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JPH0239065B2 - - Google Patents
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JPH0239065B2 - - Google Patents

Info

Publication number
JPH0239065B2
JPH0239065B2 JP57033034A JP3303482A JPH0239065B2 JP H0239065 B2 JPH0239065 B2 JP H0239065B2 JP 57033034 A JP57033034 A JP 57033034A JP 3303482 A JP3303482 A JP 3303482A JP H0239065 B2 JPH0239065 B2 JP H0239065B2
Authority
JP
Japan
Prior art keywords
active material
anode active
anode
battery
corrosion
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
JP57033034A
Other languages
Japanese (ja)
Other versions
JPS58152379A (en
Inventor
Hiroyasu Komata
Hideo Anho
Takanori Nakazawa
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP57033034A priority Critical patent/JPS58152379A/en
Publication of JPS58152379A publication Critical patent/JPS58152379A/en
Publication of JPH0239065B2 publication Critical patent/JPH0239065B2/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
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/661Metal or alloys, e.g. alloy coatings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/36Accumulators not provided for in groups H01M10/05-H01M10/34
    • H01M10/39Accumulators not provided for in groups H01M10/05-H01M10/34 working at high temperature
    • H01M10/3909Sodium-sulfur cells
    • 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)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Sealing Battery Cases Or Jackets (AREA)
  • Secondary Cells (AREA)

Description

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

本発明は高温電池に係るもので、陽極活物質に
接する陽極活物質容器、陽極集電体等に耐食性の
優れた材料を提供することにより、電池の寿命の
長期化をはかるものである。 本電池の原理は、1966年米国フオード・モータ
ー社により発表されたもので活物質としてナトリ
ウム、硫黄を用いることからナトリウム−硫黄電
池ともよばれている。その構造は、第1図に示す
ごとく、1の陰極端子、2の陰極活物質(ナトリ
ウム)、3のナトリウムイオン伝導性を有する固
体電解質管(例えばベータアルミナ)、4のカー
ボン又はグラフアイトフエルトに含浸された陽極
活物質(例えば硫黄又は多硫化ナトリウム)、5
の陽極集電体を兼ねた陽極活物質容器からなり、
固体電解質管の上部開放端には、陰極室と陽極室
を気密に密封する蓋を電気的に絶縁するための絶
縁物8(例えばアルフアアルミナ)がガラス9で
接合されている。作動温度は両極活物質の融点、
固体電解質の電導度を考慮し通常300〜350℃であ
る。 電池反応は以下の式に示すとおりである。 2Na+3S放電 ―→ ←― 充電Na2S3 高温電池は、高性能の2次電池として電力負荷
調整用、電気自動車電源用に各国で開発が進めら
れているが、開発のネツクのひとつに、耐多硫化
ナトリウム性の優れた陽極活物質容器、陽極集電
体が必要であるという点がある。多硫化ナトリウ
ムは非常に強い腐食作用をもち、陽極活物質容
器、陽極集電体等が腐食されると硫化物が生成さ
れる。腐食が進行すると、陽極活物質中の硫黄が
硫化のために消費され、活物質として作用する硫
黄の量が減り、電池容量が減少して寿命となる。
又局部的に腐食が進行すると、陽極活物質容器等
に穴があき、活物質が外部へ流出して寿命となる
場合もある。 陽極活物質容器、陽極集電体等に要求される性
能は、激しい腐食作用をもつ陽極活物質に対し耐
食性があり、かつ機械的強度がなくてはならず、
加工性に優れている材料が望ましい。さらに陽極
集電をおこなうときには良好な電気伝導性も必要
である。一般にはSUS 304、モリブデン、クロ
ムさらには本発明者らによる鉄−クロム−珪素合
金などが陽極活物質容器、陽極集電体等として検
討されているが、SUS304では腐食の進行が速
く、第2図に示すように、少ない充放電サイクル
で急激な電池容量の減少をきたす。モリブデンの
場合、陽極活物質組成がNa2S5付近の部分放電状
態で放電を打切る充放電サイクルのときは、全体
量としての腐食は少なく、第3図に示す様に電池
容量の減少は少ないが、局部的な腐食いわゆる孔
食がおこり、結局寿命は短かい。 そのうえ陽極活物質組成がNa2S3付近の完全放
電状態まで放電する充放電サイクルのときは、腐
食の進行が加速され、第4図に示す様に、第3図
に示した部分放電に比較して電池容量減少は激し
くなる。クロムはNa2S5〜Na2S3の全域で全体量
の腐食は少ないが、孔食を生ずること、また極め
て脆く、容器等に加工することは現状技術では不
可能に近いものであり、要求を満足するものでは
ない。 本発明者らはさきに陽極活物質に対して耐食性
があり、かつ加工性も優れた金属材料として鉄−
クロム−珪素合金を提案したが、さらに高純度鉄
クロム合金が、電池容量変化からなおいつそう優
れていることをみいだした。鉄クロム合金の好ま
しい範囲は、重量比でCr40〜60%、C0.02%以
下、N0.015%以下、残部が実質的に鉄である。 Crは上限を超えると加工性が悪く、下限以下
では耐食性が良好でない。CおよびNは上限を超
えると粒界腐食、孔食等の局部腐食をおこしやす
く、また加工性を損なう。 上記鉄−クロム合金にTi、Nb、Zrのうちいず
れか1種または2種以上を合計量で0.05〜1%添
加したものはさらに腐食性を改善する。Ti、
Nb、Zrを添加すると、クロム炭窒化物の粒界析
出を抑制するため耐食性を改善し、かつ延性、靭
性を向上させる。但し上限を超えて添加すると、
Ti、Nb、Zrを含む金属間化合物が生成し、延
性、靭性を害するようになる。陽極活物質は上述
の通り放電によりS(硫黄)あるいはNa2S5など
のSのNaに対する比の大きいところから、ほゞ
Na2S3の組成にまで変化するが、Na2S3による腐
食が最も激しく、陽極活物質容器、陽極集電体等
としては、Na2S3に対する十分な耐食性が必要で
ある。 以下に本発明の合金と従来の金属材料の耐食性
比較試験結果を示す。 第1表に示す本発明の合金の1mm×8mm×30mm
の試験片を、15gのNa2S3の一緒にパイレツクス
ガラス管に真空封入し、350℃で384時間の腐食試
験を行なつた。 試験片の重量減、表面積、比重より腐食厚さを
求めた。また顕微鏡により孔食の有無を調べた。 結果を第2表に示す。
The present invention relates to high-temperature batteries, and aims to extend the life of the battery by providing materials with excellent corrosion resistance for the anode active material container, anode current collector, etc. that are in contact with the anode active material. The principle of this battery was announced by Ford Motor Company in the United States in 1966, and it is also called a sodium-sulfur battery because it uses sodium and sulfur as active materials. As shown in Figure 1, its structure consists of 1 cathode terminal, 2 cathode active material (sodium), 3 solid electrolyte tube with sodium ion conductivity (e.g. beta alumina), and 4 carbon or graphite felt. impregnated anode active material (e.g. sulfur or sodium polysulfide), 5
It consists of an anode active material container that also serves as an anode current collector.
An insulator 8 (for example, alpha alumina) for electrically insulating a lid that airtightly seals the cathode chamber and the anode chamber is bonded to the upper open end of the solid electrolyte tube with a glass 9. The operating temperature is the melting point of the bipolar active material,
The temperature is usually 300 to 350°C in consideration of the conductivity of the solid electrolyte. The battery reaction is as shown in the equation below. 2Na + 3S discharge -→ ←- Rechargeable Na 2 S 3 high-temperature batteries are being developed in various countries as high-performance secondary batteries for power load adjustment and electric vehicle power supplies, but one of the key points in their development is their durability. There is a need for an anode active material container and an anode current collector with excellent sodium polysulfide properties. Sodium polysulfide has a very strong corrosive effect, and sulfides are generated when the anode active material container, anode current collector, etc. are corroded. As corrosion progresses, sulfur in the anode active material is consumed due to sulfidation, and the amount of sulfur that acts as an active material decreases, reducing battery capacity and reaching the end of its life.
Further, if corrosion progresses locally, holes may form in the anode active material container, etc., and the active material may flow out to the outside, resulting in the end of the service life. The performance required for the anode active material container, anode current collector, etc. is that it must be corrosion resistant to the severely corrosive anode active material and have mechanical strength.
Materials with excellent workability are desirable. Furthermore, good electrical conductivity is also required when performing anode current collection. In general, SUS 304, molybdenum, chromium, and the iron-chromium-silicon alloy developed by the present inventors are being considered as anode active material containers, anode current collectors, etc., but SUS304 corrodes quickly and As shown in the figure, the battery capacity rapidly decreases with a small number of charge/discharge cycles. In the case of molybdenum, during a charge/discharge cycle in which the discharge is terminated in a partially discharged state where the anode active material composition is around Na 2 S 5 , corrosion as a whole is small, and as shown in Figure 3, there is no decrease in battery capacity. Although it is rare, localized corrosion, so-called pitting corrosion, occurs, resulting in a short lifespan. Furthermore, during a charge/discharge cycle in which the anode active material composition is discharged to a fully discharged state near Na 2 S 3 , the progress of corrosion is accelerated, as shown in Figure 4, compared to the partial discharge shown in Figure 3. As a result, the battery capacity decreases rapidly. Chromium has little corrosion overall in the Na 2 S 5 to Na 2 S 3 range, but it does cause pitting corrosion and is extremely brittle, making it nearly impossible to process into containers etc. with current technology. It does not satisfy the requirements. The present inventors first discovered that iron is a metal material that has corrosion resistance and excellent workability for anode active materials.
Although we proposed a chromium-silicon alloy, we discovered that a high-purity iron-chromium alloy is even more superior in terms of battery capacity changes. The preferable range of the iron-chromium alloy is 40 to 60% Cr, 0.02% or less of C, 0.015% or less of N, and the balance is substantially iron. When Cr exceeds the upper limit, workability is poor, and when it is below the lower limit, corrosion resistance is poor. When C and N exceed the upper limits, local corrosion such as intergranular corrosion and pitting corrosion tends to occur, and workability is impaired. Corrosivity is further improved by adding one or more of Ti, Nb, and Zr in a total amount of 0.05 to 1% to the above iron-chromium alloy. Ti,
Addition of Nb and Zr improves corrosion resistance by suppressing grain boundary precipitation of chromium carbonitride, and also improves ductility and toughness. However, if added in excess of the upper limit,
Intermetallic compounds containing Ti, Nb, and Zr are formed, which impairs ductility and toughness. As mentioned above, the anode active material is made up of S (sulfur) or Na2S5 , which has a high ratio of S to Na, due to discharge.
Although the composition changes to Na 2 S 3 , the corrosion caused by Na 2 S 3 is the most severe, and the anode active material container, anode current collector, etc. must have sufficient corrosion resistance against Na 2 S 3 . The results of a comparative corrosion resistance test between the alloy of the present invention and conventional metal materials are shown below. 1 mm x 8 mm x 30 mm of the alloy of the present invention shown in Table 1
The specimen was vacuum sealed in a Pyrex glass tube with 15 g of Na 2 S 3 and subjected to a corrosion test at 350° C. for 384 hours. The corrosion thickness was determined from the weight loss, surface area, and specific gravity of the test piece. The presence or absence of pitting corrosion was also examined using a microscope. The results are shown in Table 2.

【表】【table】

【表】【table】

【表】 これらの結果から本発明の合金は、参考例の合
金に比較すると、参考例の合金4を除き腐食厚
さ、局部腐食の点から、耐Na2S3性が極めてすぐ
れている。 つぎに本発明合金(第1表1、2、3、4、
5、6)を用いて、第1図の5に示された陽極集
電体を兼ねた陽極活物質容器を作成し、ナトリウ
ム−硫黄電池を組立て、充放電サイクル試験を実
施した。 試験温度は350℃で5時間率電流(陽極活物質
容器の表面電流密度として55mA/cm2)で3時間
放電し、10分間休止の後5時間で放電量の100%
電気量を充電し、10分間休止を1サイクルとする
充放電条件である。450サイクルまでの各陽極活
物質容器を用いた電池のサイクルに対する電池容
量の変化および試験後の陽極活物質容器の調査を
行なつた。 第6図には合金試料1、2、3、4、5、6で
作成した陽極活物質容器を用いた電池の充放電サ
イクルに対する電池容量変化を示した。同様の試
験条件で行なつたモリブデンおよび鉄−クロム−
珪素合金を、陽極活物質容器として使つた電池の
結果(第3図、第5図参照)に比較しても良好な
電池容量変化である。 また試験後の容器5の陽極活物質に接していた
表面は、本発明の合金試料はいずれの試料も異常
はなく、陽極活物質に対してすぐれた耐食性をも
つていた。第7図に一例として合金試料2の写真
を示す。一方、モリブデン容器電池の陽極活物質
に接していた表面を調べたところ、第8図に示す
ごとく局部腐食が発生していた。 つぎに第9図に示す構造の電池を作成した。 第9図のナトリウム−硫黄電池は、固体電解質
管内に陽極活物質14が充填されており、第1図
の電池とは陰極、陽極が逆になつている。第1図
と同一符号は同一名称につき説明を省略する。 固体電解質管内の端子15(陽極集電体)に、
この場合は耐食性が要求される。陰極容器10は
ナトリウム12に接するだけであるためSUS
304で十分な耐食性を持つ。その他の構成は第1
図の電池と同様である。 第8図に示した電池の陽極集電体15は、陽極
活物質に接する表面のみを本発明による合金試料
(第1表の合金試料5)で作成した薄膜で覆つた。
本実験では、0.2mm厚のパイプを合金試料5で作
成し、パイプ内に鉄製の棒をはめ込み、パイプと
鉄製の棒との電気的な接触を良好にするため、陽
極集電体15の上部、中部、下部の円周上を電子
ビームで溶接した。また下端は陽極活物質が内部
の鉄と接しないように、パイプ部を若干長くし
て、線状に押しつぶした後に溶接して、鉄製の棒
を陰極活物質から完全に保護した。 この第9図に示した高温電池を、上記試験と同
条件で450サイクルの充放電試験を実施したが、
上記試験の結果と容量特性、試験後の表面状態な
どまつたく同様の結果であつた。 以上の説明のように、本発明は陽極活物質によ
る陽極活物質容器、陽極集電体等の腐食を抑え、
高温電池の長寿命化をはかるものであり、その工
業的価値は非常に大なるものである。 なお本発明は、陽極活物質に接する部分に用い
る金属材料に係るものであり、その構造および使
用方法また被覆の方法に関しては限定されるもの
ではない。
[Table] From these results, the alloys of the present invention have extremely superior Na 2 S 3 resistance in terms of corrosion thickness and local corrosion, except for reference example Alloy 4, when compared with the reference example alloys. Next, the alloys of the present invention (Table 1 1, 2, 3, 4,
5 and 6), an anode active material container serving as an anode current collector as shown in 5 in FIG. 1 was prepared, a sodium-sulfur battery was assembled, and a charge/discharge cycle test was conducted. The test temperature was 350°C, and the discharge was performed for 3 hours at a rate of current (55 mA/cm 2 as the surface current density of the anode active material container) for 5 hours, and after a 10 minute break, the discharge amount reached 100% in 5 hours.
The charging/discharging conditions are such that one cycle consists of charging an amount of electricity and resting for 10 minutes. Changes in battery capacity with respect to cycles of batteries using each anode active material container up to 450 cycles and an investigation of the anode active material container after the test were conducted. FIG. 6 shows changes in battery capacity with respect to charge/discharge cycles of batteries using positive electrode active material containers made of alloy samples 1, 2, 3, 4, 5, and 6. Molybdenum and iron-chromium under similar test conditions
This is a good change in battery capacity compared to the results of batteries using a silicon alloy as the anode active material container (see FIGS. 3 and 5). Furthermore, the surface of the container 5 that was in contact with the anode active material after the test had no abnormalities in any of the alloy samples of the present invention, and had excellent corrosion resistance against the anode active material. FIG. 7 shows a photograph of alloy sample 2 as an example. On the other hand, when the surface of the molybdenum container battery that was in contact with the anode active material was examined, local corrosion had occurred as shown in FIG. Next, a battery having the structure shown in FIG. 9 was created. In the sodium-sulfur battery shown in FIG. 9, a solid electrolyte tube is filled with an anode active material 14, and the cathode and anode are reversed from those in the battery shown in FIG. The same reference numerals as in FIG. 1 have the same names, so explanations will be omitted. At the terminal 15 (anode current collector) inside the solid electrolyte tube,
In this case, corrosion resistance is required. Since the cathode container 10 is only in contact with sodium 12, it is made of SUS.
304 has sufficient corrosion resistance. Other configurations are first
It is similar to the battery shown in the figure. In the anode current collector 15 of the battery shown in FIG. 8, only the surface in contact with the anode active material was covered with a thin film made of an alloy sample according to the present invention (alloy sample 5 in Table 1).
In this experiment, a 0.2 mm thick pipe was made from alloy sample 5, and an iron rod was fitted into the pipe. , middle and bottom circumferences were welded using an electron beam. The lower end of the pipe was made slightly longer to prevent the anode active material from coming into contact with the iron inside, and was crushed into a wire and then welded to completely protect the iron rod from the cathode active material. The high temperature battery shown in Figure 9 was subjected to a 450 cycle charge/discharge test under the same conditions as the above test.
The results were exactly the same as those of the above test, including the capacity characteristics and the surface condition after the test. As explained above, the present invention suppresses corrosion of the anode active material container, anode current collector, etc. caused by the anode active material,
It aims to extend the life of high-temperature batteries, and its industrial value is extremely large. Note that the present invention relates to a metal material used for a portion in contact with an anode active material, and is not limited to its structure, method of use, or method of coating.

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

第1図は高温電池の縦断面図、第2図はSUS
304を陽極活物質容器に用いた電池の容量特性の
グラフ、第3図はモリブデンを陽極活物質容器に
用いた電池の部分放電サイクル容量特性のグラ
フ、第4図はモリブデンを陽極活物質容器に用い
た電池の完全放電サイクル容量特性のグラフ、第
5図は鉄−クロム−珪素合金を陽極活物質容器に
用いた電池の部分放電サイクル容量特性のグラ
フ、第6図は本発明による合金試料を陽極活物質
容器に用いた電池の部分放電サイクル容量特性の
グラフ、第7図aは合金試料2で作成した陽極活
物質容器を用いた電池の部分充放電試験後の陽極
活物質に接していた表面の金属組織の顕微鏡写
真、第7図bは同じく断面の金属組織の顕微鏡写
真、第8図aはモリブデンで作成した陽極活物質
容器を用いた電池の部分充放電試験後の陽極活物
質に接していた表面の金属組織の顕微鏡写真、第
8図bは同じく断面の金属組織の顕微鏡写真、第
9図は固体電解質管内を陽極とする電池の縦断面
図である。 1……陰極端子、2……陰極活物質、3……固
体電解質管、4……陽極活物質、5……陽極集電
体を兼ねた陽極活物質容器、6……陽極蓋、7…
…陰極蓋、8……絶縁リング、9……ガラス、1
0……陰極活物質容器、12……陰極活物質、1
4……陽極活物質、15……陽極端子(集電体)。
Figure 1 is a vertical cross-sectional view of a high-temperature battery, Figure 2 is a SUS
Figure 3 is a graph of the capacity characteristics of a battery using molybdenum as the anode active material container. Figure 4 is a graph of the partial discharge cycle capacity characteristics of a battery using molybdenum as the anode active material container. FIG. 5 is a graph of the full discharge cycle capacity characteristics of the battery used. FIG. 5 is a graph of the partial discharge cycle capacity characteristic of a battery using an iron-chromium-silicon alloy as the anode active material container. FIG. A graph of the partial discharge cycle capacity characteristics of the battery used in the positive electrode active material container, Figure 7a shows the characteristics of the positive electrode active material after the partial charge/discharge test of the battery using the positive electrode active material container prepared with Alloy Sample 2. Figure 7b is a micrograph of the metallographic structure on the surface, and Figure 8a is a micrograph of the metallographic structure of the cross section. Figure 8a is a photomicrograph of the anode active material after a partial charge/discharge test of a battery using a cathode active material container made of molybdenum. FIG. 8b is a microscopic photograph of the metallographic structure of the surfaces in contact with each other, FIG. 8b is a microscopic photograph of the metallographic structure of a cross section, and FIG. 9 is a longitudinal cross-sectional view of a battery with the inside of the solid electrolyte tube serving as an anode. DESCRIPTION OF SYMBOLS 1... Cathode terminal, 2... Cathode active material, 3... Solid electrolyte tube, 4... Anode active material, 5... Anode active material container that also serves as an anode current collector, 6... Anode lid, 7...
...Cathode lid, 8...Insulation ring, 9...Glass, 1
0... Cathode active material container, 12... Cathode active material, 1
4... Anode active material, 15... Anode terminal (current collector).

Claims (1)

【特許請求の範囲】 1 陽極活物質容器、陽極集電体の少なくとも陽
極活物質に接する表面を、Cr40〜60%、C0.02%
以下、N0.015%以下で残部が実質的に鉄よりな
る鉄クロム合金を使用したことを特徴とする高温
電池。 2 陽極活物質容器、陽極集電体の少なくとも陽
極活物質に接する表面を、Cr40〜60%、C0.02%
以下、N0.015%以下で、さらにTi、Nb、Zrのう
ちいずれか1種または2種以上を0.05〜1%含み
残部が実質的に鉄よりなる鉄クロム合金を使用し
たことを特徴とする高温電池。
[Claims] 1. At least the surface of the anode active material container and the anode current collector in contact with the anode active material is made of 40 to 60% Cr and 0.02% C.
The following is a high-temperature battery characterized by using an iron-chromium alloy containing 0.015% or less of N and the remainder being substantially iron. 2. At least the surface of the anode active material container and anode current collector in contact with the anode active material is made of 40 to 60% Cr and 0.02% C.
Hereinafter, it is characterized by using an iron-chromium alloy containing 0.015% or less of N, and further containing 0.05 to 1% of any one or more of Ti, Nb, and Zr, and the balance being substantially iron. high temperature battery.
JP57033034A 1982-03-04 1982-03-04 High-temperature battery Granted JPS58152379A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57033034A JPS58152379A (en) 1982-03-04 1982-03-04 High-temperature battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57033034A JPS58152379A (en) 1982-03-04 1982-03-04 High-temperature battery

Publications (2)

Publication Number Publication Date
JPS58152379A JPS58152379A (en) 1983-09-09
JPH0239065B2 true JPH0239065B2 (en) 1990-09-04

Family

ID=12375504

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57033034A Granted JPS58152379A (en) 1982-03-04 1982-03-04 High-temperature battery

Country Status (1)

Country Link
JP (1) JPS58152379A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH048671U (en) * 1990-05-14 1992-01-27

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61264659A (en) * 1985-05-20 1986-11-22 Nippon Steel Corp Sodium-sulfur battery cathode case and its manufacture
JPS62268069A (en) * 1986-05-14 1987-11-20 Yuasa Battery Co Ltd Battery and manufacture thereof

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5220226A (en) * 1975-08-09 1977-02-16 Tokyo Shibaura Electric Co Sodiummsulfur battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH048671U (en) * 1990-05-14 1992-01-27

Also Published As

Publication number Publication date
JPS58152379A (en) 1983-09-09

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