JPS645421B2 - - Google Patents
Info
- Publication number
- JPS645421B2 JPS645421B2 JP55052191A JP5219180A JPS645421B2 JP S645421 B2 JPS645421 B2 JP S645421B2 JP 55052191 A JP55052191 A JP 55052191A JP 5219180 A JP5219180 A JP 5219180A JP S645421 B2 JPS645421 B2 JP S645421B2
- Authority
- JP
- Japan
- Prior art keywords
- sintered body
- electrode plate
- negative electrode
- nickel
- 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
Links
- 239000000835 fiber Substances 0.000 claims description 36
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 27
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 21
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 18
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims description 17
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 15
- 229910052751 metal Inorganic materials 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 10
- 238000003860 storage Methods 0.000 claims description 10
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 claims description 9
- CXKCTMHTOKXKQT-UHFFFAOYSA-N cadmium oxide Inorganic materials [Cd]=O CXKCTMHTOKXKQT-UHFFFAOYSA-N 0.000 claims description 7
- 229910052759 nickel Inorganic materials 0.000 claims description 7
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 5
- CFEAAQFZALKQPA-UHFFFAOYSA-N cadmium(2+);oxygen(2-) Chemical compound [O-2].[Cd+2] CFEAAQFZALKQPA-UHFFFAOYSA-N 0.000 claims description 5
- 238000007747 plating Methods 0.000 claims description 5
- 239000003513 alkali Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 238000011049 filling Methods 0.000 claims description 3
- 235000011187 glycerol Nutrition 0.000 claims description 3
- 239000003960 organic solvent Substances 0.000 claims description 3
- 238000004804 winding Methods 0.000 claims description 3
- 239000008151 electrolyte solution Substances 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 19
- 229910000831 Steel Inorganic materials 0.000 description 11
- 239000011149 active material Substances 0.000 description 11
- 239000010959 steel Substances 0.000 description 11
- 229910052742 iron Inorganic materials 0.000 description 10
- 238000000034 method Methods 0.000 description 8
- 239000003792 electrolyte Substances 0.000 description 7
- 239000000758 substrate Substances 0.000 description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000002585 base Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000006698 induction Effects 0.000 description 3
- 239000007773 negative electrode material Substances 0.000 description 3
- 238000005245 sintering Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 210000002268 wool Anatomy 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- -1 but for example Substances 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 241001330002 Bambuseae Species 0.000 description 1
- 229910021092 KOH—LiOH Inorganic materials 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007596 consolidation process Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229920005594 polymer fiber Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/70—Carriers or collectors characterised by shape or form
- H01M4/80—Porous plates, e.g. sintered carriers
-
- 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
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Powder Metallurgy (AREA)
- Cell Electrode Carriers And Collectors (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
産業上の利用分野
本発明は密閉型ニツケルカドミウム蓄電池の高
容量密度化に関するものである。
従来技術とその問題点
近年密閉型ニツケルカドミウム蓄電池の高容量
密度化は数百mAhの小型から数百Ahの大型にい
たるまで、全般において行なわれているが、特に
1〜5Ah程度の円筒型密閉蓄電池分野で活発に開
発されている。この分野は誘導灯、非常灯用電源
としての特殊用途があり、この場合5℃〜50℃と
いつたこれまでにない広い温度領域下、1/30C程
度の微電流で充電するといつた苛酷な使用条件に
おいても充分なる高性能を維持しなくてはならな
い。そのため、たとえばNR−C型と称する寸法
25φ×49mmの円筒型密閉蓄電池では、従来のニツ
ケル粉末焼結体による正極、負極を使用した場合
の公称容量は1.8Ah程度が限界である。これに対
し、従来のニツケル粉末焼結体正極とニツケルメ
ツキ穿孔鋼板を使用した従来のペースト負極の組
合せではいく分向上し公称容量2.0Ah程度が限界
となる。
従来ニツケルカドミウム蓄電池用負極板として
は、焼結式及びペースト式が一般的に知られてい
る。しかし、焼結式は高価なカーボニル・ニツケ
ル粉末を原料に用いること並びに大規模な設備装
置、煩雑な活物質含浸工程を必要とすること、及
び容量密度が小さいこと等が欠点となり、安価で
高容量密度の極板が要求される今日、焼結式より
もペースト式の方が有利である。一方従来のペー
スト式負極板は、酸化カドミウム、ニツケル粉
末、高分子短繊維等を混合し、有機増粘剤の少量
を溶解した粘性の水溶液を加え高粘性ペースト液
として、ニツケルメツキ穿孔鋼板芯金の両面に塗
着することによつて作成する。このペースト液に
含有される水とCdO粉末が反応し、CdO・H2O
即ちCd(OH)2として粉末間が結合され(セメン
テーシヨン)、塗着時芯金から脱落することなく
保持される。穿孔鋼板等に塗着させる場合には、
このペースト液は、上記理由により好都合な特性
を有するが、多孔性構造をもつた繊維基板には、
このセメンテーシヨン化により、液の流動性が失
われ細孔内部にペースト液を充填することができ
ない。
従つて、流動性を持ちセメンテーシヨンを生じ
ないペースト液にすることが不可決である。更
に、この従来ペースト式負極板の最大の欠点は負
極活物質が短繊維等有機高分子物によつてのみ基
材に保持されているため、充放電の繰返し等によ
つて脱落を起し焼結式よりも一般に寿命は短か
い。あるいは焼結式のようにニツケル粉末が焼結
されておらず物理的に混合されているだけである
ため、電導材としての作用が不充分であり、極板
抵抗値が焼結式よりも大きく、特に高率放電時に
は無視し得ぬものである。ペースト式負極板性能
は基材構造に左右されることが多いため上記穿孔
鋼板以外にもエキスパンデイドメタル、金網、穿
孔鋼板の両面に凹凸をつけたもの等種々、工夫さ
れている。これらの中ではエキスパンデイドメタ
ルがもつとも好ましいが価格的に高価なことと表
面が鋭利な形状をしているため不織布等の薄型セ
パレータを使用した場合対極との間で短絡を起こ
しやすいためいまだ実用化はされていない。又、
エキスパンデイドメタル、金網、穿孔鋼板等の基
板を用いるペースト式極板においては、ペースト
を基板に保持することが困難であるために結着剤
が用いられている。しかしこの結着剤は、活物質
表面を覆い、抵抗の大きい電極となり、好ましく
ない。
発明の目的
本発明は、上記従来の問題点に鑑みなされたも
ので、耐アルカリ性金属繊維焼結体を用いた集電
性、活物質の保持性、機械的強度、活物質利用率
等の優れたペースト式負極板と正極板とを組み合
わせた電池であり、容量密度を向上させ、かつ長
寿命化、コスト低減を図つた密閉型ニツケルカド
ミウム蓄電池を提供することを目的とする。
発明の構成
本発明は、上記目的を達成するべく線径4〜
100μの耐アルカリ性金属繊維を一定方向に繊維
がならぶようにし、かつニツケルメツキ厚みを
2μ以上とした多孔度90%以上の焼結体に酸化カ
ドミウムをエチレングリコール、イソプロピルア
ルコール、グリセリン等の水を含まない有機溶媒
のみによつて、流動性を維持するペースト液とし
該焼結体に充填することによつて得た負極板を用
いたことを特徴とする密閉型ニツケルカドミウム
蓄電池である。
金属繊維の作成方法は種々あるが、例えばスチ
ールウールを作成する方法は、公知のごとく古く
から行なわれている鉄のワイヤーを数十本のナイ
フによつて切削し、4〜100μ程度の線径のウー
ル状にしたものである。この鉄繊維は非常に安価
であるため、使い捨てケンマ材としての分野で使
用されてきた。今日のごとき高容量密度化が要求
されなかつたことと、スチールウール製造装置が
高価であるためペースト式負極板基材として使用
されることはなかつた。繊維長は数cmから数10cm
と自由に長繊維のものが作成し得るため、このも
のを焼結させた場合非常に強度が大なる焼結体が
得られるために、ニツケル粉末焼結体のごとき補
強のための穿孔鋼板等の導電芯体を必要としな
い。多孔度は90〜98%程度のものが使用可能であ
る。ニツケル繊維の場合はそのまま使用できるが
鉄繊維の場合は腐蝕領域があるためにニツケルメ
ツキを必要とする。この焼結体をペースト式負極
基材として使用する。巾5〜30cm、長さ50〜100
m単位で焼結体を連続的に生産させるために、こ
れらの繊維を交互にからみ合わせながら繊維が一
定の方向性をもつたフエルト状態で生産させる必
要がある。ところが方向性をもつた繊維の焼結体
であるために、表(本発明の繊維焼結体の方向
による特性の違い)のごとく(A)繊維方向に対して
は電導性、引張強度はすぐれているが、(B)長さ方
向と直角方向に対してはいく分劣る。この方向性
のために、繊維方向と直角方向の焼結体を用いて
ウズ巻き型電池を作成した場合、巻き始めと最外
周部において極板の切断が起こり多数の微細短絡
を生じた。これに対して、巻き方向を繊維方向に
した焼結体を用いた場合、この問題点が解消さ
れ、かつ比抵抗も下がり高率放電特性の向上等が
認められた。このような構成にすることによつ
て、従来の焼結式極板と同様の方法で組み立てる
ことができる。一方、ニツケルメツキをするとメ
ツキ厚みが大なるにつれてこの差が縮少して行
き、2μ以上の厚みになると第1図、第2図に示
す如く実用上無視してもよいと考えられる。
INDUSTRIAL APPLICATION FIELD The present invention relates to increasing the capacity density of a sealed nickel cadmium storage battery. Conventional technology and its problems In recent years, the capacity density of sealed nickel cadmium storage batteries has been increased in general, from small ones of several hundred mAh to large ones of several hundred Ah, but in particular, cylindrical sealed batteries of about 1 to 5 Ah have been developed. It is being actively developed in the storage battery field. This field has a special purpose as a power source for guidance lights and emergency lights, and in this case, charging with a microcurrent of about 1/30C under an unprecedentedly wide temperature range of 5℃ to 50℃ is extremely difficult. Sufficient high performance must be maintained under the conditions of use. Therefore, for example, the dimensions called NR-C type
For a 25φ x 49mm cylindrical sealed storage battery, the nominal capacity is limited to about 1.8Ah when using conventional positive and negative electrodes made of sintered nickel powder. On the other hand, the combination of a conventional nickel powder sintered positive electrode and a conventional paste negative electrode using a nickel-plated perforated steel plate improves somewhat, but the nominal capacity is limited to about 2.0 Ah. Conventionally, sintered type and paste type negative electrode plates for nickel cadmium storage batteries are generally known. However, the sintering method uses expensive carbonyl/nickel powder as a raw material, requires large-scale equipment, a complicated active material impregnation process, and has a low capacity density. Nowadays, when electrode plates with high capacity density are required, the paste type is more advantageous than the sintered type. On the other hand, conventional paste-type negative electrode plates are made by mixing cadmium oxide, nickel powder, short polymer fibers, etc., adding a viscous aqueous solution containing a small amount of an organic thickener, and creating a highly viscous paste solution. Created by painting on both sides. The water contained in this paste solution reacts with the CdO powder, forming CdO・H 2 O.
That is, the powders are bonded together as Cd(OH) 2 (cementation), and are held without falling off the core metal during coating. When applying to perforated steel plates, etc.,
This paste liquid has favorable properties for the reasons mentioned above, but it is not suitable for fiber substrates with porous structures.
Due to this cementation, the fluidity of the liquid is lost and the inside of the pores cannot be filled with the paste liquid. Therefore, it is essential to create a paste solution that has fluidity and does not cause cementation. Furthermore, the biggest drawback of this conventional paste-type negative electrode plate is that the negative electrode active material is held to the base material only by organic polymers such as short fibers, which can cause it to fall off and burn out due to repeated charging and discharging. Generally, the lifespan is shorter than that of a condensate. Or, unlike the sintered type, the nickel powder is not sintered but only physically mixed, so its action as a conductive material is insufficient, and the plate resistance value is higher than that of the sintered type. , which cannot be ignored, especially during high rate discharge. Since the performance of paste-type negative electrode plates is often influenced by the structure of the base material, in addition to the above-mentioned perforated steel plates, various other devices have been devised, such as expanded metal, wire mesh, and perforated steel plates with irregularities on both sides. Among these, expanded metal is preferable, but it is still not practical because it is expensive and has a sharp surface that tends to cause a short circuit with the opposite electrode when using a thin separator such as non-woven fabric. It has not been converted. or,
In paste-type electrode plates using substrates such as expanded metal, wire mesh, perforated steel plates, etc., binders are used because it is difficult to hold the paste on the substrate. However, this binder covers the surface of the active material and becomes an electrode with high resistance, which is not preferable. Purpose of the Invention The present invention has been made in view of the above-mentioned conventional problems, and provides excellent current collection properties, active material retention properties, mechanical strength, active material utilization rate, etc. using an alkali-resistant metal fiber sintered body. The purpose of the present invention is to provide a sealed nickel-cadmium storage battery that is a battery that combines a paste-type negative electrode plate and a positive electrode plate, and that has improved capacity density, extended life, and reduced cost. Structure of the Invention In order to achieve the above object, the present invention has a wire diameter of 4 to 4.
The 100μ alkali-resistant metal fibers are lined up in a certain direction, and the thickness is nickel-metalized.
Add cadmium oxide to a sintered body with a porosity of 2 μ or more and a porosity of 90% or more using only a water-free organic solvent such as ethylene glycol, isopropyl alcohol, or glycerin to form a paste solution that maintains fluidity. This is a sealed nickel-cadmium storage battery characterized by using a negative electrode plate obtained by filling the battery. There are various ways to create metal fibers, but for example, steel wool is created by cutting iron wire with dozens of knives to create a wire with a diameter of about 4 to 100 μm. It is made into wool. Since this iron fiber is very cheap, it has been used in the field as disposable bamboo material. Because there was no demand for high capacity density as there is today, and because steel wool manufacturing equipment was expensive, it was never used as a paste-type negative electrode plate base material. Fiber length is from several centimeters to several tens of centimeters
Since long fibers can be freely created, when sintered, a sintered body with extremely high strength can be obtained, so perforated steel plates for reinforcement such as nickel powder sintered bodies, etc. No conductive core required. Porosities of about 90 to 98% can be used. Nickel fibers can be used as is, but iron fibers require nickel plating because they have corroded areas. This sintered body is used as a paste-type negative electrode base material. Width 5-30cm, length 50-100
In order to continuously produce a sintered body in meters, it is necessary to intertwine these fibers alternately to produce a felt state in which the fibers have a certain directionality. However, since it is a sintered body of fibers with directionality, as shown in the table (differences in properties depending on the direction of the fiber sintered body of the present invention), (A) it has excellent electrical conductivity and tensile strength in the fiber direction. (B) However, it is somewhat inferior in the longitudinal direction and perpendicular direction. Due to this directionality, when a spiral-wound battery was created using a sintered body in a direction perpendicular to the fiber direction, the electrode plate was cut at the beginning of winding and at the outermost periphery, resulting in numerous micro short circuits. On the other hand, when a sintered body in which the winding direction was the fiber direction was used, this problem was solved, the specific resistance was also lowered, and high rate discharge characteristics were improved. With this configuration, it can be assembled in the same manner as a conventional sintered electrode plate. On the other hand, when nickel plating is used, this difference decreases as the plating thickness increases, and when the thickness becomes 2μ or more, it can be practically ignored as shown in FIGS. 1 and 2.
【表】
これらの金属繊維焼結体に酸化カドミウムにエ
チレングリコール、イソプロピルアルコール、グ
リセリン等の水を含まない有機溶媒のみからペー
スト液を調合し、流動性ペーストとした負極活物
質を繊維焼結体に所定量を充填する。
しかるのち通常のペースト極板を作成するごと
く、乾燥、ローラープレス、化成、所定寸法に切
断を行なつて負極板となす。従来のペースト式負
極板は電導材として10〜15wt%ニツケル粉末を
必要とするが、本発明の金属繊維焼結体は、繊維
自体にこの働らきがあるために、ニツケル粉末を
必要としない。又、穿孔鋼板のごとき補強のため
の芯体も必要としないことから、この焼結体を基
材に使用した場合従来のペースト極板にくらべて
死容積が少なくて済む。基材として非常に有効に
作用するために従来のものよりもより高容量密度
の極板を作成することができる。
正極板においてもこの焼結体を集電体として使
用できるが、40℃以上の高温下、1/30C程度の低
率充電において充電効率がニツケル粉末焼結体よ
りも劣つている。このため非常灯、誘導灯用電池
においてはニツケル粉末焼結体を正極集電体とし
て使用せざるを得ないが、通常の室温付近で使用
する場合はさほど問題がないものである。従来ニ
ツケル粉末焼結体は厚み0.7mm付近が多く用いら
れているが厚みが薄くなるほど穿孔鋼板のごとき
導電芯体のしめる割合が増加するために高容量密
度化するためにはできるかぎり厚型焼結体の方が
望ましい。しかしあまり厚くなりすぎると、電解
液の拡散等に問題を生じるために0.8〜1.0mm程度
が有効である。
使用電解液も40℃以上の高温下で使用する場合
従来のKOH−LiOH系では正極の酸素過電圧が
充分でなく、NaOH−LiOH系の方が酸素過電圧
が大であるため充電効率がすぐれている。
NaOH−LiOH系電解液においてもその濃度によ
つて電池性能が左右され最適なる濃度が存在す
る。一方放電々圧特性に対しては、低濃度電解液
ほど電圧が高く良好であるが負極反応は放電にお
いてCd→Cd(OH)4 2-→Cd(OH)2と溶解析出反応
を行なうため、アルカリ濃度が低くなると、抵抗
が増大し活物質利用率が低下する。このため5規
定以下の水酸化ナトリウム濃度を使用すると負極
制限になる場合もあり使用することができない。
ところが、繊維焼結体の場合、ニツケル粉末焼
結体のごとき10μ以下の微細孔をもたないため、
反応に必要なるOH-イオンをスムーズにバルク
より供給することができるため、たとえば4規定
程度の水酸化ナトリウム濃度を用いてもほとんど
抵抗をうけなく良好なる放電々圧特性を示す。
実施例
以下、本発明の一実施例に基き説明する。
安価で広く知られた鉄繊維の場合を例にとる
と、まず鉄を切削加工することによつて10〜30μ
程度の繊維径をもつた鉄繊維を作成する。繊維長
さは切削加工する原料鉄線の長さあるいは鉄の質
によつて変化するが、1cm以上あれば焼結体とな
つた場合の強度に大きな影響を与えることはな
い。ここでは5〜10cm程度のものを用いた。繊維
同志をからませながらも一定の方向性をもたせな
がら巾20cm、長さ80mのフエルト状態になつたも
のを還元性雰囲気にて弾力性を除去した後、プレ
スをして1000〜1100℃水素等還元性雰囲気中で焼
結せしめる。プレス圧と焼結時間は多孔度に影響
を与えるが、ここで得られた鉄繊維焼結体は平均
多孔度95%程度である。しかる後常法に従い鉄繊
維焼結体に2〜3μ厚みの電気ニツケルメツキを
ほどこす。この焼結体をカレンダーロール法によ
つて、酸化カドミウム:エチレングリコール:イ
ソプロピルアルコールがそれぞれ重量比で8:
2:0.5のペースト状活物質を塗着後、約100℃の
熱風によつて10分間乾燥せしめた後、比重1.20の
KOH電解液中3mA/cm2の充電々流で理論容量
の150%を充電し、6mA/cm2の放電々流で0Vま
で放電させた後水洗を行なう常法の化成処理によ
つてエチレングリコール、イソプロピルアルコー
ル等有機物を完全に除去する。化成終了後所定寸
法に打ち抜いて極板にする。一方正極板は穿孔鋼
板にニツケル粉末を焼結させた多孔度約80%のニ
ツケルプラークに硝酸ニツケル溶液を含浸させ、
水酸化ナトリウム中で電解還元を行なう常法の操
作を数回くり返して、活物質を充填せしめ、しか
る後化成を行なつて不純物を除去する。所定寸法
に打抜いた後、この極板等、およびセパレータを
使用して密閉型電池を作成した。作成した電池の
正極板寸法は200×39W×0.85tmm、負極板寸法
は240×39W×0.65tmmで、セパレータにはポリ
プロピレン不織布を使用した。電池寸法は25φ×
49mmの円筒型密閉電池で市販の公称容量1800m
Ah電池と同サイズである。作成した電池の公称
容量は2300mAhである。使用した電気液組成は
3〜5規定の水酸化ナトリウムおよび0.5〜1.5規
定の水酸化リチウムの混合水溶液と、5規定の水
酸化カリウムと1.0規定の水酸化リチウムの混合
水溶液である。この電池を室温における一般的な
性能1/10C充電々流で15時間充電をし1/5C、1C
の放電々流で1.00Vまで放電させる方法および5
℃、45℃における誘導灯規格試験による1/30Cの
充電々流で24時間充電し1Cの放電々流で1.15Vま
で放電させる方法、並びに45℃における非常灯規
格試験による1/30Cの充電々流で45時間充電をし
1Cの放電々流で1.15Vまで放電させる方法にて性
能を調べると、表に示すように本発明による電
池において水酸化ナトリウム、水酸化リチウム混
合水溶液を使用したものの実容量は2.7〜2.8Ahも
あり、公称容量2400〜2500mAhに相当する高容
量である。
一方誘導灯、非常灯規格試験においても現行の
シンター式正・負極板を使用した公称容量1800m
Ah電池よりも高性能である。[Table] A paste solution is prepared from only cadmium oxide and water-free organic solvents such as ethylene glycol, isopropyl alcohol, and glycerin to these metal fiber sintered bodies, and the negative electrode active material is made into a fluid paste. Fill the specified amount. Thereafter, the negative electrode plate is prepared by drying, roller pressing, chemical conversion, and cutting into predetermined dimensions, just as in the case of making a normal paste electrode plate. Conventional paste-type negative electrode plates require 10 to 15 wt% nickel powder as a conductive material, but the metal fiber sintered body of the present invention does not require nickel powder because the fibers themselves have this function. Furthermore, since a reinforcing core such as a perforated steel plate is not required, when this sintered body is used as a base material, the dead volume is smaller than that of a conventional paste electrode plate. Plates with higher capacitance densities than conventional ones can be made to act very effectively as substrates. This sintered body can also be used as a current collector in the positive electrode plate, but the charging efficiency is inferior to that of the nickel powder sintered body at low charging rates of about 1/30 C at high temperatures of 40° C. or higher. For this reason, nickel powder sintered bodies must be used as positive electrode current collectors in batteries for emergency lights and guide lights, but this does not pose much of a problem when used near normal room temperature. Conventionally, nickel powder sintered bodies are often used with a thickness of around 0.7 mm, but as the thickness decreases, the proportion of conductive cores such as perforated steel plates increases. Consolidation is preferable. However, if it becomes too thick, it will cause problems such as diffusion of the electrolyte, so a thickness of about 0.8 to 1.0 mm is effective. When using the electrolyte at high temperatures of 40℃ or higher, the conventional KOH-LiOH system does not have sufficient oxygen overvoltage at the positive electrode, and the NaOH-LiOH system has a higher oxygen overvoltage, so it has better charging efficiency. .
Battery performance is also influenced by the concentration of the NaOH-LiOH electrolyte, and there is an optimum concentration. On the other hand, regarding the discharge voltage characteristics, the lower the concentration electrolyte, the higher the voltage, and the better. When the alkali concentration becomes low, the resistance increases and the active material utilization rate decreases. For this reason, if a sodium hydroxide concentration of 5N or less is used, the negative electrode may be limited and cannot be used. However, in the case of fiber sintered bodies, they do not have micropores of 10μ or less like nickel powder sintered bodies, so
Since the OH - ions required for the reaction can be smoothly supplied from the bulk, there is almost no resistance even when a sodium hydroxide concentration of about 4N is used, and good discharge pressure characteristics are exhibited. Embodiment An embodiment of the present invention will be explained below. For example, in the case of iron fiber, which is widely known as being cheap, firstly, by cutting the iron, it becomes 10 to 30 μm.
Create iron fibers with a fiber diameter of approximately The fiber length varies depending on the length of the raw material iron wire to be cut or the quality of the iron, but if it is 1 cm or more, it will not have a major effect on the strength of the sintered body. Here, one of approximately 5 to 10 cm was used. After entwining the fibers with each other and maintaining a certain direction, the felt was made into a felt state with a width of 20 cm and a length of 80 m. After removing the elasticity in a reducing atmosphere, it was pressed and heated at 1000-1100°C with hydrogen, etc. Sinter in a reducing atmosphere. Press pressure and sintering time affect porosity, but the iron fiber sintered body obtained here has an average porosity of about 95%. Thereafter, the iron fiber sintered body is plated with electric nickel to a thickness of 2 to 3 μm according to a conventional method. This sintered body was processed by a calender roll method so that the weight ratio of cadmium oxide, ethylene glycol, and isopropyl alcohol was 8:8.
After applying a paste active material with a ratio of 2:0.5 and drying it with hot air at about 100℃ for 10 minutes,
Ethylene glycol is converted into ethylene glycol by a conventional chemical conversion treatment in which 150% of the theoretical capacity is charged with a charging current of 3 mA/cm 2 in a KOH electrolyte, discharged to 0 V with a current of 6 mA/cm 2 , and then washed with water. , completely removes organic substances such as isopropyl alcohol. After completion of chemical formation, it is punched out to a predetermined size to form an electrode plate. On the other hand, the positive electrode plate is made by impregnating a nickel plaque with a porosity of approximately 80%, which is made by sintering nickel powder on a perforated steel plate, with a nickel nitrate solution.
A conventional operation of electrolytic reduction in sodium hydroxide is repeated several times to fill the active material, and then chemical conversion is performed to remove impurities. After punching to a predetermined size, a sealed battery was created using the electrode plates and the separator. The positive electrode plate dimensions of the created battery were 200 x 39 W x 0.85 tmm, the negative electrode plate dimensions were 240 x 39 W x 0.65 tmm, and a polypropylene nonwoven fabric was used for the separator. Battery dimensions are 25φ×
Commercially available nominal capacity 1800m with 49mm cylindrical sealed battery
It is the same size as an Ah battery. The nominal capacity of the created battery is 2300mAh. The electrolyte compositions used were a mixed aqueous solution of 3-5N sodium hydroxide and 0.5-1.5N lithium hydroxide, and a mixed aqueous solution of 5N potassium hydroxide and 1.0N lithium hydroxide. This battery was charged for 15 hours at a normal performance of 1/10C charging current at room temperature, 1/5C, 1C.
Method of discharging to 1.00V with a current of discharge and 5
℃, a method of charging for 24 hours with a 1/30C constant charge current according to the induction light standard test at 45℃, and discharging to 1.15V with a 1C constant discharge current, and a method of charging at 1/30C according to the emergency light standard test at 45℃. Charge it for 45 hours with a stream of water.
When the performance was investigated by discharging to 1.15V with a 1C current, as shown in the table, the actual capacity of the battery according to the present invention using a mixed aqueous solution of sodium hydroxide and lithium hydroxide was 2.7 to 2.8Ah. It has a high capacity equivalent to a nominal capacity of 2400 to 2500mAh. On the other hand, in the guidance light and emergency light standard tests, the nominal capacity was 1800 m using the current sinter type positive and negative electrode plates.
Higher performance than Ah batteries.
【表】
(注) 表の(A)は本発明の電池構成によるもので
公称容量2300mAhであり、(B)は従来の焼結式極
板を使用した電池で公称容量1800mAhである。
は、実容量を調べるために、25℃、1/10Cで15
時間充電をし、1/5Cで終止電圧1.00Vまで放電
させた時の容量であり、は45℃、誘導灯規格試
験による性能を示し、は5℃、誘導灯規格試験
による性能を示し、は45℃非常灯規格試験によ
る性能を示したものである。放電々圧特性も第3
図に示すごとくすぐれている。この理由は第4図
に示すごとく本発明の負極活物質利用率が、従来
のシンター式にくらべて約7〜10%、従来のペー
スト式にくらべて約15%程度向上しており、かつ
繊維の特性を考慮し比抵抗をできるかぎり少なく
したために、負極分極がないため電池にした場合
完全なる正極放電特性を示し得るためと考えられ
る。
又、従来のペースト式極板がその基板が平面的
であり結着剤によつて基板に活物質を保持させな
ければ電極形成ができないのに対して、本発明に
用いたペースト式極板は活着剤を用いず繊維のか
らんだ多孔体基板によつて活物質を保持させるも
のである。
低温5℃〜高温45℃にわたつてバランスのとれ
た電解液は、水酸化ナトリウム4規定付近、水酸
化リチウム1規定付近の混合溶液と考えられる。
発明の効果
以上のごとく、本発明は繊維の特性、活物質の
充填方法、電解液の組成等総合的な改良を行い、
従来の焼結式電池をしのぐ高容量密度の電池を実
現させ、かつ長寿命でコストの低減を図ることが
出来たものであり、工業的価値ははなはだ大なる
ものである。[Table] (Note) In the table, (A) is a battery configured according to the present invention and has a nominal capacity of 2300 mAh, and (B) is a battery using a conventional sintered electrode plate and has a nominal capacity of 1800 mAh.
is 15 at 25℃ and 1/10C to check the actual capacity.
This is the capacity when charged for an hour and discharged to a final voltage of 1.00V at 1/5C. indicates the performance according to the induction light standard test at 45℃, indicates the performance according to the induction light standard test at 5℃, and This shows the performance according to the 45℃ emergency lighting standard test. The discharge pressure characteristics are also the third
It is excellent as shown in the figure. The reason for this is that, as shown in Figure 4, the utilization rate of the negative electrode active material of the present invention is improved by about 7 to 10% compared to the conventional sinter method and about 15% compared to the conventional paste method. It is thought that this is because the resistivity was minimized as much as possible in consideration of the characteristics of the battery, and since there is no negative polarization, when it is made into a battery, it can exhibit perfect positive discharge characteristics. Furthermore, while the conventional paste-type electrode plate has a planar substrate and electrodes cannot be formed unless the active material is held on the substrate by a binder, the paste-type electrode plate used in the present invention The active material is held by a porous substrate entangled with fibers without using an adhesive. An electrolytic solution that is well-balanced at a low temperature of 5°C to a high temperature of 45°C is considered to be a mixed solution containing around 4N of sodium hydroxide and around 1N of lithium hydroxide. Effects of the Invention As described above, the present invention comprehensively improves fiber properties, active material filling method, electrolyte composition, etc.
This technology has realized a battery with a high capacity density that exceeds that of conventional sintered batteries, has a long life span, and can reduce costs, so its industrial value is enormous.
第1図、第2図は本発明の繊維焼結体のニツケ
ルメツキの厚さによる特性変化を示すもので、A
が繊維方向、Bが繊維と直角方向である。第3図
のAは本発明の電池、Bは従来の焼結式極板使用
電池の45℃誘導灯規格試験における放電々圧特性
である。第4図Aは本発明の負極板、Bは従来の
焼結極板、Cは従来のペースト式極板の活物質利
用率変化を示したものである。
Figures 1 and 2 show changes in characteristics depending on the thickness of the nickel plating of the fiber sintered body of the present invention.
is the fiber direction, and B is the direction perpendicular to the fibers. In FIG. 3, A shows the discharge voltage characteristics of the battery of the present invention and B shows the discharge pressure characteristics of the conventional battery using sintered electrode plates in the 45°C guide light standard test. FIG. 4A shows the change in the active material utilization rate of the negative electrode plate of the present invention, B shows the conventional sintered electrode plate, and C shows the conventional paste-type electrode plate.
Claims (1)
定方向に繊維がならぶようにし、かつニツケルメ
ツキ厚みを2μ以上とした多孔度90%以上の焼結
体に酸化カドミウムをエチレングリコール、イソ
プロピルアルコール、グリセリン等の水を含まな
い有機溶媒のみによつて、流動性を維持するペー
スト液とし該焼結体に充填することによつて得た
負極板を用いたことを特徴とする密閉型ニツケル
カドミウム蓄電池。 2 方向性をもつた繊維焼結体を使用した負極板
をウズ巻き型密閉ニツケルカドミウム電池に使用
する場合、巻込み方向と繊維方向を一致させたこ
とを特徴とする特許請求の範囲第1項記載の密閉
型ニツケルカドミウム蓄電池。 3 使用電解液の組成が3.5〜4.5規定の水酸化ナ
トリウムと0.5〜1.0規定の水酸化リチウムを含む
混合水溶液であることを特徴とする特許請求の範
囲第1項記載の密閉型ニツケルカドミウム蓄電
池。[Scope of Claims] 1 A sintered body made of alkali-resistant metal fibers with a wire diameter of 4 to 100μ arranged in a fixed direction and with a nickel plating thickness of 2μ or more and a porosity of 90% or more, in which cadmium oxide is added to ethylene glycol. , a negative electrode plate obtained by filling the sintered body with a paste liquid that maintains fluidity using only a water-free organic solvent such as isopropyl alcohol or glycerin. type nickel cadmium storage battery. 2. Claim 1, characterized in that when a negative electrode plate using a directional fiber sintered body is used in a spiral-wound sealed nickel cadmium battery, the winding direction and the fiber direction are made to match. The sealed nickel cadmium storage battery described. 3. The sealed nickel-cadmium storage battery according to claim 1, wherein the electrolytic solution used is a mixed aqueous solution containing 3.5-4.5N sodium hydroxide and 0.5-1.0N lithium hydroxide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5219180A JPS56149768A (en) | 1980-04-18 | 1980-04-18 | Sealed nickel-cadmium storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5219180A JPS56149768A (en) | 1980-04-18 | 1980-04-18 | Sealed nickel-cadmium storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56149768A JPS56149768A (en) | 1981-11-19 |
| JPS645421B2 true JPS645421B2 (en) | 1989-01-30 |
Family
ID=12907897
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5219180A Granted JPS56149768A (en) | 1980-04-18 | 1980-04-18 | Sealed nickel-cadmium storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56149768A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5990357A (en) * | 1982-11-15 | 1984-05-24 | Japan Storage Battery Co Ltd | Positive plate for alkaline battery |
| JPS59128764A (en) * | 1983-01-13 | 1984-07-24 | Japan Storage Battery Co Ltd | Positive plate for alkaline battery |
| JPS59230259A (en) * | 1983-06-10 | 1984-12-24 | Yuasa Battery Co Ltd | Manufacture of plate for pocket type alkaline storage battery |
| JPS60211766A (en) * | 1984-04-03 | 1985-10-24 | Yuasa Battery Co Ltd | Paste type negative electrode plate for alkaline storage battery |
-
1980
- 1980-04-18 JP JP5219180A patent/JPS56149768A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56149768A (en) | 1981-11-19 |
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