Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS5910544B2 - sealed storage battery - Google Patents
[go: Go Back, main page]

JPS5910544B2 - sealed storage battery - Google Patents

sealed storage battery

Info

Publication number
JPS5910544B2
JPS5910544B2 JP52133063A JP13306377A JPS5910544B2 JP S5910544 B2 JPS5910544 B2 JP S5910544B2 JP 52133063 A JP52133063 A JP 52133063A JP 13306377 A JP13306377 A JP 13306377A JP S5910544 B2 JPS5910544 B2 JP S5910544B2
Authority
JP
Japan
Prior art keywords
anode
electrode
battery
auxiliary electrode
terminal
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
JP52133063A
Other languages
Japanese (ja)
Other versions
JPS5466426A (en
Inventor
保 城上
三司 上野
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.)
Toshiba Corp
Original Assignee
Tokyo Shibaura Electric 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 Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP52133063A priority Critical patent/JPS5910544B2/en
Publication of JPS5466426A publication Critical patent/JPS5466426A/en
Publication of JPS5910544B2 publication Critical patent/JPS5910544B2/en
Expired legal-status Critical Current

Links

Classifications

    • 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

  • Secondary Cells (AREA)

Description

【発明の詳細な説明】 本発明は密閉型蓄電池に係り、特に水素ガス吸収用の補
助極および酸化剤電極を備えた密閉型蓄電池に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sealed storage battery, and more particularly to a sealed storage battery equipped with an auxiliary electrode for absorbing hydrogen gas and an oxidizer electrode.

従来密閉型蓄電池、特にニッケル−亜鉛蓄電池ニッケル
−カドミウム蓄電池等は、充放電時や、自己放電時に水
素ガスを発生し、また過充電時に多量の酸素ガスを発生
し、電池内圧力の上昇、容器の膨張、電解液の漏れ等に
よる障害など種々の問題があつた。
Conventional sealed storage batteries, especially nickel-zinc storage batteries and nickel-cadmium storage batteries, generate hydrogen gas during charging and discharging and self-discharge, and also generate a large amount of oxygen gas during overcharging, causing an increase in internal pressure and damage to the container. There were various problems such as expansion of the battery, failure due to leakage of electrolyte, etc.

蓄電池の充電、過充電および放電時の挙動をニッケル亜
鉛電池を例にとり説明する。電極容量は、陰極(Zn極
)が陽極(NiO0H)の約2倍あるのが普通である。
z1極の電極電位は水素発生電位よりも卑であるため、
Zn極から自発的に水素が発生することはさけられない
。充電時にはその電位がさらに卑となるため水素発生速
度がさらに大きくなり、蓄積する水素量は大きくなる。
陽極が充電量80%程度に達すると酸素ガスが発生し、
さらに充電を続けて過充電状態になると、この酸素ガス
発生量は急激に増大する。この酸素は通常陰極によつて
Zn+Ko2→ZnOの反応で化学的に吸収されるので
、酸素はやがて吸収されつくのてなくなる。Zn極では
、過充電時に再生するZnが上記反応で消費されるので
、容量バランスがくじれることはない。一方水素は何者
によつても吸収されないので、これを吸収し電池内在を
低くする手段が必要となるのである。さらに過充電時に
発生する酸素ガスは、電池容量の低下、アンドライト生
成の原因となり、サイクル寿命の低下等、電池性能を低
下させるものであつた。そこで電池性能を向上させるた
めには、充放電時や自己放電時の水素ガス発生による電
池内圧力上昇を抑制する事、酸素ガス発生以前あるいは
酸素ガス発生や同時に過充電を検出する事が必要であつ
た。
The behavior of storage batteries during charging, overcharging, and discharging will be explained using a nickel-zinc battery as an example. Generally, the electrode capacity of the cathode (Zn electrode) is about twice that of the anode (NiO0H).
Since the electrode potential of the z1 electrode is less noble than the hydrogen generation potential,
Spontaneous generation of hydrogen from the Zn electrode cannot be avoided. During charging, the potential becomes even more base, so the rate of hydrogen generation becomes even greater, and the amount of hydrogen accumulated becomes larger.
When the anode reaches about 80% charge, oxygen gas is generated,
If the battery continues to be charged and becomes overcharged, the amount of oxygen gas generated increases rapidly. This oxygen is usually chemically absorbed by the cathode through the reaction of Zn+Ko2→ZnO, so that the oxygen is eventually absorbed and used up. In the Zn electrode, the Zn regenerated during overcharging is consumed in the above reaction, so the capacity balance is not disturbed. On the other hand, since hydrogen cannot be absorbed by anything, a means is needed to absorb it and lower the battery content. Furthermore, oxygen gas generated during overcharging causes a decrease in battery capacity and the formation of andrite, which deteriorates battery performance such as a decrease in cycle life. Therefore, in order to improve battery performance, it is necessary to suppress the pressure increase inside the battery due to hydrogen gas generation during charging and discharging and self-discharge, and to detect overcharging before or at the same time as oxygen gas generation. It was hot.

そこで密閉型蓄電池では水素ガス蓄積による障害を防止
するために電池内において水素ガスを吸収する方法が検
討されており、例えば以下の如き手段によつて電池内の
水素ガスを吸収することが試みられている。
Therefore, in order to prevent problems caused by hydrogen gas accumulation in sealed storage batteries, methods of absorbing hydrogen gas within the battery are being considered.For example, attempts have been made to absorb hydrogen gas within the battery using the following methods. ing.

(1)気相触媒を用いて水素ガスと酸素ガスを2■1の
割合いで化学的に結合させて水に戻す方法(2)水素ガ
スだけを化学的に吸収する方法 (3)金属水素化物とする方法 (4)補助極を用いて電気化学的に水に戻す方法しかし
ながら(1)の場合には、その消費速度が遅い上に触媒
が電解液や生成水に濡れやすく、吸収能力を急速に喪失
しやすい。
(1) Method of chemically combining hydrogen gas and oxygen gas at a ratio of 2 x 1 using a gas phase catalyst and returning it to water (2) Method of chemically absorbing only hydrogen gas (3) Metal hydride (4) Method of electrochemically returning water using an auxiliary electrode However, in the case of (1), the consumption rate is slow and the catalyst easily gets wet with the electrolyte and produced water, resulting in a rapid loss of absorption capacity. easy to lose.

その上、酸素ガス量が化学量論組成より少ない場合には
、水素ガスは完全に消費されず、徐々に電池内に蓄積す
る。(2)(3)の場合には吸収剤を収納する空間が限
られる為に、充填量が制限される。又、水素吸収が進む
につれて、吸収量は徐々に飽和し、吸収速度がしだいに
減少する。その上、吸収量、吸収速度は温度に蓄しく影
響される。また、(4)の場合、過充電もしくは転極な
どにより陽極容量をなくし、水素ガスを大量に発生した
際水素ガス吸収能力を喪失するという問題点があつた。
密閉型蓄電池においては過充電時に多量の酸素ガスを発
生し、電池内圧力の上昇、容器の膨張、電解液の漏れに
よる障害など種々の問題があつた。
Moreover, when the amount of oxygen gas is less than the stoichiometric composition, hydrogen gas is not completely consumed and gradually accumulates in the cell. In the cases of (2) and (3), the amount of filling is limited because the space for storing the absorbent is limited. Furthermore, as hydrogen absorption progresses, the amount absorbed gradually becomes saturated and the absorption rate gradually decreases. Moreover, the amount and rate of absorption are strongly influenced by temperature. Furthermore, in the case of (4), there was a problem that the anode capacity was lost due to overcharging or polarity reversal, and the hydrogen gas absorption ability was lost when a large amount of hydrogen gas was generated.
Sealed storage batteries generate a large amount of oxygen gas when overcharged, causing various problems such as an increase in the internal pressure of the battery, expansion of the container, and failures due to electrolyte leakage.

従来、このような障害を取り除くために、充電が完了し
、過充電を検出する方法として以下の如き方法が知られ
ている。(1)電池電圧検出方法、(2)通電量を記憶
させるクーロメータ一方法、(3)電池温度上昇や触媒
温度上昇による検出方法、(4)電解液比重変化による
検出方法等が知られている。
Conventionally, in order to eliminate such a problem, the following method is known as a method for detecting overcharging after charging is completed. Known methods include (1) a battery voltage detection method, (2) a coulometer method that memorizes the amount of energization, (3) a detection method based on a rise in battery temperature or catalyst temperature, and (4) a detection method based on a change in electrolyte specific gravity. .

しかし前記方法においては、いずれも検出誤差が大きく
、実用上満足できるものではなかつた。例えば蓄電池の
充電末期の端子電圧を検出し、過充電を検知する電池電
圧検出方法では電池内部抵抗の変化、充電中の発熱によ
る温度変化等のにより端子電圧を一定に保持し難いため
過充電の検出が困難であつた。このように従来、多数回
の充放電サイクルに対し安定した水素ガス吸収が得られ
かつ、過充電を正確に検出することのできる密閉型蓄電
池は見当らなかつた。本発明は上記の点に鑑み水素ガス
を効率よく吸収し、多数回の充放電サイクルに対し、電
池内圧の上昇、電池缶の膨張、電解液漏れなどを生じる
ことなく、かつ、環境温度、充電々流などの影響を受け
ずに過充電を正確に検出することのできる密閉型著電池
を提供することを目的とする。
However, all of the above methods had large detection errors and were not practically satisfactory. For example, in a battery voltage detection method that detects overcharging by detecting the terminal voltage of a storage battery at the end of charging, it is difficult to maintain a constant terminal voltage due to changes in battery internal resistance, temperature changes due to heat generation during charging, etc. It was difficult to detect. As described above, conventionally, there has been no sealed storage battery that can obtain stable hydrogen gas absorption over many charge/discharge cycles and can accurately detect overcharging. In view of the above points, the present invention efficiently absorbs hydrogen gas, and can withstand many charge/discharge cycles without causing an increase in battery internal pressure, expansion of the battery can, or leakage of electrolyte, and is designed to absorb hydrogen gas efficiently without causing any increase in battery internal pressure, expansion of the battery can, or electrolyte leakage. An object of the present invention is to provide a sealed battery that can accurately detect overcharging without being affected by currents or the like.

本発明は陰極と、陽極と、前記陰極および陽極間に介在
させたセパレータと、防水処理を施した水素ガス吸収用
の補助極と、前記補助極に非線形抵抗体および固定抵抗
体を介して接続された陽極活物質からなる酸化剤電極と
、前記陰極、陽極、セパレータ、補助極および酸化剤電
極を密閉内装する容器と、前記陽極に接続し容器外に導
出された陽極端子と、前記陰極に接続し容器外に導出さ
れた陰極端子と、前記酸化剤電極に接続され充電時には
陽極端子と電気的に導通となり、また放電時には陽極端
子と不導通になる容器外に導出された酸化剤電極端子と
前記補助極に接続され前記容器外に導出され補助極端子
を具備した密閉型蓄電池である。上記密閉型蓄電池の補
助極端子と酸化剤電極端子間の電圧変化を検出すること
により過充電を検出する密閉型蓄電池の過充電検出方法
である。なお上記において非線形抵抗体とは、逆電流を
阻市するダイオードのようなものを用い固定抵抗は酸化
剤電極端子一補助極端子間の電圧検出が容易であり、か
つ補助極に充分な水素ガス吸収電流の流れる範囲の抵抗
値、例えば10〜2000Ω程度とすることが好ましい
The present invention includes a cathode, an anode, a separator interposed between the cathode and the anode, a waterproofed auxiliary electrode for absorbing hydrogen gas, and a connection to the auxiliary electrode via a nonlinear resistor and a fixed resistor. an oxidizing agent electrode made of a positive electrode active material; a container in which the cathode, anode, separator, auxiliary electrode, and oxidizing agent electrode are sealed; an anode terminal connected to the anode and led out of the container; A cathode terminal that is connected and led out of the container, and an oxidizer electrode terminal that is connected to the oxidizer electrode and is electrically conductive with the anode terminal during charging, and is not electrically conductive with the anode terminal during discharge. The battery is a sealed storage battery having an auxiliary electrode terminal connected to the auxiliary electrode and led out of the container. This is a method for detecting overcharge of a sealed storage battery, in which overcharging is detected by detecting a voltage change between an auxiliary electrode terminal and an oxidizer electrode terminal of the sealed storage battery. In the above, the nonlinear resistor is something like a diode that blocks reverse current, and the fixed resistor is one that makes it easy to detect the voltage between the oxidizer electrode terminal and the auxiliary electrode terminal, and that there is enough hydrogen gas in the auxiliary electrode. It is preferable to set the resistance value within the range through which the absorption current flows, for example, about 10 to 2000 Ω.

さらに小形汎用電池として用いられる単一、単二、単三
タイプでは100〜500Ωの固定抵抗体を用いること
が実用上好ましい。また前記陽極端子、陰極端子は、そ
れぞれ蓋体、容器などと兼用することもできる。
Furthermore, it is practically preferable to use a fixed resistor of 100 to 500 Ω for single, double AA, and AA types used as small general-purpose batteries. Further, the anode terminal and the cathode terminal can also be used as a lid, a container, etc., respectively.

つまり上記の如き本発明に係る密閉型蓄電池においては
放電時は、陽極端子と酸化剤電極を電気的に不導通とす
ることにより、陽極の電池容量がなくなつた場合にも酸
化剤電極の容量は保持され、水素ガス吸収は中断される
ことはない。
In other words, in the sealed storage battery according to the present invention as described above, by making the anode terminal and the oxidizer electrode electrically non-conductive during discharging, even if the battery capacity of the anode is exhausted, the capacity of the oxidizer electrode is is retained and hydrogen gas absorption is not interrupted.

また、過充電において陰極から、あるいは過放電により
転極した陽極からそれぞれ水素ガスが発生した場合酸化
剤電極の容量喪失、電極電位降下を防止できるので水素
ガスを連続して吸収できるというものである。これに対
し酸化剤電極を有しないものにおいては陽極と補助極を
非線形抵抗体を介して接続した際、湯極容量がなくなつ
た場合、過充電もしくは転極などにより発生した水素ガ
スを吸収することはできなかつた。また充電時において
は陽極端子と酸化剤電極端子とを電気的に導通状態とす
ることにより、陽極と同時に酸化剤補助極が充電され水
素ガス吸収、自己放電により生じた酸化剤電極の容量減
少を回復し、新たに水素ガス吸収が可能になるというも
のである。このような酸化剤電極が容量をもつ限り、陽
極と酸化剤電極との導通、不導通にかかわらず水素ガス
吸収が行われるというものである。
In addition, when hydrogen gas is generated from the cathode during overcharging or from the anode reversed due to overdischarge, it is possible to prevent loss of capacity of the oxidizer electrode and drop in electrode potential, allowing continuous absorption of hydrogen gas. . On the other hand, in those without an oxidizer electrode, when the anode and auxiliary electrode are connected through a nonlinear resistor, if the hot water electrode capacity is exhausted, hydrogen gas generated due to overcharging or polarity reversal is absorbed. I couldn't do that. Furthermore, during charging, by making the anode terminal and the oxidizer electrode terminal electrically conductive, the oxidizer auxiliary electrode is charged at the same time as the anode, thereby reducing the capacity of the oxidizer electrode caused by hydrogen gas absorption and self-discharge. It will recover and become able to absorb hydrogen gas again. As long as such an oxidant electrode has a capacity, hydrogen gas absorption will occur regardless of whether or not there is electrical continuity between the anode and the oxidant electrode.

例えばニツケル化合物を陽極とした場合は次の如く反応
する。又、非線形抵抗体としてダイオード及び固定抵抗
体を酸化剤電極と補助極との間に介在させることにより
、補助極電位は酸化剤電極電位に対して、約0.6卑な
電位域に保たれ、水素ガスは効率的にイオン化される。
For example, when a nickel compound is used as an anode, the reaction occurs as follows. Furthermore, by interposing a diode and a fixed resistor as nonlinear resistors between the oxidizer electrode and the auxiliary electrode, the auxiliary electrode potential is maintained in a potential range approximately 0.6 base lower than the oxidizer electrode potential. , hydrogen gas is efficiently ionized.

そして補助極電位が酸素ガス発生電位に移行することを
防止して、補助極性能の劣化を防止する。又、充電時及
び過充電時の酸化剤電極端子と、水素ガス吸収補助極端
子との間の電圧を測定することにより充電末期の酸素ガ
ス発生が確認され、これにより、充電末期の検出が可能
である。
This prevents the auxiliary electrode potential from shifting to the oxygen gas generation potential, thereby preventing deterioration of the auxiliary electrode performance. Additionally, by measuring the voltage between the oxidizer electrode terminal and the hydrogen gas absorption auxiliary electrode terminal during charging and overcharging, the generation of oxygen gas at the end of charging can be confirmed, which makes it possible to detect the end of charging. It is.

つまり、充電時にガス吸収補助極は酸化剤電極電位に対
し卑方向に分極されており、充放電、自己放電により発
生した水素ガスは電気化学的に酸化され水素吸収電流H
2+20H→2H20+2eが流れる。しかし過充電時
には酸素ガス発生によりガス吸収補助極上の触媒が化学
的に酸化され、そのためにそこまで行なわれていた水素
ガス吸収反応が停止してしまうために水素圧は上昇しは
じめることになる。触媒の酸化によりガス吸収補助極の
電位は上昇し、陽極とガス吸収補助極間の電圧は急激に
減少する。なお充電を中断すると酸素ガスは陰極により
殆んど吸収され、ガス吸収補助極の電位は急激に回復す
る。従つて酸化剤電極とガス吸収補助極間の電圧を測定
する事により過充電時の酸素ガス発生に対する急激な電
圧降下が検知され、これにより、充電末期の検出が可能
となる。
In other words, during charging, the gas absorption auxiliary electrode is polarized in the base direction with respect to the oxidizer electrode potential, and the hydrogen gas generated by charging and discharging and self-discharge is electrochemically oxidized and the hydrogen absorption current H
2+20H→2H20+2e flows. However, during overcharging, the catalyst on the gas absorption auxiliary electrode is chemically oxidized due to the generation of oxygen gas, and the hydrogen gas absorption reaction that has been taking place thus far is stopped, and the hydrogen pressure begins to rise. Due to the oxidation of the catalyst, the potential of the gas absorption auxiliary electrode increases, and the voltage between the anode and the gas absorption auxiliary electrode rapidly decreases. Note that when charging is interrupted, most of the oxygen gas is absorbed by the cathode, and the potential of the gas absorption auxiliary electrode rapidly recovers. Therefore, by measuring the voltage between the oxidizer electrode and the gas absorption auxiliary electrode, a sudden voltage drop due to the generation of oxygen gas during overcharging can be detected, thereby making it possible to detect the end of charging.

次に本発明に係る密閉型蓄電池の実施例としてニツケル
一亜鉛蓄電池を挙げ、その構成例を断面的に示す第1図
に用いて、本発明を詳細に説明する。
Next, a nickel-zinc storage battery will be cited as an example of the sealed storage battery according to the invention, and the invention will be described in detail with reference to FIG.

,上記密閉型蓄電池は、例え
ば次の如く構成されている。
, the above-mentioned sealed storage battery is configured as follows, for example.

この発電部はニツケル化合物を主成分とする焼結型の陽
極1と、亜鉛化合物を主成分とする陰極2とがセパレー
タ(電解液保持層を兼ねる)3を介して積層されており
、これを渦巻状に巻回し構成されている。この発電部は
例えば一端開口の陰極端子を兼ねる金属容器7に電気的
絶縁を有する熱収縮性チユーブ9を介して収納されてい
る。陽極リード4は陽極端子を兼ねる蓋体6と、また陰
極リード5は陰極端子を兼ねる金属容器7とそれぞれ接
続されている。なお陽極端子6を兼ねる蓋体は陰極端子
を兼ねる金属容器7の開口部に電気的な絶縁材8を介し
て封止装着されている。また酸化剤電極11および防水
処理を施した水素ガス吸収用の補助極10はセパレータ
3を介して空芯部に設けられ、非線形抵抗体12として
のシリコンダイオード及び固定抵抗体13は水素ガス吸
収用の補助極10と酸化剤電極11に直列に接続されて
いる。なお酸化剤電極リード14は陽極端子兼用蓋体6
に耐電解液性の絶縁性樹脂層を介して設けられた酸化剤
電極端子15に接続されている。又、補助極リード16
は、陽極端子兼用蓋体6に耐電解液性の絶縁性樹脂層を
介して設けられた補助極端子17に接続されている。な
お単1型のニツケル一亜鉛蓄電池の場合はガス吸収補助
極10として見かけ表面積5cr11厚さQ.3llI
tの多孔質ニツケル焼結体を用い、水素ガス吸収触媒と
して白金を含侵させ、防水処理のためにポリテトラフル
オロエチレンを結着させたものを用いた。また酸化剤電
極11としては、ニツケル陽極と同一組成の焼結型ニツ
ケル極で厚さ0.7m1見掛けの表面積4C!It(2
傭×2儂)のものを使用した。又、非線形抵抗体12と
してのシリコンダイオード固定抵抗体13、酸化剤電極
リード14及び補助極リード16はそれぞれ、電気的絶
縁性で、耐電解液性の樹脂例えば、エポキシ樹脂などで
被覆されている。第2図は、上記のニツケル一亜鉛蓄電
池において充電電流300mA15時間て1。
In this power generation section, a sintered anode 1 mainly composed of a nickel compound and a cathode 2 mainly composed of a zinc compound are laminated with a separator 3 (also serving as an electrolyte holding layer) interposed therebetween. It has a spiral structure. This power generation section is housed, for example, in a metal container 7, which is open at one end and also serves as a cathode terminal, via a heat-shrinkable tube 9 having electrical insulation. The anode lead 4 is connected to a lid 6 which also serves as an anode terminal, and the cathode lead 5 is connected to a metal container 7 which also serves as a cathode terminal. The lid, which also serves as the anode terminal 6, is sealed and attached to the opening of the metal container 7, which also serves as the cathode terminal, via an electrical insulating material 8. In addition, an oxidizer electrode 11 and a waterproof auxiliary electrode 10 for absorbing hydrogen gas are provided in the air core through a separator 3, and a silicon diode as a nonlinear resistor 12 and a fixed resistor 13 are for absorbing hydrogen gas. The auxiliary electrode 10 and the oxidizer electrode 11 are connected in series. Note that the oxidizer electrode lead 14 is connected to the lid 6 which also serves as an anode terminal.
It is connected to an oxidizer electrode terminal 15 provided through an electrolyte-resistant insulating resin layer. In addition, the auxiliary pole lead 16
is connected to an auxiliary electrode terminal 17 provided on the lid body 6 which also serves as an anode terminal via an electrolyte-resistant insulating resin layer. In the case of a single-type nickel-zinc storage battery, the gas absorption auxiliary electrode 10 has an apparent surface area of 5cr11 and a thickness of Q. 3llI
A porous nickel sintered body of T was used, impregnated with platinum as a hydrogen gas absorption catalyst, and bound with polytetrafluoroethylene for waterproofing. The oxidizer electrode 11 is a sintered nickel electrode with the same composition as the nickel anode, with a thickness of 0.7 m and an apparent surface area of 4 C! It(2
I used one from Recruit x 2. Further, the silicon diode fixed resistor 13 as the nonlinear resistor 12, the oxidizing agent electrode lead 14, and the auxiliary electrode lead 16 are each coated with an electrically insulating and electrolyte-resistant resin, such as an epoxy resin. . Figure 2 shows the charging current of 300 mA for 15 hours in the above-mentioned nickel-zinc storage battery.

5Ah〕、放電電流600mA,1V放電停止の充放電
を各々2時間のインターバルを置いて測定したもので、
充放電サイクルに伴なう電池内(開路)の圧力を実線で
示してある。
5Ah], a discharge current of 600mA, and a discharge stop of 1V were measured at intervals of 2 hours.
The solid line indicates the pressure inside the battery (open circuit) during charge/discharge cycles.

なお、充電時には酸化剤電極端子15と陽極端子6とは
、電気的に導通とし、また、放電時及び開路時には不導
通とした。本実施例では、固定抵抗体13として、10
0Ωの抵抗体を使用した。さらに、本発明の効果を明ら
かにする為に、酸化剤電極端子15と陽極端子6とを電
気的に不導通としたままで、上記と同様な条件で、充放
電を行つた場合の電池内の圧力を破線で示す。第2図よ
り明らかな如く、本発明の電池内水素ガス吸収効果は、
酸化剤電極端子15と陽極端子6とを電気的に不導通と
したままで、充放電を行つた場合に比べて、多数回充放
電を繰り返した場合に(本実施例では100サイクル以
後)、その効果は著しい。
Note that the oxidizer electrode terminal 15 and the anode terminal 6 were electrically conductive during charging, and were non-conductive during discharging and opening. In this embodiment, as the fixed resistor 13, 10
A 0Ω resistor was used. Furthermore, in order to clarify the effects of the present invention, the inside of the battery when charging and discharging was performed under the same conditions as above while keeping the oxidizer electrode terminal 15 and the anode terminal 6 electrically non-conducting. The pressure at is shown by the dashed line. As is clear from FIG. 2, the hydrogen gas absorption effect in the battery of the present invention is as follows:
When charging and discharging are repeated many times (after 100 cycles in this example), compared to the case where charging and discharging are performed while the oxidizer electrode terminal 15 and the anode terminal 6 are electrically disconnected, The effect is remarkable.

即ち、本発明は、充電の度ごとに酸化剤電極の充電がな
され酸化剤電極が容量を回復するので、水素ガス吸収は
効率的に行われる。
That is, in the present invention, the oxidizer electrode is charged every time it is charged and the oxidizer electrode recovers its capacity, so that hydrogen gas absorption is efficiently performed.

一方、酸化剤電極端子15と陽極端子6とを電気的に不
導通したままで充放電を繰り返した場合、水素ガス吸収
と自己放電により徐々に酸化剤電極容量を減少し、容量
を喪失した時点で、水素ガス吸収は停止し、水素ガスは
徐々に電池内に蓄積する。
On the other hand, if charging and discharging are repeated with the oxidizer electrode terminal 15 and the anode terminal 6 electrically disconnected, the oxidizer electrode capacity gradually decreases due to hydrogen gas absorption and self-discharge, and the point at which the capacity is lost is reached. At this point, hydrogen gas absorption stops and hydrogen gas gradually accumulates inside the battery.

本実施例では、100サイクル以後酸化剤電極容量喪失
に伴う、水素ガス吸収能力の停止が顕著に示されている
。次に、過放電もしくは転極時に水素ガスが電池内に7
気圧蓄積した時点で、開路にし、電池内圧力を測定した
結果を第3図に示す。
In this example, it is clearly shown that the hydrogen gas absorption ability stops after 100 cycles due to loss of oxidant electrode capacity. Next, hydrogen gas enters the battery during overdischarge or polarity reversal.
When the atmospheric pressure had accumulated, the circuit was opened and the internal pressure of the battery was measured. The results are shown in Figure 3.

実線は、本発明に係る密閉型亜鉛アルカリ2次電池を用
いた場合を示し、破線は、充放電サイクルの間、酸化剤
電極端子15と陽極端子6とを電気的に導通したままの
場合の結果である。
The solid line shows the case where the sealed zinc-alkaline secondary battery according to the present invention is used, and the broken line shows the case where the oxidizer electrode terminal 15 and the anode terminal 6 remain electrically connected during the charge/discharge cycle. This is the result.

本発明では、酸化剤電極は陽極と電気的に独立している
ので、陽極が過放電もしくは転極しても、酸化剤電極が
過放電もしくは転極することはない。
In the present invention, since the oxidizing agent electrode is electrically independent from the anode, even if the anode is over-discharged or polarized, the oxidizing agent electrode will not be over-discharged or polarized.

即ち、酸化剤電極容量は保持されるので、発生した水素
ガス(,ま連続して吸収される。これに対して、酸化剤
電極端子15と陽極端子6とを電気的に導通にしたまま
過放電もしくは転極した場合、陽極と共に酸化剤電極も
過放電もしくは転極する為に、陽極容量喪失時に酸化剤
電極容量も喪失してその電極電位は降下する。この為に
、水素ガスは有効に吸収されなくなる。即ち、本発明は
、充電のたびごとに酸化剤電極端子15と、陽極端子6
とを、電気的に導通することによつて酸化剤電極を充電
することが出来るので、酸化剤電極の容量喪失に伴う、
水素ガス吸収の停止は生じない。
That is, since the oxidizer electrode capacity is maintained, the generated hydrogen gas (,) is continuously absorbed. When discharged or polarized, the oxidizer electrode is also over-discharged or reversed along with the anode, so when the anode capacity is lost, the oxidizer electrode capacity is also lost and its electrode potential drops.For this reason, hydrogen gas is effectively That is, the present invention allows the oxidant electrode terminal 15 and the anode terminal 6 to be connected each time charging is performed.
Since the oxidizer electrode can be charged by electrically conducting the
No cessation of hydrogen gas absorption occurs.

さらに、放電時開路時に酸化剤電極端子15と、陽極端
子6とを電気的に不導通にすることによつて、酸化剤電
極の過放電乃至は転極は生じないので発生した水素ガス
は連続して吸収される。以上のように、水素ガスを吸収
するのに水素吸収補助極と酸化剤電極を具備し、補助極
と非線形抵抗及び固定抵抗体とを介して電気的に接続し
、さらに、陽極と酸化剤電極とを充電時にのみ電気的に
導通とし(短絡し)、放電時、開路時には、電気的に不
導通になるように意図した本発明は、充放電、自己放電
の間に水素ガスを発生する蓄電池全般に適用できるもの
である。
Furthermore, by making the oxidizing agent electrode terminal 15 and the anode terminal 6 electrically non-conductive when the circuit is opened during discharge, overdischarge or polarity reversal of the oxidizing agent electrode does not occur, so that the generated hydrogen gas continues. and is absorbed. As described above, in order to absorb hydrogen gas, a hydrogen absorption auxiliary electrode and an oxidizing agent electrode are provided, the auxiliary electrode is electrically connected to the nonlinear resistor and the fixed resistor, and furthermore, the anode and the oxidizing agent electrode are provided. The present invention is intended to be electrically conductive (short-circuited) only when charging, and electrically non-conductive when discharging or opening. It is generally applicable.

なお上記実施例においては、充放電時における酸化剤電
極と陽極との導通、不導通をスイツチによつて行つたが
、所要の効果を得るものであれば適宜構成を変えられる
ことは言うまでもない。また、他の蓄電池への本発明の
適用に際しては、蓄電池の陽極と酸化剤電極の組成は同
一にすることが望ましい。
In the above embodiment, conduction and disconnection between the oxidizer electrode and the anode during charging and discharging was performed using a switch, but it goes without saying that the configuration can be changed as appropriate if the desired effect is obtained. Furthermore, when applying the present invention to other storage batteries, it is desirable that the anode and oxidizer electrode of the storage battery have the same composition.

例えば鉛蓄電池の場合には二酸化鉛の酸化剤電極を、酸
化銀一亜鉛蓄電池では、酸化銀の酸化剤電極を使用する
。このように酸化剤電極組成を陽極組成と同一にするこ
とによつて、充電時にいずれかの電極からのガス発生を
防止して、両極を同様な充電状態にすることが出来る。
For example, in the case of a lead-acid battery, a lead dioxide oxidizer electrode is used, and in the case of a silver-zinc oxide battery, a silver oxide oxidizer electrode is used. By making the oxidizer electrode composition the same as the anode composition in this manner, gas generation from either electrode can be prevented during charging, and both electrodes can be brought into a similar charged state.

次に、過充電時に発生する酸素ガスを検出することを特
徴とした過充電検出方法について実施例により説明する
Next, an overcharge detection method characterized by detecting oxygen gas generated during overcharge will be described using examples.

まず第4図は300mAで充電を行つた時の充電時間に
対する陽極一陰極間電圧El2(第4図一a)酸化剤電
極一補助極間電圧E,3(第4図−b)および電池内圧
力(第4図−c)の変化を示す。
First, Figure 4 shows the anode-to-cathode voltage El2 (Figure 4-1a), the oxidizer electrode-auxiliary electrode voltage E,3 (Figure 4-b), and the battery internal voltage with respect to the charging time when charging at 300 mA. The change in pressure (Fig. 4-c) is shown.

第4図−aにおいてA1〜A2は充電時のE,2変化を
示し、この間水素ガスは発生しているが、ガス吸収補助
極の良好な水素ガス吸収により、第4図一C(7)C1
〜C2に示す如く電池内圧力の変化はほとんど見られな
かつた。またA2〜A3の電圧上昇は過充電の進行を示
す。A3に至つて充電々流の大部分は酸素ガス発生に使
用されこの時陽極からの酸素ガス発生は急増し第4図−
CO)C3に示さす如く電池内圧力が急激に上昇する。
またEl3を示す第4図−bではB2から急激な電圧降
下が見られる。これは酸素ガス発生と同時にガス吸収補
助極の電位が貴方向に分極するからである。なおり4に
おいては酸素ガスが陰極により殆んど吸収されEl3は
再び急激に回復する。第5図は環境温度を変化させた場
合の充電時間に対するE,2およびEl3を示す。
In Fig. 4-a, A1 to A2 show changes in E,2 during charging, and during this time hydrogen gas is generated, but due to the good hydrogen gas absorption of the gas absorption auxiliary electrode, Fig. 4-C (7) C1
As shown in C2, almost no change in the internal pressure of the battery was observed. Further, the voltage increase of A2 to A3 indicates the progress of overcharging. At A3, most of the charging current is used for oxygen gas generation, and at this time, oxygen gas generation from the anode rapidly increases, as shown in Figure 4-
As shown in CO)C3, the pressure inside the battery rises rapidly.
Further, in FIG. 4-b showing El3, a rapid voltage drop is seen from B2. This is because the potential of the gas absorption auxiliary electrode is polarized in the noble direction at the same time as oxygen gas is generated. In Naori 4, most of the oxygen gas is absorbed by the cathode, and El3 rapidly recovers again. FIG. 5 shows E, 2 and El3 with respect to charging time when the environmental temperature is changed.

その結果過充電時のEl2の変化率は環境温度により著
しく影響を受け高温になる程変化(電圧上昇)が小さく
なり過充電の検出が困難となる。しかしE,3の変化率
は環境温度の変化により影響される事なく、過充電時に
おいては急激な変化(電圧降下)を示し、過充電の検出
を正確に行える。第6図は充電々流を変化させた際の、
また第7図は充放電サイクル数を変化させた際の充電時
間に対するEl2およびE,3を示す。
As a result, the rate of change in El2 during overcharging is significantly affected by the environmental temperature, and the higher the temperature is, the smaller the change (voltage rise) becomes, making it difficult to detect overcharge. However, the rate of change of E,3 is not affected by changes in environmental temperature and shows a rapid change (voltage drop) during overcharging, allowing accurate detection of overcharging. Figure 6 shows when the charging current is changed,
Further, FIG. 7 shows El2 and E,3 with respect to charging time when the number of charging/discharging cycles is changed.

その結果El2は充電々流や充放電サイクル数の変化に
よる電池容最低下、内部抵抗増加等により著しい影響を
受け、過充電の検出が困難となる。これに対しEl3は
過充電時に急激な変化(電圧降下)を示し、確実に過充
電を検出する事ができる。以上の如く陽極一陰極端子間
電圧E,2の変化は環境温度、充電々流、充放電サイク
ル数等の影響を受け、過充電の検出が困難であつた。
As a result, El2 is significantly affected by the lowest battery capacity due to changes in charge current and number of charge/discharge cycles, increase in internal resistance, etc., making it difficult to detect overcharge. On the other hand, El3 shows a sudden change (voltage drop) during overcharging, and overcharging can be reliably detected. As described above, the change in the voltage E,2 between the anode and cathode terminals is affected by the environmental temperature, charging current, number of charging/discharging cycles, etc., and it has been difficult to detect overcharging.

これに対し本発明により設けた第3電極である補助極端
子と酸化剤電極間との電圧を測定することにより、上記
諸条件の影響を受ける事なく過充電を容易に検出する事
ができる。次に第1図の如き密閉型蓄電池を用い過充電
を防ぎ充放電をくり返した場合の電池容量変化(第8図
曲線a)と、300mA5時間充電、600mA放電、
放電停止1,1サイクルごとに2時間の間隔を置いた定
電流定時間の充放電をくり返した場合の電池容量(第8
図曲線b)との比較を第8図に示す。
On the other hand, by measuring the voltage between the auxiliary electrode terminal, which is the third electrode provided according to the present invention, and the oxidizer electrode, overcharging can be easily detected without being affected by the above conditions. Next, the change in battery capacity when a sealed storage battery as shown in Fig. 1 is repeatedly charged and discharged to prevent overcharging (curve a in Fig. 8), charging at 300 mA for 5 hours, discharging at 600 mA,
Battery capacity when constant current constant time charging and discharging are repeated with 2 hour intervals between each cycle of discharge stop (8th
A comparison with curve b) is shown in FIG.

つまり本発明に係る密閉型蓄電池を用た場合、従来の定
電流定時間の場合に比べ電池容量の劣化も少なく、サイ
クル寿命も著しく改良された。以上の如く本発明に係る
密閉型蓄電池を用いることにより水素ガスを効率よく吸
収し、多数回の充放電サイクルに対し、電池内圧の上昇
、電池缶の膨張、電解液漏れなどを生じることなく、か
つ環境温度、充電々流などの影響を受けずに過充電を正
確に検出することのできるというものである。
In other words, when the sealed storage battery according to the present invention was used, there was less deterioration in battery capacity and the cycle life was significantly improved compared to the conventional constant current constant time battery. As described above, by using the sealed storage battery according to the present invention, hydrogen gas can be efficiently absorbed, and even after many charge/discharge cycles, there will be no increase in internal pressure of the battery, expansion of the battery can, leakage of electrolyte, etc. Moreover, overcharging can be accurately detected without being affected by environmental temperature, charging current, etc.

なお本発明に用いる充電回路としては例えば第9図の如
き概略図で示されるものが用いられる。即ち陽極端子6
および陰極端子を兼ねる金属容器7間には電圧記録計1
8および充電々源19が、また陽極端子6および補助極
端子7間には電圧記録計20が接続されている。さらに
陽極端子6および酸化剤電極端子15間にはスイツチ2
1が設けられておりこのスイツチ21は充電時において
導通とし、放電時には不導通とする。この結果、酸化剤
電極端子15および補助極端子7間の充電時における電
圧変化は電圧計録計20により測定される。ただし第9
図は充電回路の一例を示すものであり、所要の機能を有
するものであれば本発明に用いることができることは言
うまでもない。
As the charging circuit used in the present invention, for example, one shown in a schematic diagram as shown in FIG. 9 is used. That is, anode terminal 6
and a voltage recorder 1 between the metal container 7 which also serves as a cathode terminal.
8 and a charging source 19, and a voltage recorder 20 is connected between the anode terminal 6 and the auxiliary electrode terminal 7. Furthermore, a switch 2 is connected between the anode terminal 6 and the oxidizer electrode terminal 15.
1 is provided, and this switch 21 is made conductive during charging and non-conductive during discharging. As a result, the voltage change between the oxidizer electrode terminal 15 and the auxiliary electrode terminal 7 during charging is measured by the voltmeter 20. However, the 9th
The figure shows an example of a charging circuit, and it goes without saying that any circuit having the required functions can be used in the present invention.

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

第1図および第9図は本発明に係る密閉型蓄電池および
その過充電検出装置の構成例を示す説明図、第2図乃至
第8図は本発明に係る実施例の諸特性を示す曲線図。 なお図中において、1・・・・・・陽極、2・・・・・
・陰極、3・・・・・・セパレータ、ト・・・・・陽極
端子(蓋体を兼用)7・・・・・・容器(陰極端子を兼
用)、10・・・・・・補助極、11・・・・・・酸化
剤電極、12・・・・・・非線形抵抗体、13・・・・
・・固定抵抗体、15・・・・・・酸化剤電極端子、1
7・・・・・・補助極端子。
1 and 9 are explanatory diagrams showing configuration examples of a sealed storage battery and its overcharge detection device according to the present invention, and FIGS. 2 to 8 are curve diagrams showing various characteristics of the embodiment according to the present invention. . In the figure, 1... Anode, 2...
・Cathode, 3... Separator, G... Anode terminal (also serves as lid) 7... Container (also serves as cathode terminal), 10... Auxiliary electrode , 11... Oxidizer electrode, 12... Nonlinear resistor, 13...
... Fixed resistor, 15 ... Oxidizer electrode terminal, 1
7...Auxiliary pole terminal.

Claims (1)

【特許請求の範囲】[Claims] 1 陰極と、陽極と、前記陰極および陽極間に介在させ
たセパレータと防水処理を施した水素ガス吸収用の補助
極と、前記補助極に非線形抵抗体および固定抵抗体を介
して接続された前記陽極を構成する陽極活物質からなる
酸化剤電極と、前記陰極、陽極、セパレータ、補助極お
よび酸化剤電極を密閉内装する容器と、前記陰極に接続
し容器外に導出された陰極端子と、前記陽極に接続し容
器外に導出された陽極端子と、前記酸化剤電極に接続し
て、充電時は陽極端子と電気的に導通とし、放電時は陽
極端子と不導通とする前記容器外に導出された酸化剤電
極端子と、前記補助極に接続され前記容器外に導出され
た補助極端子とを具備したことを特徴とした密閉型蓄電
池。
1 a cathode, an anode, a separator interposed between the cathode and the anode, a waterproofed auxiliary electrode for absorbing hydrogen gas, and the auxiliary electrode connected to the auxiliary electrode via a nonlinear resistor and a fixed resistor. an oxidizing agent electrode made of an anode active material constituting an anode; a container in which the cathode, anode, separator, auxiliary electrode, and oxidizing agent electrode are hermetically sealed; a cathode terminal connected to the cathode and led out of the container; An anode terminal connected to the anode and led out of the container, and an anode terminal connected to the oxidizing agent electrode to be electrically conductive with the anode terminal during charging and non-conductive with the anode terminal during discharge. What is claimed is: 1. A sealed storage battery comprising: an oxidizing agent electrode terminal; and an auxiliary electrode terminal connected to the auxiliary electrode and led out of the container.
JP52133063A 1977-11-08 1977-11-08 sealed storage battery Expired JPS5910544B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52133063A JPS5910544B2 (en) 1977-11-08 1977-11-08 sealed storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52133063A JPS5910544B2 (en) 1977-11-08 1977-11-08 sealed storage battery

Publications (2)

Publication Number Publication Date
JPS5466426A JPS5466426A (en) 1979-05-29
JPS5910544B2 true JPS5910544B2 (en) 1984-03-09

Family

ID=15095955

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52133063A Expired JPS5910544B2 (en) 1977-11-08 1977-11-08 sealed storage battery

Country Status (1)

Country Link
JP (1) JPS5910544B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS566463B2 (en) * 1973-10-02 1981-02-12

Also Published As

Publication number Publication date
JPS5466426A (en) 1979-05-29

Similar Documents

Publication Publication Date Title
JP3019326B2 (en) Lithium secondary battery
US6377030B1 (en) Method of charging secondary battery by varying current or voltage at an inflection point in a storage region before full charge and device therefor
US4143212A (en) Sealed storage battery
CA2157930C (en) Sealed rechargeable battery
JPH1167284A (en) Battery with corrosion protection insulation case
JP2004273139A (en) Lithium secondary battery
CA1232634A (en) Battery cell
US3485673A (en) Nickel-zinc battery system having an aqueous electrolyte consisting of potassium hydroxide and potassium carbonate
US4444854A (en) Electrochemical cell having internal short inhibitor
JP2000353502A (en) Non-aqueous electrolyte secondary battery
JP2001283926A (en) Lithium secondary battery with safety mechanism
JPS6255274B2 (en)
US3257238A (en) Hermetically sealed cell
Berndt et al. Batteries, 1. General
JP2000150000A (en) How to manage backup power
JPS60220574A (en) Chargeable electrochemical apparatus
US3528855A (en) Hermetically sealed battery and method of making
JPS5910544B2 (en) sealed storage battery
JPH11121040A (en) Lithium secondary battery
Barsukov Battery selection, safety, and monitoring in mobile applications
JP2001357895A (en) Non-aqueous electrolyte secondary battery
JP3198774B2 (en) Lithium secondary battery
JPS6046516B2 (en) Overcharge detection method for sealed storage batteries
JP4040264B2 (en) Electrode body evaluation method
JPH1050293A (en) Electrochemical equipment