WO2001020699A1 - A method of producing a lead-base plate for a storage battery - Google Patents

A method of producing a lead-base plate for a storage battery Download PDF

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Publication number
WO2001020699A1
WO2001020699A1 PCT/CN1999/000146 CN9900146W WO0120699A1 WO 2001020699 A1 WO2001020699 A1 WO 2001020699A1 CN 9900146 W CN9900146 W CN 9900146W WO 0120699 A1 WO0120699 A1 WO 0120699A1
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WIPO (PCT)
Prior art keywords
lead
battery
plate
grid
manufacturing
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PCT/CN1999/000146
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French (fr)
Chinese (zh)
Inventor
Yuerong Liu
Yuesheng Feng
Yifeng Feng
Rong Sun
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Yuerong Liu
Yuesheng Feng
Yifeng Feng
Rong Sun
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Application filed by Yuerong Liu, Yuesheng Feng, Yifeng Feng, Rong Sun filed Critical Yuerong Liu
Priority to AU57257/99A priority Critical patent/AU5725799A/en
Priority to PCT/CN1999/000146 priority patent/WO2001020699A1/en
Publication of WO2001020699A1 publication Critical patent/WO2001020699A1/en

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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/14Electrodes for lead-acid accumulators
    • H01M4/16Processes of manufacture
    • H01M4/20Processes of manufacture of pasted electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/72Grids
    • H01M4/73Grids for lead-acid accumulators, e.g. frame plates
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/44Methods for charging or discharging
    • H01M10/446Initial charging measures
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Definitions

  • the invention belongs to the field of battery electrode plates, and particularly relates to a method for manufacturing a lead plate for a battery.
  • the battery we have seen is manufactured by a more mature traditional process, and its electrode plate process includes grid formation, filling and curing of active materials (lead paste), and formation of three main processes.
  • the shaped grid is called the electrode plate after being filled with the solidified lead paste, and the electrode plate is called the cooked electrode plate after being processed (formed) by the electrification process.
  • the active materials lead and lead dioxide that participate in the battery flow reaction are loose porous bodies that need to be fixed on a carrier, which is called a grid or lattice (framework).
  • a carrier which is called a grid or lattice (framework).
  • the role of the grid is to support activity
  • the material also transmits current, and the grid with good conductivity and reasonable structure can make the current be evenly distributed on the active material along the ribs, thereby improving the utilization rate of the active material.
  • the grid is usually made of a lead-based alloy, and there are also pure lead or lead-plated copper mesh (for the negative electrode).
  • the molding process usually uses casting, and a few use the method of drawing a mesh.
  • Lead-based alloys are mainly lead, usually accounting for about 95% or more.
  • the metals added are antimony, arsenic, cadmium, tin, calcium, silver, aluminum, strontium, etc., or combinations thereof.
  • Lead-based alloy grids formed by the hot casting method may not only form characteristic solid solution bodies, but also may form mesophases with different crystal structures, most of which are compounds between metals or between metals and metalloids. Studies have shown that this compound is dominated by metal bonds and often does not follow the valence law, which has an effect on the conduction capacity of the alloy. Since the industrial control conditions of the hot-cast lead substrate grid are not absolutely the same, even if the grids manufactured by the same hot-casting machine have the same number of internal bubbles and alloy lattices, there are certain differences. There have been many literature reports on the aging hardening of metal dissolution for a long time.
  • the lead-based alloy grid is also only improved from the shape of the grid, such as GB2127614, April 11, 1984, by Sonnenschein A company application discloses an electrode grid having a honeycomb structure, and the shape of the electrode grid is substantially similar to an oblique quadrangle or a regular hexagon.
  • the electrode plate of a lead storage battery is made of lead paste filled on a grid.
  • the formula of the lead paste, the method of the paste, and the curing conditions have an important effect on the phase composition of the electrode plate.
  • various countries have matured and mastered the formulation and curing conditions of lead paste, and have seen it in a large number of literature reports, such as EP0348702, which was applied by Sonnenschein Company on January 3, 1990.
  • a method for coating an electrode grid is made of lead and is performed by dipping a solution of a coating material.
  • the energization process of the electrode plates is called formation, and the electrode plates are called cooked plates after being formed.
  • the electrolytic plate is usually formed by using an electrolytic cell. After the formation, the electrode is washed and dried. Dry, and then battery assembly. Because the chemical conversion tank uses dilute sulfuric acid as the electrolyte, acid mist and environmental pollution generated during the chemical conversion process have always been difficult problems for the battery industry.
  • the purpose of the present invention is to provide a method for manufacturing a lead plate for a storage battery, that is, to utilize the inherent characteristics of the metal, change the formula of the lead paste and the formation of the electrode plate, so as to prolong the service life of the manufactured plate and enhance the conductivity. And the battery can reduce environmental pollution.
  • the manufacturing method of the present invention includes three main steps: hot-casting grids, filling and curing active materials on the grids, and transforming the electrode plates with the cured active materials, which are characterized by: Cold extrusion is applied to the rear grid; or hydrated silicate is added to the grid to fill and solidify the active material and paste formulation; or pulsed current is used to form the solidified electrode plate.
  • the cold extrusion applied to the grid is applied pressure from the outside to the inside, and the pressure is 100-800Kg / C m 2.
  • the cold extrusion may be applied to the grid more than once.
  • the hydrated silicate added to the lead paste formula can be added to the positive lead paste, or to the negative lead paste, or to both the positive and negative lead paste formulations.
  • the proportion of hydrated silicate added to the lead paste formula is 0.1 to 3% by weight in the lead paste formula.
  • the hydrated silicate added in the lead paste formulation is subjected to an industrial acid dipping treatment in advance.
  • the electrode plate formation can be performed either before the battery or battery pack is assembled, or after the green plate is assembled into a battery or a battery pack. After the green board is assembled into a battery or a battery pack, it is charged and formed, and its lead paste formulation does not need to be added with Pb 3 0 4 .
  • the pulsating current used in the formation is a periodic pulsating current, and the frequency is an arbitrary value.
  • the waveform of the current is a square wave, a sawtooth wave, a negative pulse wave, a sine half wave, a full sine wave, or any combination thereof.
  • the current intensity of the pulsating current is greater than 0.2C, and the average charging voltage is 1-2 times the rated voltage of the battery or battery pack.
  • the air bubbles inside can easily cause the plate to conduct Heating, meanwhile, the shape of the metal lattice is irregular and the arrangement and combination are loose, these factors directly affect the conductivity of the grid.
  • the lattice arrangement of lead-based alloys is easily deformed by force.
  • a cold extrusion process is added. That is, a conventional punch (for example, 100-800K g / cm 2 pressure) or a hydraulic press is used to form the lead substrate.
  • the cold-extruded grid can be used for both positive and negative electrodes.
  • Formula of positive lead paste It is made by mixing H 2 S0 4 , H 2 0 and Pb powder with proper proportion, and the apparent density is controlled at
  • Negative lead paste formula On the basis of 1), organic swelling agents such as barium sulfate and humic acid, 0-hydroxy-naphthoic acid, sodium lignosulfonate, acetylene black, and synthetic tanning agent are selected to be added. You can choose one or several kinds to mix according to a certain proportion.
  • organic swelling agents such as barium sulfate and humic acid, 0-hydroxy-naphthoic acid, sodium lignosulfonate, acetylene black, and synthetic tanning agent are selected to be added. You can choose one or several kinds to mix according to a certain proportion.
  • the hydrated silicates according to the present invention are, for example, Montmorillorite, and the weight percentage of the montmorillonite additive in the lead paste formulation is 0.1 to 3%.
  • the chemical activity of the positive electrode Pb is mainly determined by the hydrogen content, while the hydrogen contained in the positive electrode Pb (3 ⁇ 4 exists mainly on the surface of the crystal of Pb in the form of adsorbed water.
  • the smallest unit of the structure of the positive electrode active material is PbC ⁇ particles, not Pb02 crystals.
  • Pb (3 ⁇ 4 particles are composed of hydrated Pbft-PbO (0H) 2, a few! ⁇
  • the particles contact to form a microporous structure Aggregates and aggregate skeletons with macroporous structures. Electrochemical reactions occur on microporous aggregates, which transfer ions and form PbSO on the macroporous aggregates.
  • Montmorillonite is a hydrated silicate with extremely strong water absorption capacity. After absorbing water, its volume expansion can increase several times to ten times. It has strong adsorption and cation exchange performance. The proper addition of montmorillonite to the positive lead paste can first improve the chemical activity of Pbi ⁇ due to the water-absorbing dependence of montmorillonite. On the other hand, since PbCfe is converted to PbSO ⁇ and PbSC ⁇ is larger than PbOj when the battery is discharged, the volume of the entire positive electrode substance is increased.
  • an appropriate amount of montmorillonite is added to the positive lead paste, and its volume expands after absorbing water Physical properties can effectively alleviate the softening and loosening of the active material caused by the volume change during the charge and discharge process, and prolong the service life of the positive electrode plate.
  • Adding an appropriate amount of montmorillonite to the negative lead paste is mainly used to inhibit the passivation of the negative electrode at different temperatures at low temperatures (below -15 ° C) and high rate discharge (above 1 hour rate), that is, the potential of the negative electrode is obvious. Moving forward, the reaction speed will obviously decrease. It is generally believed that the negative charge capacity of the negative electrode at -4 ° C is only 10% at 25 ° C and the low-temperature discharge capacity is also limited by the negative electrode. The proper addition of montmorillonite in the negative electrode lead paste can greatly improve the negative electrode material.
  • the energization process of the electrode plates is called formation, and the electrode plates are called cooked plates after being formed.
  • the traditional electrochemical theory has fully recognized the charge formation.
  • the electrode materials prepared by chemical methods lack electrochemical activity and are not suitable for use as plates in batteries. Only by electrochemical processing can the chemical activity of the plate materials be fully activated. So that the battery has a useful value of capacity.
  • the method of using the charging method to activate the activity of the plate material is called chemical conversion.
  • Pb prepared by electrochemical methods contains far more hydrogen than that prepared by chemical methods. the content of hydrogen in the form of dependency determines the degree of chemical activity of Pb0 2.
  • Table 1 lists the general formation methods of non-dry-charge plate.
  • dry-charge electrode plates in order to ensure the first discharge capacity after adding acid, a "two charge and one discharge" formation method is sometimes used.
  • the electrode plate formation method there are also a few products that use green plates (unformed electrode plates) to form batteries or battery packs and then charge and form them.
  • the battery or battery pack formation method is divided into two acid injection methods and one The acid injection method, Pb 3 04 must be added to the lead paste used to make the electrode plate, and the comparison process and the advantages and disadvantages of the acidification with one and two injections are shown in Table 2.
  • the charging current of the above-mentioned existing electrode formation methods adopts continuous DC power (constant current or phased DC). Advantages and disadvantages of the formation process
  • the battery has
  • Power on time is at least 72h 2. Long formation time
  • the method for forming a pulsating current according to the present invention belongs to the formation of a battery or a battery pack.
  • the difference from the existing methods is that:
  • Lead paste does not need to be added with Pb 3 0 4 , the formation time does not need to be as long as 36-72 hours, and the battery or battery pack charging time is only 10-18 hours to achieve the purpose of electrode formation and full charge.
  • This formed current is characterized by the use of periodic pulsating current, such as square wave, sawtooth wave, negative pulse wave, sine half wave, sine full wave, etc., as shown in Figure 1-5.
  • the frequency of the pulsating current can be the mains frequency, and it can be formed by one-time charging.
  • the current intensity of the pulsating current is generally greater than 0.2C, but smaller than the withstand capacity of the plates.
  • the pulse depth is changed (for example, the negative pulse depth is changed to 1 / 2 peak, square wave low voltage changed to 1/5 peak, 1/3 peak, etc.)
  • the charging method is changed to two rushes, one discharge, Three chargers, two amplifiers, etc. To the purpose of charge formation.
  • the above-mentioned methods of cold-pressing the grid, adding montmorillonite to the formulation of lead paste, or charging the battery or battery pack with a periodic pulsating current can be applied to the plates of lead-acid batteries, as well as
  • the embodiment described above is only a preferred embodiment of the principle of the present invention to a battery plate of a silicon sol (salt) as an electrolyte.
  • the grid can be cold extruded more than once. For example, if the grid is extruded twice (front and back), the montmorillonite is treated by acid dipping before the paste. The montmorillonite is added to the lead paste formula. Prior to the industrial acid (such as sulfuric acid) impregnation treatment, it is beneficial to fully mix with the paste.
  • the electrode plate manufactured by the cold extrusion method of the present invention increases the bonding strength between the metal lattices and increases the external tensile force. Therefore, in a grid with an appearance structure of equal weight, it can withstand more lead powder adhesion. In other words, with the same amount of lead powder adhered, the grid's ability to resist stress deformation is enhanced. Therefore, after the cold extrusion method is adopted, the amount of lead used can be reduced to achieve the same grid effect, thereby reducing the weight of the battery and increasing the specific energy of the battery.
  • the utilization rate of active materials can be effectively improved, and the life of the plate and the charging and discharging characteristics can be improved.
  • the present invention uses a periodic pulsating current formation method to enable the plate material to more effectively activate the chemical activity of the plate material under the action of the pulsating current, while reducing the time required for the plate to form.
  • FIG. 1 Schematic diagram of square waveform current used for charging
  • FIGS. (a), (b), and (c) are schematic diagrams of the sawtooth wave current used for charging formation
  • FIG. 1 Schematic diagram of negative pulse waveform current used for charge formation
  • Figure 4 Schematic diagram of sine half-wave pulsating current used for charging formation
  • Figure 5 Schematic diagram of sinusoidal full-wave pulsating current used for charge formation.
  • the lead substrate grid hot-formed by a conventional method is placed in a grid mold designed for the same, and a 500 Kg / cm 2 pressure punch is used to perform a cold extrusion process on the hot-formed lead substrate grid.
  • the paste is transformed into an assembly and a charge, and a 12V100AH battery is finally prepared.
  • the internal resistance becomes smaller and the charge and discharge capacity is increased.
  • Example 2 The lead substrate grid hot-formed by a conventional method is placed in a grid mold designed for the same, and a 300 kg / cm 2 pressure punch is used to cold-press the front and back sides of the lead substrate grid after hot-casting. After processing, the tensile force of the grid after cold extrusion is significantly increased, so the amount of lead-based materials in each grid can be appropriately reduced, and the paste is transformed into an assembly and charged, and a 4V8AH battery is finally prepared. Compared with batteries that do not reduce the amount of grid lead-based materials, their specific energy is greater.
  • Example 3 Example 3
  • Example 4 Except for a press using a pressure of 10OKg / cm 2 , the other steps and effects are the same as in Example 1.
  • Example 4 Except for a press using a pressure of 10OKg / cm 2 , the other steps and effects are the same as in Example 1.
  • Example 4 Except for a press using a pressure of 10OKg / cm 2 , the other steps and effects are the same as in Example 1.
  • Example 4
  • Example 5 Except for a press using a pressure of 800 Kg / n 2 , the other steps and effects are the same as in Example 1.
  • Example 5 Except for a press using a pressure of 800 Kg / n 2 , the other steps and effects are the same as in Example 1.
  • Example 5 Except for a press using a pressure of 800 Kg / n 2 , the other steps and effects are the same as in Example 1.
  • Example 5
  • Example 6 Comparing the battery manufactured in Example 1 with the battery formed by only the hot-casting method using 0.3C constant current charging, it was determined by conventional methods that the temperature of the battery plate of the battery formed by only the hot-cast method quickly increased. To 45-50, or even higher, and the battery plate temperature of the cold extrusion method to treat the grid is only between 37-45'C. Example 6.
  • Example 7 100 kg of 80% oxidized lead powder, 0.6 kg of montmorillonite, 8 L of ion-exchanged water, and 12 L of sulfuric acid with a specific gravity of 1.35-1.38, the above raw materials are mixed in accordance with a conventional method to prepare a lead paste, and fill the positive electrode of a lead storage battery. On the grid, the battery prepared by assembling and charging according to conventional methods is used to test and compare the number of charge and discharge cycles. long. Example 7.
  • Example 8 Before adding the montmorillonite to the lead paste, the battery was first impregnated with industrial sulfuric acid with a specific gravity of 1.25 for 24 hours, and other steps and effects were the same as in Example 7.
  • Example 9 Before adding the montmorillonite to the lead paste, the battery was first impregnated with industrial sulfuric acid with a specific gravity of 1.25 for 24 hours, and other steps and effects were the same as in Example 7.
  • Example 9 Example 9
  • Example 11 Charge the assembled battery or battery pack. Using a sinusoidal full-wave current with a frequency of 50 Hz, the charging current intensity is 0.8C, and the average voltage is 1.3 times the rated voltage. The battery or battery pack is continuously charged for 10 to 18 hours, which can achieve the formation of a battery and a fully charged battery. purpose.
  • Example 11 Using a sinusoidal full-wave current with a frequency of 50 Hz, the charging current intensity is 0.8C, and the average voltage is 1.3 times the rated voltage. The battery or battery pack is continuously charged for 10 to 18 hours, which can achieve the formation of a battery and a fully charged battery. purpose. Example 11.
  • the charging current intensity is 1C
  • the average voltage is 1.35 times the rated voltage
  • the characteristic waveform is a square wave
  • This characteristic charging current is used Continuously charging the battery or battery pack for 10-15 hours can achieve the purpose of forming the electrode plate and fully charging the battery.
  • the lead substrate grid manufactured in Example 1 was filled with the lead paste of Example 6 on the positive grid of a lead-acid battery, and was formed-assembled according to a conventional method. After a charge-discharge index and cycle number comparison test, this method was used to manufacture The resulting lead-acid battery has not only enhanced charge and discharge capabilities, reduced internal resistance, but also extended service life.
  • Example 13
  • the lead-based electrode plate manufactured in Example 7 is used to assemble a battery or battery pack, and the battery or battery pack is charged using the charging method of Example 9.
  • the purpose of forming the electrode plate and fully charging the battery can be achieved.
  • the low-temperature discharge experiments were compared.
  • the lead-acid battery produced by the combined method not only enhanced the high-current discharge capacity, reduced the internal resistance, and especially improved the low-temperature discharge performance.

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Abstract

The invention relates to a storage-battery plate, and more particularly, to a method of producing a lead-base plate for a storage battery. The method includes three main steps: hot-casting a plate grid into final shape, coating and solidifying active materials on the plate grid, and forming the solidified electrode plate. The method is characterized by that cold extrusion is applied to the plate grid after hot-casting the plate grid into final shape, or a hydrated silicate is added into the active materials to be coated and solidified on the plate grid, or forming the electrode plate with the active materials solidified by charge method using cyclic pulse current. The resultant plate has prolonged use life, enhanced electric conductivity, and increased specific energy of the storage battery, large current discharge capacity and low-temperature discharge characteristic, at the same time eliminating environment pollution during producting the storage-battery plate.

Description

一种蓄电池铅基极板的制作方法 发明领域  Method for manufacturing lead base electrode plate of battery
本发明属于蓄电池极板领域, 特别涉及蓄电池铅基极板的制作方法。  The invention belongs to the field of battery electrode plates, and particularly relates to a method for manufacturing a lead plate for a battery.
背景技术 Background technique
目前, 我们所见到的蓄电池是由较成熟的传统工艺所制造的, 其极板工艺包 括板栅成型、 填涂并固化活性物质 (上铅膏)和化成三个主要工序。 成型的板栅 填涂固化铅膏后称之为生极板, 生极板经通电工艺处理 (化成) 后称之为熟极 板。  At present, the battery we have seen is manufactured by a more mature traditional process, and its electrode plate process includes grid formation, filling and curing of active materials (lead paste), and formation of three main processes. The shaped grid is called the electrode plate after being filled with the solidified lead paste, and the electrode plate is called the cooked electrode plate after being processed (formed) by the electrification process.
在蓄电池中, 参加电池成流反应的活性物质铅和二氧化铅是疏松的多孔体, 需要固定在载体上, 该载体称之为板栅或格子体 (骨架) , 板栅的作用是支持活 性物质并传输电流, 导电良好、 结构合理的板栅, 可使电流沿筋条均匀分布于活 性物质上, 从而提高活性物质的利用率。  In storage batteries, the active materials lead and lead dioxide that participate in the battery flow reaction are loose porous bodies that need to be fixed on a carrier, which is called a grid or lattice (framework). The role of the grid is to support activity The material also transmits current, and the grid with good conductivity and reasonable structure can make the current be evenly distributed on the active material along the ribs, thereby improving the utilization rate of the active material.
板栅通常采用铅基合金, 也有采用纯铅或镀铅铜网 (用于负极) , 成型工艺 通常采用浇铸, 少数采用拉网方法。 铅基合金以铅为主, 通常占 95%左右甚至更 多, 所添加的金属有锑、 砷、 镉、 锡、 钙、 银、 铝、 锶等或其组合。  The grid is usually made of a lead-based alloy, and there are also pure lead or lead-plated copper mesh (for the negative electrode). The molding process usually uses casting, and a few use the method of drawing a mesh. Lead-based alloys are mainly lead, usually accounting for about 95% or more. The metals added are antimony, arsenic, cadmium, tin, calcium, silver, aluminum, strontium, etc., or combinations thereof.
应用热铸方法成型的铅基合金板栅, 除可能形成特征固溶体外, 还可能形成 晶体结构不同的中间相, 多数为金属之间或金属与类金属之间的化合物。 研究表 明, 这种化合物以金属键为主, 往往不遵守化合价规律, 对合金导带能力有影 响。 由于热铸铅基板栅的工业控制条件非绝对同一, 即使同一热铸机制造出的板 栅, 其内部气泡、 合金晶格排布规律虽大数相同, 但有一定差别。 对金属脱溶的 时效硬化研究长期以来已有较多的文献报道, 对铅基合金板栅也只是从板栅的形 状上进行改进, 如 GB2127614, 1984年 4月 11日, 由阳光 (Sonnenschein) 公司申 请, 其公开了 ^种电极板栅, 该电极板栅具有蜂窝状结构, 其形状为大致相似的 斜角四边形或者规则六边形。  Lead-based alloy grids formed by the hot casting method may not only form characteristic solid solution bodies, but also may form mesophases with different crystal structures, most of which are compounds between metals or between metals and metalloids. Studies have shown that this compound is dominated by metal bonds and often does not follow the valence law, which has an effect on the conduction capacity of the alloy. Since the industrial control conditions of the hot-cast lead substrate grid are not absolutely the same, even if the grids manufactured by the same hot-casting machine have the same number of internal bubbles and alloy lattices, there are certain differences. There have been many literature reports on the aging hardening of metal dissolution for a long time. The lead-based alloy grid is also only improved from the shape of the grid, such as GB2127614, April 11, 1984, by Sonnenschein A company application discloses an electrode grid having a honeycomb structure, and the shape of the electrode grid is substantially similar to an oblique quadrangle or a regular hexagon.
铅蓄电池的生极板是由铅膏填涂在板栅上而成, 铅膏的配方及和膏的方法、 固化条件对生极板的相组成有重要影响。 近几十年来, 各国对铅膏配方及和膏方 法及固化条件己成熟掌握, 并见诸于大量文献报导, 如 EP0348702 , 1990年 1月 3 日, 由阳光 (Sonnenschein) 公司申请, 其公开了一种涂敷电极板栅的方法, 该 板栅为铅制的, 是采用涂敷材料的溶体浸渍来进行。  The electrode plate of a lead storage battery is made of lead paste filled on a grid. The formula of the lead paste, the method of the paste, and the curing conditions have an important effect on the phase composition of the electrode plate. In recent decades, various countries have matured and mastered the formulation and curing conditions of lead paste, and have seen it in a large number of literature reports, such as EP0348702, which was applied by Sonnenschein Company on January 3, 1990. A method for coating an electrode grid. The grid is made of lead and is performed by dipping a solution of a coating material.
生极板的通电过程称之为化成, 生极板经过化成后称为熟极板。 在传统的蓄 电池生产工艺流程中, 通常是使用电解槽对生极板进行化成, 化成后经洗涤、 干 燥, 再进行蓄电池装配。 由于化成槽采用稀硫酸作为电解液, 化成工序产生的酸 雾和环境污染一直是蓄电池业的难题。 The energization process of the electrode plates is called formation, and the electrode plates are called cooked plates after being formed. In the traditional battery production process, the electrolytic plate is usually formed by using an electrolytic cell. After the formation, the electrode is washed and dried. Dry, and then battery assembly. Because the chemical conversion tank uses dilute sulfuric acid as the electrolyte, acid mist and environmental pollution generated during the chemical conversion process have always been difficult problems for the battery industry.
近年各国有部分厂家开始采用电池或电池组化成方法, 即将生极板先组装成 电池或电池组, 加入电解液进行化成, 这种方法可有效提高组装效率, 抑制产生 酸雾。 但无论电池或电池组化成时是采用两次注酸法还是一次注酸法, 铅膏必须 要添加 Pb304, 研究认为, 上述采用的化成方法均存在充电时间长、 电能损耗 大、 污染环境等缺点, 尤其是传统电解槽的化成方法带来的公众污染一直是蓄电 池业的治理重点。 In recent years, some manufacturers in various countries have begun to use a battery or battery pack formation method. That is, the electrode plate is first assembled into a battery or battery pack, and the electrolyte is added to form the battery. This method can effectively improve the assembly efficiency and suppress the generation of acid mist. But matter into a cell or battery using the acid injection method or a two injection acid method, the pastel is necessary to add Pb 3 04, studies suggest that the above-mentioned chemical conversion methods are employed there is a long charging time, a large power loss, pollution of the environment Disadvantages such as public pollution caused by traditional electrolytic cell formation methods have always been the focus of governance of the battery industry.
发明的公开 Disclosure of invention
本发明的目的在于提供一种蓄电池铅基极板的制作方法, 即利用金属的固有 特性、 改变铅膏的配方和生极板的化成, 使制造出的极板使用寿命延长, 导电能 力增强, 而且制作出的电池还能减少环境污染。  The purpose of the present invention is to provide a method for manufacturing a lead plate for a storage battery, that is, to utilize the inherent characteristics of the metal, change the formula of the lead paste and the formation of the electrode plate, so as to prolong the service life of the manufactured plate and enhance the conductivity. And the battery can reduce environmental pollution.
本发明的制作方法包括三个主要工序: 热铸成型板栅、 在板栅上填涂并固化 活性物质和对固化有活性物质的极板进行化成,其特征在于: 对所述的热铸成型 后的板栅施加冷挤压; 或在板栅上填涂并固化活性物质的和膏配方中添加水化硅 酸盐; 或对固化有活性物质的极板进行化成时采用脉动电流。  The manufacturing method of the present invention includes three main steps: hot-casting grids, filling and curing active materials on the grids, and transforming the electrode plates with the cured active materials, which are characterized by: Cold extrusion is applied to the rear grid; or hydrated silicate is added to the grid to fill and solidify the active material and paste formulation; or pulsed current is used to form the solidified electrode plate.
所述的以上三种方法中的任意两种或三种方法可组合运用。 所述的对板栅施 加冷挤压是自外向内施加压力, 压力是 100— 800Kg/Cm2, 对板栅施加冷挤压可以 是一次以上。 所述的铅膏配方中添加水化硅酸盐可添加在正极铅膏中,或添加在 负极铅膏中,或同时添加在正、 负极铅膏配方中。 所述的水化硅酸盐是蒙脱土, 其中蒙脱土复合分子结构为 (Na, Ca)0.33(AL,Mg)2(Si4O10) (ΟΗ)2·ηΗ20, η =正整 数。 在铅膏配方中添加水化硅酸盐的比例是占铅膏配方中的重量百分比 0.1〜 3% 。 所述的铅膏配方中添加的水化硅酸盐是预先经过工业酸浸渍处理。 所述的 极板化成既可以在电池或电池组装配前进行极板化成, 也可以在生板装配成电池 或电池组后充电化成。 在生板装配成电池或电池组后充电化成, 其铅膏配方中无 须加入 Pb304。 所述的化成时采用脉动的电流是周期性的脉动电流, 频率为任意 值。 电流的波形为方波、 锯齿波、 负脉冲波、 正弦半波、 正弦全波或它们的任意 组合叠加波。 脉动电流的电流强度大于 0.2C, 充电平均电压为电池或电池组额定 电压的 1 - 2倍。 Any two or three of the above three methods can be used in combination. The cold extrusion applied to the grid is applied pressure from the outside to the inside, and the pressure is 100-800Kg / C m 2. The cold extrusion may be applied to the grid more than once. The hydrated silicate added to the lead paste formula can be added to the positive lead paste, or to the negative lead paste, or to both the positive and negative lead paste formulations. The hydrated silicate is montmorillonite, wherein montmorillonite composite molecular structure (Na, Ca) 0. 33 (AL, Mg) 2 (Si 4 O 10) (ΟΗ) 2 · ηΗ 2 0, η = positive integer. The proportion of hydrated silicate added to the lead paste formula is 0.1 to 3% by weight in the lead paste formula. The hydrated silicate added in the lead paste formulation is subjected to an industrial acid dipping treatment in advance. The electrode plate formation can be performed either before the battery or battery pack is assembled, or after the green plate is assembled into a battery or a battery pack. After the green board is assembled into a battery or a battery pack, it is charged and formed, and its lead paste formulation does not need to be added with Pb 3 0 4 . The pulsating current used in the formation is a periodic pulsating current, and the frequency is an arbitrary value. The waveform of the current is a square wave, a sawtooth wave, a negative pulse wave, a sine half wave, a full sine wave, or any combination thereof. The current intensity of the pulsating current is greater than 0.2C, and the average charging voltage is 1-2 times the rated voltage of the battery or battery pack.
由于仅采用热铸法制造出的铅基板栅表面有很多微孔 (其产生原因是热铸过 程中空气分子堆在铅基合金内残留逸出所引起) , 里面的气泡容易引起极板导电 时发热, 同时金属晶格形状不规则且排列组合松散, 这些因素直接影响了板栅的 导电率。 铅基合金的晶格排布容易受力变型, 在热铸铅基板栅成型后增加冷挤压 工序, 即用常规冲床 (例如 100— 800Kg/cm2压力)或液压机对成型后的铅基板栅 进行一次或一次以上冷挤压加工处理, 可使板栅性能大大改善, 微孔大部分可去 掉。 通过冷挤压, 铅基合金晶格因受外部对板栅的压力, 合金晶格发生明显的晶 格集合变形, 使金属晶格排列组合变得进一步紧密, 填充在脱溶过程中气泡排出 后留存的晶格空位中, 从而增强合金导带能力, 同时也使板栅对填涂并固化活性 物质的拉力增强, 导电时内阻变小。 经过冷挤压后的板栅,既可用于正极,也可用 于负极。 Because there are many micropores on the surface of the lead substrate grid manufactured by only the hot casting method (the reason for this is caused by the residual and escape of air molecules piled up in the lead-based alloy during the hot casting process), the air bubbles inside can easily cause the plate to conduct Heating, meanwhile, the shape of the metal lattice is irregular and the arrangement and combination are loose, these factors directly affect the conductivity of the grid. The lattice arrangement of lead-based alloys is easily deformed by force. After the hot-cast lead substrate grid is formed, a cold extrusion process is added. That is, a conventional punch (for example, 100-800K g / cm 2 pressure) or a hydraulic press is used to form the lead substrate. Barrier Performing the cold extrusion processing once or more can greatly improve the grid performance, and most of the micropores can be removed. Through cold extrusion, the lead-based alloy crystal lattice undergoes significant lattice set deformation due to external pressure on the grid, which makes the metal lattice arrangement and combination become closer. After the bubbles are discharged during the dissolution process, In the remaining lattice vacancies, the alloy's conduction band capacity is enhanced, and at the same time, the grid's pull force to fill and solidify the active material is enhanced, and the internal resistance becomes smaller when conducting electricity. The cold-extruded grid can be used for both positive and negative electrodes.
目前较标准的铅蓄电池极板铅膏配方为:  At present, the more standard lead battery lead plate lead paste formula is:
1 ) 正极铅膏配方: 由适量配比的 H2S04、 H20和 Pb粉混合制成, 视密度控制在 1) Formula of positive lead paste: It is made by mixing H 2 S0 4 , H 2 0 and Pb powder with proper proportion, and the apparent density is controlled at
4.0 ±0.1 (g/cm3 ); 4.0 ± 0.1 (g / cm 3 );
2) 负极铅膏配方: 在 1 )基础上选择添加硫酸钡和腐植酸、 0 -羟基 -萘酸、 木 素磺酸钠、 乙炔黑、 合成鞣剂等有机膨胀剂, 根据不同用途, 添加物可选择 一种或数种按一定的配比混合。  2) Negative lead paste formula: On the basis of 1), organic swelling agents such as barium sulfate and humic acid, 0-hydroxy-naphthoic acid, sodium lignosulfonate, acetylene black, and synthetic tanning agent are selected to be added. You can choose one or several kinds to mix according to a certain proportion.
本发明所述的水化硅酸盐类例如是蒙脱土 (Montmorillorite) ,蒙脱土添加物 在铅膏配方中的重量百分比为 0.1〜3%。  The hydrated silicates according to the present invention are, for example, Montmorillorite, and the weight percentage of the montmorillonite additive in the lead paste formulation is 0.1 to 3%.
现代电化学理论认为, 正极 Pb 的化学活性主要由含氢量决定, 而正极 Pb(¾ 中所含的氢主要以吸附水的形式存在于 Pb 晶体表面。 根据具有质子和电子传输 功能的凝胶一晶体体系观点, 正极活性物质结构的最小单元是 PbC^颗粒, 而不是 Pb02晶体, 这种 Pb(¾颗粒由水化 Pbft—PbO ( 0H) 2构成, 若干!^ 颗粒接触构成具 微孔结构的聚集体和具大孔结构的聚集体骨骼。 电化学反应在微孔聚集体上发 生, 在大孔聚集体上进行离子的传递和形成 PbSO, 。  According to modern electrochemical theory, the chemical activity of the positive electrode Pb is mainly determined by the hydrogen content, while the hydrogen contained in the positive electrode Pb (¾ exists mainly on the surface of the crystal of Pb in the form of adsorbed water. According to gels with proton and electron transport functions From the perspective of a crystal system, the smallest unit of the structure of the positive electrode active material is PbC ^ particles, not Pb02 crystals. Such Pb (¾ particles are composed of hydrated Pbft-PbO (0H) 2, a few! ^ The particles contact to form a microporous structure Aggregates and aggregate skeletons with macroporous structures. Electrochemical reactions occur on microporous aggregates, which transfer ions and form PbSO on the macroporous aggregates.
蒙脱土是一种吸水能力极强的水化硅酸盐, 吸水后其体积膨胀可增大数倍至 十数倍, 具有很强的吸附力和阳离子交换性能。 蒙脱土在正极铅膏中的适量添 加, 首先可使 Pbi^因蒙脱土的吸水依附作用而提髙化学活性。 另一方面, 由于蓄 电池放电时 PbCfe转化为 PbSO^ 而 PbSC^的比容要比 PbOj大, 导致整个正极物质体 积要增加, 因此蒙脱土在正极铅膏中的适量添加, 其吸水后体积膨胀的物理特 性, 可有效地缓解活性物质在充放电过程中因体积改变引起的软化和松散脱落, 使正极板使用寿命延长。  Montmorillonite is a hydrated silicate with extremely strong water absorption capacity. After absorbing water, its volume expansion can increase several times to ten times. It has strong adsorption and cation exchange performance. The proper addition of montmorillonite to the positive lead paste can first improve the chemical activity of Pbi ^ due to the water-absorbing dependence of montmorillonite. On the other hand, since PbCfe is converted to PbSO ^ and PbSC ^ is larger than PbOj when the battery is discharged, the volume of the entire positive electrode substance is increased. Therefore, an appropriate amount of montmorillonite is added to the positive lead paste, and its volume expands after absorbing water Physical properties can effectively alleviate the softening and loosening of the active material caused by the volume change during the charge and discharge process, and prolong the service life of the positive electrode plate.
在负极铅膏中添加适量的蒙脱土, 其作用主要是抑制负极在低温 (-15°C以 下) 和高倍率放电 (1 小时率以上) 时出现的不同程度钝化, 即负极电极电势明 显正移, 反应速度明显下降的趋势。 一般认为, 负极在 - 4(TC下充电接受能力仅 有常温 25°C时的 10%, 低温放电能力亦受限于负极。 蒙脱土在负极铅膏中的适量 添加, 可大大提高负极物质的表面活性, 提髙负极的高倍率放电能力, 尤其是有 效地抑制了在低温条件下的负极表面积收縮, 同时, 可有效阻滞氢气析出和铅电 极化成后贮存过程中的氧化。 因此在负极铅膏配方中适量添加蒙脱土, 可使蓄电 池负极板的自放电减少, 尤其是低温特性得到增强。 Adding an appropriate amount of montmorillonite to the negative lead paste is mainly used to inhibit the passivation of the negative electrode at different temperatures at low temperatures (below -15 ° C) and high rate discharge (above 1 hour rate), that is, the potential of the negative electrode is obvious. Moving forward, the reaction speed will obviously decrease. It is generally believed that the negative charge capacity of the negative electrode at -4 ° C is only 10% at 25 ° C and the low-temperature discharge capacity is also limited by the negative electrode. The proper addition of montmorillonite in the negative electrode lead paste can greatly improve the negative electrode material. Surface activity, improving the high rate discharge capacity of the anode, especially effectively suppressing the surface area shrinkage of the anode under low temperature conditions, at the same time, it can effectively block hydrogen evolution and lead charge Oxidation during storage after polarization. Therefore, adding an appropriate amount of montmorillonite to the negative electrode lead paste formula can reduce the self-discharge of the negative electrode plate of the battery, especially the low temperature characteristics.
生极板的通电过程称之为化成, 生极板经过化成后称为熟极板。 传统电化学 理论对充电化成已有充分认识, 化学方法制备的极板物质缺乏电化学活性, 不适 合在蓄电池中作极板使用, 只有通过电化学加工制备, 才能充分激活极板物质的 化学活性, 使蓄电池具有使用价值的容量。 利用充电方法激活极板物质活性的方 法称之为化成, 根据氢 (质子) 活性模型观点和工业实验证明, 电化学方法制备 的 Pb 含氢量远比化学方法制备的多, 而 ΡΜ¾以吸附水形式依存的氢的含量决定 了 Pb02的化学活性程度。 The energization process of the electrode plates is called formation, and the electrode plates are called cooked plates after being formed. The traditional electrochemical theory has fully recognized the charge formation. The electrode materials prepared by chemical methods lack electrochemical activity and are not suitable for use as plates in batteries. Only by electrochemical processing can the chemical activity of the plate materials be fully activated. So that the battery has a useful value of capacity. The method of using the charging method to activate the activity of the plate material is called chemical conversion. According to the viewpoint of the hydrogen (proton) activity model and industrial experiments, Pb prepared by electrochemical methods contains far more hydrogen than that prepared by chemical methods. the content of hydrogen in the form of dependency determines the degree of chemical activity of Pb0 2.
目前大部分生产厂家的极板槽化成条件大同小异, 表 1 列出的是非干荷极板 的一般化成方法。 对于干荷电极板, 为保证加酸后首次放电容量, 有时也采用 "两充一放"的化成方法。 除极板槽化成方法外, 也有少数产品采用生板(未经 化成的极板)装配成电池或电池组后再充电化成的方法, 电池或电池组化成方法 分为两次注酸法和一次注酸法, 使用该化成方法制作极板的铅膏须添加 Pb304, 其一次和两次注酸化成比较过程及优缺点详见表 2。 表 1 At present, the formation conditions of the plate grooves of most manufacturers are similar. Table 1 lists the general formation methods of non-dry-charge plate. For dry-charge electrode plates, in order to ensure the first discharge capacity after adding acid, a "two charge and one discharge" formation method is sometimes used. In addition to the electrode plate formation method, there are also a few products that use green plates (unformed electrode plates) to form batteries or battery packs and then charge and form them. The battery or battery pack formation method is divided into two acid injection methods and one The acid injection method, Pb 3 04 must be added to the lead paste used to make the electrode plate, and the comparison process and the advantages and disadvantages of the acidification with one and two injections are shown in Table 2. Table 1
Figure imgf000006_0001
上述已有的极板化成方法的充电电流均采用持续直流电 (恒流或分阶段的直 流) 。 化成过程 优缺点
Figure imgf000006_0001
The charging current of the above-mentioned existing electrode formation methods adopts continuous DC power (constant current or phased DC). Advantages and disadvantages of the formation process
注酸方式 Acid injection method
两次注酸 1. 第一次注入的酸相对密度为 1. 化成周期较短 Two injections of acid 1. The relative density of the first injection of acid is 1. The formation period is shorter
1.065-1.180 2. 铅膏中需加 Pb304,电池有1.065-1.180 2. Pb 3 0 4 needs to be added to the lead paste. The battery has
2. 大电流充电 24h j、电流充电 好的初期性能 2. High-current charging 24h j, good initial performance of current charging
121 g、计 36h 3. 需要倒酸设备  121g, 36h 3. Require acid pouring equipment
3. 倒出电解液,注入相对密度  3. Pour out the electrolyte and inject the relative density
1.290-1.40的酸  1.290-1.40 acid
4. 用小电流充电 61^最终酸的浓度  4. Charge with a small current 61 ^ Final acid concentration
要控制在所需的浓度  To control at the desired concentration
一次注酸 1. 经过估算注入所需酸的密度和 1. 铅膏中需加入 Pb304,否则 数量,一般要在 1.200以上 初期容量不及两次注酸者One injection of acid 1. After estimating the density of the acid to be injected and 1. The lead paste needs to be added with Pb 3 0 4 , otherwise the amount is generally above 1.200 and the initial capacity is less than the two injections
2. 通电时间至少为 72h 2. 化成时间长 2. Power on time is at least 72h 2. Long formation time
3. 不需要倒酸设备  3. No acid pouring equipment required
传统电解槽化成极板的蓄电池制造流程:  Battery manufacturing process of traditional electrolytic cell forming electrode plate:
板栅一上膏一化成一装配一充电一包装  One grid, one paste, one assembly, one charge, one package
电池或电池组化成的蓄电池制造流程:  Manufacturing process of battery or battery:
板栅一上膏一装配一 (充电化成)一包装  One grid, one paste, one assembly (charging and forming), one package
本发明所述的采用脉动电流化成方法属电池或电池组化成, 与现有方法的区 别在于:  The method for forming a pulsating current according to the present invention belongs to the formation of a battery or a battery pack. The difference from the existing methods is that:
1 )采用不同于恒压或恒流的脉动电流进行充电化成:  1) Charging using a pulsating current different from constant voltage or constant current:
2)铅膏无须加入 Pb304,化成时间无需长达 36 - 72小时, 对电池或电池组充 电时间仅需 10- 18个小时就能达到极板化成及充满电荷的目的。 2) Lead paste does not need to be added with Pb 3 0 4 , the formation time does not need to be as long as 36-72 hours, and the battery or battery pack charging time is only 10-18 hours to achieve the purpose of electrode formation and full charge.
实验表明, 当采用电池或电池组化成的方法时, 配合运用非恒压或非恒流的 脉动电流充电, 对于短时间充电激活极板活性物质的活性, 效果更好。 这种化成 电流的特征在于运用周期性脉动电流, 例如方波、 锯齿波、 负脉冲波、 正弦半 波、 正弦全波等等, 如图 1-5示例。 脉动电流的频率可采用市电频率, 可一次性充 电完成化成。  Experiments show that when a battery or battery formation method is used, combined with the use of non-constant voltage or non-constant current pulsating current charging, the effect of activating the active material of the electrode plate in a short period of time is better. This formed current is characterized by the use of periodic pulsating current, such as square wave, sawtooth wave, negative pulse wave, sine half wave, sine full wave, etc., as shown in Figure 1-5. The frequency of the pulsating current can be the mains frequency, and it can be formed by one-time charging.
在极板化成时, 脉动电流的电流强度一般大于 0.2C, 但要小于极板的承受能 力。 可以通过电流波形的改变 (例如图 2锯齿波改为反向锯齿、 齿峰居中的前后 对称锯齿; 或另采用双锯峰锯齿状等等) ,脉动深度改变 (例如负脉冲深度改为 1/2峰值、 方波低压改为 1/5峰值、 1/3峰值等) , 频率取不同于市电 n倍数 (n = 50)的任意周期电流 (变频) , 充电方法改为两冲一放、 三充两放等等, 都可达 到充电化成的目的。 When the plates are formed, the current intensity of the pulsating current is generally greater than 0.2C, but smaller than the withstand capacity of the plates. By changing the current waveform (for example, the sawtooth wave in Figure 2 is changed to reverse sawtooth, the front and back symmetrical sawtooth is centered; or the double sawtooth sawtooth is used, etc.), the pulse depth is changed (for example, the negative pulse depth is changed to 1 / 2 peak, square wave low voltage changed to 1/5 peak, 1/3 peak, etc.), the frequency is taken to be any periodic current (frequency conversion) different from the n multiple of the city power (n = 50), and the charging method is changed to two rushes, one discharge, Three chargers, two amplifiers, etc. To the purpose of charge formation.
以上所述的对板栅冷挤压、 在铅膏配方中添加蒙脱土或用周期性脉动电流对 电池或电池组充电化成的方法, 既可应用在铅酸蓄电池的极板, 也可应用到硅溶 胶体 (盐) 作电解质的蓄电池极板, 所述实施例仅是本发明原理的优选实施例。 对板栅可进行一次以上的冷挤压, 如对板栅进行两次 (正反面)冷挤压方法, 蒙 脱土在和膏之前先进行酸浸渍处理, 蒙脱土于添加在铅膏配方前先进行工业酸 (如硫酸)浸渍处理, 有利于和膏的充分混合。  The above-mentioned methods of cold-pressing the grid, adding montmorillonite to the formulation of lead paste, or charging the battery or battery pack with a periodic pulsating current can be applied to the plates of lead-acid batteries, as well as The embodiment described above is only a preferred embodiment of the principle of the present invention to a battery plate of a silicon sol (salt) as an electrolyte. The grid can be cold extruded more than once. For example, if the grid is extruded twice (front and back), the montmorillonite is treated by acid dipping before the paste. The montmorillonite is added to the lead paste formula. Prior to the industrial acid (such as sulfuric acid) impregnation treatment, it is beneficial to fully mix with the paste.
本发明通过冷挤压制造出的极板, 增加了金属晶格间结合强度, 对外拉力加 大, 因而在同等重量外观结构的板栅中, 可承受更多的铅粉粘附。 换言之, 在粘 附同样多铅粉的情况下, 板栅抗受力变形的能力加强。 因此, 采用冷挤压方法 后, 要达到同样的板栅效果可减少用铅量, 从而使蓄电池的重量减轻, 提高电池 的比能量。  The electrode plate manufactured by the cold extrusion method of the present invention increases the bonding strength between the metal lattices and increases the external tensile force. Therefore, in a grid with an appearance structure of equal weight, it can withstand more lead powder adhesion. In other words, with the same amount of lead powder adhered, the grid's ability to resist stress deformation is enhanced. Therefore, after the cold extrusion method is adopted, the amount of lead used can be reduced to achieve the same grid effect, thereby reducing the weight of the battery and increasing the specific energy of the battery.
研究表明, 金属晶格形状不规则及微孔是铅基蓄电池大电流充电发热的根源 之一, 经冷挤压板栅制作出的蓄电池, 当其它制造方法相同时, 可承受更大的充 电电流, 或同样充电电流时温升明显减少。  Studies have shown that the irregular shape of the metal lattice and micropores are one of the sources of high-temperature charging of lead-based batteries. The battery produced by cold extrusion of the grid can withstand greater charging current when other manufacturing methods are the same. , Or the temperature rise is significantly reduced at the same charging current.
本发明通过在铅蓄电池极板铅膏配方中加入蒙脱土, 可以有效提高活性物质 的利用率, 改善极板寿命和充放电特性。  In the present invention, by adding montmorillonite to the lead battery lead plate lead paste formula, the utilization rate of active materials can be effectively improved, and the life of the plate and the charging and discharging characteristics can be improved.
本发明通过周期性脉动电流化成方法, 使极板物质在脉动电流的作用下, 可 更有效地激活极板物质的化学活性, 同时缩短极板化成所需的时间。  The present invention uses a periodic pulsating current formation method to enable the plate material to more effectively activate the chemical activity of the plate material under the action of the pulsating current, while reducing the time required for the plate to form.
附图说明  BRIEF DESCRIPTION OF THE DRAWINGS
下面结合附图及实施例对本发明的技术方案作进一步的描述。  The technical solution of the present invention is further described below with reference to the accompanying drawings and embodiments.
图 1.用作充电化成的方波形电流示意图;  Figure 1. Schematic diagram of square waveform current used for charging;
图 2.(a)、 (b)、 (c)分别为用作充电化成的锯齿波电流示意图;  Figures 2. (a), (b), and (c) are schematic diagrams of the sawtooth wave current used for charging formation;
图 3.用作充电化成的负脉冲波形电流示意图;  Figure 3. Schematic diagram of negative pulse waveform current used for charge formation;
图 4.用作充电化成的正弦半波脉动电流示意图;  Figure 4. Schematic diagram of sine half-wave pulsating current used for charging formation;
图 5.用作充电化成的正弦全波脉动电流示意图。  Figure 5. Schematic diagram of sinusoidal full-wave pulsating current used for charge formation.
木发明的实施例  Examples of wooden inventions
实施例 1.  Example 1.
将用常规方法热铸成型后的铅基板栅放在为其相应设计的板栅模具内, 采用 500Kg/cm2压力的冲床, 对热铸成型后的铅基板栅进行一次冷挤压加工, 经上膏一 化成一装配一充电, 最终制备出 12V100AH蓄电池, 与不加冷挤压而其它工序相同 的蓄电池相比, 其内阻变小, 充放电能力增大。 The lead substrate grid hot-formed by a conventional method is placed in a grid mold designed for the same, and a 500 Kg / cm 2 pressure punch is used to perform a cold extrusion process on the hot-formed lead substrate grid. The paste is transformed into an assembly and a charge, and a 12V100AH battery is finally prepared. Compared with a battery that is not subjected to cold extrusion and other processes, the internal resistance becomes smaller and the charge and discharge capacity is increased.
实施例 2. 将用常规方法热铸成型后的铅基板栅放在为其相应设计的板栅模具内, 采用 300Kg/cm2压力的冲床, 对热铸成型后的铅基板栅进行正反面各一次冷挤压加工, 经冷挤压加工后的板栅拉力明显增加, 因而可适当减少每片板栅的铅基材料量, 经上膏一化成一装配一充电, 最终制备出 4V8AH蓄电池, 与不加冷挤压, 不减少 板栅铅基材料量的蓄电池相比, 其比能量较大。 实施例 3 Example 2. The lead substrate grid hot-formed by a conventional method is placed in a grid mold designed for the same, and a 300 kg / cm 2 pressure punch is used to cold-press the front and back sides of the lead substrate grid after hot-casting. After processing, the tensile force of the grid after cold extrusion is significantly increased, so the amount of lead-based materials in each grid can be appropriately reduced, and the paste is transformed into an assembly and charged, and a 4V8AH battery is finally prepared. Compared with batteries that do not reduce the amount of grid lead-based materials, their specific energy is greater. Example 3
除了压力采用 lOOKg/cm2压力的冲床, 其它步骤和效果同实施例 1。 实施例 4 Except for a press using a pressure of 10OKg / cm 2 , the other steps and effects are the same as in Example 1. Example 4
除了压力采用 800Kg/ n2压力的冲床, 其它步骤和效果同实施例 1。 实施例 5 Except for a press using a pressure of 800 Kg / n 2 , the other steps and effects are the same as in Example 1. Example 5
将实施例 1制造出的蓄电池与仅用热铸法成型板栅的蓄电池, 用 0. 3C恒流充 电比较, 经常规方法测定, 仅用热铸法成型板栅的蓄电池极板温度很快上升至 45-50 , 甚至更高, 而增加冷挤压方法处理板栅的蓄电池极板温度仅在 37-45'C 之间。 实施例 6.  Comparing the battery manufactured in Example 1 with the battery formed by only the hot-casting method using 0.3C constant current charging, it was determined by conventional methods that the temperature of the battery plate of the battery formed by only the hot-cast method quickly increased. To 45-50, or even higher, and the battery plate temperature of the cold extrusion method to treat the grid is only between 37-45'C. Example 6.
将氧化度 80%的铅粉 100kg, 蒙脱土 0.6kg, 离子交换水 8L, 比重 1.35 - 1.38 的硫酸 12L, 按常规方法将上述原料进行混合制出铅膏, 并填涂在铅蓄电池的正 极板栅上, 按常规方法进行化成一装配一充电制备出的蓄电池, 用充放电循环次 数测试比较, 可有效地提高正极活性物质利用率, 比正极铅膏不添加蒙脱土的蓄 电池使用寿命要长。 实施例 7.  100 kg of 80% oxidized lead powder, 0.6 kg of montmorillonite, 8 L of ion-exchanged water, and 12 L of sulfuric acid with a specific gravity of 1.35-1.38, the above raw materials are mixed in accordance with a conventional method to prepare a lead paste, and fill the positive electrode of a lead storage battery. On the grid, the battery prepared by assembling and charging according to conventional methods is used to test and compare the number of charge and discharge cycles. long. Example 7.
将氧化度 80%的铅粉 150kg, 250目硫酸钡 0.6kg,蒙脱土 0.8kg, 离子交换水 6L, 比重 1.30 - 1.35的硫酸 12L,按常规方法将上述原料进行混合制出铅膏, 并填涂在 铅蓄电池的负极板栅上, 按常规方法进行化成一装配一充电制备出的蓄电池, 用 常温大电流放电和低温放电实验进行比较, 可证明在负极铅膏添加蒙脱土, 可有 效地提高负极活性物质利用率, 抑制钝化, 使蓄电池大电流放电 (>1小时率) 和 低温(- 5(TC〜0'C )放电能力明显增强。  150 kg of 80% oxidized lead powder, 0.6 kg of 250 mesh barium sulfate, 0.8 kg of montmorillonite, 6 L of ion-exchanged water, 12 L of sulfuric acid with a specific gravity of 1.30-1.35, and the above raw materials are mixed to prepare a lead paste according to a conventional method, and Filled and coated on the negative electrode grid of lead battery, and converted into a battery prepared by assembling and charging according to conventional methods. Comparing the high temperature current discharge and low temperature discharge experiments at normal temperature can prove that adding montmorillonite to the negative electrode lead paste can be effective. It can improve the utilization rate of the negative electrode active material, suppress the passivation, and make the battery discharge capacity at high current (> 1 hour rate) and low temperature (-5 (TC ~ 0'C)) significantly enhanced.
z实施例 8. 蒙脱土在添加在铅膏前, 先用比重为 1. 25的电池用工业硫酸浸渍处理 24小 时, 其它步骤和效果同实施例 7。 实施例 9. zExample 8. Before adding the montmorillonite to the lead paste, the battery was first impregnated with industrial sulfuric acid with a specific gravity of 1.25 for 24 hours, and other steps and effects were the same as in Example 7. Example 9.
对完成生板装配的电池或电池组进行充电。 采用频率为 1000赫兹的负脉冲波 (负脉冲深度为峰值电压的 80%) , 峰值电压为额定电压 1.5倍, 首先用 0.6C的负 脉冲电流对电池或电池组充电 7-10小时, 将电池或电池组完全放电后, 继续充电 3 - 5小时, 可达到生极板化成暨蓄电池充满电荷的目的。 实施例 10.  Charge the assembled battery or battery pack. Use a negative pulse wave with a frequency of 1000 Hz (the negative pulse depth is 80% of the peak voltage), and the peak voltage is 1.5 times the rated voltage. First, charge the battery or battery pack with a negative pulse current of 0.6C for 7-10 hours. Or after the battery pack is completely discharged, continue to charge for 3-5 hours to achieve the purpose of forming the electrode plate and fully charging the battery. Example 10.
对完成生板装配的电池或电池组进行充电。 采用频率为 50赫兹的正弦全波电 流, 充电电流强度为 0.8C, 平均电压为额定电压 1.3倍, 对电池或电池组连续进行 10 - 18小时充电, 可达到生极板化成暨蓄电池充满电荷的目的。 实施例 11.  Charge the assembled battery or battery pack. Using a sinusoidal full-wave current with a frequency of 50 Hz, the charging current intensity is 0.8C, and the average voltage is 1.3 times the rated voltage. The battery or battery pack is continuously charged for 10 to 18 hours, which can achieve the formation of a battery and a fully charged battery. purpose. Example 11.
对完成生板装配的电池或电池组进行充电。 充电电流强度为 1C, 平均电压为 1.35倍额定电压, 特征波形为方波, 采用变频技术将频率调制至市电频率的 n倍 (n = 2、 3、 4〜) , 运用这种特征充电电流对电池或电池组进行 10— 15小时连续 充电, 可达到生极板化成暨蓄电池充满电荷的目的。 实施例 12.  Charge the assembled battery or battery pack. The charging current intensity is 1C, the average voltage is 1.35 times the rated voltage, the characteristic waveform is a square wave, and the frequency is modulated to n times (n = 2, 3, 4 ~) the frequency of the mains frequency using a frequency conversion technology. This characteristic charging current is used Continuously charging the battery or battery pack for 10-15 hours can achieve the purpose of forming the electrode plate and fully charging the battery. Example 12.
将实施例 1制造出的铅基板栅用实施例 6的铅膏填涂在铅蓄电池的正极板栅 上, 按常规方法进行化成—装配, 经充放电指标及循环次数对比测试, 用此方法 制造出的铅蓄电池不仅充放电能力增强, 内阻变小, 而且使用寿命延长。 实施例 13.  The lead substrate grid manufactured in Example 1 was filled with the lead paste of Example 6 on the positive grid of a lead-acid battery, and was formed-assembled according to a conventional method. After a charge-discharge index and cycle number comparison test, this method was used to manufacture The resulting lead-acid battery has not only enhanced charge and discharge capabilities, reduced internal resistance, but also extended service life. Example 13.
用实施例 7制造出的铅基极板组装成电池或电池组, 采用实施例 9的充电方法 电池或电池组充电, 可达到生极板化成暨电池充满电荷的目的, 用常温大电流 放电及低温放电实验进行比较, 用该组合方法制作出的铅蓄电池不仅大电流放电 能力增强, 内阻变小, 尤其是低温放电性能得到改善。  The lead-based electrode plate manufactured in Example 7 is used to assemble a battery or battery pack, and the battery or battery pack is charged using the charging method of Example 9. The purpose of forming the electrode plate and fully charging the battery can be achieved. The low-temperature discharge experiments were compared. The lead-acid battery produced by the combined method not only enhanced the high-current discharge capacity, reduced the internal resistance, and especially improved the low-temperature discharge performance.

Claims

Gall
1.一种蓄电池铅基极板的制作方法, 包括三个主要工序: 热铸成型板栅、 在板栅上填涂并固化活性物质和对固化有活性物质的极板进行化成,其特征在 于: 对所述的热铸成型后的板栅施加冷挤压; 或在板栅上填涂并固化活性物质 的铅膏配方中添加水化硅酸盐; 或对固化有活性物质的极板进行化成时采用脉 动电流。 A method for manufacturing a lead plate for a storage battery, comprising three main steps: a hot-cast grid, filling and curing an active material on the grid, and forming a solidified electrode plate, characterized in that: : Applying cold extrusion to the grid after hot-casting; or adding a hydrated silicate to a lead paste formula that fills and cures the active material on the grid; or performs curing on the electrode plate with the active material During the formation, a pulsating current is used.
2.如权利要求 1所述的蓄电池铅基极板的制作方法, 其特征在于所述的以 上三种方法中的任意两种或三种方法组合运用。  The method for manufacturing a lead base plate for a battery according to claim 1, wherein any two or three of the above three methods are used in combination.
3.如权利要求 1所述的蓄电池铅基极板的制作方法, 其特征在于所述的对 板栅施加冷挤压是自外向内施加压力。  The method for manufacturing a lead base plate for a battery according to claim 1, characterized in that the cold extrusion of the grid is to apply pressure from the outside to the inside.
4.如权利要求 1所述的蓄电池铅基极板的制作方法, 其特征在于所述的对 板栅施加冷挤压是一次或一次以上。  The method for manufacturing a lead base plate for a battery according to claim 1, characterized in that the cold extrusion is applied to the grid once or more than once.
5.如权利要求 1或 3所述的蓄电池铅基极板的制作方法, 其特征在于所述的 压力是 100— 800Kg/cm2The method for manufacturing a lead base plate for a battery according to claim 1 or 3, wherein the pressure is 100-800 Kg / cm 2 .
6.如权利要求 1所述的蓄电池铅基极板的制作方法, 其特征在于所述的铅膏 配方中添加水化硅酸盐可添加在正极铅膏中,或添加在负极铅膏中,或同时添加 在正、 负极铅膏配方中。  6. The method for manufacturing a lead base electrode plate for a battery according to claim 1, characterized in that the hydration silicate added to the formulation of the lead paste can be added to the positive lead paste, or the negative lead paste, Or added to the positive and negative lead paste formula at the same time.
7.如权利要求 1或 6所述的蓄电池铅基极板的制作方法, 其特征在于所述的 水化硅酸盐是蒙脱土, 其中蒙脱土复合分子结构为 (Na, Ca)0. 33(AL,Mg)2(Si4O10) (ΟΗ)2·ηΗ20, 。=正整数。 7. The manufacturing method of claim 16 or the base plate of a lead storage battery as claimed in claim, wherein the hydrated silicate is montmorillonite, wherein montmorillonite composite molecular structure (Na, Ca) 0 33 (AL, Mg) 2 (Si 4 O 10 ) (ΟΗ) 2 · ηΗ 2 0,. = Positive integer.
8.如权利要求 1或 6所述的蓄电池铅基极板的制作方法, 其特征在于所述 的铅膏配方中添加水化硅酸盐的比例是占铅膏配方中的重量百分比 0.1〜3%。  The method for manufacturing a lead base plate for a battery according to claim 1 or 6, wherein the proportion of the hydrated silicate added to the lead paste formula is 0.1 to 3 weight percent of the lead paste formula. %.
9.如权利要求 1或 6所述的蓄电池铅基极板的制作方法, 其特征在于所述的 铅膏配方中添加的水化硅酸盐是预先经过工业酸浸渍处理。  The method for manufacturing a lead base electrode plate for a battery according to claim 1 or 6, wherein the hydrated silicate added to the lead paste formulation is subjected to an industrial acid impregnation treatment in advance.
10.如权利要求 1所述的蓄电池铅基极板的制作方法, 其特征在于所述的极 板化成既可以在电池或电池组装配前进行极板化成, 也可以在生板装配成电池 或电池组后充电化成。  10. The method for manufacturing a lead base electrode plate for a battery according to claim 1, wherein the electrode plate formation can be performed either before the battery or battery pack is assembled, or the green plate can be assembled into a battery or The battery pack becomes charged after charging.
11.如权利要求 10所述的蓄电池铅基极板的制作方法, 其特征在于所述的 在生板装配成电池或电池组后充电化成, 其铅膏配方中无须加入 Pb304The method for manufacturing a lead base electrode plate for a battery according to claim 10, wherein Pb 3 0 4 is not required to be added to the lead paste formulation after the green plate is assembled into a battery or a battery pack.
12.如权利要求 1所述的蓄电池铅基极板的制作方法, 其特征在于所述的化 成时采用的脉动电流是周期性的脉动电流, 频率为任意值。 12. The method for manufacturing a lead base plate for a battery according to claim 1, wherein the pulsating current used in the formation is a periodic pulsating current, and the frequency is an arbitrary value.
13.如权利要求 1或 12所述的蓄电池铅基极板的制作方法, 其特征在于所述 的脉动电流的波形为方波、 锯齿波、 负脉冲波、 正弦半波、 正弦全波或它们的 任意组合叠加波。 13. The method for manufacturing a lead plate for a storage battery according to claim 1 or 12, wherein the waveform of the pulsating current is a square wave, a sawtooth wave, a negative pulse wave, a sine half wave, a sine full wave, or these Any combination of superimposed waves.
14.如权利要求 1或 12所述的蓄电池铅基极板的制作方法, 其特征在于所述 的脉动电流的电流强度大于 0.2C, 充电平均电压为电池或电池组额定电压的 1—2倍。  14. The method for manufacturing a lead base plate for a battery according to claim 1 or 12, characterized in that the current intensity of the pulsating current is greater than 0.2C, and the average charging voltage is 1-2 times the rated voltage of the battery or battery pack .
PCT/CN1999/000146 1999-09-13 1999-09-13 A method of producing a lead-base plate for a storage battery WO2001020699A1 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109546155A (en) * 2018-12-21 2019-03-29 山东圣阳电源股份有限公司 Superbattery and its negative plate
CN114267888A (en) * 2021-12-28 2022-04-01 河南超威正效电源有限公司 2V battery production system and production process thereof
CN114497780A (en) * 2022-02-14 2022-05-13 广州小鹏汽车科技有限公司 Formation method of lithium ion battery cell
CN114583116A (en) * 2022-01-27 2022-06-03 淄博火炬能源有限责任公司 Starting forming lead accumulator

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110707329A (en) * 2019-10-23 2020-01-17 福建华祥电源科技有限公司 Battery grid with good conductivity and long service life

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1045199A (en) * 1989-02-25 1990-09-05 中科院长春应用化学研究所 The preparation method of slab lattice alloy of lead-acid battery
CN1099523A (en) * 1994-05-27 1995-03-01 陈有孝 Active mass composition for negative electrode of lead-acid accumulator
WO1996017426A1 (en) * 1994-11-30 1996-06-06 3266991 Manitoba, Ltd. Charging and conditioning batteries

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1045199A (en) * 1989-02-25 1990-09-05 中科院长春应用化学研究所 The preparation method of slab lattice alloy of lead-acid battery
CN1099523A (en) * 1994-05-27 1995-03-01 陈有孝 Active mass composition for negative electrode of lead-acid accumulator
WO1996017426A1 (en) * 1994-11-30 1996-06-06 3266991 Manitoba, Ltd. Charging and conditioning batteries

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109546155A (en) * 2018-12-21 2019-03-29 山东圣阳电源股份有限公司 Superbattery and its negative plate
CN114267888A (en) * 2021-12-28 2022-04-01 河南超威正效电源有限公司 2V battery production system and production process thereof
CN114267888B (en) * 2021-12-28 2023-09-26 河南超威正效电源有限公司 2V battery production system and production process thereof
CN114583116A (en) * 2022-01-27 2022-06-03 淄博火炬能源有限责任公司 Starting forming lead accumulator
CN114497780A (en) * 2022-02-14 2022-05-13 广州小鹏汽车科技有限公司 Formation method of lithium ion battery cell

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