JPH0351066B2 - - Google Patents

Info

Publication number
JPH0351066B2
JPH0351066B2 JP58203255A JP20325583A JPH0351066B2 JP H0351066 B2 JPH0351066 B2 JP H0351066B2 JP 58203255 A JP58203255 A JP 58203255A JP 20325583 A JP20325583 A JP 20325583A JP H0351066 B2 JPH0351066 B2 JP H0351066B2
Authority
JP
Japan
Prior art keywords
anode
sodium
sulfur
solid electrolyte
molten
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
JP58203255A
Other languages
Japanese (ja)
Other versions
JPS6095864A (en
Inventor
Hisamitsu Hato
Hiroyuki Kawamoto
Hajime Wada
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP58203255A priority Critical patent/JPS6095864A/en
Publication of JPS6095864A publication Critical patent/JPS6095864A/en
Publication of JPH0351066B2 publication Critical patent/JPH0351066B2/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
    • 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

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Secondary Cells (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明はナトリウム−硫黄電池に係り、特に陰
極活物質の溶融ナトリウム、陽極活物質に炭素繊
維に含浸させた溶融硫黄、電解質に固体電解質が
使用されているナトリウム−硫黄電池に関するも
のである。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention relates to a sodium-sulfur battery, and in particular uses molten sodium as a cathode active material, molten sulfur impregnated with carbon fiber as an anode active material, and a solid electrolyte as an electrolyte. This relates to a sodium-sulfur battery.

〔発明の背景〕[Background of the invention]

ナトリウム−硫黄電池はナトリウムイオンのみ
を通過させる固体電解質を介して一方に陰極活物
質である溶融ナトリウム、他方に陽極活物質であ
る溶融硫黄が設けられ、約300から350℃で充放電
が行なわれる高温二次電池である。この充放電反
応は 2Na+xS放電 ――→ ←―― 充電Na2Sx で、放電時には陰極活物質のナトリウムNaは電
子を遊離してナトリウムイオンとなり、固体電解
質の隔壁を通過して陽極活物質の硫黄Sと反応
し、多硫化ナトリウムNa2Sxを生成する。そし
て充電時には電池の開路電圧より大きな負電圧を
付加することにより、多硫化ナトリウムNa2Sx
はナトリウムNaと硫黄Sに分離される。
Sodium-sulfur batteries have molten sodium, the cathode active material, on one side and molten sulfur, the anode active material, on the other side, through a solid electrolyte that allows only sodium ions to pass through, and are charged and discharged at approximately 300 to 350 degrees Celsius. It is a high temperature secondary battery. This charging/discharging reaction is 2Na + xS discharge ---> ← -- Charged Na 2 Sx. During discharge, sodium Na in the cathode active material liberates electrons and becomes sodium ions, which pass through the partition wall of the solid electrolyte and form sulfur in the anode active material. Reacts with S to produce sodium polysulfide, Na 2 Sx. Then, during charging, by applying a negative voltage greater than the open circuit voltage of the battery, sodium polysulfide Na 2 Sx
is separated into sodium Na and sulfur S.

第1図にはこの種ナトリウム−硫黄電池の従来
例が示されている。同図に示されているようにナ
トリウム−硫黄電池は、管状の固体電解質1の内
側に陰極活物質の溶融ナトリウム2が充填され、
外側に陽極活物質の溶融硫黄3が充填されて構成
されているが、この溶融硫黄3は電子伝導性がな
いので、電子伝導性を付与するために多孔質の炭
素繊維4に含浸されている。この溶融硫黄3を密
封する陽極容器5および溶融ナトリウム2を密封
する陰極容器6は夫々電極としての機能を有して
おり、これら陽極容器5と陰極容器6とは絶縁材
であるα−アルミナ7で絶縁して接続されてい
る。そして陽極容器5に設けられた陽極キヤツプ
8も、陰極容器6に設けられた陰極キヤツプ9も
共に、陰極容器6,5と、同様に電極としての機
能を有しており、溶融ナトリウム2中に挿入され
た多孔質の金属繊維10は、固体電解質1が破損
した場合の溶融ナトリウム2と溶融硫黄3との急
激な発熱反応を防止するための溶融ナトリウム2
の保持材としての機能を有している。そしてまた
陰極キヤツプ9には陰極容器6内にナトリウムを
注入するナトリウム注入管11が設けられてい
る。なお同図において2aは溶融ナトリウム2お
よび金属繊維10等を有する陰極である。
FIG. 1 shows a conventional example of this type of sodium-sulfur battery. As shown in the figure, the sodium-sulfur battery has a tubular solid electrolyte 1 filled with molten sodium 2 as a cathode active material.
The outside is filled with molten sulfur 3, which is an anode active material, but since this molten sulfur 3 has no electronic conductivity, it is impregnated into porous carbon fibers 4 to impart electronic conductivity. . The anode container 5 that seals the molten sulfur 3 and the cathode container 6 that seals the molten sodium 2 each have a function as an electrode. are insulated and connected. The anode cap 8 provided in the anode container 5 and the cathode cap 9 provided in the cathode container 6 both have the function of electrodes in the same way as the cathode containers 6 and 5. The inserted porous metal fibers 10 serve as molten sodium 2 to prevent a rapid exothermic reaction between molten sodium 2 and molten sulfur 3 in the event that the solid electrolyte 1 is damaged.
It has the function of a holding material. The cathode cap 9 is also provided with a sodium injection tube 11 for injecting sodium into the cathode container 6. In the figure, 2a is a cathode having molten sodium 2, metal fibers 10, and the like.

このように構成されたナトリウム−硫黄電池で
溶融硫黄3を含浸した炭素繊維4を有する陽極3
aにおける反応率を円筒座標系で解析した結果
が、横軸に陽極3aの厚さをとり、縦軸に陽極3
aの反応率をとつて陽極3aの厚さによる反応率
の変化特性が示されている第2図に示されてい
る。同図に示されているように固体電解質側Pお
よび金属の陽極容器側Qの反応率が高く不均一で
あつたが、固体電解質側Pの反応率が高いと次の
ような不具合を生じる。放電時には固体電解質側
Pの陽極は反応率が高いため融点の高い、絶縁性
を有する多硫化ナトリウムNa2Sx(x≦3)が固
体電解質側Pの陽極中に生成され、固体電解質側
Pの陽極に絶縁層を形成し、放電容量を低下させ
る。充電時に放電によつて生成された多硫化ナト
リウムNa2SxがナトリウムNaと硫黄Sとに分離
するが、こほ分離現象は反応率の高い固体電解質
側Pが顕著で、固体電解質側Pの陽極中に電子伝
導性のない溶融硫黄Sが多く生成され、充電容量
を低下させる。
Anode 3 having carbon fiber 4 impregnated with molten sulfur 3 in a sodium-sulfur battery constructed in this way
The result of analyzing the reaction rate at a in a cylindrical coordinate system is the thickness of the anode 3a on the horizontal axis and the thickness of the anode 3a on the vertical axis.
FIG. 2 shows the change characteristics of the reaction rate depending on the thickness of the anode 3a, taking the reaction rate of a. As shown in the figure, the reaction rates on the solid electrolyte side P and the metal anode container side Q were high and non-uniform; however, if the reaction rate on the solid electrolyte side P is high, the following problems occur. During discharge, the anode on the solid electrolyte side P has a high reaction rate, so sodium polysulfide Na 2 Sx (x≦3), which has a high melting point and has insulating properties, is generated in the anode on the solid electrolyte side P. An insulating layer is formed on the anode to reduce discharge capacity. Sodium polysulfide Na 2 Sx generated by discharging during charging separates into sodium Na and sulfur S, but this separation phenomenon is noticeable on the solid electrolyte side P where the reaction rate is high, and the anode on the solid electrolyte side P A large amount of molten sulfur S, which has no electronic conductivity, is generated inside the battery, reducing the charging capacity.

これらのことは理論容量56Ahのナトリウム−
硫黄電池について横軸に充放電量をとり、縦軸に
端子電圧をとつて充放電量と端子電圧との関係を
検討した第3図からも明らかである。すなわち放
電時の特性を示した放電時特性曲線Aで放電容量
50Ah近傍で電圧が急激に低下している。これは
上述のように放電時に形成される絶縁性を有する
多硫化ナトリウムNa2Sx(x≦3)が、反応率の
高い固体電解質側の陽極中に形成されるためで、
このために電池の放電容量が低下する。そして充
電時の特性を示した充電特性曲線Bで充電容量
30Ah近傍で電圧が急激に上昇している。これは
多硫化ナトリウムNa2Sxの単相域から多硫化ナ
トリウムNa2Sxと溶融硫黄Sとの2相域になる
付近、すなわち30Ah近傍で反応率の高い固体電
解質側に溶融硫黄Sの絶縁層が形成され、陽極中
の内部抵抗が急激に大きくなつたためである。
These things are true for sodium with a theoretical capacity of 56Ah.
This is also clear from FIG. 3, which examines the relationship between the charge and discharge amount and the terminal voltage for a sulfur battery, with the horizontal axis representing the charge and discharge amount and the vertical axis representing the terminal voltage. In other words, the discharge capacity is determined by the discharge characteristic curve A that shows the discharge characteristics.
The voltage drops rapidly near 50Ah. This is because, as mentioned above, the insulating sodium polysulfide Na 2 Sx (x≦3) formed during discharge is formed in the anode on the solid electrolyte side, where the reaction rate is high.
This reduces the discharge capacity of the battery. Then, the charging capacity is determined by charging characteristic curve B, which shows the characteristics during charging.
The voltage increases rapidly near 30Ah. This occurs near the point where the single-phase region of sodium polysulfide Na 2 Sx changes to the two-phase region of sodium polysulfide Na 2 Sx and molten sulfur S, that is, near 30 Ah, an insulating layer of molten sulfur S is formed on the solid electrolyte side with a high reaction rate. was formed, and the internal resistance in the anode suddenly increased.

〔発明の目的〕[Purpose of the invention]

本発明は以上の点に鑑みなされたものであり、
充放電効率の向上を可能としたナトリウム−硫黄
電池を提供することを目的とするものである。
The present invention has been made in view of the above points,
The object of the present invention is to provide a sodium-sulfur battery that can improve charging and discharging efficiency.

〔発明の概要〕[Summary of the invention]

すなわち本発明は陰極活物質を有する陰極およ
び陽極活物質を有する陽極と、これらの間に配置
された固体電解質とを備え、陰極活物質には溶融
ナトリウムが使用され、陽極活物質には炭素繊維
に含浸した溶融硫黄が使用されているナトリウム
−硫黄電池において、陽極と固体電解質との間
に、溶融硫黄を含浸した炭素繊維のそれより大き
な表面積を有する炭素繊維を設けたことを特徴と
するものであり、これによつて固体電解質の炭素
繊維の表面積比すなわち溶融硫黄を含浸した炭素
繊維とこの炭素繊維より大きな表面積を有する炭
素繊維との表面積比が小さくなる。
That is, the present invention includes a cathode having a cathode active material, an anode having an anode active material, and a solid electrolyte disposed between them, in which molten sodium is used as the cathode active material, and carbon fiber is used as the anode active material. A sodium-sulfur battery using molten sulfur impregnated with molten sulfur, characterized in that a carbon fiber having a surface area larger than that of the carbon fiber impregnated with molten sulfur is provided between the anode and the solid electrolyte. As a result, the surface area ratio of the carbon fibers of the solid electrolyte, that is, the surface area ratio of the carbon fibers impregnated with molten sulfur to the carbon fibers having a larger surface area than the carbon fibers becomes smaller.

ナトリウム−硫黄電池の充放電効率を向上させ
るに当つて溶融硫黄を含浸させている炭素繊維に
着目した。そして陽極中の固体電解質側に表面積
の大きな炭素繊維を設け、これと溶融硫黄を含浸
させている表面積の小さな炭素繊維との比、すな
わち表面積比を変えて陽極の固体電解質側の反応
率を検討した。検討結果は縦軸に陽極の固体電解
質側の反応率をとり、横軸に炭素繊維の表面積比
をとつて炭素繊維の表面積比による反応率の変化
特性が示されている第4図に示されているよう
に、表面積比が小さくなるほど陽極の固体電解質
側の反応率は小さくなつている。そこでこの結果
を基に陽極の固体電解質側に溶融硫黄を含浸して
いる炭素繊維より大きな表面積の炭素繊維を設け
て電池をつくり、陽極の厚さによる陽極の反応率
を円筒座標系で解析検討した。検討結果は横軸に
陽極の厚さをとり、縦軸に陽極の反応率をとつて
陽極の厚さによる反応率の変化特性が示されてい
る第5図に示されているように、固体電解質側P
の反応率が低下しており、反応率が従来よりも均
一化しているのが認められた。これらのことから
陽極の固体電解質側に表面積の大きな炭素繊維を
設け、溶融硫黄を含浸している炭素繊維との表面
積比を小さくしてやれば陽極の固体電解質側の反
応率が低下でき、反応率が均一化できることが確
かめられた。そこで本発明では陽極と固体電解質
との間に、溶融硫黄を含浸した炭素繊維より表面
積の大きな炭素繊維を設けた。このようにするこ
とにより充放電効率の向上を可能としたナトリウ
ム−硫黄電池を得ることを可能としたものであ
る。
In order to improve the charging and discharging efficiency of sodium-sulfur batteries, we focused on carbon fibers impregnated with molten sulfur. Next, carbon fibers with a large surface area are provided on the solid electrolyte side of the anode, and the reaction rate on the solid electrolyte side of the anode is examined by changing the ratio of carbon fibers with a small surface area impregnated with molten sulfur, that is, the surface area ratio. did. The results of the study are shown in Figure 4, which plots the reaction rate on the solid electrolyte side of the anode on the vertical axis and the surface area ratio of the carbon fiber on the horizontal axis, and shows the change characteristics of the reaction rate depending on the surface area ratio of the carbon fiber. As shown, the smaller the surface area ratio, the smaller the reaction rate on the solid electrolyte side of the anode. Based on this result, we fabricated a battery by installing carbon fiber with a larger surface area than the carbon fiber impregnated with molten sulfur on the solid electrolyte side of the anode, and analyzed the reaction rate of the anode depending on the thickness of the anode using a cylindrical coordinate system. did. The study results are as shown in Figure 5, where the horizontal axis shows the anode thickness and the vertical axis shows the reaction rate of the anode. Electrolyte side P
It was observed that the reaction rate had decreased and the reaction rate was more uniform than before. For these reasons, by providing carbon fibers with a large surface area on the solid electrolyte side of the anode and reducing the surface area ratio with the carbon fibers impregnated with molten sulfur, the reaction rate on the solid electrolyte side of the anode can be reduced. It was confirmed that uniformity could be achieved. Therefore, in the present invention, carbon fibers having a larger surface area than carbon fibers impregnated with molten sulfur are provided between the anode and the solid electrolyte. By doing so, it is possible to obtain a sodium-sulfur battery with improved charging and discharging efficiency.

〔発明の実施例〕[Embodiments of the invention]

以下、図示した実施例に基づいて本発明を説明
する。第6図には本発明の一実施例が示されてい
る。なお従来と同じ部品には同じ符号を付したの
で説明を省略する。本実施例では陽極3aと固体
電解質1との間に、溶融硫黄3を含浸した炭素繊
維4のそれより大きな表面積を有する炭素繊維1
2を設けた。このようにすることにより陽極3a
の固体電解質1側の炭素繊維4,12の表面積比
が小さくなつて、充放電効率の向上を可能とした
ナトリウム−硫黄電池を得ることができる。
The present invention will be explained below based on the illustrated embodiments. FIG. 6 shows an embodiment of the invention. Note that parts that are the same as those in the conventional system are given the same reference numerals, and therefore their explanations will be omitted. In this embodiment, a carbon fiber 1 having a surface area larger than that of the carbon fiber 4 impregnated with molten sulfur 3 is placed between the anode 3a and the solid electrolyte 1.
2 was established. By doing this, the anode 3a
Since the surface area ratio of the carbon fibers 4 and 12 on the solid electrolyte 1 side is reduced, it is possible to obtain a sodium-sulfur battery in which charging and discharging efficiency can be improved.

このことは陽極3aの固体電解質1側に表面積
の大きな炭素繊維12を設けてつくつた理論容量
56Ahのナトリウム−硫黄電池について、その充
放電量と端子電圧との関係を検討した結果からも
明らかである。検討結果は縦軸に端子電圧をと
り、横軸に充放電量をとつて示した第7図に示さ
れているように放電時においては、放電特性曲線
A0に示されているように56Ahまで端子電圧の大
きな低下は認められず、また充電時においては、
充電特性曲線B0に示されているように2相液に
なる30Ah近傍においても従来のように端子電圧
の上昇が認められなかつた。このように良好な充
放電量特性を示したのは陽極の固体電解質側の反
応率が低下し、陽極の反応率が均一化したためで
ある。すなわち放電時には反応率の均一化により
融点が高く、絶縁性を有する多硫化ナトリウム
Na2Sx(x≦3)の生成時期が遅れ、放電容量が
向上する。そして充電時には反応率の均一化によ
り電子伝導性のない溶融硫黄Sが局部的に生成さ
れて、固体電解質側の陽極に絶縁層を形成するこ
とがなくなり、充電容量が向上する。
This is due to the theoretical capacity created by providing the carbon fiber 12 with a large surface area on the solid electrolyte 1 side of the anode 3a.
This is clear from the results of examining the relationship between the charge/discharge amount and terminal voltage for a 56Ah sodium-sulfur battery. The study results are shown in Figure 7, where the vertical axis shows the terminal voltage and the horizontal axis shows the amount of charge and discharge.During discharging, the discharge characteristic curve
As shown in A 0 , no significant drop in terminal voltage was observed up to 56Ah, and during charging,
As shown in the charging characteristic curve B0 , even near 30Ah where the liquid becomes a two-phase liquid, no increase in terminal voltage was observed as in the conventional case. The reason why such good charge/discharge characteristics were exhibited is that the reaction rate on the solid electrolyte side of the anode decreased and the reaction rate of the anode became uniform. In other words, sodium polysulfide has a high melting point and insulating properties due to uniform reaction rate during discharge.
The generation time of Na 2 Sx (x≦3) is delayed, and the discharge capacity is improved. During charging, molten sulfur S having no electron conductivity is locally generated due to uniformity of the reaction rate, and an insulating layer is no longer formed on the anode on the solid electrolyte side, thereby improving the charging capacity.

〔発明の効果〕〔Effect of the invention〕

上述のように本発明は陽極の反応率が均一化す
るようになつて、充放電容量が向上するようにな
り、充放電効率の向上を可能としたナトリウム−
硫黄電池を得ることができる。
As mentioned above, in the present invention, the reaction rate of the anode becomes uniform, the charge/discharge capacity improves, and the sodium-containing material improves the charge/discharge efficiency.
You can get sulfur batteries.

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

第1図は従来のナトリウム−硫黄電池の縦断側
面図、第2図は従来のナトリウム−硫黄電池の陽
極の厚さと陽極の反応率との関係を示す特性図、
第3図は従来のナトリウム−硫黄電池の充放電量
と端子電圧との関係を示す特性図、第4図はナト
リウム−硫黄電池の表面積の大きい炭素繊維と表
面積の小さな炭素繊維との表面積比による陽極の
固体電解質側の反応率の変化特性図、第5図はナ
トリウム−硫黄電池の陽極の固体電解質側に表面
積の大きい炭素繊維を設けた場合の陽極の厚さと
陽極の反応率との関係を示す特性図、第6図は本
発明のナトリウム−硫黄電池の一実施例の縦断側
面図、第7図は同じく一実施例の充放電量と端子
電圧との関係を示す特性図である。 1……固体電解質、2……溶融ナトリウム、2
a……陰極、3……溶融硫黄、3a……陽極、4
……溶融硫黄を含浸した炭素繊維、5……陽極容
器、6……陰極容器、7……α−アルミナ、10
……金属繊維、12……表面積の大きな炭素繊
維。
FIG. 1 is a longitudinal side view of a conventional sodium-sulfur battery, and FIG. 2 is a characteristic diagram showing the relationship between the thickness of the anode and the reaction rate of the anode in a conventional sodium-sulfur battery.
Figure 3 is a characteristic diagram showing the relationship between the charge/discharge amount and terminal voltage of a conventional sodium-sulfur battery, and Figure 4 shows the surface area ratio between carbon fibers with a large surface area and carbon fibers with a small surface area in a sodium-sulfur battery. Figure 5 shows the relationship between the thickness of the anode and the reaction rate of the anode when carbon fiber with a large surface area is provided on the solid electrolyte side of the anode of a sodium-sulfur battery. FIG. 6 is a longitudinal cross-sectional side view of one embodiment of the sodium-sulfur battery of the present invention, and FIG. 7 is a characteristic diagram showing the relationship between charge/discharge amount and terminal voltage of the same embodiment. 1... Solid electrolyte, 2... Molten sodium, 2
a... cathode, 3... molten sulfur, 3a... anode, 4
... Carbon fiber impregnated with molten sulfur, 5 ... Anode container, 6 ... Cathode container, 7 ... α-alumina, 10
...Metal fiber, 12...Carbon fiber with a large surface area.

Claims (1)

【特許請求の範囲】 1 陰極活物質を有する陰極および陽極活物質を
有する陽極と、これらの間に配置された固体電解
質とを備え、前記陰極活物質には溶融ナトリウム
が使用され、前記陽極活物質には炭素繊維に含浸
した溶融硫黄が使用されているナトリウム−硫黄
電池において、前記陽極と前記固体電解質との間
に、前記溶融硫黄を含浸した炭素繊維のそれより
大きな表面積を有する炭素繊維を設けたことを特
徴とするナトリウム−硫黄電池。 2 前記溶融硫黄を含浸した炭素繊維が、合成繊
維を約2000℃で焼成して形成されたものである特
許請求の範囲第1項記載のナトリウム−硫黄電
池。 3 前記表面積の大きな炭素繊維が、合成繊維を
約800℃以下で焼成して形成されたものである特
許請求の範囲第1項記載のナトリウム−硫黄電
池。
[Scope of Claims] 1 Comprising a cathode having a cathode active material, an anode having an anode active material, and a solid electrolyte disposed between them, molten sodium is used for the cathode active material, and the anode active material In a sodium-sulfur battery in which molten sulfur impregnated with carbon fiber is used as a material, a carbon fiber having a surface area larger than that of the carbon fiber impregnated with molten sulfur is provided between the anode and the solid electrolyte. A sodium-sulfur battery characterized by comprising: 2. The sodium-sulfur battery according to claim 1, wherein the carbon fiber impregnated with molten sulfur is formed by firing synthetic fiber at about 2000°C. 3. The sodium-sulfur battery according to claim 1, wherein the carbon fiber with a large surface area is formed by firing synthetic fiber at about 800° C. or lower.
JP58203255A 1983-10-28 1983-10-28 Sodium-sulfur battery Granted JPS6095864A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58203255A JPS6095864A (en) 1983-10-28 1983-10-28 Sodium-sulfur battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58203255A JPS6095864A (en) 1983-10-28 1983-10-28 Sodium-sulfur battery

Publications (2)

Publication Number Publication Date
JPS6095864A JPS6095864A (en) 1985-05-29
JPH0351066B2 true JPH0351066B2 (en) 1991-08-05

Family

ID=16470992

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58203255A Granted JPS6095864A (en) 1983-10-28 1983-10-28 Sodium-sulfur battery

Country Status (1)

Country Link
JP (1) JPS6095864A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4011473A1 (en) 2020-12-11 2022-06-15 ARKRAY, Inc. Method for measurement of hemoglobin

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01253170A (en) * 1988-03-31 1989-10-09 Ngk Insulators Ltd Sodium-surfur battery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5024411A (en) * 1973-07-04 1975-03-15

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4011473A1 (en) 2020-12-11 2022-06-15 ARKRAY, Inc. Method for measurement of hemoglobin

Also Published As

Publication number Publication date
JPS6095864A (en) 1985-05-29

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