WO2019114435A1 - Lead paste formulation of cyclic lead-acid storage battery for communication and preparation method - Google Patents

Lead paste formulation of cyclic lead-acid storage battery for communication and preparation method Download PDF

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Publication number
WO2019114435A1
WO2019114435A1 PCT/CN2018/112350 CN2018112350W WO2019114435A1 WO 2019114435 A1 WO2019114435 A1 WO 2019114435A1 CN 2018112350 W CN2018112350 W CN 2018112350W WO 2019114435 A1 WO2019114435 A1 WO 2019114435A1
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Prior art keywords
lead
acid storage
paste formulation
lead paste
storage battery
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PCT/CN2018/112350
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French (fr)
Chinese (zh)
Inventor
马晓曾
钱晓杰
张明
楼志强
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双登集团股份有限公司
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Publication of WO2019114435A1 publication Critical patent/WO2019114435A1/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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10Primary casings; Jackets or wrappings
    • H01M50/116Primary casings; Jackets or wrappings characterised by the material
    • H01M50/121Organic material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/06Lead-acid accumulators
    • H01M10/12Construction or manufacture
    • 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
    • H01M2220/00Batteries for particular applications
    • H01M2220/20Batteries in motive systems, e.g. vehicle, ship, plane
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present invention relates to a lead-acid battery lead paste formulation, and in particular to a circulating lead-acid battery lead paste formulation, and more particularly to a circulating-type lead-acid battery lead paste formulation for communication.
  • the present invention also relates to a method for preparing a lead-acid battery lead paste for communication.
  • the power supply of the communication base station and the outdoor integrated cabinet is mostly a lead-acid battery. Since most of the communication base stations are built in the wild or in the suburbs of the city, these partial or urban-rural junctions are subject to geographical constraints, the supply of the mains is not normal, and there is a blackout.
  • a lead-acid battery is a device that continuously converts electrical energy and chemical energy. The number of conversions is directly related to the quality of the lead paste. This frequent start-stop condition has a negative impact on the battery life of the battery.
  • the lead-acid storage battery of the prior art has a high amount of dilute sulfuric acid in the lead paste, and the corrosion amount of the positive and negative plates is correspondingly large in the electrochemical reaction process. Therefore, it can be said that dilute sulfuric acid is the main factor for reducing the cycle life of the lead-acid battery.
  • dilute sulfuric acid is the main factor for reducing the cycle life of the lead-acid battery.
  • the present invention is mainly directed to the deficiencies of the prior art, and proposes a lead-acid battery lead paste formulation for communication, which is resistant to over-discharge and charge-receiving, and proposes a corresponding preparation method.
  • the present invention achieves the technical object by the following technical solutions.
  • a circulating lead-acid battery lead paste formulation for communication comprising a positive lead paste formulation and a negative lead paste formulation, wherein the positive lead paste formulation is composed of the following raw materials in terms of weight percent: dilute sulfuric acid 5.5 ⁇ 6.5%, deionized water 10 ⁇ 11%, short fiber 0.1 ⁇ 0.15%, the rest is lead powder; the negative lead paste formula is as follows by weight
  • the dilute sulfuric acid has a density of 25 ° ( : 1400 ⁇ 0.002 ⁇ / ⁇ 113) .
  • the barium sulfate particle size of 3000 mesh.
  • the lead powder has an oxidation degree of 72 to 78% .
  • a method for preparing a lead-acid battery lead paste for communication wherein the positive lead paste and the negative lead paste are separately prepared, and the equipment used is a fully automatic and paste machine.
  • the improvement is as follows: in the preparation of the positive lead paste, the short fiber is first added to the paste machine according to the ratio, and the barium sulfate and the lignosulfonic acid are added to the paste machine at the same time. Sodium, carbon black and short fibers, and then the separately taken lead powder is added to the corresponding paste machine, and the lead powder is added while stirring.
  • the apparent density index of lead paste is 4.4 ⁇ 4.55 ⁇ / ⁇ 113
  • the apparent density index of negative lead paste is 4.25 ⁇ 4.45 ⁇ / ⁇ 113.
  • the temperature is less than 45 ° ( : when the paste is obtained.
  • the present invention has the following positive effects:
  • the cycle life of the battery 100% 000 is increased from about 100 times to about 500 times.
  • the battery can be used in three types of grid environment;
  • the battery recharging performance is improved, to solve the problem that the battery is actually attenuated in the actual use of the floating charge voltage charging capacity, the battery recharging capacity factor 3 ⁇ 4 ⁇ 241 1 increased from 92% ⁇ 9 7% to 100% ⁇ 105%.
  • the circulating type lead-acid battery lead paste formulation for communication of the present invention comprises a positive lead paste formulation and a negative lead paste formulation.
  • the positive lead paste formula and the negative lead paste formulation are all measured by weight percentage.
  • the ratio of different examples of the positive lead paste is shown in Table 1.
  • the ratios of the negative and lead paste different examples are shown in Table 2.
  • the dilute sulfuric acid used in the present invention is 25° (the density is 1400 ⁇ 0.002 ⁇ / ⁇ 113, and the barium sulfate particle size is 3000). ⁇ 02 019/114435 ⁇ (:17 € ⁇ 2 018/112350
  • the oxidation degree of the lead powder used is arbitrarily selected from 72 to 78% .
  • the lead-acid battery lead paste for communication of the present invention is prepared in the following manner.
  • the positive lead paste and the negative lead paste are separately prepared, and the equipment used is a fully automatic and paste machine.
  • the short fibers are first added to the heating machine and the paste machine according to the ratio.
  • barium sulfate, sodium lignin sulfonate, carbon black and short fibers are also added to the paste machine at a time, and then the respectively taken lead powder is added to the corresponding paste machine, lead powder. It was added by stirring while adding, and the dry stirring was continued after the lead powder was discharged, wherein Examples 1 and 2 were dry-stirred 3.0 11 ⁇ 11 , and Examples 3 to 5 were dry-stirred 5.0 111111 .
  • the deionized water is injected once during the stirring process, and after adding at least 5.0 1 ⁇ 11 , the diluted sulfuric acid is sequentially added, and the diluted sulfuric acid is continuously added under stirring, and the diluted sulfuric acid is added in the examples 1 and 2
  • Embodiments 3 to 4 take 15 11 ⁇ 11 .
  • the automatic and paste machine set the temperature to 73 ° ⁇ ! and maintain After that, the cooling water, the dust-removing fan and the cooling damper that are automatically turned on and the paste machine are automatically turned on, and the rapid cooling causes the lead paste to produce 4:88 crystal.
  • the paste machine was continuously stirred, and Examples 1 and 2 were stirred at 12 1 ⁇ 11 , and Examples 3 to 5 were stirred at 15 11 ⁇ 11 .
  • the apparent density of the lead paste was measured.
  • the apparent density of the positive lead paste was 4.4 ⁇ 4.55 ⁇ / ⁇ 113
  • the apparent density of the negative lead paste was 4.25 ⁇ 4. / ⁇ 113 .
  • the over-discharge performance and recharging performance of the lead-acid battery produced by the embodiment of the invention are significantly improved, and the lead-acid battery is effectively solved in the actual application due to the poor grid environment, causing frequent over-discharge and capacity recovery.
  • the cycle life of the lead-acid battery 100% 000 made by the embodiment of the invention is greatly improved, wherein the embodiment 1 reaches 4 76 times, the embodiment 2 reaches 485 times, and the embodiment 3 reaches 51 7 times, the embodiment 4 reached 508 times, and Example 5 reached 503 times, while the prior art only had about 100 times.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Cell Electrode Carriers And Collectors (AREA)
  • Secondary Cells (AREA)

Abstract

Disclosed in the present invention is a lead paste formulation of a cyclic lead-acid storage battery for communication, comprising a positive electrode lead paste formulation and a negative electrode lead paste formulation. The positive electrode lead paste formulation comprises the following raw materials by weight percentages: 5.5 to 6.5% of dilute sulphuric acid, 10 to 11% of deionized water, 0.1 to 0.15% of short fibers, and the balance being lead powders. The negative electrode lead paste formulation comprises the following raw materials by weight percentages: 6 to 7% of dilute sulphuric acid, 10 to 10.5% of deionized water, 1.0 to 1.3% of barium sulfate, 0.1 to 0.5% of sodium ligninsulfonate, 0.1 to 0.15% of carbon black, 0.1 to 0.15% of short fibers, and the balance being lead powders. The present invention further comprises a preparation method for the lead paste of a cyclic lead-acid storage battery for communication. The over-discharging property and the recharging property of the lead-acid storage battery manufactured by using the present invention are significantly improved, thereby effectively solving the problems of frequent over-discharging and slow capacity recovery of lead-acid storage batteries during practical application due to a poor grid environment, and the recharging capacity is improved. Thus, the 100% DOD cycle life of the lead-acid storage battery is greatly improved.

Description

\¥0 2019/114435 卩(:17 \2018/112350  \¥0 2019/114435 卩(:17 \2018/112350
1  1
通信用循环型铅酸蓄电池铅膏配方及制备方法 技术领域 Recycling lead-acid battery lead paste formulation for communication and preparation method thereof
[0001] 本发明涉及一种铅酸蓄电池铅膏配方, 具体地讲, 本发明涉及一种循环型铅酸 蓄电池铅膏配方, 特别是一种通信用循环型铅酸蓄电池铅膏配方。 本发明还涉 及通信用循环型铅酸蓄电池铅膏制备方法。  [0001] The present invention relates to a lead-acid battery lead paste formulation, and in particular to a circulating lead-acid battery lead paste formulation, and more particularly to a circulating-type lead-acid battery lead paste formulation for communication. The present invention also relates to a method for preparing a lead-acid battery lead paste for communication.
背景技术  Background technique
[0002] 通信基站、 室外一体化机柜配置的电源多数是铅酸蓄电池。 由于通信基站绝大 部分建在野外或城市郊区, 这些偏辟处或城乡结合部受地理条件限制, 市电供 应不够正常, 时有停电。 铅酸蓄电池是一种电能与化学能不断转换的设备, 其 转换次数与铅膏质量直接有关系, 这种频繁启停工况对配套的蓄电池循环使用 寿命带来负面影响。  [0002] The power supply of the communication base station and the outdoor integrated cabinet is mostly a lead-acid battery. Since most of the communication base stations are built in the wild or in the suburbs of the city, these partial or urban-rural junctions are subject to geographical constraints, the supply of the mains is not normal, and there is a blackout. A lead-acid battery is a device that continuously converts electrical energy and chemical energy. The number of conversions is directly related to the quality of the lead paste. This frequent start-stop condition has a negative impact on the battery life of the battery.
发明概述  Summary of invention
技术问题  technical problem
[0003] 现有技术的铅酸蓄电池内置铅膏含稀硫酸量偏高, 在电化学反应过程中正负极 板的腐蚀量也相应大, 因此可以说稀硫酸是减少铅酸蓄电池循环使用寿命的主 要因素之一。  [0003] The lead-acid storage battery of the prior art has a high amount of dilute sulfuric acid in the lead paste, and the corrosion amount of the positive and negative plates is correspondingly large in the electrochemical reaction process. Therefore, it can be said that dilute sulfuric acid is the main factor for reducing the cycle life of the lead-acid battery. One of the factors.
问题的解决方案  Problem solution
技术解决方案  Technical solution
[0004] 本发明主要针对现有技术的不足, 提出一种耐过放电性能和充电接受能力强的 通信用循环型铅酸蓄电池铅膏配方, 并且提出相应的制备方法。  [0004] The present invention is mainly directed to the deficiencies of the prior art, and proposes a lead-acid battery lead paste formulation for communication, which is resistant to over-discharge and charge-receiving, and proposes a corresponding preparation method.
[0005] 本发明通过下述技术方案实现技术目标。  The present invention achieves the technical object by the following technical solutions.
[0006] 通信用循环型铅酸蓄电池铅膏配方, 它包括正极铅膏配方和负极铅膏配方, 其 改进之处在于: 所述正极铅膏配方由以下按重量百分比计量的原料组成: 稀硫 酸 5.5〜 6.5%、 去离子水 10〜 11%、 短纤维 0.1〜 0.15%、 其余为铅粉; 所述负极 铅膏配方由以下按重量百分  [0006] A circulating lead-acid battery lead paste formulation for communication, comprising a positive lead paste formulation and a negative lead paste formulation, wherein the positive lead paste formulation is composed of the following raw materials in terms of weight percent: dilute sulfuric acid 5.5~ 6.5%, deionized water 10~11%, short fiber 0.1~0.15%, the rest is lead powder; the negative lead paste formula is as follows by weight
比计量的原料组成, 稀硫酸 6〜 7%、 去离子水 10〜 10.5%、 硫酸钡 1.0〜 1.3%、 木 \¥02019/114435 卩(:17€\2018/112350 Ratio of raw material composition, dilute sulfuric acid 6~ 7%, deionized water 10~10.5%, barium sulfate 1.0~1.3%, wood \¥02019/114435卩(: 17€\2018/112350
2 素磺酸钠 0.1〜 0.5%、炭黑 0.1〜 0.15%、短纤维 0.1〜 0.15%, 其余为铅粉。  2 sodium sulfonate 0.1~0.5%, carbon black 0.1~0.15%, short fiber 0.1~0.15%, the rest is lead powder.
[0007] 作为进一步的改进方案, 所述稀硫酸在 25° (:时密度为 1400±0.002§/113 [0007] As a further improvement, the dilute sulfuric acid has a density of 25 ° ( : 1400 ± 0.002 § /113) .
[0008] 作为进一步的改进方案, 所述硫酸钡粒度为 3000目。 [0008] As a further refinement, the barium sulfate particle size of 3000 mesh.
[0009] 作为进一步的改进方案, 所述铅粉氧化度在 7278% [0009] As a further improvement, the lead powder has an oxidation degree of 72 to 78% .
[0010] 通信用循环型铅酸蓄电池铅膏制备方法, 该方法中正极铅膏、 负极铅膏分开制 备, 所用设备都是全自动和膏机。 其改进之处在于: 所述正极铅膏制备时首先 按配比一次性往和膏机内加入短纤维, 负极铅膏制备时也按配比一次性往和膏 机内加入硫酸钡、木素磺酸钠、炭黑和短纤维, 然后将分别量取的铅粉加到对 应的和膏机内, 铅粉采用边加入边搅拌方  [0010] A method for preparing a lead-acid battery lead paste for communication, wherein the positive lead paste and the negative lead paste are separately prepared, and the equipment used is a fully automatic and paste machine. The improvement is as follows: in the preparation of the positive lead paste, the short fiber is first added to the paste machine according to the ratio, and the barium sulfate and the lignosulfonic acid are added to the paste machine at the same time. Sodium, carbon black and short fibers, and then the separately taken lead powder is added to the corresponding paste machine, and the lead powder is added while stirring.
法加入, 放完铅粉后继续干搅拌 3.0〜 5.011^11, 接着在搅拌过程中一次性注入去 离子水, 经至少 5.01^11搅拌后顺序加入稀硫酸, 在搅拌状态持续 10〜 151^11加完 稀硫酸, 当设定温达到 73° (:并维持 3.01^11后, 开启和膏机配套的冷却水、 除尘 风机和冷却风门, 急冷促使和成的铅膏产生大量 4:88晶体, 在此过程中和膏机 继续搅拌 12〜 151^11, 同期要测定铅膏视密度, 正极 Adding, after the lead powder is discharged, continue to dry and stir 3.0~ 5.0 11 ^ 11 , then inject a little once into the deionized water during the stirring process, add at least 5.0 1 ^ 11 and then add the dilute sulfuric acid in sequence, and continue to stir for 10~ 15 1 ^ 11 after the addition of dilute sulfuric acid, when the set temperature reaches 73 ° ( : and maintain 3.0 1 ^ 11 , open the cooling water, dust blower and cooling damper associated with the paste machine, quenching and causing a large amount of lead paste 4 : 88 crystals, in this process and the paste machine continues to stir 12~ 15 1 ^ 11 , the same time to determine the apparent density of lead paste, positive
铅膏视密度指标为 4.4〜 4.55§/113, 负极铅膏视密度指标为 4.25〜 4.45§/113, 待 铅膏视密度达标后在温度小于 45° (:时出膏。 The apparent density index of lead paste is 4.4~4.55 §/113 , and the apparent density index of negative lead paste is 4.25~ 4.45 §/113. After the apparent density of lead paste reaches the standard, the temperature is less than 45 ° ( : when the paste is obtained.
发明的有益效果  Advantageous effects of the invention
有益效果  Beneficial effect
[0011] 本发明与现有技术相比, 具有以下积极效果: [0011] Compared with the prior art, the present invention has the following positive effects:
[0012] 1、正、 负极铅膏组分搭配合理, 原料易得, 而且在常规工艺条件下制备, 故 实施容易; [0012] 1. The positive and negative lead paste components are reasonably matched, the raw materials are easily available, and are prepared under conventional process conditions, so that the implementation is easy;
[0013] 2、 蓄电池 100%000循环使用寿命由 100次左右提升至 500次左右。 显著提升蓄 电池循环使用寿命, 该蓄电池可应用于三类电网环境; [0013] 2. The cycle life of the battery 100% 000 is increased from about 100 times to about 500 times. Significantly improve battery cycle life, the battery can be used in three types of grid environment;
[0014] 3、铅酸蓄电池过度放电性能提升, 解决铅酸蓄电池在实际应用中因电网环境 恶劣导致频繁过度放电、容量恢复慢的问题; [0014] 3. The over-discharge performance of the lead-acid battery is improved, and the problem of frequent over-discharge and slow recovery of the lead-acid battery in the practical application due to the poor grid environment is solved;
[0015] 4、 蓄电池再充电性能提升, 解决蓄电池在实际采用浮充电压充电容量衰减较 快问题, 蓄电池再充电能力因素 ¾^2411由 92%〜 97%提升至 100%〜 105%。 实施该发明的最佳实施例 \¥0 2019/114435 卩(:17 \2018/112350 [0015] 4, the battery recharging performance is improved, to solve the problem that the battery is actually attenuated in the actual use of the floating charge voltage charging capacity, the battery recharging capacity factor 3⁄4 ^ 241 1 increased from 92% ~ 9 7% to 100% ~ 105%. BEST MODE FOR CARRYING OUT THE INVENTION \¥0 2019/114435 卩(:17 \2018/112350
3 本发明的最佳实施方式  3 Best Mode for Carrying Out the Invention
[0016] 下面通过实施例对本发明作进一步说明。 [0016] The invention is further illustrated by the following examples.
[0017] 本发明通信用循环型铅酸蓄电池铅膏配方, 它包括正极铅膏配方和负极铅膏配 方。 所述正极铅膏配方和负极铅膏配方均按重量百分比计量, 正极铅膏不同实 施例的配比见表 1, 负及铅膏不同实施例的配比见表 2。  [0017] The circulating type lead-acid battery lead paste formulation for communication of the present invention comprises a positive lead paste formulation and a negative lead paste formulation. The positive lead paste formula and the negative lead paste formulation are all measured by weight percentage. The ratio of different examples of the positive lead paste is shown in Table 1. The ratios of the negative and lead paste different examples are shown in Table 2.
[0018] 表 1 :  [0018] Table 1:
[] [表 1]  [] [Table 1]
Figure imgf000005_0001
Figure imgf000005_0001
[0019] 表 2:  [0019] Table 2:
[] [表 ¾ [] [Table 3⁄4
Figure imgf000005_0002
Figure imgf000005_0002
[0020] 本发明中应用的稀硫酸在 25° (:时密度为 1400±0.002§/〇113, 硫酸钡粒度为 3000 \¥02019/114435 卩(:17€\2018/112350 [0020] The dilute sulfuric acid used in the present invention is 25° (the density is 1400±0.002 § /〇113, and the barium sulfate particle size is 3000). \¥02 019/114435卩(:17€\2 018/112350
4  4
目, 所用铅粉氧化度在 7278%之间任意选取。 For the purpose, the oxidation degree of the lead powder used is arbitrarily selected from 72 to 78% .
[0021] 在备足原料的基础上, 本发明通信用循环型铅酸蓄电池铅膏按以下方法制备。 [0021] On the basis of preparing raw materials, the lead-acid battery lead paste for communication of the present invention is prepared in the following manner.
首先要求正极铅膏和负极铅膏分开制备, 所用设备都是全自动和膏机。 制备正 极铅膏时首先按配比一次性往正在升温的和膏机内加入短纤维。 负极铅膏制备 时也按配比一次性往和膏机内加入硫酸钡、木素磺酸钠、炭黑和短纤维, 然后 将分别量取的铅粉加到对应的和膏机内, 铅粉采用边加入边搅拌方法加入, 放 完铅粉后继续干搅拌, 其中实施例 1和 2干搅拌 3.011^11, 实施例 3〜 5干搅拌 5.0111111 。 接着在搅拌过程中一次性注入去离子水, 经至少 5.01^11搅拌后顺序加入稀硫 酸, 在搅拌状态下持续加完稀硫酸, 添加稀硫酸实施例 12耗时 First, the positive lead paste and the negative lead paste are separately prepared, and the equipment used is a fully automatic and paste machine. When preparing the positive lead paste, the short fibers are first added to the heating machine and the paste machine according to the ratio. In the preparation of the negative lead paste, barium sulfate, sodium lignin sulfonate, carbon black and short fibers are also added to the paste machine at a time, and then the respectively taken lead powder is added to the corresponding paste machine, lead powder. It was added by stirring while adding, and the dry stirring was continued after the lead powder was discharged, wherein Examples 1 and 2 were dry-stirred 3.0 11 ^ 11 , and Examples 3 to 5 were dry-stirred 5.0 111111 . Then, the deionized water is injected once during the stirring process, and after adding at least 5.0 1 ^ 11 , the diluted sulfuric acid is sequentially added, and the diluted sulfuric acid is continuously added under stirring, and the diluted sulfuric acid is added in the examples 1 and 2
10111111, 实施例 3〜 4耗时 1511^11。 当全自动和膏机设定温度达至 73°〇!并维持
Figure imgf000006_0001
后, 自动开启和膏机配套的冷却水、 除尘风机和冷却风门, 急冷促使和成的铅 膏产生 4:88晶体。 在冷却过程中和膏机继续搅拌, 实施例 1和 2搅拌 121^11, 实施 例 3〜 5搅拌 1511^11。 此过程中同期测定铅膏视密度, 正极铅膏视密度指标为 4.4 〜 4.55§/113, 负极铅膏视密度指标为 4.25〜 4. /〇113, 待铅膏视密度达标后并 在温度小于 45° (:时出膏。
10 111111, Embodiments 3 to 4 take 15 11 ^ 11 . When the automatic and paste machine set the temperature to 73 ° 〇! and maintain
Figure imgf000006_0001
After that, the cooling water, the dust-removing fan and the cooling damper that are automatically turned on and the paste machine are automatically turned on, and the rapid cooling causes the lead paste to produce 4:88 crystal. During the cooling process, the paste machine was continuously stirred, and Examples 1 and 2 were stirred at 12 1 ^ 11 , and Examples 3 to 5 were stirred at 15 11 ^ 11 . During the process, the apparent density of the lead paste was measured. The apparent density of the positive lead paste was 4.4 ~ 4.55 § /113 , and the apparent density of the negative lead paste was 4.25~ 4. /〇 113 . After the apparent density of the lead paste reached the standard and at the temperature Less than 45 ° ( : When the cream is released.
[0022] 本发明实施例制作的铅酸蓄电池过度放电性能和再充电性能得到显著提升, 有 效解决铅酸蓄电池在实际应用中因电网环境恶劣导致频繁过度放电、容量恢复
Figure imgf000006_0002
[0022] The over-discharge performance and recharging performance of the lead-acid battery produced by the embodiment of the invention are significantly improved, and the lead-acid battery is effectively solved in the actual application due to the poor grid environment, causing frequent over-discharge and capacity recovery.
Figure imgf000006_0002
〜 105%。 因此, 本发明实施例制成的铅酸蓄电池 100%000循环使用寿命均有 很大提高, 其中实施例 1达到 476次, 实施例 2达到 485次, 实施例 3达到 517次, 实施例 4达到 508次, 实施例 5达到 503次, 而现有技术仅有 100次左右。 ~ 105%. Therefore, the cycle life of the lead-acid battery 100% 000 made by the embodiment of the invention is greatly improved, wherein the embodiment 1 reaches 4 76 times, the embodiment 2 reaches 485 times, and the embodiment 3 reaches 51 7 times, the embodiment 4 reached 508 times, and Example 5 reached 503 times, while the prior art only had about 100 times.

Claims

\¥0 2019/114435 卩(:17 \2018/112350 \¥0 2019/114435 卩(:17 \2018/112350
5 权利要求书  5 Claims
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