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JPS6366029B2 - - Google Patents
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JPS6366029B2 - - Google Patents

Info

Publication number
JPS6366029B2
JPS6366029B2 JP55030803A JP3080380A JPS6366029B2 JP S6366029 B2 JPS6366029 B2 JP S6366029B2 JP 55030803 A JP55030803 A JP 55030803A JP 3080380 A JP3080380 A JP 3080380A JP S6366029 B2 JPS6366029 B2 JP S6366029B2
Authority
JP
Japan
Prior art keywords
block
battery
zinc
weight
laminated dry
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
JP55030803A
Other languages
Japanese (ja)
Other versions
JPS56126268A (en
Inventor
Seigo Sato
Shiro Azuma
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 JP3080380A priority Critical patent/JPS56126268A/en
Publication of JPS56126268A publication Critical patent/JPS56126268A/en
Publication of JPS6366029B2 publication Critical patent/JPS6366029B2/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
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/42Grouping of primary cells into batteries
    • H01M6/46Grouping of primary cells into batteries of flat cells
    • H01M6/48Grouping of primary cells into batteries of flat cells with bipolar electrodes

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Primary Cells (AREA)

Description

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

この発明は積層乾電池の製造法の改良に関し、
保存性能の向上を目的とする。 一般に積層乾電池における素電池7は、第1図
に示すように、亜鉛板1の片面に炭素膜2を形成
した炭素―亜鉛結合電極3の亜鉛板1側と、陽極
合剤4との間にセパレータ5を介在させ、これに
電解液を添加し、熱収縮性樹脂チユーブ6で被覆
し、この熱収縮性樹脂チユーブ6を加熱して収縮
させ、陽極合剤4とセパレータ5との間、セパレ
ータ5と炭素―亜鉛結合電極3との間、ならびに
これらの部材と熱収縮性樹脂チユーブ6との間を
密着させた構造となつている。 そして積層乾電池は、このような素電池7を積
み重ね、上方より加圧して整形してブロツクとな
し、ついで溶融したワツクスなどの密封材浴に浸
漬しブロツク表面を密封材で被覆する工程を経て
製造されるが、前記加圧の際に、素電池上面およ
び下面の熱収縮性樹脂チユーブがパツキングとし
ての役目を果すため、陽極合剤中の空気は逃げ場
がなくなり、第2図に示すようにセパレータ5と
熱収縮性樹脂チユーブ6との間の空間に溜まり、
そのままの状態で密封材が外面を覆うため、多量
の空気がかかえこまれたままで積層乾電池に仕上
げられる。 このように多量の空気が含有されたままで電池
が製造されると、製造直後より空気中の酸素によ
つて亜鉛が酸化された腐食が生じ、電池性能が低
下する。 これは塩化亜鉛を主電解質とする積層乾電池に
おいて、特に著しく初度特性は塩化アンモニウム
を主電解質とする積層乾電池に比べてすぐれてい
るが、次式 MnO2+4Zn+ZnCl2+8H2O→1/2Mn2O3・H2O+ZnCl2・4Z
n(OH)2 に示されるような水を消費する放電反応を行な
い、この放電反応が保存中に一部陽極合剤中で生
じ、これを捕なうためセパレータに形成した糊層
中の水分が陽極合剤に引きよせられる傾向があ
り、その結果、容量劣化が惹起されるとともに、
糊層中の水分の減少により亜鉛と糊層との密着性
が低下し、亜鉛が腐食されやすい状態になる。 亜鉛の腐食は亜鉛表面(固相)と、電解液(液
相)と空気(気相)との三相界面で促進されるも
のであり、塩化亜鉛を主電解質とする積層乾電池
では前述のように亜鉛表面の電解液が保存中に減
少するため、電池内に空気が多量に残存すると上
記三相界面が増大し、亜鉛の腐食による電池性能
の低下が著しい。これは塩化アンモニウムを主電
解質とする積層乾電池に比べてはるかに大きく使
用に耐えなくなることがある。 この発明はこのような事情に照らしてなされた
ものであり、素電池を必要個数積重して加圧整形
したブロツクを減圧下に放置して、陽極合剤中な
どに存在する素電池内の空気および樹脂チユーブ
とセパレータ間に存在する素電池内の空気などを
抜き取つたのち、前記ブロツクの表面に密封材層
を形成し密封材層の周囲を熱収縮性樹脂チユーブ
で包被することにより、塩化亜鉛を主電解質とす
る積層乾電池の保存性を向上させたものである。 この発明において、減圧度は、放置時間との関
係で決められるものであり特に限定されないが、
通常は200mmHg以下が採用される。そして減圧下
での放置時間は減圧度や素電池の大きさなどによ
つて変化し特に限定されるものではないが、通常
1〜60分間程度とされる。素電池内の空気を完全
に抜き取ることは実際上不可能なので、実質的に
素電池内の空気を除去できれば、それで目的を達
しうる。 また電解液組成は、塩化亜鉛濃度が20重量%〜
35重量%、塩化アンモニウム濃度が7重量%以下
が使用され好ましくは塩化亜鉛濃度が20重量%〜
35重量%、塩化アンモニウム濃度が2重量%〜5
重量%が使用される。 つぎに実施例をあげ、この発明をさらに詳細に
説明する。 実施例 二酸化マンガンとアセチレンブラツクとを80:
15(重量比)で混合した混合物21重量部を、塩化
亜鉛23重量%、塩化アンモニウム5重量%および
水72重量%からなる電解液9重量部で湿潤し成形
して陽極合剤を作製した。 つぎに熱収縮性ポリ塩化ビニルチユーブに、炭
素膜の周縁に接着剤を塗布した炭素―亜鉛結合電
極を挿入し、加熱して炭素―亜鉛結合電極の炭素
膜の周縁部に前記熱収縮性チユーブの周縁部を接
着させた。 ついで該炭素―亜鉛結合電極上に片面に糊層を
形成したセパレータおよび前記陽極合剤を挿入
し、前記組成の電解液を4.2重量部注入してセパ
レータに吸収させたのち、加熱して前記熱収縮性
チユーブを収縮させて素電池を作製した。 つぎにこの素電池を6個積み重ね、その上端お
よび下端に金属板を当接し、加圧して整形してブ
ロツクを形成し、このブロツクを20分間、200mm
Hgに調整、維持した減圧室に入れ、素電池内の
空気を抜き取つた。これを125℃に溶融されたワ
ツクスよりなる密封材浴に浸漬し、ブロツク表面
に密封材層を形成し、さらにその周囲を熱収縮性
ポリ塩化ビニルチユーブで包被し、以後常法によ
りリード体、端子板をとりつけ、外装缶に挿入
し、外装缶を締め付けて006P型の積層乾電池を
製造した。 つぎに上記実施例によるこの発明の積層乾電池
Aと、前記のようなブロツク内の空気の除去を行
なうことなく従来法で製造した積層乾電池B、お
よび電解液を塩化アンモニウム28重量%、塩化亜
鉛20重量%および水57%からなる塩化アンモニウ
ム型に変え、かつブロツク内の空気の除去を行な
うことなく製造した積層乾電池C、ならびに電解
液として積層乾電池Cと同様に塩化アンモニウム
を主電解質とするものを用いブロツク内の空気を
抜き取つたのち製造した積層乾電池Dについて初
度および45℃で3ケ月貯蔵後の電池特性を測定
し、その結果を第1表に示した。
This invention relates to an improvement in the manufacturing method of a laminated dry battery.
The purpose is to improve storage performance. In general, a unit cell 7 in a stacked dry battery is constructed between a carbon-zinc bonded electrode 3, which has a carbon film 2 formed on one side of a zinc plate 1, and an anode mixture 4, as shown in FIG. A separator 5 is interposed, an electrolytic solution is added thereto, and the heat-shrinkable resin tube 6 is covered with the heat-shrinkable resin tube 6, and the heat-shrinkable resin tube 6 is heated to shrink. 5 and the carbon-zinc bonded electrode 3, as well as between these members and the heat-shrinkable resin tube 6. The laminated dry battery is manufactured by stacking such unit cells 7, applying pressure from above and shaping them into a block, and then immersing it in a bath of molten wax or other sealant to cover the surface of the block with the sealant. However, during the pressurization, the heat-shrinkable resin tubes on the top and bottom surfaces of the cell serve as packing, so the air in the anode mixture has no place to escape, and the separator is removed as shown in Figure 2. 5 and the heat-shrinkable resin tube 6,
Since the sealing material covers the outer surface of the battery in its original state, a large amount of air is trapped inside the battery, allowing it to be finished into a laminated dry cell battery. If a battery is manufactured with such a large amount of air still contained, corrosion due to oxidation of zinc will occur immediately after manufacture due to oxygen in the air, resulting in a decrease in battery performance. This is particularly true for laminated dry batteries that use zinc chloride as the main electrolyte, which has significantly superior initial characteristics compared to laminated dry cells that use ammonium chloride as the main electrolyte, but the following formula MnO 2 +4Zn+ZnCl 2 +8H 2 O→1/2Mn 2 O 3・H 2 O+ZnCl 2・4Z
A discharge reaction that consumes water, as shown in tend to be attracted to the anode mixture, resulting in capacity deterioration and
As the water content in the glue layer decreases, the adhesion between the zinc and the glue layer decreases, making the zinc susceptible to corrosion. Corrosion of zinc is accelerated at the three-phase interface between the zinc surface (solid phase), electrolyte (liquid phase), and air (vapor phase), and as mentioned above, in laminated dry batteries with zinc chloride as the main electrolyte, Since the electrolyte on the zinc surface decreases during storage, if a large amount of air remains in the battery, the three-phase interface increases, and the battery performance deteriorates significantly due to zinc corrosion. This is much larger than a laminated dry cell battery that uses ammonium chloride as the main electrolyte, and may become unusable. This invention was made in light of the above circumstances, and a block obtained by stacking a required number of unit cells and forming them under pressure is left under reduced pressure to collect the contents of the unit cells present in the anode mixture, etc. After removing air and the air inside the cell existing between the resin tube and the separator, a sealant layer is formed on the surface of the block, and the sealant layer is surrounded by a heat-shrinkable resin tube. This is a stacked dry battery with improved storage stability that uses zinc chloride as the main electrolyte. In this invention, the degree of pressure reduction is determined in relation to the standing time and is not particularly limited, but
Usually 200mmHg or less is adopted. The time for leaving under reduced pressure varies depending on the degree of reduced pressure, the size of the unit cell, etc., and is not particularly limited, but is usually about 1 to 60 minutes. Since it is practically impossible to completely remove the air inside the unit cell, if the air inside the unit cell can be substantially removed, the objective can be achieved. In addition, the electrolyte composition has a zinc chloride concentration of 20% by weight or more.
35% by weight, an ammonium chloride concentration of 7% by weight or less is used, preferably a zinc chloride concentration of 20% by weight or less
35% by weight, ammonium chloride concentration between 2% and 5% by weight
Weight percentages are used. Next, the present invention will be explained in more detail with reference to Examples. Example 80% manganese dioxide and acetylene black:
15 (weight ratio) was moistened with 9 parts by weight of an electrolytic solution consisting of 23% by weight of zinc chloride, 5% by weight of ammonium chloride, and 72% by weight of water, and molded to prepare an anode mixture. Next, a carbon-zinc bonded electrode coated with an adhesive around the periphery of the carbon film is inserted into the heat-shrinkable polyvinyl chloride tube, and heated so that the heat-shrinkable tube is attached to the periphery of the carbon film of the carbon-zinc bonded electrode. The periphery of the rim was glued. Next, a separator with a glue layer formed on one side and the anode mixture were inserted onto the carbon-zinc bonded electrode, and 4.2 parts by weight of the electrolytic solution having the above composition was injected and absorbed into the separator, and then heated to absorb the heat. A unit cell was fabricated by shrinking the shrinkable tube. Next, six of these cells are stacked, a metal plate is brought into contact with the upper and lower ends, and a metal plate is pressed and shaped to form a block.
The cell was placed in a depressurized chamber adjusted to and maintained at Hg, and the air inside the cell was removed. This is immersed in a sealing material bath made of wax melted at 125°C to form a sealing material layer on the surface of the block, and the surrounding area is further covered with a heat-shrinkable polyvinyl chloride tube. A 006P type laminated dry battery was manufactured by attaching the terminal plate, inserting it into the outer can, and tightening the outer can. Next, the laminated dry battery A of the present invention according to the above embodiment, the laminated dry battery B manufactured by the conventional method without removing the air inside the block as described above, and the electrolyte were made of 28% by weight of ammonium chloride and 20% by weight of zinc chloride. A laminated dry battery C manufactured by changing to an ammonium chloride type consisting of 57% by weight and 57% water and without removing the air inside the block, and a battery using ammonium chloride as the main electrolyte like laminated dry battery C as an electrolyte. After removing the air from the block used, the battery characteristics of the manufactured laminated dry cell D were measured both initially and after storage at 45° C. for 3 months, and the results are shown in Table 1.

【表】 第1表に示されるように、この発明法による積
層乾電池Aは従来法による積層乾電池BおよびC
に比べて初度および貯蔵後の電池特性が良好で、
しかも保存による電池性能の低下が少ない。 また塩化アンモニウムを主電解質とし、この発
明と同様にブロツク内の空気を抜き取つて製造さ
れた積層乾電池Dと比べても、この発明の積層乾
電池Aは電池性能がすぐれている。 以上詳述したように、この発明は塩化亜鉛を主
電解質とする積層乾電池を製造するにあたり、ブ
ロツクを減圧下に放置してブロツク内の空気を除
去することにより、保存性を向上させたものであ
る。
[Table] As shown in Table 1, the laminated dry batteries A made by the method of this invention are laminated dry batteries B and C made by the conventional method.
The battery characteristics are better both initially and after storage, compared to
Moreover, there is little deterioration in battery performance due to storage. Furthermore, the battery performance of the stacked dry battery A of the present invention is superior to that of the stacked dry battery D, which uses ammonium chloride as the main electrolyte and is manufactured by removing air from the block as in the present invention. As detailed above, this invention improves storage stability by leaving the block under reduced pressure to remove the air inside the block when producing a laminated dry battery using zinc chloride as the main electrolyte. be.

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

第1図は素電池の一例を示す断面図、第2図は
従来法により積層乾電池を製造する際に積重され
た素電池内の空気が加圧により熱収縮性樹脂チユ
ーブとセパレータとの間に溜まる状態を示す断面
図である。第3図は、本発明の製造工程を示す工
程フロー図である。 5……セパレータ、6……熱収縮性樹脂チユー
ブ、7……素電池。
Figure 1 is a cross-sectional view showing an example of a unit cell, and Figure 2 is a cross-sectional view showing an example of a unit cell, and Figure 2 is a cross-sectional view of an example of a unit cell. FIG. FIG. 3 is a process flow diagram showing the manufacturing process of the present invention. 5...Separator, 6...Heat-shrinkable resin tube, 7...Battery.

Claims (1)

【特許請求の範囲】 1 塩化亜鉛を主電解質とする積層乾電池を製造
するにあたり、 イ 塩化亜鉛を主電解質とする素電池7を必要個
数積層し、加圧成形してブロツクを形成する工
程と、 ロ 前記イのブロツクを減圧下に放置して各素電
池7内の空気を抜き取る工程と、 ハ 前記ロのブロツクの表面に密閉材層を形成す
る工程と、 ニ 前記ハのブロツクに形成された密閉材層の周
囲を熱収縮性樹脂チユーブで包被する工程とか
らなる積層乾電池の製造法。
[Scope of Claims] 1. In manufacturing a laminated dry battery using zinc chloride as the main electrolyte, (a) stacking a required number of unit cells 7 using zinc chloride as the main electrolyte and forming a block by pressure forming; (b) A step of leaving the block in (A) under reduced pressure to remove the air inside each unit cell 7; (c) Forming a sealing material layer on the surface of the block in (B); (d) Forming a sealing material layer on the block in (C) above. A method for manufacturing a laminated dry cell battery that includes the step of enclosing the periphery of the sealing material layer with a heat-shrinkable resin tube.
JP3080380A 1980-03-10 1980-03-10 Fabrication of layer-built dry battery Granted JPS56126268A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3080380A JPS56126268A (en) 1980-03-10 1980-03-10 Fabrication of layer-built dry battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3080380A JPS56126268A (en) 1980-03-10 1980-03-10 Fabrication of layer-built dry battery

Publications (2)

Publication Number Publication Date
JPS56126268A JPS56126268A (en) 1981-10-03
JPS6366029B2 true JPS6366029B2 (en) 1988-12-19

Family

ID=12313830

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3080380A Granted JPS56126268A (en) 1980-03-10 1980-03-10 Fabrication of layer-built dry battery

Country Status (1)

Country Link
JP (1) JPS56126268A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62198051A (en) * 1986-02-25 1987-09-01 Toshiba Battery Co Ltd Laminated type zinc chloride cell

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5220231A (en) * 1975-08-08 1977-02-16 Toshiba Ray O Vac Layerrbuilt dry element battery

Also Published As

Publication number Publication date
JPS56126268A (en) 1981-10-03

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