JPS6191859A - Manufacture of battery plate - Google Patents

Manufacture of battery plate

Info

Publication number
JPS6191859A
JPS6191859A JP59212055A JP21205584A JPS6191859A JP S6191859 A JPS6191859 A JP S6191859A JP 59212055 A JP59212055 A JP 59212055A JP 21205584 A JP21205584 A JP 21205584A JP S6191859 A JPS6191859 A JP S6191859A
Authority
JP
Japan
Prior art keywords
mix
mixture
active material
battery
discharge capacity
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP59212055A
Other languages
Japanese (ja)
Inventor
Toru Matsui
徹 松井
Junichi Yamaura
純一 山浦
Yoshinori Toyoguchi
豊口 吉徳
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP59212055A priority Critical patent/JPS6191859A/en
Publication of JPS6191859A publication Critical patent/JPS6191859A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • H01M4/04Processes of manufacture in general
    • H01M4/0402Methods of deposition of the material
    • H01M4/0416Methods of deposition of the material involving impregnation with a solution, dispersion, paste or dry powder
    • 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
    • H01M4/04Processes of manufacture in general
    • 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
    • H01M4/04Processes of manufacture in general
    • H01M4/043Processes of manufacture in general involving compressing or compaction
    • H01M4/0433Molding
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To obtain a battery plate having uniform discharge capacity and good current collecting efficiency by crushing an active material mix in a wet state containing liquid such as water or alcohol, drying, and molding. CONSTITUTION:A battery active material mix kneaded with conductive material and binder is crushed in a wet state containing liquid such as water or alcohol, and dried, then a specified amount of the mix is molded. Since conductive material in the mix has adsorbed water or alcohol, apparent density of the conductive material is similar to that of active material. Therefore, when the mix is crushed, separation of the active material from the conductive material is prevented. Since uniform mix powder is obtained, a battery plate whose discharge capacity is made uniform and current collecting efficiency is increased can be obtained.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、電池、特に扁平形電池の極板の製造法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for producing electrode plates for batteries, particularly flat batteries.

従来の技術 近年、電子機器、電子ウォッチ等の普及にともない、小
形で高エネルギー密度を有する電池に対する需要が急速
に増えている。これらの機器に搭載される電池として、
リチウム、ナトリウム等のアルカリ金属を負極活物質と
する有機電解質電池がある。この種の電池に用いられる
正極活物質としては、弗化炭素、二酸化マンガン、酸化
銅等の化合物が知られている。
BACKGROUND OF THE INVENTION In recent years, with the spread of electronic devices, electronic watches, etc., the demand for small batteries with high energy density has rapidly increased. As batteries installed in these devices,
There are organic electrolyte batteries that use alkali metals such as lithium and sodium as negative electrode active materials. Compounds such as carbon fluoride, manganese dioxide, and copper oxide are known as positive electrode active materials used in this type of battery.

従来より、これらの正極活物質を用いる電池、特に扁平
形電池の極板を作製する際、概ね以下の手順で行なわれ
る。すなわち、活物質、導電剤としてのカーボン、及び
四弗化エチレン樹脂等の結着剤を乾式もしくは水、アル
コール等を用いて湿式で練合する。この後、練合したも
の(以後、合剤と言う)を乾燥し、ミキサー等で粉砕し
、所定量を加圧圧着して極板に成形する。
Conventionally, when producing electrode plates for batteries, particularly flat batteries, using these positive electrode active materials, the following procedure is generally performed. That is, the active material, carbon as a conductive agent, and a binder such as tetrafluoroethylene resin are kneaded dryly or wetly using water, alcohol, or the like. Thereafter, the kneaded mixture (hereinafter referred to as a mixture) is dried, pulverized using a mixer, etc., and a predetermined amount is pressed under pressure to form an electrode plate.

発明が解決しようとする問題点 上記のような方法によると5合剤を乾燥してから粉砕と
いう過程であるため、二酸化マンガン等の活物質自体の
密度と、導電剤であるカーボンの密度の大きな差により
、粉砕時、活物質が合剤より遊離する。このため、粉砕
後の合剤は、二酸化マンガン等の活物質が容器の下にた
まり、カーボンを多く含む合剤が上にたまるという、合
剤の不均一化が起こる。したがって、この様な不均一の
合剤を極板製造に用いると、放電容量にばらつきの多い
集電効率の悪い電池ができるという問題点があった。
Problems to be Solved by the Invention According to the method described above, the 5 mixture is dried and then pulverized, so the density of the active material itself, such as manganese dioxide, and the density of carbon, which is a conductive agent, are large. Due to the difference, the active material is liberated from the mixture during pulverization. For this reason, in the mixture after pulverization, the active material such as manganese dioxide accumulates at the bottom of the container, and the mixture containing a large amount of carbon accumulates at the top, resulting in non-uniformity of the mixture. Therefore, when such a non-uniform mixture is used in the manufacture of electrode plates, there is a problem that a battery with a large variation in discharge capacity and poor current collection efficiency is produced.

本発明は、このような従来の欠点を除去するものであり
、放電容量にばらつきの小さい集電効率の良い、信頼性
の高い極板の製造法を提供、するものである。
The present invention eliminates such conventional drawbacks, and provides a method for manufacturing a highly reliable electrode plate with small variations in discharge capacity, good current collection efficiency, and high reliability.

問題点を解決するための手段 本発明の電池極板の製造法は、合剤を、水、アルコール
等を含んだ湿潤状態で粉砕した後、乾燥し、所定量を加
圧成形することを特徴とするものである。
Means for Solving the Problems The method for manufacturing battery electrode plates of the present invention is characterized by pulverizing the mixture in a wet state containing water, alcohol, etc., drying it, and press-molding it into a predetermined amount. That is.

作用 本発明によれば、合剤中の導電剤は水、アルコール等を
吸着しているので、見掛は上の密度は活物質のそれとほ
ぼ等しくなり、合剤を粉砕しても、活物質及び導電剤が
分離することがない。したがって、均一な合剤粉末がで
きるため、放電容量にばらつきの小さい集電効率の良い
極板を有する電池が得られる。
Function According to the present invention, since the conductive agent in the mixture adsorbs water, alcohol, etc., the apparent density is almost equal to that of the active material, and even if the mixture is pulverized, the active material And the conductive agent does not separate. Therefore, since a uniform mixture powder is produced, a battery having electrode plates with good current collection efficiency and small variations in discharge capacity can be obtained.

実施例 以下、本発明の実施例について説明する。Example Examples of the present invention will be described below.

実施例に 酸化マンガン、カーボンブラックを重量比100対5の
割合で混合し、これに適量のメチルアルコールを加え攪
拌した後、四弗化エチレン樹り合わせた。この合剤を8
0°Cで所定時間予備乾燥し、乾燥前と乾燥後の重量差
から湿潤の様子を求めた。これをミキサーで粉砕し、8
0’Cで本乾燥した。ここで合剤は粉砕してから本乾燥
されるので、粉砕せずに合剤のかたまりのまま乾燥する
場合に比べて、乾燥時間は約1/4に短縮することがで
きた。乾燥粉末合剤20011+pをとり、平扁形電池
ケース内に加圧成形し、電池を組み立てた。
In the example, manganese oxide and carbon black were mixed at a weight ratio of 100:5, and after adding an appropriate amount of methyl alcohol and stirring, the mixture was laminated with tetrafluoroethylene. 8 of this mixture
Preliminary drying was carried out at 0°C for a predetermined period of time, and the state of wetting was determined from the difference in weight before and after drying. Grind this with a mixer and
Main drying was carried out at 0'C. Here, since the mixture is ground and then subjected to main drying, the drying time can be reduced to about 1/4 compared to the case where the mixture is dried as a lump without being crushed. Dry powder mixture 20011+p was taken and pressure-molded into a flat battery case to assemble a battery.

負極には、金属リチウムを用い、電解液には、グロビレ
ンカーボネートとジメトキシエタンを等体積で混合した
ものに、過塩素酸リチウムを1モル/lの割合で溶解し
たものを用いた。セパレータにはポリプロピレン不織布
を用いた。このように6ペーノ 構成した電池を2mムの定電流で放電し、終止電圧2v
で放電容量を求めた。
For the negative electrode, metallic lithium was used, and for the electrolytic solution, lithium perchlorate was dissolved in a mixture of equal volumes of globylene carbonate and dimethoxyethane at a ratio of 1 mol/l. A polypropylene nonwoven fabric was used as the separator. The battery configured with 6 panels was discharged at a constant current of 2mm, and the final voltage was 2v.
The discharge capacity was determined.

第1図は、各電池の最大放電容量と最小放電容量の差を
粉砕前の合剤の吸湿量に対してプロットしたものである
。ここで吸湿量は次式によって求めた。
FIG. 1 is a plot of the difference between the maximum discharge capacity and minimum discharge capacity of each battery against the moisture absorption amount of the mixture before pulverization. Here, the moisture absorption amount was determined by the following formula.

第1図より、吸湿量6%以上の湿潤状態で合剤を粉砕す
ることにより放電容量にばらつきの小さい電池を得るこ
とができる。ここで吸湿量80%以上の湿潤状態の合剤
はペースト状でありミキサーで粉砕することは困難であ
った。
From FIG. 1, it is possible to obtain batteries with small variations in discharge capacity by pulverizing the mixture in a wet state with a moisture absorption of 6% or more. Here, the mixture in a wet state with a moisture absorption of 80% or more was in the form of a paste, and it was difficult to crush it with a mixer.

実施例2 五酸化バナジウム、アセチレンブラック、四弗化エチレ
ン樹脂粉末を重量比100対10対16で混合し練り合
わせた。この合剤にメチルアルコールを滴下し合剤を適
宜湿らせた。湿潤の様子は実施例1と同様にして求めた
。この合剤を粉砕し、80’Cで本乾燥の後、実施例、
と同さく扁平形電6ペー2 池を構成し、2mムの定電流、2.4〜3.8vの電圧
範囲で充放電をくり返した。
Example 2 Vanadium pentoxide, acetylene black, and tetrafluoroethylene resin powder were mixed and kneaded at a weight ratio of 100:10:16. Methyl alcohol was added dropwise to this mixture to moisten the mixture appropriately. The state of wetting was determined in the same manner as in Example 1. This mixture was pulverized and after main drying at 80'C, Example
A flat type battery was constructed in the same manner as above, and charging and discharging were repeated at a constant current of 2 mm and a voltage range of 2.4 to 3.8 V.

第2図は各充放電サイクルにおける放電容量をプロット
したもので、実線は、吸湿量26%の合剤を粉砕し乾燥
したものを極板に用いた場合、破線はメチルアルコール
を滴下しない吸湿量0%の合剤を粉砕したものを極板に
用いた場合である。
Figure 2 plots the discharge capacity in each charge/discharge cycle, where the solid line shows the amount of moisture absorbed when a pulverized and dried mixture with a moisture absorption of 26% is used for the electrode plate, and the broken line shows the amount of moisture absorbed without dropping methyl alcohol. This is a case where a pulverized 0% mixture was used for the electrode plate.

第2図より、明らかに湿潤状態で粉砕し乾燥した合剤を
用いた方がサイクル特性にすぐれることがわかる。これ
は、湿潤状態で粉砕すると、五酸化バナジウムと導電剤
が離れず、うまく集電されることによる。
From FIG. 2, it is clear that the use of a mixture that has been crushed in a wet state and dried has better cycle characteristics. This is because when crushed in a wet state, the vanadium pentoxide and the conductive agent do not separate and the current is successfully collected.

なお、実施例ではメチルアルコールを用いたが。Note that methyl alcohol was used in the examples.

アルコール類に限らず、エーテル、ベンゼン等蒸発性の
あるものであれば同様の結果が得られる。
Similar results can be obtained not only with alcohols but also with evaporable substances such as ether and benzene.

発明の効果 以上のように本発明によれば、電池放電容量にばらつき
の小さい、集電効率の良い電池極板が得られる。
Effects of the Invention As described above, according to the present invention, a battery plate with small variations in battery discharge capacity and high current collection efficiency can be obtained.

77、 第1図は本発明の実施例及び比較例の電池における最大
放電容量と最小放電容量の差を、粉砕前の合剤の吸湿量
に対してプロットした図であり、第2図は吸湿量26%
の合剤を粉砕、乾燥して用いた場合と、吸湿量0%の合
剤を粉砕して正極に用いた場合のサイクル特性を示す図
である。
77, Figure 1 is a diagram in which the difference between the maximum discharge capacity and the minimum discharge capacity of the batteries of Examples and Comparative Examples of the present invention is plotted against the amount of moisture absorbed by the mixture before pulverization, and Figure 2 shows the difference between the moisture absorption and Amount 26%
FIG. 3 is a diagram showing the cycle characteristics when a mixture of 1 is used after being crushed and dried, and when a mixture with a moisture absorption amount of 0% is crushed and used for a positive electrode.

代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 50             10θ吸湿量(2)
Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Figure 50 10θ moisture absorption amount (2)

Claims (1)

【特許請求の範囲】[Claims] 電池活物質、導電剤、結着剤を練合し、粉砕の後、所定
量を加圧成形して極板を形成する製造過程において、粉
砕時、練合物を液体を含んだ湿潤状態で粉砕し、乾燥す
ることを特徴とする電池極板の製造法。
During the manufacturing process in which battery active materials, conductive agents, and binders are kneaded and crushed, a predetermined amount is pressure-molded to form electrode plates. A method for manufacturing battery electrode plates, which is characterized by crushing and drying.
JP59212055A 1984-10-09 1984-10-09 Manufacture of battery plate Pending JPS6191859A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59212055A JPS6191859A (en) 1984-10-09 1984-10-09 Manufacture of battery plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59212055A JPS6191859A (en) 1984-10-09 1984-10-09 Manufacture of battery plate

Publications (1)

Publication Number Publication Date
JPS6191859A true JPS6191859A (en) 1986-05-09

Family

ID=16616113

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59212055A Pending JPS6191859A (en) 1984-10-09 1984-10-09 Manufacture of battery plate

Country Status (1)

Country Link
JP (1) JPS6191859A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1297920A1 (en) * 2001-09-28 2003-04-02 HOPPECKE Batterien GmbH & Co. KG. Surface active lead dust and method for its treatment

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS575265A (en) * 1980-06-11 1982-01-12 Sanyo Electric Co Ltd Manufacture of pasted cadmium cathode

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS575265A (en) * 1980-06-11 1982-01-12 Sanyo Electric Co Ltd Manufacture of pasted cadmium cathode

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1297920A1 (en) * 2001-09-28 2003-04-02 HOPPECKE Batterien GmbH & Co. KG. Surface active lead dust and method for its treatment
WO2003028926A1 (en) * 2001-09-28 2003-04-10 Hoppecke Batterien Gmbh & Co. Kg Highly active lead dusts and method for treatment thereof

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