后制得负极生板。Mix and stir 1T of negative lead powder, 10Kg of barium sulfate, 3Kg of lignin, 4Kg of acetylene black and 1Kg of fiber, then add 113Kg of pure water, and then add 86Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the apparent specific gravity is 4.40g. /cm3 of negative lead paste. The negative electrode lead paste is coated on the cast negative grid, and the negative electrode green plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
将制备的正极生板和负极生板经包片、组装、加酸、充电、配组整理后制得6-GF-100浮充用长寿命铅蓄电池。6-GF-100 long-life lead-acid battery for floating charge was prepared by wrapping, assembling, adding acid, charging, and grouping the prepared positive green plate and negative green plate.
取1只上述铅蓄电池进行10小时率容量检测,结果见表1。将上述铅蓄电池满充后在60±2℃的温度下以13.80V电压连续恒压充电30天,将铅蓄电池取出后在25±2℃的温度下静置24h,然后以10A的电流放电至10.50V,计算电池的放电容量。以上作为为一个测试周期,当电池放电容量低于额定容量的80%时,循环测试结束对上述电池进行解剖,结果见表2,最后一次循环不计入电池的寿命周期。Take one of the above-mentioned lead-acid batteries for 10-hour rate capacity testing, and the results are shown in Table 1. After the above-mentioned lead-acid battery is fully charged, it is continuously charged at a constant voltage of 13.80V for 30 days at a temperature of 60±2°C. 10.50V, calculate the discharge capacity of the battery. The above is a test cycle. When the battery discharge capacity is lower than 80% of the rated capacity, the battery is dissected at the end of the cycle test. The results are shown in Table 2. The last cycle is not included in the battery life cycle.
实施例2Example 2
将正极合金铅制成厚度为3.2mm的铅带,冲网后制得尺寸为237mm×151mm的6-GF-300正板栅,再用尺寸为0.5×0.5mm,深度为0.15mm的滚花处理。The positive alloy lead is made into a lead tape with a thickness of 3.2mm, and the 6-GF-300 positive grid with a size of 237mm×151mm is made after punching the net, and then knurled with a size of 0.5×0.5mm and a depth of 0.15mm deal with.
以质量百分比计,将100份纯水和3份磷酸钴混合,加热使悬浊液温度上升到45℃后把正极板栅放入搅拌中的磷酸钴悬浊液中,加热使水温回升至45℃后,取出正极板栅放入相对湿度为70%、温度为50℃环境中静置3h,然后再将正极板栅放入相对湿度为30%、温度为50℃环境中静置8h,最后将正极板栅放入相对湿度为30%的环境中2小时将温度降至室温,得处理后的正极板栅。In terms of mass percentage, mix 100 parts of pure water and 3 parts of cobalt phosphate, heat to make the temperature of the suspension rise to 45°C, put the positive grid into the stirring cobalt phosphate suspension, and heat to make the water temperature rise to 45°C. After ℃, take out the positive grid and put it in an environment with a relative humidity of 70% and a temperature of 50 ℃ for 3 hours, then put the positive grid in an environment with a relative humidity of 30% and a temperature of 50 ℃ for 8 hours, and finally The positive electrode grid is placed in an environment with a relative humidity of 30% for 2 hours, and the temperature is lowered to room temperature to obtain a treated positive electrode grid.
将正极铅粉1T与纤维0.8Kg混合搅拌,再加入115Kg的纯水,然后加入比重为1.40g/mL硫酸82Kg进行和膏,得视比重为4.32g/cm3的正极铅膏。将正极铅膏涂覆在处理后的正极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得正极生板。Mix and stir 1T of positive lead powder and 0.8Kg of fiber, then add 115Kg of pure water, and then add 82Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the positive lead paste with a specific gravity of 4.32g/cm3 can be obtained. The positive electrode lead paste is coated on the treated positive electrode grid, and the positive electrode green plate is obtained after acid dipping, surface drying, curing, drying and slice grinding.
将负极铅粉1T、硫酸钡8Kg、木素1Kg、乙炔黑2Kg和纤维0.7Kg混合搅拌,再加入113Kg纯水,然后加入比重为1.40g/mL硫酸76Kg进行和膏,制得视比重为4.42g/cm3的负极铅膏。将负极铅膏涂覆在浇铸制得的负板栅上,经淋酸、表干、固化、干燥、分片打磨后制得负极生板。Mix 1T of negative lead powder, 8Kg of barium sulfate, 1Kg of lignin, 2Kg of acetylene black and 0.7Kg of fiber, then add 113Kg of pure water, and then add 76Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the apparent specific gravity is 4.42. g/cm3 negative lead paste. The negative electrode lead paste is coated on the cast negative grid, and the negative electrode green plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
将制备的正极生板和负极生板经包片、组装、加酸、充电、配组整理后制得6-GF-300浮充用长寿命铅蓄电池。6-GF-300 long-life lead-acid battery for floating charge is prepared by wrapping the prepared positive electrode green plate and negative electrode green plate, assembling, adding acid, charging, and grouping.
取3只上述铅蓄电池串联后进行10小时率容量检测,结果见表1。将上述铅蓄电池满充后在60±2℃的温度下以6.75V电压连续恒压充电30天,将铅蓄电池取出后在25±2℃的温度下静置24h,然后以30A的电流放电至5.25V,计算电池的放电容量,以上作为一个循环周期,当电池放电容量低于额定容量的 80%,循环测试结束对上述电池进行解剖,结果见表2,最后一次循环不计入电池的寿命周期。Three above-mentioned lead-acid batteries were connected in series for 10-hour rate capacity detection. The results are shown in Table 1. After the above-mentioned lead-acid battery is fully charged, it is continuously charged at a constant voltage of 6.75V for 30 days at a temperature of 60±2°C. 5.25V, calculate the discharge capacity of the battery, the above is regarded as a cycle, when the discharge capacity of the battery is lower than 80% of the rated capacity, the battery is dissected at the end of the cycle test, the results are shown in Table 2, the last cycle is not included in the life of the battery cycle.
实施例3Example 3
将正极合金铅制成厚度为2.2mm的铅带,冲网后制得尺寸为150mm×122mm的6-FM-38正板栅,再用尺寸为0.5×0.5mm,深度为0.10mm的滚花处理。The positive alloy lead is made into a lead tape with a thickness of 2.2mm, and the 6-FM-38 positive grid with a size of 150mm×122mm is made after punching the net, and then knurled with a size of 0.5×0.5mm and a depth of 0.10mm deal with.
以质量百分比计,将100份纯水和5份磷酸钴混合,加热使悬浊液温度上升到50℃后把正极板栅放入搅拌中的磷酸钴悬浊液中,加热使水温回升至50℃后,取出正极板栅放入相对湿度为75%、温度为55℃环境中静置5h,然后再将正极板栅放入相对湿度为35%、温度为55℃环境中静置5h,最后将正极板栅放入相对湿度为35%的环境中2小时将温度降至室温,得处理后的正极板栅。In terms of mass percentage, mix 100 parts of pure water and 5 parts of cobalt phosphate, heat to raise the temperature of the suspension to 50 °C, put the positive grid into the stirring cobalt phosphate suspension, and heat to make the water temperature rise to 50 °C. After ℃, take out the positive grid and put it in an environment with a relative humidity of 75% and a temperature of 55 ℃ for 5 hours, and then put the positive grid in an environment with a relative humidity of 35% and a temperature of 55 ℃ for 5 hours, and finally The positive electrode grid was placed in an environment with a relative humidity of 35% for 2 hours, and the temperature was lowered to room temperature to obtain a treated positive electrode grid.
将正极铅粉1T与纤维0.9Kg混合搅拌,再加入115Kg的纯水,然后加入比重为1.40g/mL硫酸82Kg进行和膏,得视比重为4.30g/cm3的正极铅膏。将正极铅膏涂覆在处理后的正极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得正极生板。Mix 1T of positive lead powder with 0.9Kg of fiber, then add 115Kg of pure water, and then add 82Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the positive lead paste with a specific gravity of 4.30g/cm3 can be obtained. The positive electrode lead paste is coated on the treated positive electrode grid, and the positive electrode green plate is obtained after acid dipping, surface drying, curing, drying and slice grinding.
将负极铅粉1T、硫酸钡9Kg、木素2Kg、乙炔黑3Kg和纤维0.8Kg混合搅拌,再加入113Kg纯水,然后加入比重为1.40g/mL硫酸81Kg进行和膏, 得视比重为4.41g/cm3的负极铅膏。将负极铅膏涂覆在浇铸制得的负板栅上,经淋酸、表干、固化、干燥、分片打磨后制得负极生板。Mix and stir 1T of negative lead powder, 9Kg of barium sulfate, 2Kg of lignin, 3Kg of acetylene black and 0.8Kg of fiber, then add 113Kg of pure water, and then add 81Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the specific gravity is 4.41g /cm3 of negative lead paste. The negative electrode lead paste is coated on the cast negative grid, and the negative electrode green plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
将制备的正极生板和负极生板经包片、组装、加酸、充电、配组整理后制得6-MF-38浮充用长寿命铅蓄电池。The prepared positive electrode green plate and negative electrode green plate are packaged, assembled, acidified, charged, assembled and arranged to obtain 6-MF-38 long-life lead-acid battery for floating charge.
取1只上述铅蓄电池进行10小时率容量检测,结果见表1。将上述铅蓄电池满充后在60±2℃的温度下以13.80V电压连续恒压充电30天,将铅蓄电池取出后在25±2℃的温度下静置24h,然后以3.8A的电流放电至10.50V,计算电池的放电容量。以上作为为一个测试周期,当电池放电容量低于额定容量的80%时,循环测试结束对上述电池进行解剖,结果见表2,最后一次循环不计入电池的寿命周期。Take one of the above-mentioned lead-acid batteries for 10-hour rate capacity testing, and the results are shown in Table 1. After the above-mentioned lead-acid battery is fully charged, it is continuously charged at a constant voltage of 13.80V for 30 days at a temperature of 60±2°C. After taking out the lead-acid battery, it is left for 24h at a temperature of 25±2°C, and then discharged at a current of 3.8A. To 10.50V, calculate the discharge capacity of the battery. The above is a test cycle. When the battery discharge capacity is lower than 80% of the rated capacity, the battery is dissected at the end of the cycle test. The results are shown in Table 2. The last cycle is not included in the battery life cycle.
对比例1Comparative Example 1
将正极铅粉1T和纤维1Kg混合搅拌,再加入115Kg纯水,然后加入92Kg比重为1.40g/mL硫酸进行和膏,得视比重为4.30g/cm3的正极铅膏。将正极铅膏涂覆在浇铸制得的正极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得的6-GF-100正极生板。Mix and stir 1T of positive lead powder and 1Kg of fiber, then add 115Kg of pure water, and then add 92Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, depending on the positive lead paste with a specific gravity of 4.30g/cm3. The 6-GF-100 positive electrode green plate is prepared by coating the positive electrode lead paste on the cast positive electrode grid, leaching acid, surface drying, curing, drying, and slicing polishing.
将负极铅粉1T和硫酸钡10Kg、木素3Kg、乙炔黑4Kg和纤维1Kg混合搅拌,再加入113Kg纯水,然后加入86Kg比重为1.40g/mL硫酸进行和膏,得视比重为4.40g/cm3的负极铅膏。将负极铅膏涂在浇铸制得的6-GF-100负极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得负极极板。Mix and stir 1T of negative lead powder, 10Kg of barium sulfate, 3Kg of lignin, 4Kg of acetylene black and 1Kg of fiber, then add 113Kg of pure water, then add 86Kg of sulfuric acid with a specific gravity of 1.40g/mL to mix the paste, and the specific gravity is 4.40g/mL. cm3 negative lead paste. The negative electrode lead paste is coated on the casted 6-GF-100 negative electrode grid, and the negative electrode plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
将制得的正极极板和负极极板经包片、组装、加酸、充电、配组整理后制得6-GF-100铅蓄电池。6-GF-100 lead-acid battery is prepared by wrapping, assembling, adding acid, charging, and arranging the prepared positive electrode plate and negative electrode plate.
取1只上述铅蓄电池进行10小时率容量检测,结果如表1。铅蓄电池满充后在60±2℃在环境下以13.80V电压连续充电30天,将电池取出后在25±2℃在温度下静置24h后,再以10A的电流放电至10.50V,计算电池的放电容量。以上作为为一个测试周期,当电池放电容量低于额定容量的80%时,循环测试结束对上述电池进行解剖,结果见表2,最后一次循环不计入电池的寿命周期。Take one of the above-mentioned lead-acid batteries for 10-hour rate capacity testing, and the results are shown in Table 1. After the lead-acid battery is fully charged, it is continuously charged at 13.80V at 60±2℃ for 30 days. After taking out the battery, let it stand at 25±2℃ for 24h, and then discharge it to 10.50V at a current of 10A. Calculate The discharge capacity of the battery. The above is a test cycle. When the battery discharge capacity is lower than 80% of the rated capacity, the battery is dissected at the end of the cycle test. The results are shown in Table 2. The last cycle is not included in the battery life cycle.
对比例2Comparative Example 2
将正极铅粉1T和纤维0.8Kg混合搅拌,再加入115Kg纯水,然后加入82Kg比重为1.40g/mL硫酸进行和膏,制得视比重为4.32g/cm3的正极铅膏。将正极铅膏涂覆在浇铸制得的正极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得的6-GF-100正极生板。Mix and stir 1T of positive lead powder and 0.8Kg of fiber, add 115Kg of pure water, and then add 82Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste to obtain a positive lead paste with a specific gravity of 4.32g/cm3. The 6-GF-100 positive electrode green plate is prepared by coating the positive electrode lead paste on the cast positive electrode grid, leaching acid, surface drying, curing, drying, and slicing polishing.
将负极铅粉1T和硫酸钡8Kg、木素1Kg、乙炔黑2Kg和纤维0.7Kg混合搅拌,再加入113Kg纯水,然后加入76Kg比重为1.40g/mL硫酸进行和膏,制得视比重为4.42g/cm3的负极铅膏。将负极铅膏涂在浇铸制得的6-GF-300负极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得负极极板。Mix and stir 1T of negative lead powder, 8Kg of barium sulfate, 1Kg of lignin, 2Kg of acetylene black and 0.7Kg of fiber, then add 113Kg of pure water, and then add 76Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the apparent specific gravity is 4.42. g/cm3 negative lead paste. The negative electrode lead paste is coated on the casted 6-GF-300 negative electrode grid, and the negative electrode plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
将制得的正极极板和负极极板经包片、组装、加酸、充电、配组整理后制得6-GF-300铅蓄电池。6-GF-300 lead-acid battery is prepared by wrapping, assembling, adding acid, charging, and arranging the prepared positive electrode plate and negative electrode plate.
取3只上述铅蓄电池串联后进行10小时率容量检测,结果如表1。铅蓄电池满充后在60±2℃在环境下以6.75V电压连续充电30天,将电池取出后在25±2℃在温度下静置24h后,再以30A的电流放电至5.25V,计算电池的放电容量。以上作为为一个测试周期,当电池放电容量低于额定容量的80%时,循环测试结束对上述电池进行解剖,结果见表2,最后一次循环不计入电池的寿命周期。Three above-mentioned lead-acid batteries were connected in series for 10-hour rate capacity detection. The results are shown in Table 1. After the lead-acid battery is fully charged, it is continuously charged at 6.75V at 60±2℃ for 30 days. After taking out the battery, let it stand at 25±2℃ for 24h, and then discharge it to 5.25V at a current of 30A. Calculate The discharge capacity of the battery. The above is a test cycle. When the battery discharge capacity is lower than 80% of the rated capacity, the battery is dissected at the end of the cycle test. The results are shown in Table 2. The last cycle is not included in the battery life cycle.
对比例3Comparative Example 3
将正极铅粉1T和纤维0.9Kg混合搅拌,再加入115Kg纯水,然后加入92Kg比重为1.40g/mL硫酸进行和膏,制得视比重为4.30g/cm3的正极铅膏。将正极铅膏涂覆在浇铸制得的正极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得的6-MF-38正极生板。Mix and stir 1T of positive lead powder and 0.9Kg of fiber, then add 115Kg of pure water, and then add 92Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste to obtain a positive lead paste with a specific gravity of 4.30g/cm3. The 6-MF-38 positive electrode green plate is prepared by coating the positive electrode lead paste on the positive electrode grid made by casting, and after acid leaching, surface drying, curing, drying, and slice grinding.
将负极铅粉1T和硫酸钡9Kg、木素2Kg、乙炔黑3Kg和纤维0.8Kg混合搅拌,再加入113Kg纯水,然后加入81Kg比重为1.40g/mL硫酸进行和膏,调制得视比重为4.41g/cm3的负极铅膏。将负极铅膏涂在浇铸制得的6-MF-38负极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得负极极板。Mix and stir 1T of negative lead powder, 9Kg of barium sulfate, 2Kg of lignin, 3Kg of acetylene black and 0.8Kg of fiber, then add 113Kg of pure water, and then add 81Kg of sulfuric acid with a specific gravity of 1.40g/mL to mix the paste, and the specific specific gravity is 4.41. g/cm3 negative lead paste. The negative electrode lead paste is coated on the casted 6-MF-38 negative electrode grid, and the negative electrode plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
将制得的正极极板和负极极板经包片、组装、加酸、充电、配组整理后制得6-MF-38铅蓄电池。A 6-MF-38 lead-acid battery is prepared by wrapping, assembling, adding acid, charging, and arranging the prepared positive electrode plate and negative electrode plate.
取1只上述铅蓄电池进行10小时率容量检测,结果如表1。铅蓄电池满充后在60±2℃在环境下以13.80V电压连续充电30天,将电池取出后在25土2℃ 在温度下静置24h后,再以3.8A的电流放电至10.50V,计算电池的放电容量。以上作为为一个测试周期,当电池放电容量低于额定容量的80%时,循环测试结束对上述电池进行解剖,结果见表2,最后一次循环不计入电池的寿命周期。Take one of the above-mentioned lead-acid batteries for 10-hour rate capacity testing, and the results are shown in Table 1. After the lead-acid battery is fully charged, it is continuously charged at 13.80V at 60±2℃ for 30 days. After taking out the battery, it is allowed to stand at 25±2℃ for 24h, and then discharged to 10.50V with a current of 3.8A. Calculate the discharge capacity of the battery. The above is a test cycle. When the battery discharge capacity is lower than 80% of the rated capacity, the battery is dissected at the end of the cycle test. The results are shown in Table 2. The last cycle is not included in the battery life cycle.
对比例4Comparative Example 4
将正极合金铅制成厚度为2.5mm的铅带,冲网后制得尺寸为151mm×151mm的6-GF-100正板栅,再用尺寸为0.5×0.5mm,深度为0.12mm的滚花处理。The positive alloy lead is made into a lead tape with a thickness of 2.5mm, and the 6-GF-100 positive grid with a size of 151mm×151mm is made after punching, and then knurled with a size of 0.5×0.5mm and a depth of 0.12mm deal with.
以质量百分比计,将100份纯水和5份磷酸钴混合,加热使溶液温度上升到55℃,停止搅拌待磷酸钴颗粒沉淀后,获得磷酸钴的饱和水溶液,未溶解的部分沉淀后去除,将正极板栅放入磷酸钴水溶液中,加热使水温回升至55℃。取出正极板栅放入相对湿度为80%、温度为60℃环境中静置4h,然后再将正极板栅放入相对湿度为40%、温度为60℃环境中静置6.5h,最后将正极板栅放入相对湿度为40%的环境中2小时将温度降至室温,得处理后的正极板栅。In terms of mass percentage, 100 parts of pure water and 5 parts of cobalt phosphate were mixed, heated to raise the temperature of the solution to 55°C, and the stirring was stopped until the cobalt phosphate particles were precipitated to obtain a saturated aqueous solution of cobalt phosphate, and the undissolved part was precipitated and removed, The positive grid was placed in the cobalt phosphate aqueous solution, and heated to bring the water temperature back to 55°C. Take out the positive grid and put it in an environment with a relative humidity of 80% and a temperature of 60 °C for 4 hours, then put the positive grid in an environment with a relative humidity of 40% and a temperature of 60 °C for 6.5 hours, and finally put the positive electrode The grid is placed in an environment with a relative humidity of 40% for 2 hours, and the temperature is lowered to room temperature to obtain a treated positive grid.
将正极铅粉1T与纤维1Kg混合搅拌,再加入115Kg的纯水,然后加入比重为1.40g/mL硫酸92Kg进行和膏,得视比重为4.30g/cm3的正极铅膏。将正极铅膏涂覆在处理后的正极板栅上,经淋酸、表干、固化、干燥、分片打磨后制得正极生板。Mix and stir 1T of positive lead powder and 1Kg of fiber, then add 115Kg of pure water, and then add 92Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, depending on the positive lead paste with a specific gravity of 4.30g/cm3. The positive electrode lead paste is coated on the treated positive electrode grid, and the positive electrode green plate is obtained after acid dipping, surface drying, curing, drying and slice grinding.
将负极铅粉1T、硫酸钡10Kg、木素3Kg、乙炔黑4Kg和纤维1Kg混合搅拌,再加入113Kg纯水,然后加入比重为1.40g/mL硫酸86Kg进行和膏,制 得视比重为4.40g/cm3的负极铅膏。将负极铅膏涂覆在浇铸制得的负板栅上,经淋酸、表干、固化、干燥、分片打磨后制得负极生板。Mix and stir 1T of negative lead powder, 10Kg of barium sulfate, 3Kg of lignin, 4Kg of acetylene black and 1Kg of fiber, then add 113Kg of pure water, and then add 86Kg of sulfuric acid with a specific gravity of 1.40g/mL to make a paste, and the apparent specific gravity is 4.40g. /cm3 of negative lead paste. The negative electrode lead paste is coated on the cast negative grid, and the negative electrode green plate is obtained after acid leaching, surface drying, curing, drying and slice grinding.
将制备的正极生板和负极生板经包片、组装、加酸、充电、配组整理后制得6-GF-100浮充用长寿命铅蓄电池。6-GF-100 long-life lead-acid battery for floating charge was prepared by wrapping, assembling, adding acid, charging, and grouping the prepared positive green plate and negative green plate.
取1只上述铅蓄电池进行10小时率容量检测,结果见表1。将上述铅蓄电池满充后在60±2℃的温度下以13.80V电压连续恒压充电30天,将铅蓄电池取出后在25±2℃的温度下静置24h,然后以10A的电流放电至10.50V,计算电池的放电容量。以上作为为一个测试周期,当电池放电容量低于额定容量的80%时,循环测试结束对上述电池进行解剖,结果见表2,最后一次循环不计入电池的寿命周期。Take one of the above-mentioned lead-acid batteries for 10-hour rate capacity testing, and the results are shown in Table 1. After the above-mentioned lead-acid battery is fully charged, it is continuously charged at a constant voltage of 13.80V for 30 days at a temperature of 60±2°C. 10.50V, calculate the discharge capacity of the battery. The above is a test cycle. When the battery discharge capacity is lower than 80% of the rated capacity, the battery is dissected at the end of the cycle test. The results are shown in Table 2. The last cycle is not included in the battery life cycle.
表1铅蓄电池进行10小时率容量Table 1 Lead-acid battery for 10-hour rate capacity
从表1中可以看出,采用本申请中的方法制备的铅蓄电池的10小时率容量与对比组没有区别。As can be seen from Table 1, the 10-hour rate capacity of the lead storage battery prepared by the method in the present application is no different from that of the control group.
表2铅蓄电池的容检放电周期和有效循环周期次数Table 2 The capacity inspection discharge cycle and effective cycle number of lead-acid battery
从表2中可以看出,本申请中经磷酸钴悬浊液浸泡时效后的正极板栅更耐腐蚀,经磷酸钴水溶液浸泡后的正极板栅的耐腐蚀能力略强于不浸泡的正极板栅;正极板栅经磷酸钴悬浊液浸泡时效后与活性物质结合力增强,采用本申请方案中的正极板栅制备的铅蓄电池的放电循环周期提升33.3%以上。As can be seen from Table 2, the positive electrode grid after soaking and aging in the cobalt phosphate suspension in this application is more corrosion-resistant, and the corrosion resistance of the positive grid after soaking in the cobalt phosphate aqueous solution is slightly stronger than that of the non-immersed positive electrode plate grid; the positive electrode grid is soaked in cobalt phosphate suspension for aging, and the bonding force with the active material is enhanced, and the discharge cycle period of the lead battery prepared by using the positive grid in the solution of the present application is increased by more than 33.3%.
本领域技术人员可以理解附图只是一个优选实施场景的示意图,附图中的模块或流程并不一定是实施本申请实施例所必须的。Those skilled in the art can understand that the accompanying drawing is only a schematic diagram of a preferred implementation scenario, and the modules or processes in the accompanying drawing are not necessarily necessary for implementing the embodiments of the present application.
本领域技术人员可以理解实施场景中的装置中的模块可以按照实施场景描述进行分布于实施场景的装置中,也可以进行相应变化位于不同于本实施场 景的一个或多个装置中。上述实施场景的模块可以合并为一个模块,也可以进一步拆分成多个子模块。Those skilled in the art can understand that the modules in the device in the implementation scenario may be distributed in the device in the implementation scenario according to the description of the implementation scenario, or may be located in one or more devices different from the implementation scenario with corresponding changes. The modules of the above implementation scenarios may be combined into one module, or may be further split into multiple sub-modules.
以上公开的仅为本申请实施例的具体实施场景,但是,本申请实施例并非局限于此,任何本领域的技术人员能思之的变化都应落入本申请实施例的业务限制范围。The above disclosures are only specific implementation scenarios of the embodiments of the present application, however, the embodiments of the present application are not limited thereto, and any changes that can be conceived by those skilled in the art should fall within the scope of service limitations of the embodiments of the present application.
Claims (10)
- 一种正极板的制备方法,其特征在于,包括以下步骤:A method for preparing a positive plate, comprising the following steps:(1)制备正极板栅;(1) Preparation of positive grid;(2)正极板栅的浸泡,(2) Immersion of the positive grid,按质量比计,每100份纯水和3~5份磷酸钴配置成磷酸钴悬浊液,将正极板栅放入磷酸钴悬浊液中浸泡;According to the mass ratio, every 100 parts of pure water and 3 to 5 parts of cobalt phosphate are prepared into a cobalt phosphate suspension, and the positive grid is placed in the cobalt phosphate suspension to soak;(3)正极板栅的干燥降温,(3) Drying and cooling of the positive grid,浸泡后的正极板栅先在相对湿度为70%~80%、温度为50~60℃的条件下静置3h~5h,再在相对湿度为30%~40%、温度为50~60℃的条件下静置5~8h,最后在相对湿度为30%~40%的条件下2小时内将温度降至室温;The immersed positive grid is first kept for 3h to 5h under the conditions of relative humidity of 70% to 80% and temperature of 50 to 60°C, and then placed under the conditions of relative humidity of 30% to 40% and temperature of 50 to 60°C. Under the condition of standing for 5-8 hours, the temperature is finally lowered to room temperature within 2 hours under the condition of relative humidity of 30%-40%;(4)和膏,制备正极铅膏;(4) and paste to prepare positive lead paste;(5)涂板,将正极铅膏涂板到正极板栅。(5) Coating, apply the positive lead paste to the positive grid.
- 如权利要求1所述的正极板的制备方法,其特征在于,步骤(1)中先将合金铅熔化后制成铅带,再经过辊压、冲网、滚花,得正极板栅。The method for preparing a positive electrode plate according to claim 1, wherein in step (1), the alloy lead is first melted and then made into a lead strip, and then rolled, punched, and knurled to obtain a positive electrode grid.
- 如权利要求2所述的正极板的制备方法,其特征在于,辊压后铅带的厚度为2.2~3.2mm。The method for preparing a positive electrode plate according to claim 2, wherein the thickness of the lead strip after rolling is 2.2-3.2 mm.
- 如权利要求2所述的正极板的制备方法,其特征在于,滚花的深度为0.1~0.15mm。The method for preparing a positive electrode plate according to claim 2, wherein the depth of the knurling is 0.1-0.15 mm.
- 如权利要求1所述的正极板的制备方法,其特征在于,步骤(2)中加热使磷酸钴悬浊液的温度上升到45~55℃后,再把正极板栅浸泡入磷酸钴悬浊液 中,加热使水温回升到45~55℃。The method for preparing a positive electrode plate according to claim 1, characterized in that, after heating in step (2) to raise the temperature of the cobalt phosphate suspension to 45-55°C, the positive electrode grid is immersed in the cobalt phosphate suspension again. In the liquid, heating to make the water temperature rise back to 45 ~ 55 ℃.
- 如权利要求1所述的正极板的制备方法,其特征在于,干燥降温完成后8h内进行涂板。The method for preparing a positive plate according to claim 1, wherein the plate is coated within 8 hours after the drying and cooling are completed.
- 如权利要求1所述的正极板的制备方法,其特征在于,正极铅膏包括铅粉以及占铅粉质量0.08%~0.10%的纤维,占铅粉质量11.5%的水和占铅粉质量8.2%~9.2%、比重为1.40g/mL的硫酸。The method for preparing a positive plate according to claim 1, wherein the positive lead paste comprises lead powder and fibers accounting for 0.08% to 0.10% of the mass of the lead powder, water accounting for 11.5% of the mass of the lead powder and 8.2% of the mass of the lead powder % to 9.2% sulfuric acid with a specific gravity of 1.40 g/mL.
- 如权利要求7所述的正极板的制备方法,其特征在于,正极铅膏的和膏过程如下:先将铅粉和纤维混合搅拌,再加入水和硫酸进行和膏。The method for preparing a positive plate according to claim 7, wherein the process of mixing the positive lead paste is as follows: firstly, the lead powder and the fiber are mixed and stirred, and then water and sulfuric acid are added to carry out the mixing process.
- 一种铅蓄电池,其特征在于,包含正极板和负极板,正极板使用权利要求1~8任一制备方法制备的正极板。A lead storage battery, characterized in that it comprises a positive electrode plate and a negative electrode plate, and the positive electrode plate adopts the positive electrode plate prepared by any one of the preparation methods of claims 1-8.
- 如权利要求9所述的铅蓄电池,其特征在于,The lead storage battery according to claim 9, wherein负极铅膏的配方:铅粉、占铅粉质量0.8%~1%的硫酸钡、占铅粉质量0.1%~0.3%的木素、占铅粉质量0.2%~0.4%的乙炔黑、占铅粉质量0.07%~0.1%的纤维、占铅粉质量11.3%的水和占铅粉质量7.6%~8.6%、比重为1.4g/mL的硫酸;The formula of negative lead paste: lead powder, barium sulfate accounting for 0.8%-1% by mass of lead powder, lignin accounting for 0.1%-0.3% by mass of lead powder, acetylene black accounting for 0.2%-0.4% by mass of lead powder, lead powder accounting for 0.2%-0.4% by mass 0.07%-0.1% of the powder mass of fiber, 11.3% of the lead powder mass of water and 7.6% to 8.6% of the lead powder mass of sulfuric acid with a specific gravity of 1.4g/mL;负极板的制备过程如下:将铅粉以及硫酸钡、木素、乙炔黑和纤维混合搅拌,再加入水和硫酸和膏,得负极铅膏,将负极铅膏涂覆在负极板栅两侧,得负极板。The preparation process of the negative electrode plate is as follows: the lead powder, barium sulfate, lignin, acetylene black and fiber are mixed and stirred, and then water, sulfuric acid and paste are added to obtain the negative electrode lead paste, and the negative electrode lead paste is coated on both sides of the negative electrode grid. Get the negative plate.
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