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JPS6243306B2 - - Google Patents
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JPS6243306B2 - - Google Patents

Info

Publication number
JPS6243306B2
JPS6243306B2 JP54172713A JP17271379A JPS6243306B2 JP S6243306 B2 JPS6243306 B2 JP S6243306B2 JP 54172713 A JP54172713 A JP 54172713A JP 17271379 A JP17271379 A JP 17271379A JP S6243306 B2 JPS6243306 B2 JP S6243306B2
Authority
JP
Japan
Prior art keywords
anode
battery
anodes
metal
warpage
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.)
Expired
Application number
JP54172713A
Other languages
Japanese (ja)
Other versions
JPS5697970A (en
Inventor
Osamu Yumimoto
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.)
Maxell Ltd
Original Assignee
Hitachi Maxell 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 Hitachi Maxell Ltd filed Critical Hitachi Maxell Ltd
Priority to JP17271379A priority Critical patent/JPS5697970A/en
Publication of JPS5697970A publication Critical patent/JPS5697970A/en
Publication of JPS6243306B2 publication Critical patent/JPS6243306B2/ja
Granted 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
    • H01M4/06Electrodes for primary cells
    • H01M4/08Processes of manufacture
    • 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

Landscapes

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

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は金属網状体と陽極合剤とを一体に加
圧成形してなる陽極を使用する非水電解液電池の
製造法の改良に係り、加圧成形時に生じた陽極の
反りを矯正し、電池製造時の封口不良の発生を防
止することを目的とする。 電池応用機器の薄型化に伴ない、電池陽極も
増々薄くすることが要請されているが、厚さの薄
い陽極は加圧成形時に割れが発生しやすいため、
金網、エキスパンデツドメタルなどの金属網状体
で陽極合剤を補強することが行なわれている。 このような金属網状体で補強された陽極は、通
常所定の金型内に陽極合剤粉末を充填し、その上
に金属網状体を配置して加圧成形するか、あるい
は陽極合剤粉末を予備成形したのち、その上に金
属網状体を配置し加圧成形することによつて製造
されているが、金型内から取り出したときに陽極
の陽極合剤部分が径方向ないし厚さ方向に伸びよ
うとする、いわゆるスプリングバツク現象を引き
おこす。 この場合、金属網状体が付された側では、径方
向外方の伸張力が金属網状体によつて食い止めら
れるため、第2図に示すように、陽極1に金属網
状体2側を凹部とした反りが発生する。 このような反りの発生した陽極を使用して電池
を製造すると、電池の封口時に陽極に割れが生じ
たり、あるいは陽極が所定位置からずれ、陽極の
周縁部が陽極缶と環状ガスケツトとの間にかみこ
んだ状態で封口されるなどの封口不良が発生す
る。 そこで陽極を加熱処理することによつて、金属
網状体に一種の焼鈍的効果を与え、金属網状体の
構成金属をばね弾性の低い塑性変形のしやすい性
質に改質して陽極の反りを矯正する方法が見出さ
れ、この出願人によつてすでに特許出願されてい
るが、この方法によつて工業的生産に適する程度
に多量の陽極を加熱処理すると、陽極同士が部分
的に重なりあつた状態で加熱処理される場合が発
生し、その結果、他の陽極が乗かつた部分とそう
でない部分とで反りの矯正度合に相違が生じ、そ
のため陽極が加熱処理前よりもかえつて好ましく
ない状態に変形する場合が発生するため、この発
明者はさらに研究を重ねた結果、陽極の部分的な
重なりを防止しつつ慎重に加熱処理を行なうより
も、むしろ積極的に陽極を積み重ね、その状態で
加熱処理するときの方が、前述のごとき陽極の変
形が生じないことはもとより、反りが均斉に矯正
されることを見出し、この発明を完成するにいた
つた。 すなわち、この発明は金属網状体と陽極合剤と
を一体に加圧成形してなる陽極を使用する非水電
解液電池を製造するにあたり、陽極を水平に積み
重ねた状態で加熱処理を行なうことにより、加圧
成形時に生じた陽極の反りを矯正することを特徴
とする非水電解液電池の製造法に関する。 この発明の実施に際して、陽極を水平に積み重
ねるには、陽極の外径よりも若干大きい内径を有
する金属、陶磁器などの耐熱性円筒を用い、該円
筒内に陽極をたとえば100〜200個程度積み重ねる
ことによつて行なうのが好ましい。しかして、こ
の発明において、水平とは真正な水平のみを意味
するものではなく、ほぼ水平に近い状態をも含む
ものである。 この発明において、陽極の加熱処理時の温度と
しては、金属網状体に焼鈍的効果を与え、かつ陽
極活物質の活性能に悪影響を及ぼさない範囲内の
温度を選択することが必要であり、このような観
点から、加熱処理時の下限温度としては約300℃
を採用するのが好ましく、またその上限温度とし
ては陽極活物質の種類に応じて決定するのが望ま
しく、たとえば陽極活物質が二酸化マンガンの場
合は約450℃、硫化鉄の場合は約800℃、硫化第一
銅の場合は約600℃にするのが好ましい。なお処
理時間は処理温度によつても異なるが通常は30分
〜4時間である。 この発明において金属網状体としては、金網ま
たはエキスパンデツドメタルが使用され、材質的
にはステンレス製またはニツケル製のものが使用
される。そして金網の場合は線径が0.05〜0.12mm
φで網目が15〜100メツシユのものを使用するこ
とが好ましく、エキスパンデツドメタルの場合は
厚さが0.10〜0.35mmで開口率が55〜85面積%のも
のを使用することが好ましい。 陽極合剤としては、二酸化マンガン、硫化鉄、
硫化銅、酸化銅、フツ化カーボン、クロム酸銀な
どの陽極活物質、りん状黒鉛などの導電助剤およ
びポリテトラフルオロエチレンなどの結着剤から
なるものが使用され、加圧成形時の圧力として
は、通常1〜5t/cm2、好ましくは3t/cm2前後が採
用される。また陰極活物質としてはリチウム、ナ
トリウム、マグネシウムなどの軽金属が使用され
る。 第1図はこの発明の方法により製造される非水
電解液電池の構成例を示すものであり、図面にお
いて、1は金属網状体2と陽極合剤3とを加圧成
形したのち、金属製円筒内で積み重ね、その状態
で加熱処理された陽極であり、4はステンレス、
ニツケル、ステンレス−ニツケルなどの金属板で
形成される陽極缶であり、陽極1はその金属網状
体2側が陽極缶4の缶底に接するようにして陽極
缶4内に収納されている。5は金属リチウムより
なる円板状の陰極剤であり、この陰極剤5は前記
陽極缶4と同様の金属板で形成される陰極缶6の
内面にスポツト溶接されたニツケルまたはステン
レス製の金網7に圧着されている。8は陽極1と
陰極剤5との間に配置されたポリエチレン、ポリ
プロピレン、ガラス繊維などの不織布よりなるセ
パレータであり、9は陽極缶4の開口部と陰極缶
6との間に介装されたポリエチレン、ポリプロピ
レン、ナイロンなどからなる環状ガスケツトであ
る。そして、この電池には、たとえば1,2−ジ
メトキシエタン、炭酸プロピレン、テトラヒドロ
フラン、γ−ブチロラクトンなどの単独または2
種以上の混合溶媒に過塩素酸リチウムまたはホウ
フツ化リチウムを溶解させてなる非水電解液が注
入されている。 つぎの第1表は、1000個ずつの陽極を、この発
明の方法Aと後述する比較のための方法Bとによ
つて加熱処理した場合の陽極の反りの矯正状態の
相違を示すものである。使用された陽極は二酸化
マンガン100部(重量部、以下同様)、りん状黒鉛
10部およびポリテトラフルオロエチレン1.7部か
らなる陽極合剤粉末を1t/cm2で予備成形したの
ち、線径0.08mmφ、網目60メツシユのステンレス
製網と3t/cm2で一体に加圧成形したものであり、
この陽極の設計寸法は直径15.7mmφ、厚さ0.51mm
である。
This invention relates to an improvement in the manufacturing method of a non-aqueous electrolyte battery that uses an anode formed by integrally press-molding a metal mesh and an anode mixture, by correcting the warping of the anode that occurs during pressure-forming, and The purpose is to prevent sealing defects during battery manufacturing. As battery application devices become thinner, battery anodes are also required to become thinner and thinner, but thinner anodes are more likely to crack during pressure molding.
The anode mixture is reinforced with a metal mesh such as wire mesh or expanded metal. An anode reinforced with such a metal mesh is usually produced by filling the anode mixture powder into a predetermined mold, placing the metal mesh on top of the mold, and press-molding it, or by filling the anode mixture powder into a mold. After preforming, a metal mesh is placed on top of the preform and pressure molded. However, when the anode is taken out of the mold, the anode mixture part of the anode does not move in the radial or thickness direction. This causes a so-called springback phenomenon in which the material tries to stretch. In this case, on the side where the metal mesh is attached, the radially outward stretching force is stopped by the metal mesh, so as shown in FIG. Warpage occurs. If a battery is manufactured using such a warped anode, the anode may crack when the battery is sealed, or the anode may shift from its designated position, causing the periphery of the anode to become stuck between the anode can and the annular gasket. Poor sealing occurs, such as when the seal is stuck in place. Therefore, by heat-treating the anode, a kind of annealing effect is applied to the metal network, modifying the constituent metals of the metal network to have low spring elasticity and easy plastic deformation, thereby correcting the warpage of the anode. A method has been discovered and a patent application has already been filed by the applicant; however, when a large number of anodes are heat-treated to the extent suitable for industrial production, the anodes partially overlap each other. As a result, there is a difference in the degree of warpage correction between the part where the other anode is placed and the part where it is not, which makes the anode even more unfavorable than before the heat treatment. As a result of further research, the inventor found that rather than carefully heat treating the anodes while preventing their partial overlap, the inventors actively stacked the anodes and left them in that state. It was discovered that heat treatment not only does not cause the above-described deformation of the anode but also corrects the warpage more uniformly, leading to the completion of this invention. That is, when manufacturing a non-aqueous electrolyte battery using an anode formed by integrally press-forming a metal mesh and an anode mixture, the present invention is able to produce a , relates to a method for manufacturing a non-aqueous electrolyte battery characterized by correcting warpage of an anode that occurs during pressure molding. When carrying out this invention, in order to stack anodes horizontally, a heat-resistant cylinder made of metal, ceramic, or the like having an inner diameter slightly larger than the outer diameter of the anode is used, and about 100 to 200 anodes are stacked in the cylinder. Preferably, this is carried out by. However, in this invention, horizontal does not mean only true horizontality, but also includes a nearly horizontal state. In this invention, it is necessary to select the temperature during the heat treatment of the anode within a range that gives an annealing effect to the metal network and does not adversely affect the activity of the anode active material. From this point of view, the lower limit temperature during heat treatment is approximately 300℃.
It is preferable to adopt the upper limit temperature, and it is desirable to determine the upper limit temperature according to the type of anode active material. For example, if the anode active material is manganese dioxide, about 450°C, if iron sulfide, about 800°C, In the case of cuprous sulfide, the temperature is preferably about 600°C. Although the treatment time varies depending on the treatment temperature, it is usually 30 minutes to 4 hours. In this invention, a wire mesh or an expanded metal is used as the metal net, and the material used is stainless steel or nickel. And in the case of wire mesh, the wire diameter is 0.05 to 0.12mm.
It is preferable to use a material with a diameter of 15 to 100 meshes, and in the case of expanded metal, a material with a thickness of 0.10 to 0.35 mm and an aperture ratio of 55 to 85% by area is preferred. The anode mixture includes manganese dioxide, iron sulfide,
A material consisting of anode active materials such as copper sulfide, copper oxide, carbon fluoride, and silver chromate, a conductive agent such as phosphorous graphite, and a binder such as polytetrafluoroethylene is used, and the pressure during pressure molding is Generally, 1 to 5 t/cm 2 , preferably around 3 t/cm 2 is adopted. Furthermore, light metals such as lithium, sodium, and magnesium are used as the cathode active material. FIG. 1 shows an example of the structure of a non-aqueous electrolyte battery manufactured by the method of the present invention. The anodes are stacked in a cylinder and heat-treated in that state; 4 is stainless steel;
The anode can is made of a metal plate such as nickel or stainless-nickel, and the anode 1 is housed in the anode can 4 with its metal mesh 2 side in contact with the bottom of the anode can 4. Reference numeral 5 denotes a disc-shaped cathode material made of metallic lithium, and this cathode material 5 includes a wire mesh 7 made of nickel or stainless steel that is spot-welded to the inner surface of a cathode can 6 made of the same metal plate as the anode can 4. is crimped to. 8 is a separator made of non-woven fabric such as polyethylene, polypropylene, glass fiber, etc. placed between the anode 1 and the cathode agent 5, and 9 is interposed between the opening of the anode can 4 and the cathode can 6. An annular gasket made of polyethylene, polypropylene, nylon, etc. In this battery, for example, 1,2-dimethoxyethane, propylene carbonate, tetrahydrofuran, γ-butyrolactone, etc. may be used alone or in combination.
A non-aqueous electrolyte made by dissolving lithium perchlorate or lithium borofluoride in a mixed solvent of more than one species is injected. Table 1 below shows the difference in the state of correction of anode warpage when 1000 anodes were heat treated by method A of the present invention and method B for comparison, which will be described later. . The anode used was 100 parts of manganese dioxide (parts by weight, the same applies hereinafter) and phosphorous graphite.
After preforming an anode mixture powder consisting of 10 parts and 1.7 parts of polytetrafluoroethylene at 1 t/cm 2 , it was integrally press-formed with a stainless steel mesh with a wire diameter of 0.08 mmφ and a mesh size of 60 mesh at 3 t/cm 2 . It is a thing,
The design dimensions of this anode are diameter 15.7mmφ and thickness 0.51mm.
It is.

【表】 この発明の方法Aは陽極を内径16mmφ、外径30
mmφのセラミツク製円筒内に100個積み重ね、そ
の状態で400℃で4時間加熱処理する方法であ
り、方法Bは内径1300mmφ、高さ50mmのセラミツ
ク製容器に陽極を100個任意に投入し、その状態
で400℃で4時間加熱処理する方法である。そし
て、第1表に示す反りは、第2図に示すように陽
極1を水平に置いた際に、陽極の全高をh、厚さ
をtとした場合にh−tで示されるものである。 第1表に示されるように、この発明の方法Aに
よる場合は、方法Bの場合に比べて、陽極の反り
が小さくなり、かつほとんどのものが電池製造上
望ましいと考えられる0.08mm以下の反りになる。 第2表は第1図に示すような構成からなり、前
記方法Aにより加熱処理された陽極を用いた電池
A、前記方法Bにより加熱処理された陽極を用い
た電池Bおよび加熱処理を行なわなかつたほかは
電池Aの場合と同様の陽極を用いた電池Cを各
1000個ずつ製造した際の封口不良個数を調べた結
果を示すものである。なお、これらの電池の設計
寸法はいずれも直径20mmφ、高さ1.6mmである。
[Table] Method A of this invention uses an anode with an inner diameter of 16 mmφ and an outer diameter of 30 mm.
Method B involves stacking 100 anodes in a ceramic cylinder with a diameter of 1300 mm and heating them at 400°C for 4 hours. This method involves heat treatment at 400°C for 4 hours. The warpage shown in Table 1 is expressed as h-t when the anode 1 is placed horizontally as shown in Figure 2, where h is the total height of the anode and t is the thickness. . As shown in Table 1, when using method A of the present invention, the warpage of the anode is smaller than when using method B, and in most cases, the warpage is 0.08 mm or less, which is considered desirable for battery manufacturing. become. Table 2 consists of the configuration shown in Figure 1, and includes battery A using an anode heat-treated by method A, battery B using an anode heat-treated by method B, and battery B that was not heat-treated. In addition, battery C using the same anode as battery A was used.
This shows the results of investigating the number of sealing failures when 1000 pieces were manufactured. The design dimensions of these batteries are 20 mm in diameter and 1.6 mm in height.

【表】 第2表に示されるように、この発明の方法によ
る電池Aの場合は封口不良の発生個数が少ない。 以上詳述したように、この発明は金属網状体と
陽極合剤とを一体に加圧成形してなる陽極を使用
する非水電解液電池を製造するにあたり、陽極を
水平に積み重ねた状態で加熱処理を行なうことに
より、加圧成形時に生じた陽極の反りを矯正し、
陽極の反りに基づく封口不良の発生を防止するよ
うにしたものである。
[Table] As shown in Table 2, in the case of battery A manufactured by the method of the present invention, the number of sealing failures was small. As described in detail above, the present invention involves heating the anodes in a horizontally stacked state when manufacturing a non-aqueous electrolyte battery using an anode formed by integrally press-molding a metal mesh and an anode mixture. By performing the treatment, the warpage of the anode that occurred during pressure molding is corrected, and
This is to prevent sealing failures caused by warping of the anode.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はこの発明の方法により製造される非水
電解液電池の構成例を示す断面図、第2図は陽極
に反りが発生した状態を示す断面図である。 1……陽極、2……金属網状体、3……陽極合
剤。
FIG. 1 is a sectional view showing an example of the structure of a non-aqueous electrolyte battery manufactured by the method of the present invention, and FIG. 2 is a sectional view showing a state where the anode is warped. 1...Anode, 2...Metal network, 3...Anode mixture.

Claims (1)

【特許請求の範囲】[Claims] 1 金属網状体と陽極合剤とを一体に加圧成形し
てなる陽極を使用する非水電解液電池を製造する
にあたり、陽極を水平に積み重ねた状態で加熱処
理を行なうことにより、加圧成形時に生じた陽極
の反りを矯正することを特徴とする非水電解液電
池の製造法。
1. When manufacturing a non-aqueous electrolyte battery that uses an anode formed by integrally press-molding a metal mesh and an anode mixture, the anodes are stacked horizontally and subjected to heat treatment. A method for manufacturing a non-aqueous electrolyte battery, which is characterized by correcting warpage of an anode that sometimes occurs.
JP17271379A 1979-12-29 1979-12-29 Manufacture of nonaqueous electrolyte battery Granted JPS5697970A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17271379A JPS5697970A (en) 1979-12-29 1979-12-29 Manufacture of nonaqueous electrolyte battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17271379A JPS5697970A (en) 1979-12-29 1979-12-29 Manufacture of nonaqueous electrolyte battery

Publications (2)

Publication Number Publication Date
JPS5697970A JPS5697970A (en) 1981-08-07
JPS6243306B2 true JPS6243306B2 (en) 1987-09-12

Family

ID=15946947

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17271379A Granted JPS5697970A (en) 1979-12-29 1979-12-29 Manufacture of nonaqueous electrolyte battery

Country Status (1)

Country Link
JP (1) JPS5697970A (en)

Also Published As

Publication number Publication date
JPS5697970A (en) 1981-08-07

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