JPH0555980B2 - - Google Patents

Info

Publication number
JPH0555980B2
JPH0555980B2 JP61305747A JP30574786A JPH0555980B2 JP H0555980 B2 JPH0555980 B2 JP H0555980B2 JP 61305747 A JP61305747 A JP 61305747A JP 30574786 A JP30574786 A JP 30574786A JP H0555980 B2 JPH0555980 B2 JP H0555980B2
Authority
JP
Japan
Prior art keywords
negative electrode
battery
internal pressure
layer
paste
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
Application number
JP61305747A
Other languages
Japanese (ja)
Other versions
JPS63158747A (en
Inventor
Masako Kusaka
Yoshimasa Inaba
Hideo Kaiya
Minoru Yamaga
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP61305747A priority Critical patent/JPS63158747A/en
Publication of JPS63158747A publication Critical patent/JPS63158747A/en
Publication of JPH0555980B2 publication Critical patent/JPH0555980B2/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
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/246Cadmium electrodes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • 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】 産業上の利用分野 本発明は、密閉型アルカリ蓄電池に用いられる
ペースト式カドミウム負極に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a paste-type cadmium negative electrode used in a sealed alkaline storage battery.

従来の技術 一般に、密閉型アルカリ蓄電池では、過充電時
に水の電気分解によるガス発生が起こり、電池内
圧が上昇するのを防ぐため、(1)正極から発生する
酸素ガスは負極の充電生成物である金属カドミウ
ムに吸収させる、(2)負極に充填する活物質の電気
化学的容量を、正極に充填する活物質の電気化学
的容量より多くすることにより、負極からの水素
ガスの発生を防ぐという方法がとられている。し
かし、これらの方法を用いても過充電時の内圧レ
ベルが高いため、さらに電池内圧の上昇を防ぐこ
とのできる特性を持つた負極が必要となつてき
た。
Conventional technology In general, in sealed alkaline storage batteries, in order to prevent the internal pressure from increasing due to gas generation due to water electrolysis during overcharging, (1) the oxygen gas generated from the positive electrode is replaced by the charging product of the negative electrode. (2) By making the electrochemical capacity of the active material filled in the negative electrode larger than the electrochemical capacity of the active material filled in the positive electrode, hydrogen gas generation from the negative electrode is prevented. A method is being taken. However, even when these methods are used, the internal pressure level during overcharging is high, so there is a need for a negative electrode that has characteristics that can further prevent the internal pressure of the battery from increasing.

発明が解決しようとする問題点 このような問題を解決するために、特開昭60−
81765号公報に見られるように、電極表面に炭素
粉末層を形成することが提案されているが、この
ような負極では、酸素ガス吸収性を高めることは
できるが、充電を受け入れることができる水酸化
カドミウムが極板中に残つていない場合の水素ガ
スによる内圧上昇をおさえることができなかつ
た。
Problems to be solved by the invention In order to solve these problems, the invention
As seen in Publication No. 81765, it has been proposed to form a carbon powder layer on the electrode surface, but such negative electrodes can increase oxygen gas absorption, but do not have water that can accept charge. It was not possible to suppress the increase in internal pressure due to hydrogen gas when no cadmium oxide remained in the electrode plate.

本発明は、以上のような従来の欠点を解消し、
過酷な充電条件でも水素ガスによる内圧上昇が極
めて少ないペースト式カドミウム負極を提供する
ことを目的とする。
The present invention solves the above-mentioned conventional drawbacks,
The purpose of the present invention is to provide a paste-type cadmium negative electrode that exhibits extremely little increase in internal pressure due to hydrogen gas even under severe charging conditions.

問題点を解決するための手段 上記の問題解決のため、本発明のペースト式カ
ドミウム負極は、電極表面に触媒を担持させた担
体粉末と結着剤とから成る層を形成し、次いでこ
の層の表面に弗素樹脂多孔膜を形成したものであ
る。
Means for Solving the Problems In order to solve the above problems, the paste-type cadmium negative electrode of the present invention forms a layer consisting of a carrier powder supporting a catalyst and a binder on the electrode surface, and then A porous fluororesin membrane is formed on the surface.

作 用 このようなペースト式カドミウム負極は、電極
表面に触媒を担持させた担体粉末と結着剤から成
る層を形成し、さらにこの層の表面に弗素樹脂の
多孔膜を形成したものである。、過充電時に発生
する水素ガスを電気化学的に吸収することが可能
となり、水素ガスにより内圧上昇を防ぐことがで
きる。
Function This type of paste-type cadmium negative electrode has a layer made of a binder and a carrier powder supporting a catalyst formed on the electrode surface, and a porous film of fluororesin is further formed on the surface of this layer. , it becomes possible to electrochemically absorb hydrogen gas generated during overcharging, and hydrogen gas can prevent internal pressure from increasing.

実施例 以下実施例により、本発明を詳述する。Example The present invention will be explained in detail with reference to Examples below.

平均粒径約1μの酸化カドミウム粉末に、ポリ
ビニルアルコールのエチレングリコール溶液を加
え、混練してペースト状にする。このペーストを
導電性支持体である厚さ0.1mmのニツケルメツキ
した開孔鋼板に塗着し、約140℃で30分間乾燥し、
厚さ約0.5mmの電極を得た。
A solution of polyvinyl alcohol in ethylene glycol is added to cadmium oxide powder with an average particle size of approximately 1μ, and the mixture is kneaded to form a paste. This paste was applied to a conductive support, a nickel-plated perforated steel plate with a thickness of 0.1 mm, and dried at approximately 140°C for 30 minutes.
An electrode with a thickness of about 0.5 mm was obtained.

また、塩化パラジウムを塩酸で溶解した溶液に
人造黒鉛粉末を加え、混練してパラジウムを黒鉛
に吸着させる。ここに、水酸化ナトリウム水溶液
およびホルマリンを加え、吸着されたパラジウム
を還元した後、水洗、乾燥し、約1重量パーセン
トパラジウムを吸着した黒鉛粉末を得た。
Furthermore, artificial graphite powder is added to a solution of palladium chloride dissolved in hydrochloric acid, and the mixture is kneaded to cause palladium to be adsorbed onto the graphite. An aqueous sodium hydroxide solution and formalin were added thereto to reduce the adsorbed palladium, followed by washing with water and drying to obtain graphite powder adsorbing about 1% by weight of palladium.

純水にこの黒鉛粉末を重量比で30%、ポリビニ
ルアルコールを重量比5%分散させた溶液に、前
記電極を約10秒間浸漬した後、80℃で乾燥させ、
電極表面に層を形成させた。次にこの電極をアル
カリ溶液中で理論容量の約40%充電し、水洗、乾
燥し、さらに弗素樹脂の多孔膜を形成するため、
例えば3重量%濃度の弗素樹脂デイスパージヨン
液に浸漬し、乾燥してペースト式カドミウム負極
を得た。この負極をaとする。
The electrode was immersed for about 10 seconds in a solution in which 30% by weight of this graphite powder and 5% by weight of polyvinyl alcohol were dispersed in pure water, and then dried at 80°C.
A layer was formed on the electrode surface. Next, this electrode was charged to about 40% of its theoretical capacity in an alkaline solution, washed with water, and dried to form a porous fluororesin membrane.
For example, it was immersed in a 3% by weight fluororesin dispersion liquid and dried to obtain a paste-type cadmium negative electrode. Let this negative electrode be a.

一方、上記の方法により表面に層を形成させな
い他は同様の構成による比較例のカドミウム負極
を用意した。これをbとする。
On the other hand, a cadmium negative electrode of a comparative example having the same structure except that no layer was formed on the surface by the above method was prepared. Let this be b.

さらに、パラジウムを吸着させていない人造黒
鉛粉末を重量比で30%、ポリビニルアルコールを
重量比で5%とした溶液を用い、同様に表面に層
を形成させた比較例のカドミウム負極Cを得た。
Furthermore, using a solution containing 30% by weight of artificial graphite powder without adsorbing palladium and 5% by weight of polyvinyl alcohol, a comparative example of cadmium negative electrode C was obtained in which a layer was similarly formed on the surface. .

上記、3種類のカドミウム負極を、焼結式ニツ
ケル正極と組み合せて、密閉形蓄電池を試作し、
過充電時の内圧試験および電池保存後の充電時の
内圧試験を行つた。過充電時の内圧試験は、次の
条件で行つた。電池を20℃で0.1C相当の電流で15
時間充電し、20℃で2時間放置した後、0℃で
1.5C相当の電流で2時間充電し、0℃で1.5C相当
の電流で放電した。この時、0℃での充電開始時
間を0とし、電池内圧の経時変化を測定した。ま
た、電子保存後の充電時の内圧試験は、次のよう
に行つた。電池を20℃で0.1C相当の電流で10時間
充電し、45℃で1ケ月間放置した後、20℃で0.2C
相当の電流で2時間充電し、20℃で0.2C相当の電
流で放電した。この時、0.2Cでの充電開始時間を
0とし、電池内圧の経時変化を測定した。
A sealed storage battery was prototyped by combining the three types of cadmium negative electrodes mentioned above with a sintered nickel positive electrode.
Internal pressure tests were conducted during overcharging and during charging after battery storage. The internal pressure test during overcharging was conducted under the following conditions. 15 at a current equivalent to 0.1C at 20℃
After charging for 2 hours and leaving at 20℃ for 2 hours, at 0℃
The battery was charged for 2 hours at a current equivalent to 1.5C and discharged at a current equivalent to 1.5C at 0°C. At this time, the charging start time at 0° C. was set as 0, and the change in battery internal pressure over time was measured. Furthermore, an internal pressure test during charging after electronic storage was conducted as follows. Charge the battery at 20℃ for 10 hours with a current equivalent to 0.1C, leave it at 45℃ for one month, and then charge the battery at 20℃ with a current equivalent to 0.2C.
The battery was charged for 2 hours at an equivalent current and discharged at a current equivalent to 0.2C at 20°C. At this time, the charging start time at 0.2C was set as 0, and the change in battery internal pressure over time was measured.

第1図は、過充電時の内圧試験における電池内
圧と時間との関係を示す。aは本発明の負極を用
いた電池、b,cは比較のための負極を用いた電
池を示す。また放電後の平衡圧hは、電池内の水
素残存圧を示す。この結果から明らかなように、
電極表面に黒鉛粉末を含む層が形成された負極a
およびcを用いた電池a,cは、電極表面に特に
層を形成されていない負極bを用いた電池に比べ
て内圧が大幅に減少している。これは、電極表面
に導電性を持つ層が形成されたことにより、表面
付近にガス吸収に関与する金属カドミウムが生成
されやすくなつたためであると考えられる。ま
た、パラジウムを吸着させた黒鉛粉末を表面層に
用いた負極aによる電池aは、放電後の水素残存
圧が0となつている。これは触媒の作用により、
発生した水素ガスが電気化学的に吸収されるため
と考えられる。さらに、電池aにおける内圧カー
ブをパラジウムを吸着させていない黒鉛粉末を用
いた負極cによる電池における内圧カーブと比較
すると、ほぼ同じ形をしているから、触媒の作用
は、おもに水素ガス吸収に及んでいるものと考え
られる。
FIG. 1 shows the relationship between battery internal pressure and time in an internal pressure test during overcharging. A shows a battery using the negative electrode of the present invention, and b and c show batteries using negative electrodes for comparison. Further, the equilibrium pressure h after discharge indicates the residual hydrogen pressure within the battery. As is clear from this result,
Negative electrode a with a layer containing graphite powder formed on the electrode surface
Batteries a and c using negative electrodes a and c have a significantly reduced internal pressure compared to a battery using negative electrode b in which no layer is particularly formed on the electrode surface. This is thought to be because the formation of a conductive layer on the electrode surface facilitated the generation of metal cadmium, which is involved in gas absorption, near the surface. Further, in battery a using negative electrode a in which graphite powder on which palladium is adsorbed is used for the surface layer, the hydrogen residual pressure after discharge is zero. This is due to the action of a catalyst.
This is thought to be because the generated hydrogen gas is absorbed electrochemically. Furthermore, when comparing the internal pressure curve of battery a with the internal pressure curve of battery using negative electrode c using graphite powder that does not adsorb palladium, they have almost the same shape, so the action of the catalyst mainly affects hydrogen gas absorption. It is thought that it is being carried out.

第2図は、電池保存後の充電時の内圧試験にお
ける電池内圧と時間の関係を示す。図から明らか
なように、この試験においても過充電時の内圧試
験における結果と同様の結果が得られた。過充電
を行なうことにより負極中の水酸化カドミウムが
金属カドミウムに変化し、充電を受け入れること
ができる水酸化カドミウムがなくなつた場合、さ
らに充電を続けると水素ガスが発生する。また、
電池保存により、充電を受け入れ易いγ型水酸化
カドミウムが充電を受け入れにくいβ型水酸化カ
ドミウムに変化するため、充電を行うと水素ガス
が発生する。本実施例では、いずれの場合でも水
素ガスを電気化学的に吸収することができる。そ
して、層の表面に弗素樹脂の多孔膜を形成してい
るので、水素ガス導入のための気相は容易にしか
も確実に保たれ、触媒への水素ガス到達が促進さ
れて触媒による水素ガス消失をより円滑に行え
る。
FIG. 2 shows the relationship between battery internal pressure and time in an internal pressure test during charging after battery storage. As is clear from the figure, results similar to those obtained in the internal pressure test during overcharging were obtained in this test as well. By overcharging, the cadmium hydroxide in the negative electrode changes to metallic cadmium, and when there is no longer any cadmium hydroxide that can accept charging, hydrogen gas is generated if charging is continued. Also,
When a battery is stored, γ-type cadmium hydroxide, which easily accepts charge, changes to β-type cadmium hydroxide, which does not easily accept charge, so hydrogen gas is generated when the battery is charged. In this embodiment, hydrogen gas can be electrochemically absorbed in any case. Since a porous film of fluororesin is formed on the surface of the layer, the gas phase for introducing hydrogen gas is easily and reliably maintained, promoting hydrogen gas to reach the catalyst, and eliminating hydrogen gas by the catalyst. can be carried out more smoothly.

なお、実施例では触媒をパラジウムとしたが、
白金を用いても同様の効果が得られる。層の厚み
については、技術的に0.5μ以下にするのは困難で
あり、また20μ以上の厚い層になると、実際の充
放電が不可能となるので、層の厚みとしては0.5
〜20μが適当であるといえる。また、実施例では
結着剤としてポリビニルアルコールを用いたが、
メチルセルロースなどのような他の水溶性結着
剤、あるいはフツ素樹脂などのような非水溶性の
結着剤を用いても同様の効果が得られる。
In addition, although palladium was used as the catalyst in the examples,
A similar effect can be obtained by using platinum. Regarding the layer thickness, it is technically difficult to reduce it to 0.5μ or less, and if the layer becomes thicker than 20μ, actual charging and discharging becomes impossible, so the layer thickness should be 0.5μ or less.
It can be said that ~20μ is appropriate. In addition, although polyvinyl alcohol was used as a binder in the examples,
Similar effects can be obtained by using other water-soluble binders such as methylcellulose or water-insoluble binders such as fluororesin.

発明の効果 以上のように、本発明によれば過酷な充電条件
下でも、アルカリ蓄電池の内部圧力の上昇をおさ
えることができる。
Effects of the Invention As described above, according to the present invention, an increase in internal pressure of an alkaline storage battery can be suppressed even under severe charging conditions.

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

第1図および第2図は本発明における負極を用
いたニツケル−カドミウム蓄電池の内圧の経時変
化を示す図である。
FIGS. 1 and 2 are diagrams showing changes over time in the internal pressure of a nickel-cadmium storage battery using the negative electrode of the present invention.

Claims (1)

【特許請求の範囲】 1 電極表面に触媒を担持させた担体粉末と結着
剤とから成る層を形成し、さらにこの層の表面に
弗素樹脂の多孔膜を形成したことを特徴とするペ
ースト式カドミウム負極。 2 触媒が、パラジウムまたは白金である特許請
求の範囲第1項記載のペースト式カドミウム負
極。 3 担体粉末が炭素粉末である特許請求の範囲第
1項又は第2項記載のペースト式カドミウム負
極。 4 層の厚みが0.5〜20μである特許請求の範囲第
1項記載のペースト式カドミウム負極。
[Claims] 1. A paste type, characterized in that a layer consisting of a carrier powder supporting a catalyst and a binder is formed on the surface of an electrode, and a porous film of fluororesin is further formed on the surface of this layer. Cadmium negative electrode. 2. The paste-type cadmium negative electrode according to claim 1, wherein the catalyst is palladium or platinum. 3. The paste-type cadmium negative electrode according to claim 1 or 2, wherein the carrier powder is carbon powder. 4. The paste-type cadmium negative electrode according to claim 1, wherein the layer has a thickness of 0.5 to 20μ.
JP61305747A 1986-12-22 1986-12-22 Paste type cadmium negative electrode Granted JPS63158747A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61305747A JPS63158747A (en) 1986-12-22 1986-12-22 Paste type cadmium negative electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61305747A JPS63158747A (en) 1986-12-22 1986-12-22 Paste type cadmium negative electrode

Publications (2)

Publication Number Publication Date
JPS63158747A JPS63158747A (en) 1988-07-01
JPH0555980B2 true JPH0555980B2 (en) 1993-08-18

Family

ID=17948854

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61305747A Granted JPS63158747A (en) 1986-12-22 1986-12-22 Paste type cadmium negative electrode

Country Status (1)

Country Link
JP (1) JPS63158747A (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2452064C3 (en) * 1974-11-02 1981-06-19 Varta Batterie Ag, 3000 Hannover Gas-tight sealed alkaline accumulator
JPS6081765A (en) * 1983-10-12 1985-05-09 Sanyo Electric Co Ltd Manufacturing method for paste type cadmium negative electrode plate
JPS60100382A (en) * 1983-11-07 1985-06-04 Matsushita Electric Ind Co Ltd Sealed nickel-hydrogen storage battery
JPS61208755A (en) * 1985-03-13 1986-09-17 Sanyo Electric Co Ltd Pasted negative cadmium plate for sealed alkaline storage battery

Also Published As

Publication number Publication date
JPS63158747A (en) 1988-07-01

Similar Documents

Publication Publication Date Title
JP2000251896A (en) Lead storage battery and method of manufacturing the same
CN101662024A (en) Cathode active substance and preparation method thereof, cathode and battery
JPH0624148B2 (en) Sealed nickel cadmium storage battery
JP3788484B2 (en) Nickel electrode for alkaline storage battery
JPS61163569A (en) Metal oxide-hydrogen secondary cell
JPH0555980B2 (en)
JP2610565B2 (en) Manufacturing method of sealed alkaline storage battery using paste-type nickel positive electrode
JPS5983347A (en) Sealed nickel-cadmium storage battery
JP2797554B2 (en) Nickel cadmium storage battery
JP2994850B2 (en) Paste cadmium negative electrode for alkaline storage batteries
JP3030032B2 (en) Sintered cadmium negative electrode for alkaline storage battery and method for producing the same
JPH09223514A (en) Sealed lead-acid battery
JPH10275619A (en) Paste cadmium electrode
JPH028419B2 (en)
JP2589750B2 (en) Nickel cadmium storage battery
JP3196234B2 (en) Cadmium negative electrode plate for alkaline storage battery and method of manufacturing the same
JP2792913B2 (en) Non-sintered cadmium negative electrode plate for alkaline storage batteries
JP3995288B2 (en) Cadmium negative electrode for alkaline storage battery and method for producing the same
JPS63170851A (en) Cadmium electrode for alkaline storage battery
JP2754800B2 (en) Nickel cadmium storage battery
JPH079806B2 (en) Zinc electrode for alkaline storage battery
JPH04284369A (en) Nickel-metal hydride storage battery
JP2810460B2 (en) Positive plate for alkaline storage battery
JPS61233967A (en) Manufacturing method for sealed nickel-hydrogen storage batteries
JP2854920B2 (en) Nickel-metal hydride battery