JP2990725B2 - Sealed nickel-cadmium battery - Google Patents
Sealed nickel-cadmium batteryInfo
- Publication number
- JP2990725B2 JP2990725B2 JP2054214A JP5421490A JP2990725B2 JP 2990725 B2 JP2990725 B2 JP 2990725B2 JP 2054214 A JP2054214 A JP 2054214A JP 5421490 A JP5421490 A JP 5421490A JP 2990725 B2 JP2990725 B2 JP 2990725B2
- Authority
- JP
- Japan
- Prior art keywords
- battery
- electrode plate
- cadmium
- charging
- nickel
- 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 - Lifetime
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Secondary Cells (AREA)
- Connection Of Batteries Or Terminals (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は、急速充電が可能な密閉形のニッケル−カド
ミウム電池に関するものである。Description: TECHNICAL FIELD The present invention relates to a sealed nickel-cadmium battery capable of quick charging.
従来の技術とその課題 現在、一般的に用いられている二次電池は主として鉛
電池およびニッケル−カドミウム電池である。特に、ニ
ッケル−カドミウム電池は、鉛電池に比べて高率放電の
性能が優れていることや長寿命であるなどの理由で広く
用いられている。しかし一方では、近年の電子機器の小
形化にともなって電池の容量密度の増加や充電時間の短
縮が望まれている。しかしながら、従来のニッケル−カ
ドミウム電池におけるこれらの特性の向上は、すでに限
界であった。2. Description of the Related Art Conventionally, secondary batteries commonly used at present are mainly lead batteries and nickel-cadmium batteries. In particular, nickel-cadmium batteries are widely used because of their superior high-rate discharge performance and long life compared to lead batteries. However, on the other hand, with the recent miniaturization of electronic devices, it is desired to increase the capacity density of batteries and to shorten the charging time. However, the improvement of these properties in conventional nickel-cadmium batteries has already been limited.
最近、以上の問題を解決するものとして、例えば特願
昭62−83582号、特願昭63−13345号および特願平1−39
513号などで、いわゆるリザーブ用の水酸化カドミウム
をほとんど有せずしかも充電性能の優れたカドミウム負
極板を備えた新しい密閉形ニッケル−カドミウム電池が
提案されている。この電池はカドミウム負極板の充電時
の水素発生に至る電位変化を電池電圧の変化として検出
することで充電が制御できるものであり、温度補償を必
要とせずに短時間での充電が可能である。Recently, as a solution to the above problems, for example, Japanese Patent Application Nos. 62-83582, 63-13345, and 1-39.
No. 513 and the like propose a new sealed nickel-cadmium battery provided with a cadmium negative electrode plate having little cadmium hydroxide for reserve and having excellent charging performance. This battery can control charging by detecting a potential change leading to hydrogen generation during charging of a cadmium negative electrode plate as a change in battery voltage, and can be charged in a short time without requiring temperature compensation. .
しかし、この電池は従来のリザーブ用の水酸化カドミ
ウムを有する密閉形ニッケル−カドミウム電池において
一般的に用いられている金属電槽を用いた場合にサイク
ル使用での寿命が短いという問題点を有していた。However, this battery has a problem that the life in cycle use is short when a metal battery case generally used in a sealed nickel-cadmium battery having cadmium hydroxide for a conventional reserve is used. I was
理由は次の通りである。 The reason is as follows.
すでに述べたように、この電池の充電特性の特徴は、
充電終期に負極板の水素発生に至る電位変化に基づくき
わめて大きな電池電圧の変化が生じることである。しか
し、この電池に金属電槽を適用すると充電終期の電池電
圧の変化が大きく減少することがわかった。As already mentioned, the characteristics of the charging characteristics of this battery are:
At the end of charging, an extremely large change in battery voltage is caused based on a change in potential that leads to the generation of hydrogen on the negative electrode plate. However, it was found that when a metal battery case was applied to this battery, the change in battery voltage at the end of charging was greatly reduced.
これは一般に金属電槽の材質として鉄に水素過電圧が
小さい性質を有するニッケルをめっきしたものが用いら
れることによる。つまり充電終期の電圧変化の大きさ
は、本来主としてカドミウム負極板の水素発生の分極の
大きさに基づくものであるが、金属電槽を用いた場合に
は、電槽内面のニッケルをサイトとする水素発生によっ
て著しく減少する。さらに、このことは水素ガスの蓄積
による酸素ガス吸収性能の低下すなわち電解液量の著し
い減少を生じる原因にもなる。This is because, in general, iron plated with nickel having a property of low hydrogen overvoltage is used as the material of the metal battery case. In other words, the magnitude of the voltage change at the end of charging is primarily based on the magnitude of the polarization of hydrogen generation of the cadmium negative electrode plate, but when a metal battery case is used, nickel on the inner surface of the battery case is Significantly reduced by the generation of hydrogen. Further, this also causes a decrease in oxygen gas absorption performance due to accumulation of hydrogen gas, that is, a significant decrease in the amount of electrolyte.
なお、従来の密閉形ニッケル−カドミウム電池でこの
ような問題が生じないのは、いわゆるリザーブ用の水酸
化カドミウムを有していることによってカドミウム負極
板がニッケルの水素発生の電位にまで分極しないためで
ある。Note that such a problem does not occur in the conventional sealed nickel-cadmium battery because the cadmium negative electrode plate does not polarize to the potential of hydrogen generation of nickel by having cadmium hydroxide for so-called reserve. It is.
以上のことからわかるように負極板の水素発生に至る
電位変化を電池電圧の変化として検出して充電を制御す
る電池に対しては金属電槽の適用は避けるべきであり、
合成樹脂製の電槽が用いられていた。As can be seen from the above, the application of a metal container should be avoided for a battery that controls charging by detecting a potential change leading to hydrogen generation on the negative electrode plate as a change in battery voltage,
A battery case made of synthetic resin was used.
しかしながら、合成樹脂製の電槽は、金属製のものに
比べて機械的強度が弱いために電槽壁の厚みを大きくし
てその強度を保つ必要がある。つまり、合成樹脂製の電
槽を備えた電池は、金属電槽を用いた電池よりも体積当
りの容量密度が小さいことが知られている。また、合成
樹脂製の電槽を備えた電池は、電極端子部でアルカリ電
解液がリークする現象や、電槽壁を水蒸気が透過する現
象の抑制が充分でない問題もあった。However, a synthetic resin battery case has a lower mechanical strength than a metal battery case, and therefore it is necessary to maintain the strength by increasing the thickness of the battery case wall. That is, it is known that a battery provided with a battery case made of a synthetic resin has a smaller capacity density per volume than a battery using a metal battery case. In addition, the battery provided with the battery case made of synthetic resin also has a problem that the phenomenon that the alkaline electrolyte leaks at the electrode terminal portion and the phenomenon that water vapor permeates through the battery case wall are not sufficiently suppressed.
課題を解決するための手段 本発明は、先述の特願昭62−83582号、特願昭63−133
45号および特願平1−39513号などの提案に係る電池す
なわち負極板中の水酸化カドミウムの重量が正極板中の
水酸化ニッケルの重量の0.95倍以下である密閉形ニッケ
ル−カドミウム電池に関するものであり、以下の構造で
あることを特徴とする。すなわち、本発明は正極板、負
極板およびセパレータ等からなる極板群と、これを収容
した金属電槽との間に合成樹脂層を有することを特徴と
する。Means for Solving the Problems The present invention relates to the aforementioned Japanese Patent Application Nos. 62-83582 and 63-133.
No. 45 and Japanese Patent Application No. 1-39513, related to a sealed nickel-cadmium battery in which the weight of cadmium hydroxide in the negative electrode plate is 0.95 times or less the weight of nickel hydroxide in the positive electrode plate. And is characterized by the following structure. That is, the present invention is characterized in that a synthetic resin layer is provided between an electrode plate group including a positive electrode plate, a negative electrode plate, a separator, and the like, and a metal container containing the electrode plate group.
作用 本発明は、極板群と金属電槽との間に合成樹脂層を有
することによって金属電槽内面での水素の発生を抑制す
る効果を有する。Action The present invention has an effect of suppressing generation of hydrogen on the inner surface of the metal battery case by having a synthetic resin layer between the electrode group and the metal battery case.
すなわち、合成樹脂フィルムを備えていない構造の電
池では、エレメントと金属ケースとの間で電解液を経由
して電流が流れることによって充電終期に金属電槽内面
から水素が発生する。一方、合成樹脂フィルムを備えた
構造の電池では、電解液を経由する通電経路が遮断され
ることから金属電槽内面からの水素発生を防ぐことがで
きる。つまり、合成樹脂フィルムを備えた本発明の構造
の電池は、繰り返しの使用で電解液の減少をほとんど示
さず長寿命である。That is, in a battery having no structure including a synthetic resin film, a current flows between the element and the metal case via the electrolytic solution, so that hydrogen is generated from the inner surface of the metal container at the end of charging. On the other hand, in a battery having a structure provided with a synthetic resin film, the passage of electricity through the electrolytic solution is cut off, so that generation of hydrogen from the inner surface of the metal container can be prevented. That is, the battery having the structure of the present invention provided with the synthetic resin film has a long life with almost no decrease in the electrolytic solution due to repeated use.
また、本発明の電池の負極板の水素発生に至る電位変
化は、ニッケル面からの水素発生がほとんど無いことに
よって合成樹脂フィルムを備えていない電池におけるも
のよりも大きい。つまり、合成樹脂フィルムを備えた本
発明の電池はそうでない電池よりも大きな電池電圧の変
化を充電終期に示す。Further, the change in potential of the negative electrode plate of the battery of the present invention leading to the generation of hydrogen is larger than that of the battery having no synthetic resin film due to almost no generation of hydrogen from the nickel surface. That is, the battery of the present invention provided with the synthetic resin film shows a larger change in battery voltage at the end of charging than the battery which does not.
したがって、本発明の電池は合成樹脂フィルムを備え
ていない電池に比べて高い電圧で充電制御することが可
能であり充電制御の信頼性が高いといえる。このこと
は、例えば電池を温度補償のない定電圧充電方式で充電
した際の放電容量におよぼす充電時の雰囲気温度の影響
が少ないことを意味する。Therefore, the battery of the present invention can perform charge control at a higher voltage than a battery having no synthetic resin film, and it can be said that the charge control has high reliability. This means that the influence of the ambient temperature during charging on the discharge capacity when the battery is charged by the constant voltage charging method without temperature compensation is small, for example.
以上のように、本発明は長寿命で、しかも充電制御の
信頼性が高い急速充電可能な密閉形アルカリ二次電池を
供給するものである。As described above, the present invention provides a sealed alkaline secondary battery that has a long life and can be charged quickly with high reliability of charge control.
なお、本発明の構造の電池は、内面に合成樹脂をコー
ティングした金属電槽に極板群を収容する方法で製作で
きる他、極板群を合成樹脂製の袋に収容した後、これを
金属電槽に挿入する方法によっても製作することができ
る。特に、合成樹脂製の袋として、いわゆる熱収縮チュ
ーブを用いる方法は、極板群が複数の平板状の極板から
なるものである場合、すなわち電池の形状が角形である
場合に積層された極板同志の位置のずれを矯正する効果
や極板群の取り扱いにおける破損を防ぐ効果がある。ま
た、熱収縮チューブを装着した極板群を角形の金属電槽
に挿入する際に、極板群の先端部の極板の厚みをその他
の部分の厚みよりも薄くすることにより、極板群を電槽
に挿入する工程での不良の発生率が著しく減少する。こ
れらの効果は、合成樹脂フィルムのチューブが収縮する
作用に基づくものであり、通常の収縮しないチューブを
用いた場合に比較して好都合である。なお、収縮チュー
ブの厚みは、エネルギー密度の観点から0.1mm以下であ
ることが望ましい。In addition, the battery of the structure of the present invention can be manufactured by a method in which the electrode group is housed in a metal battery case coated with a synthetic resin on the inner surface, and after the electrode group is housed in a synthetic resin bag, It can also be manufactured by inserting it into a battery case. In particular, a method of using a so-called heat-shrinkable tube as a bag made of a synthetic resin is a method in which the electrode group is formed of a plurality of flat electrode plates, that is, the stacked electrodes are used when the battery has a rectangular shape. This has the effect of correcting the positional deviation between the plates and the effect of preventing breakage in handling the electrode plate group. Also, when inserting the electrode group with the heat-shrinkable tube into a square metal battery case, the thickness of the electrode plate at the tip of the electrode group is made thinner than the thickness of the other parts. The occurrence rate of defects in the step of inserting the battery into the battery case is significantly reduced. These effects are based on the action of shrinking the tube of the synthetic resin film, which is more advantageous than using a normal tube that does not shrink. The thickness of the shrink tube is desirably 0.1 mm or less from the viewpoint of energy density.
以上で説明した本発明の構造の例を第1図、第2図お
よび第3図に示す。FIGS. 1, 2 and 3 show examples of the structure of the present invention described above.
第1図は、内面を合成樹脂でコーティングした金属電
槽を用いた角形密閉電池の断面図であり、一方、第2図
および第3図は熱収縮チューブを装着した極板群を金属
電槽に収容することで製作した角形密閉電池の断面図で
ある。特に、第3図に示した構造の電池は、以下の理由
で組み立てが容易である。FIG. 1 is a cross-sectional view of a rectangular sealed battery using a metal battery case whose inner surface is coated with a synthetic resin, while FIGS. 2 and 3 show a metal battery case equipped with heat-shrinkable tubes. FIG. 4 is a cross-sectional view of a prismatic sealed battery manufactured by being housed in a battery. In particular, the battery having the structure shown in FIG. 3 is easy to assemble for the following reasons.
すなわち、角形電池の組立工程での問題点の1つは電
解液の注入方法であるが、第3図に示した構造の場合、
電池は金属電槽に可とう性を有する樹脂板、電解液、熱
収縮チューブを装着した極板群の順でこれらを収容する
ことで容易に製作できる。この際、樹脂板の大きさは、
金属電槽底面部の内寸よりも長さあるいは巾の一方がわ
ずかに大きいことが望ましい。この理由は、樹脂板の長
さ及び巾の寸法が電槽内底面の寸法よりも小さい場合に
は、電解液注入時に比重の差によって樹脂板が浮き上が
るためである。That is, one of the problems in the process of assembling the prismatic battery is the method of injecting the electrolytic solution. In the case of the structure shown in FIG.
A battery can be easily manufactured by housing a flexible resin plate, an electrolytic solution, and an electrode plate group equipped with a heat-shrinkable tube in a metal battery case in this order. At this time, the size of the resin plate is
It is desirable that one of the length or the width is slightly larger than the inner size of the bottom portion of the metal container. The reason for this is that when the length and width of the resin plate are smaller than the size of the inner bottom surface of the battery case, the resin plate rises due to a difference in specific gravity when the electrolyte is injected.
本発明において合成樹脂層を備える目的は、すでに述
べたように極板群と金属電槽との間で電解液を経由して
電流が流れるのを抑制することである。したがって、合
成樹脂層は、電解液を透過しないものであることが必要
である。また、合成樹脂フィルムの材質は、ポリオレフ
ィン系の樹脂,フッ素系の樹脂,ポリ塩化ビニル樹脂あ
るいはポリサルフォン系の樹脂などの耐酸化性および耐
アルカリ性を兼ね備えたものであることが望ましい。こ
の理由は、炭酸根の増加など合成樹脂フィルムの変質や
変形が電池の性能劣化の一因になるためである。The purpose of providing the synthetic resin layer in the present invention is to suppress the flow of current between the electrode group and the metal battery case via the electrolytic solution as described above. Therefore, the synthetic resin layer needs to be impermeable to the electrolytic solution. The material of the synthetic resin film is desirably a material having both oxidation resistance and alkali resistance, such as a polyolefin resin, a fluorine resin, a polyvinyl chloride resin or a polysulfone resin. The reason for this is that the deterioration or deformation of the synthetic resin film, such as an increase in the number of carbonates, contributes to the performance degradation of the battery.
なお、本発明に類似した電池構造は、すでに実公平1
−22223号公報で提案されている。しかし本発明は次の
点で明らかにこの提案とは異なるものである。すなわち
実公平1−22223号の提案における合成樹脂製の袋の使
用は、容量が異なる極板群すなわち積層方向の厚みが異
なるいくつかの極板群に対して共通の金属電槽を用いる
ことを目的としており、極板群と金属電槽との間に適当
な寸法の間隔板を挿入することを前提としている。この
理由はこの提案がコスト低減の点から蓄電要素の寸法に
関わらず電槽として一定の大きさのものを用いることを
可能とするために、蓄電要素が電槽内寸の大きさに比べ
て小さいほど多くの間隔板を必要とすることに起因す
る。つまり、合成樹脂製の袋を備えていない場合には間
隔板の数が多いほど蓄電要素の保持すべき電解液が間隔
板と他の間隔板との間の部分および間隔板と電槽との間
の部分へ多く滞留するために、蓄電要素は電解液が不足
した状態になりやすい。いいかえれば、この提案におけ
る合成樹脂製の袋の使用は間隔板を用いない場合には必
要でないといえる。Note that a battery structure similar to the present invention has already
No. -22223. However, the present invention clearly differs from this proposal in the following points. That is, the use of a bag made of synthetic resin in the proposal of Japanese Utility Model Publication No. 1-222223 requires the use of a common metal container for electrode groups having different capacities, that is, several electrode groups having different thicknesses in the stacking direction. The purpose is to insert a spacing plate of an appropriate size between the electrode plate group and the metal battery case. The reason for this is that this proposal makes it possible to use a battery container of a fixed size regardless of the size of the storage element in terms of cost reduction, so that the storage element is smaller than the inner size of the container. This is because smaller spacers require more spacing plates. In other words, when a bag made of synthetic resin is not provided, the larger the number of spacing plates, the more the electrolytic solution to be held by the electricity storage element is located between the spacing plate and the other spacing plate and between the spacing plate and the battery case. Since a large amount of stagnation occurs in the space between the two, the power storage element is likely to be in a state of lack of electrolyte. In other words, it can be said that the use of the synthetic resin bag in this proposal is not necessary unless a spacing plate is used.
これに対し本発明は、間隔板を用いないことを前提と
し、その目的とするところはカドミウム負極板の水素発
生に至る電位変化を検出して充電を制御する電池に特に
有効な構造を供給するものである。さらに本発明は、熱
収縮チューブの使用など製造工程の簡略化や不良発生率
の低下にも効果を有するものである。このように本発明
は、従来の提案とは異なるものである。On the other hand, the present invention is based on the premise that a spacing plate is not used, and the purpose is to provide a particularly effective structure for a battery which controls charging by detecting a potential change leading to hydrogen generation of a cadmium negative electrode plate. Things. Further, the present invention has an effect on simplification of a manufacturing process such as use of a heat-shrinkable tube and reduction of a defect occurrence rate. Thus, the present invention is different from the conventional proposal.
実施例 以下、本発明を好適な実施例を用いて説明する。Examples Hereinafter, the present invention will be described using preferred examples.
本発明の要旨は、カドミウム負極板の水素発生に至る
電位変化を検出して充電を制御する電池において、極板
群と金属電槽との間で電解液を経由して電流が流れるこ
とを抑制することによって金属電槽内面での水素発生を
抑制することである。これによって電池の充電終期の電
圧変化は、カドミウム負極板が本来有している水素発生
に至る電位の変化量に基づく大きいものになる。そこ
で、以下の実施例では極板群と金属電槽との間に合成樹
脂の層を備えた電池とそうでない電池との充電特性およ
びサイクル試験における寿命の比較を行った。また、本
発明の目的は、電池の充電終期での電圧変化を大きくす
ることである。そこで、カドミウム負極板の集電体とし
てニッケルおよび銅を用いた電池の性能の比較をも行な
った。The gist of the present invention is to suppress the flow of current through an electrolyte between an electrode group and a metal battery case in a battery that controls charging by detecting a potential change leading to hydrogen generation of a cadmium negative electrode plate. By doing so, the generation of hydrogen on the inner surface of the metal battery case is suppressed. As a result, the voltage change at the end of charging of the battery becomes large based on the amount of change in potential inherent in the cadmium negative electrode plate, which leads to hydrogen generation. Therefore, in the following examples, a comparison was made between the battery having a synthetic resin layer between the electrode group and the metal battery case and the battery having no such layer, and the life in a cycle test. Another object of the present invention is to increase the voltage change at the end of charging of a battery. Therefore, the performance of batteries using nickel and copper as the current collector of the cadmium negative electrode plate was also compared.
[実施例1] 酸化カドミウム粉末100重量部と金属カドミウム粉末3
0重量部と長さ1mmのポリプロピレン製の矩繊維0.1重量
部とを0.4重量部のヒドロキシエチルセルロースを含む
エチレングリコール45重量部で混合してペースト状にし
た。このペーストをニッケルめっきした穿孔鋼板に塗着
し次いで乾燥および加圧を行なって酸化カドミウムの理
論容量が400mAhおよび220mAhで寸法が各々0.68×15×53
(mm)および0.40×15×53(mm)である2種類のカドミ
ウム負極板を製作した。[Example 1] 100 parts by weight of cadmium oxide powder and metal cadmium powder 3
0 parts by weight and 0.1 part by weight of a polypropylene rectangular fiber having a length of 1 mm were mixed with 45 parts by weight of ethylene glycol containing 0.4 parts by weight of hydroxyethyl cellulose to form a paste. This paste is applied to a nickel-plated perforated steel sheet, and then dried and pressed to obtain a theoretical capacity of cadmium oxide of 400 mAh and 220 mAh and dimensions of 0.68 × 15 × 53, respectively.
(Mm) and 0.40 × 15 × 53 (mm), two kinds of cadmium negative electrode plates were produced.
一方、正極板は次の方法で製作した。 On the other hand, the positive electrode plate was manufactured by the following method.
多孔度が約80%の焼結式ニッケル基板にコバルトおよ
びカドミウムの含有率が各々8モル%および3.5モル%
である硝酸ニッケル、硝酸コバルトおよび硝酸カドミウ
ムからなる混合水溶液[pH=2、比重1.50(20℃)]を
含浸した後、比重1.20(20℃)の水酸化ナトリウム水溶
液に浸漬し、次いで、湯洗および乾燥を行なった。この
操作を繰り返して水酸化ニッケルの理論容量が350mAhで
寸法が0.92×15×53(mm)である水酸化ニッケル正極板
を製作した。A sintered nickel substrate with a porosity of about 80% contains 8 mol% and 3.5 mol% of cobalt and cadmium, respectively.
Impregnated with a mixed aqueous solution consisting of nickel nitrate, cobalt nitrate and cadmium nitrate [pH = 2, specific gravity 1.50 (20 ° C.)], immersed in a sodium hydroxide aqueous solution having a specific gravity 1.20 (20 ° C.), and then washed with hot water And drying. This operation was repeated to produce a nickel hydroxide positive electrode plate having a theoretical capacity of 350 mAh and dimensions of 0.92 × 15 × 53 (mm).
電池は次の方法で製作した。 The battery was manufactured by the following method.
正極板を厚みが0.17mmのポリサリフォン製の不織布セ
パレータで包んだ後、この正極板2枚の間に厚みが0.68
mmの負極板1枚をはさみ、さらにその両面を厚みが0.40
mmの負極板2枚ではさむことで負極板と正極板とがセパ
レータを介して交互に積層された構造の極板群を製作し
た。次にこの極板群を第3図に示したのと同様に上端お
よび下端が開口した筒状のポリ塩化ビニル製の熱収縮チ
ューブ(商品名:ヒシレックス、厚み:約30μm)で包
んだ後、加熱してチューブを収縮させた。さらにこの極
板群の正極板および負極板をニッケルめっきした鉄製の
蓋上に形成された各々の端子部に接続した。電池は上面
開口の角形の金属電槽の底面に厚みが100μmのポリ塩
化ビニル製の板を挿入した後電解液の注入と極板群の挿
入とを行ない、さらに金属電槽の上面開口部と蓋とをレ
ーザー溶接で接合することによって製作した。用いた電
解液は、体積比が85:15である比重1.33(20℃)水酸化
カリウム水溶液と比重1.25(20℃)水酸化ナトリウム水
溶液との混合水溶液1.4mlである。電池の外径寸法は4.8
×16.5×64(mm)であり、公称容量は650mAhである。ま
たこの電池は0.5kg/cm2の圧力差で作動する安全弁を備
えている。これを電池Aとする。After wrapping the positive electrode plate with a polysaliphone nonwoven fabric separator having a thickness of 0.17 mm, a thickness of 0.68
mm negative electrode plate, and both sides are 0.40 mm thick.
By sandwiching between two negative electrode plates having a thickness of 2 mm, an electrode plate group having a structure in which the negative electrode plates and the positive electrode plates were alternately laminated via a separator was manufactured. Next, after wrapping this electrode plate group in a tubular heat-shrinkable tube made of polyvinyl chloride (trade name: Hishilex, thickness: about 30 μm) having upper and lower ends opened in the same manner as shown in FIG. The tube was shrunk by heating. Further, the positive electrode plate and the negative electrode plate of this electrode plate group were connected to respective terminal portions formed on a nickel-plated iron lid. After inserting a 100-μm-thick polyvinyl chloride plate into the bottom of the square metal battery case with the top opening, the battery is injected with the electrolyte and the electrode plates are inserted. It was manufactured by joining the lid and the lid by laser welding. The electrolytic solution used was 1.4 ml of a mixed aqueous solution of a specific gravity 1.33 (20 ° C.) aqueous potassium hydroxide solution and a specific gravity 1.25 (20 ° C.) aqueous sodium hydroxide solution having a volume ratio of 85:15. Battery outer diameter is 4.8
× 16.5 × 64 (mm) with a nominal capacity of 650 mAh. The battery also has a safety valve that operates with a pressure difference of 0.5 kg / cm 2 . This is called battery A.
[実施例2] 実施例1の負極板におけるニッケルめっきした穿孔鋼
板の代わりに銅メッキした穿孔鋼板を用いた以外は全2
実施例1と同様にして公称容量が650mAhである密閉角形
ニッケル−カドミウム電池を製作した。これを電池Bと
する。[Example 2] Except that a nickel-plated perforated steel plate was used in place of the nickel-plated perforated steel plate in the negative electrode plate of Example 1, and that
A sealed rectangular nickel-cadmium battery having a nominal capacity of 650 mAh was manufactured in the same manner as in Example 1. This is called battery B.
[比較例1] 熱収縮チューブおよび電槽内底面における樹脂板を用
いないこと以外は、全て実施例1と同様にして公称容量
が650mAhである密閉角形ニッケル−カドミウム電池を製
作した。これを電池Cとする。Comparative Example 1 A sealed prismatic nickel-cadmium battery having a nominal capacity of 650 mAh was manufactured in the same manner as in Example 1 except that the heat-shrinkable tube and the resin plate on the inner bottom surface of the battery case were not used. This is called battery C.
なお、これらの電池の負極板は、リザーブ用の水酸化
カドミウムをほとんど有していない。つまり負極板中の
水酸化カドミウムの重量は、正・負極板中の水酸化ニッ
ケルの重量の約0.95倍[2.73(g/Ah)/2.88(g/Ah)]
である。したがって電池の充電終期の端子電圧は負極板
の水素発生に至る電位変化に基づき急激に増大する。The negative plates of these batteries have almost no cadmium hydroxide for reserve. In other words, the weight of cadmium hydroxide in the negative electrode plate is about 0.95 times the weight of nickel hydroxide in the positive and negative electrode plates [2.73 (g / Ah) /2.88 (g / Ah)]
It is. Therefore, the terminal voltage at the end of charging of the battery sharply increases based on a potential change leading to hydrogen generation on the negative electrode plate.
次に、製作した各電池の充電特性について説明する。 Next, the charging characteristics of each manufactured battery will be described.
電池A,BおよびCを20℃の雰囲気温度において化成充
放電を行なったのちに、40℃の雰囲気温度において5Cす
なわち3.25Aの電流で過充電領域までの充電を行なっ
た。5C充電の特性を第4図に示す。同図より本発明の電
池AおよびBは比較例の電池Cに比べて充電終期の電圧
変化が大きいことがわかる。この理由は、電池Aおよび
Bではカドミウム負極板の水素発生に至る電位変化が電
槽内面のニッケル面での水素発生による妨げの影響をほ
とんど受けていないためである。つまり、本発明の電池
AおよびBは、比較例の電池Cよりも広い電圧範囲で充
電を制御することが可能である。このことは、広い温度
範囲で温度補償のない充電が可能であることを示す。な
お、試験時の雰囲気温度を40℃に設定した理由は、ニッ
ケル−カドミウム電池の充電が通常0℃〜40℃の範囲で
行われることおよび雰囲気温度が高いほど主としてカド
ミウム負極板の水素発生に至る電位変化の量が減少する
ことによる。すなわち、電池の充電終期に達する電圧
は、雰囲気温度が最も高い40℃で最も低くなる。したが
って、例えば0℃〜40℃の範囲で、しかも温度補償がな
い方式で電池を充電する際の制御電圧は、電池が40℃の
充電で達することができる値に設定する必要がある。こ
のように、充電制御の条件は雰囲気温度が最も高い場合
の電池の充電特性を考慮して設定すべきである。After the batteries A, B and C were subjected to formation charge / discharge at an ambient temperature of 20 ° C., they were charged at a current of 5 C, that is, 3.25 A, at an ambient temperature of 40 ° C. to an overcharge region. Fig. 4 shows the characteristics of 5C charging. It can be seen from the figure that the batteries A and B of the present invention have a larger voltage change at the end of charging than the battery C of the comparative example. The reason for this is that in the batteries A and B, the potential change leading to hydrogen generation on the cadmium negative electrode plate is hardly affected by the generation of hydrogen on the nickel surface inside the battery case. That is, the batteries A and B of the present invention can control charging in a wider voltage range than the battery C of the comparative example. This indicates that charging without temperature compensation is possible over a wide temperature range. The reason why the ambient temperature during the test was set to 40 ° C. is that the charging of the nickel-cadmium battery is usually performed in the range of 0 ° C. to 40 ° C., and that the higher the ambient temperature, the higher the hydrogen generation of the cadmium negative electrode plate. This is because the amount of potential change is reduced. That is, the voltage that reaches the end of charging of the battery becomes lowest at the highest ambient temperature of 40 ° C. Therefore, for example, the control voltage when charging the battery in a range of 0 ° C. to 40 ° C. and without temperature compensation needs to be set to a value that the battery can reach by charging at 40 ° C. As described above, the charge control conditions should be set in consideration of the charge characteristics of the battery when the ambient temperature is the highest.
次に、電池のサイクル寿命について説明する。電池A,
BおよびCを20℃で化成充放電を行った後に次に示す条
件でサイクル試験を行なった。すなわち40℃において最
大5Cの電流で1.5〜2.0Vの定電圧充電を15分間行った後
に0.2Cの定電流で1Vまで放電するサイクルを繰り返し行
なった。サイクル寿命および1サイクル目の放電容量に
およぼす充電時の定電圧設定値の影響を第5図に示す。
なお、電池のサイクル寿命は、試験中の放電容量が1サ
イクル目の60%以下に低下した際に尽きたものとした。
同図より本発明の電池AおよびBは、比較例の電池Cに
比べて寿命が長く、特に電池Bは負極集電体の表面が銅
であることによって広い定電圧設定の範囲で長寿命であ
ることがわかる。Next, the cycle life of the battery will be described. Battery A,
After performing chemical conversion charge and discharge of B and C at 20 ° C., a cycle test was performed under the following conditions. That is, a cycle of performing a constant voltage charge of 1.5 to 2.0 V at a maximum current of 5 C at 40 ° C. for 15 minutes and then discharging the battery to 1 V at a constant current of 0.2 C was repeatedly performed. FIG. 5 shows the influence of the constant voltage set value during charging on the cycle life and the discharge capacity at the first cycle.
The cycle life of the battery was exhausted when the discharge capacity during the test was reduced to 60% or less in the first cycle.
As can be seen from the figure, the batteries A and B of the present invention have a longer life than the battery C of the comparative example. In particular, the battery B has a long life in a wide constant voltage setting range because the surface of the negative electrode current collector is copper. You can see that there is.
一方、放電容量におよぼす定電圧設定値の影響につい
てみると、放電容量は定電圧設定値が1.65V以上である
場合に安定して多いことがわかる。定電圧設定値が1.65
Vよりも低い条件で充電した場合に放電容量が少ない理
由は、充電過程の電池電圧で充電電流が制御されること
による充電不足である。On the other hand, looking at the effect of the constant voltage set value on the discharge capacity, it can be seen that the discharge capacity is stably large when the constant voltage set value is 1.65 V or more. Constant voltage setting value is 1.65
The reason why the discharge capacity is small when charged under a condition lower than V is insufficient charging due to control of the charging current by the battery voltage in the charging process.
なお、比較例の電池Cの放電容量が他の電池よりも多
い理由は、電槽内面から水素が発生することによって定
電圧充電領域で流れる電流値が大きいことに起因すると
考えられる。また、図から各々の電池を充電するに適し
た定電圧設定の範囲を求めると、本発明による電池Aで
は1.65V以上1.85V以下の範囲が、一方本発明の電池Bで
は1.65V以上2.0以上の範囲が適していると考えられる。
これに対し、比較例の電池Cでは安定した放電容量およ
びサイクル寿命を得るに適した定電圧設定値の範囲が認
められない。このように本発明の電池は、広い定電圧設
定値の範囲で長寿命である。It is considered that the reason why the discharge capacity of the battery C of the comparative example is larger than that of the other batteries is that the current value flowing in the constant voltage charging region due to the generation of hydrogen from the inner surface of the battery case is large. In addition, when the range of the constant voltage setting suitable for charging each battery is determined from the figure, the range of 1.65 V to 1.85 V for the battery A according to the present invention, while the range of 1.65 V to 2.0 for the battery B of the present invention. Range is considered suitable.
On the other hand, in the battery C of the comparative example, a constant voltage set value range suitable for obtaining a stable discharge capacity and cycle life is not recognized. As described above, the battery of the present invention has a long life in a wide range of constant voltage setting values.
なお、本発明の実施例では、最も簡易でしかも実用性
の高い方法としてポリ塩化ビニル製の熱収縮チューブを
用いた電池について説明したが、これ以外にもフッ素樹
脂製の熱収縮チューブを用いた場合にも同様の効果が得
られた。本発明の要旨は、極板群と金属電槽との間で電
解液を経由して電流が流れるのを防げることである。し
たがって本発明の効果は、内面を合成樹脂でコートした
金属電槽を用いることや合成樹脂製の袋に極板群を収容
することによっても得ることができる。In the examples of the present invention, a battery using a heat-shrinkable tube made of polyvinyl chloride was described as the simplest and most practical method. In this case, the same effect was obtained. The gist of the present invention is to prevent a current from flowing between the electrode group and the metal battery case via the electrolytic solution. Therefore, the effects of the present invention can also be obtained by using a metal battery case whose inner surface is coated with a synthetic resin, or by storing the electrode plate group in a synthetic resin bag.
発明の効果 以上述べたように、本発明はリザーブ用の水酸化カド
ミウムをほとんど有せず負極板の水素発生に至る電位変
化を充電電圧の変化として検出して充電を制御する電池
において、金属電槽を備えた場合における電池のサイク
ル寿命を向上させる効果を有する。また、本発明は電池
の製造工程の簡略化や不良発生率の低下にも効果を有す
る。Effect of the Invention As described above, the present invention relates to a battery that has little cadmium hydroxide for reserve and detects a potential change leading to hydrogen generation on the negative electrode plate as a change in charging voltage, and controls charging by using a metal battery. This has the effect of improving the cycle life of the battery when the tank is provided. The present invention is also effective in simplifying the battery manufacturing process and reducing the rate of occurrence of defects.
第1図、第2図および第3図は本発明の実施例に係る電
池の断面図である。第4図は本発明の電池および比較例
の電池の充電電圧特性を比較した図である。第5図は本
発明の電池および比較例の電池のサイクル寿命と放電容
量とにおよぼす充電時の定電圧設定値の影響を示した図
である。 2……合成樹脂コーティング 3……熱収縮チューブ 4……合成樹脂板,5……カドミウム負極板1, 2 and 3 are sectional views of a battery according to an embodiment of the present invention. FIG. 4 is a diagram comparing the charging voltage characteristics of the battery of the present invention and the battery of the comparative example. FIG. 5 is a diagram showing the influence of a constant voltage set value during charging on the cycle life and discharge capacity of the battery of the present invention and the battery of the comparative example. 2 ... Synthetic resin coating 3 ... Heat shrink tube 4 ... Synthetic resin plate, 5 ... Cadmium negative electrode plate
Claims (1)
と負極端子を兼ねる金属電槽とを備え、しかも負極板中
の水酸化カドミウムの重量が正極板中の水酸化ニッケル
のの重量の0.95倍以下であり、さらに、金属電槽と極板
群との間に極板群の側面および底面を覆う合成樹脂槽を
有することを特徴とする密閉形ニッケル−カドミウム電
池。A cadmium negative electrode plate, a nickel hydroxide positive electrode plate, and a metal container serving also as a negative electrode terminal, wherein the weight of cadmium hydroxide in the negative electrode plate is 0.95 times the weight of nickel hydroxide in the positive electrode plate. The sealed nickel-cadmium battery according to claim 1, further comprising a synthetic resin tank that covers a side surface and a bottom surface of the electrode group between the metal battery case and the electrode group.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2054214A JP2990725B2 (en) | 1990-03-06 | 1990-03-06 | Sealed nickel-cadmium battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2054214A JP2990725B2 (en) | 1990-03-06 | 1990-03-06 | Sealed nickel-cadmium battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03257765A JPH03257765A (en) | 1991-11-18 |
| JP2990725B2 true JP2990725B2 (en) | 1999-12-13 |
Family
ID=12964299
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2054214A Expired - Lifetime JP2990725B2 (en) | 1990-03-06 | 1990-03-06 | Sealed nickel-cadmium battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2990725B2 (en) |
-
1990
- 1990-03-06 JP JP2054214A patent/JP2990725B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03257765A (en) | 1991-11-18 |
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