JPH02142066A - Sodium-sulphur cell - Google Patents

Sodium-sulphur cell

Info

Publication number
JPH02142066A
JPH02142066A JP63295847A JP29584788A JPH02142066A JP H02142066 A JPH02142066 A JP H02142066A JP 63295847 A JP63295847 A JP 63295847A JP 29584788 A JP29584788 A JP 29584788A JP H02142066 A JPH02142066 A JP H02142066A
Authority
JP
Japan
Prior art keywords
plating layer
sodium
container
corrosion
chromium
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.)
Granted
Application number
JP63295847A
Other languages
Japanese (ja)
Other versions
JP2574016B2 (en
Inventor
Nobuo Tsuno
伸夫 津野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP63295847A priority Critical patent/JP2574016B2/en
Publication of JPH02142066A publication Critical patent/JPH02142066A/en
Application granted granted Critical
Publication of JP2574016B2 publication Critical patent/JP2574016B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
    • H01M10/39—Accumulators not provided for in groups H01M10/05-H01M10/34 working at high temperature
    • H01M10/3909—Sodium-sulfur cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/124—Primary casings; Jackets or wrappings characterised by the material having a layered structure
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/116—Primary casings; Jackets or wrappings characterised by the material
    • H01M50/117—Inorganic material
    • H01M50/119—Metals
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/131—Primary casings; Jackets or wrappings characterised by physical properties, e.g. gas permeability, size or heat resistance
    • H01M50/133—Thickness
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/10—Primary casings; Jackets or wrappings
    • H01M50/14—Primary casings; Jackets or wrappings for protecting against damage caused by external factors
    • H01M50/145—Primary casings; Jackets or wrappings for protecting against damage caused by external factors for protecting against corrosion
    • 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

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

Abstract

PURPOSE:To improve the anticorrosive property of a cathode container by forming the cathode container to form a cathode chamber with an aluminum alloy such as an aluminum-manganese-chromium alloy or an aluminum- manganese alloy, and providing an anticorrosive membrane of a chromium plating layer at the inner surface of the container. CONSTITUTION:A cathode container 1 to form a cathode chamber R2 is formed of an aluminum alloy such as an aluminum-manganese-chromium alloy or an aluminum-manganese alloy, and an anticorrosive membrane of a chromium plating layer is provided at the inner surface of the container 1. That is, while the cathode container 1 is formed of an aluminum alloy, an anticorrosive membrane of a chromium plating layer whose cracking density is less increased even though the temperature is raised near the operational temperature of the cell is provided. As a result, the cathode container 1 is made lightweight, the anticorrosive property is improved, and the cell can bear the service for a long period.

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は陽極容器の耐久性を向上することができるナ
トリウム−硫黄電池に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a sodium-sulfur battery that can improve the durability of the anode container.

[従来の技術] 従来のナトリウム−VR貴電池として第2図に示すよう
に、陽極活物質である溶融硫黄Sを含浸したカーボンマ
ットなどの陽極用導電材Mを収納する円筒状の陽極容器
1と、該陽極容器1の上端部に対し、α−アルミナ製の
絶縁リング2を介して連結された陰極容器3と、前記絶
縁リング2の内周部に固着され、かつ、電極活物質であ
る溶融金属ナトリウムNaを貯留し、ナトリウムイオン
Na+を選択的に透過させる機能を有した下方へ延びる
多結晶β″−アルミナ製の有底円筒状をなす固体電解質
管4とから構成したものがある。
[Prior Art] As shown in FIG. 2, a conventional sodium-VR precious battery includes a cylindrical anode container 1 that houses a conductive material M for the anode, such as a carbon mat impregnated with molten sulfur S, which is an anode active material. A cathode container 3 is connected to the upper end of the anode container 1 via an insulating ring 2 made of α-alumina, and a cathode container 3 is fixed to the inner circumference of the insulating ring 2 and is an electrode active material. There is one constructed of a solid electrolyte tube 4 having a bottomed cylindrical shape made of polycrystalline β''-alumina and extending downward and having the function of storing molten metal sodium Na and selectively transmitting sodium ions Na+.

そして、放電時には陰極室R1からナトリウムイオンN
a+が固体電解質管4を透過して陽極室R2内の硫黄S
と次のように反応し、多硫化ナトリウムを生成する。
During discharge, sodium ions N from the cathode chamber R1
a+ passes through the solid electrolyte tube 4 and becomes sulfur S in the anode chamber R2.
The following reaction occurs with sodium polysulfide.

2Na+X5−Na1 Sx また、充電時には放電時とは逆の反応が起こり、多硫化
ナトリウムがナトリウムNa及び硫黄Sに分解する。
2Na+X5-Na1 Sx Furthermore, during charging, a reaction opposite to that during discharging occurs, and sodium polysulfide decomposes into sodium Na and sulfur S.

前記陽極容器1内には腐蝕性の高い溶融多硫化ナトリウ
ムが形成されるため、陽極容器1の材料を、耐腐蝕性の
高いステンレス鋼により形成していた。
Since highly corrosive molten sodium polysulfide is formed in the anode container 1, the material of the anode container 1 is made of highly corrosion-resistant stainless steel.

前記陽極容器の耐腐蝕特性を向上させる第1の従来例と
して特公昭54−293号公報に示すように、陽極容器
1の内周面に対し厚さ7μm以上のモリブテンまたはタ
ングステンの電解メッキを施して防蝕被膜を形成するも
のがあった。
As shown in Japanese Patent Publication No. 54-293 as a first conventional example for improving the corrosion resistance of the anode container, the inner peripheral surface of the anode container 1 is electrolytically plated with molybdenum or tungsten to a thickness of 7 μm or more. There were some that formed a corrosion-resistant coating.

また、第2の従来例として特公昭56−46233号公
報に示すように、陽極容器のステンレス鋼よりなる基材
にクロムメッキ層を形成したものが堤案されている。
Further, as a second conventional example, as shown in Japanese Patent Publication No. 56-46233, an anode container is proposed in which a chromium plating layer is formed on a base material made of stainless steel.

さらに、第3の従来例として特開昭62−276767
号公報に示すように、陽極容器1の内周面に対し、主成
分として鉄、ニッケル、コバルト、及びクロムを含む合
金よりなる防蝕被膜を施したものが開示されている。
Furthermore, as a third conventional example, Japanese Patent Application Laid-Open No. 62-276767
As shown in the publication, an anti-corrosion coating made of an alloy containing iron, nickel, cobalt, and chromium as main components is disclosed on the inner circumferential surface of an anode container 1.

[発明が解決しようとする課題] ところが、前述した第1の従来例はモリブテンまたはタ
ングステンの電解メッキ膜の安定性が不足しているため
、実用化されておらず、信頼性に欠けるという問題点が
あった。
[Problems to be Solved by the Invention] However, the first conventional example described above has not been put to practical use because the molybdenum or tungsten electrolytic plating film lacks stability, and there is a problem that it lacks reliability. was there.

また、第2の従来例は、クロムメッキ層に多数のInA
[IIなりラックが存在し、しかもクロムと基材のステ
ンレス鋼とは熱膨張係数が異なるため、昇温により前記
クラックの幅が増大しflit nU性が低下するとい
う問題があった。
In addition, the second conventional example has a large number of InA layers in the chromium plating layer.
[II] Since there is a rack and the coefficient of thermal expansion is different between chromium and stainless steel as the base material, there was a problem that the width of the crack increases with temperature rise and the flit nU property deteriorates.

さらに、第3の従来例は硫化物を形成し易い鉄をベース
とする合金を使用しているため、耐蝕性が劣り、長期の
使用に耐えないばかりでなく、陽極活物質の一部が前記
硫化物となるため、陽極活物質の有効利用が図れず、電
池効率が低下するという問題もあった。
Furthermore, since the third conventional example uses an iron-based alloy that easily forms sulfides, it has poor corrosion resistance and cannot withstand long-term use. Since it becomes a sulfide, the positive electrode active material cannot be used effectively, and there is also the problem that battery efficiency decreases.

この発明の目的は陽極容器の耐蝕性を向上して、陽極容
器が腐蝕により破口して陽極活物質が漏出する事故を未
然に防止することができるとともに、陽極活物質を有効
に利用して電池効率を向上することができるナトリウム
−硫黄電池を提供することにある。
The purpose of this invention is to improve the corrosion resistance of the anode container, to prevent accidents in which the anode container breaks due to corrosion and the anode active material leaks out, and to make effective use of the anode active material. An object of the present invention is to provide a sodium-sulfur battery that can improve battery efficiency.

[課題を解決するための手段] 請求項1記載の発明は、上記目的を達成するため、アル
カリイオン伝導性を有する固体電解質管により陽極室と
陰極室を区画形成し、陽極室内には溶融硫黄を収容し、
陰極室内にはナトリウムを収容したナトリウム−硫黄電
池において、前記陽極室を形成する陽極容器をアルミニ
ウム−マンガン−クロム合金又はアルミニウム−マンガ
ン合金などのアルミニウム合金により形成し、該陽極容
器の内表面に対し、クロムメッキ層からなる防蝕被膜を
設けている。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the invention as claimed in claim 1 divides an anode chamber and a cathode chamber by solid electrolyte tubes having alkali ion conductivity, and contains molten sulfur in the anode chamber. accommodates,
In a sodium-sulfur battery containing sodium in the cathode chamber, the anode container forming the anode chamber is formed of an aluminum alloy such as an aluminum-manganese-chromium alloy or an aluminum-manganese alloy, and the inner surface of the anode container is A corrosion-resistant coating consisting of a chrome plating layer is provided.

また、請求項2−3記載の発明は一前記防蝕被膜を非晶
質のクロムメッキ層、又は非晶質のクロムと炭素からな
るクロムメッキ層にするものである。
Further, the invention according to claims 2 to 3 is such that the corrosion-resistant coating is an amorphous chromium plating layer or a chromium plating layer consisting of amorphous chromium and carbon.

さらに、請求項4記載の発明は、前記防蝕被膜のクラッ
ク密度を2ゲ/ c m〜10ケcm程度にするもので
ある。
Furthermore, the invention as set forth in claim 4 is such that the crack density of the corrosion-resistant coating is approximately 2 g/cm to 10 g/cm.

さらにまた請求項5記載の発明は、前記防蝕被膜の厚さ
を、5〜50μmにするものである。
Furthermore, in a fifth aspect of the invention, the corrosion-resistant coating has a thickness of 5 to 50 μm.

[作 用] この発明は、陽極容器をアルミニウム合金により形成す
るとともに、該陽極容器の内周面に厚さが5〜50μm
で、かつクラック密度が2ゲ/cm〜10ゲ/ c m
であり、しかも電池の作動温度である350℃付近の温
度まで昇温してもクラック密度の増加が小さいクロムメ
ッキ層からなる防蝕被膜を設けたので、陽極容器が軽量
化されるとともに陽極容器の耐食性が向上し、長期間の
使用に耐えることができる。
[Function] In this invention, the anode container is formed of an aluminum alloy, and the inner peripheral surface of the anode container has a thickness of 5 to 50 μm.
and the crack density is 2ge/cm to 10ge/cm
In addition, we have provided a corrosion-resistant coating consisting of a chrome plating layer that exhibits a small increase in crack density even when the temperature rises to around 350°C, which is the operating temperature of the battery. Improved corrosion resistance and can withstand long-term use.

上記クラック密度の低減は、メッキ浴の温度やPHある
いは電流密度等のメッキ条件の調整、メッキ層の厚さあ
るいはアルミニウム容器の表面粗さの調整で行ってもよ
いし、多硫化ナトリウムに対する耐食性があり、しかも
クロムの電着応力を緩和することが可能な、炭素のよう
な材料をクロムメッキ層中に分散させることで達成して
もよい。
The crack density may be reduced by adjusting the plating conditions such as the temperature, pH, or current density of the plating bath, or by adjusting the thickness of the plating layer or the surface roughness of the aluminum container. This may be achieved by dispersing a material, such as carbon, in the chromium plating layer, which is also capable of relieving the stress of electrodeposition of chromium.

上記手段によりクラック密度を2ケ/ c m〜10ケ
/ c mとしたクロムメッキ層では、電池作動温度へ
の昇温に際し、アルミニウム容器とクロムとの熱膨張の
差に起因する応力が有効に緩和され、メッキ層中でのク
ラック発生が抑制されるので、クロムメッキ層の剥離が
防止されるとともに、陽極容器の耐食性が向上する。
In a chromium plating layer with a crack density of 2/cm to 10/cm by the above method, the stress caused by the difference in thermal expansion between the aluminum container and chromium is effectively absorbed when the temperature is raised to the battery operating temperature. This suppresses the occurrence of cracks in the plating layer, thereby preventing the chrome plating layer from peeling off and improving the corrosion resistance of the anode container.

また、クロムメツ−’r層中に分散させた炭素は、炭素
自身が多硫化ナトリウムに対する耐食性に優れているの
で、クロムと炭素からなるメッキ層も多硫化ナトリウム
に対する耐食性に優れている。
Further, since the carbon dispersed in the chrome metal layer has excellent corrosion resistance against sodium polysulfide, the plating layer made of chromium and carbon also has excellent corrosion resistance against sodium polysulfide.

さらにまた、メッキ層中の炭素は、メツ”rM中のクラ
ックの低減ばかりでなく、クロムメッキ層の非晶質化を
促進し、メッキ層の耐食性をさらに向上させる。
Furthermore, carbon in the plating layer not only reduces cracks in the metal, but also promotes amorphization of the chromium plating layer, further improving the corrosion resistance of the plating layer.

さらに、防蝕被膜の厚さを、5〜50μmにすることで
、クロムメッキ層中のクラック密度が減少するとともに
、電池作動温度への昇温によるクラック密度の増加も減
少するので、陽極容器の耐食性が向上し、長期間の使用
に耐えることができる。
Furthermore, by setting the thickness of the corrosion-resistant coating to 5 to 50 μm, the crack density in the chrome plating layer is reduced, and the increase in crack density due to temperature rise to the battery operating temperature is also reduced, thereby improving the corrosion resistance of the anode container. improved and can withstand long-term use.

[実施例] 以下、この発明を具体化した実施例を説明する。[Example] Hereinafter, embodiments embodying this invention will be described.

この実施例のナトリウム−硫黄電池の基本構成は、前述
した第2図に示す電池と同様であるため、本発明の要旨
である陽極容器1の材料及び陽極容器1の内周面に塗布
される防蝕被膜の組成、形成方法及びその特性などにつ
いて以下に詳述する。
The basic structure of the sodium-sulfur battery of this embodiment is the same as that of the battery shown in FIG. The composition, formation method, and characteristics of the corrosion-resistant coating will be described in detail below.

前記陽極容器1は密度が小さく、かつ電池の作動温度(
約350℃)で十分な機械的強度を備えたAl−Mn−
Cr合金又はAl−Mn合金などのアルミニウム合金に
より形成され、軽盟化を図っている。また、該陽極容器
1の内表面に対し、クロムメッキ層からなる防蝕被膜を
設けた。
The anode container 1 has a low density, and the operating temperature of the battery (
Al-Mn- with sufficient mechanical strength at about 350℃)
It is made of an aluminum alloy such as a Cr alloy or an Al-Mn alloy, and is intended to be lightweight. Furthermore, a corrosion-resistant coating consisting of a chrome plating layer was provided on the inner surface of the anode container 1.

表1 前記防蝕被膜の主成分として、クロムを選択した理由に
ついて述べる。
Table 1 The reason for selecting chromium as the main component of the corrosion-resistant coating will be described.

最初に、タンタル、ニオブ、鉄、アルミニウム、マクネ
シウム、並びにクロムの各材料から、直径:5曲、長さ
=30−の棒状試験片を作製し、組成がNaz S4で
ある溶融多硫化ナトリウム中に各試験片を浸漬して通電
試験を行った後、各試験片の重量減少量を測定した。し
かる後、各試験片の比重を用いて直径の減少量(減厚量
と称す)を算出し、得られた結果を第1図に示した0通
電試験は窒素雰囲気中で、350℃に加熱した多硫化ナ
トリウム中に各試験片を浸漬した後、各試験片に電流密
度:100mA/cjlの電流を500時間流して行っ
た。
First, rod-shaped specimens with a diameter of 5 curves and a length of 30 mm were prepared from tantalum, niobium, iron, aluminum, macnesium, and chromium, and were placed in molten sodium polysulfide having a composition of Naz S4. After each test piece was immersed and subjected to a current test, the amount of weight loss of each test piece was measured. After that, the amount of reduction in diameter (referred to as the amount of thickness reduction) was calculated using the specific gravity of each test piece, and the obtained results are shown in Figure 1. The zero current test was performed by heating to 350°C in a nitrogen atmosphere. After each test piece was immersed in sodium polysulfide, a current with a current density of 100 mA/cjl was passed through each test piece for 500 hours.

この第1図から明らかなように、今回試験した金属材料
の中では、クロムの腐蝕試験後の減少量が最も少なく、
耐蝕性に優れていることがわかる。
As is clear from Figure 1, among the metal materials tested this time, chromium showed the least amount of decrease after the corrosion test.
It can be seen that it has excellent corrosion resistance.

このため、多硫化ナトリウムに対する防蝕被膜としてク
ロムを選択した。しかし、金属クロムは脆いため、金属
クロムで陽極容器を形成することは困難である。陽極容
器は多硫化ナトリウムに接する表面が多硫化ナトリウム
対する耐蝕性を有していればよいので、アルミニウム合
金からなる陽極容器の内表面に薄いクロムメッキ層から
なる防蝕被膜を設けて本発明のように構成したのである
。
For this reason, chromium was selected as a corrosion-resistant coating for sodium polysulfide. However, since metallic chromium is brittle, it is difficult to form an anode container with metallic chromium. Since the surface of the anode container that comes into contact with sodium polysulfide only needs to have corrosion resistance against sodium polysulfide, a corrosion-resistant coating consisting of a thin chromium plating layer is provided on the inner surface of the anode container made of an aluminum alloy as in the present invention. It was constructed as follows.

防蝕被膜の組成としては、クロムメッキ層のみからなる
もの、クロムメッキ層とアルミニウム容器表面の間に両
者の中間の熱膨張係数を有する金属からなる1ffr層
を設けたもの、あるいは1〜5重量%の炭素と残部クロ
ムからなるメッキ層が好ましい、また、構造的には非晶
質構造を有するものがより好ましい。
The composition of the anti-corrosion coating is one consisting only of a chrome plating layer, one with a 1ffr layer made of a metal having a coefficient of thermal expansion between the two, or 1 to 5% by weight between the chrome plating layer and the aluminum container surface. A plating layer consisting of carbon and the remainder chromium is preferable, and a layer having an amorphous structure is more preferable.

次に、前掲した表1の三種類のクロムメッキ浴を使用し
てメッキを施した試験片について、該メッキ層断面中の
クラック数と、厚さとが、多硫化ナトリウムに対する耐
蝕性に及す影響を試験した結果、表2のようになった。
Next, regarding the test pieces plated using the three types of chromium plating baths listed in Table 1 above, we examined the effects of the number of cracks in the cross section of the plated layer and the thickness on the corrosion resistance against sodium polysulfide. The results of the test are shown in Table 2.

この試験では、まず直径:5市、長さ:3011s+の
アルミニウム合金製の丸棒の表面に、表1記載のメ・ツ
キ浴でクロムメッキをし、表2記載の試験片を作製した
6表1記載のメッキ浴No1.2は一日刊工業新聞社発
行「めっき技術便覧」第216頁記載の公知のメッキ浴
である。また、メッキ浴No3は、昭和61年8月12
日に公開された特開昭61−179890号公報に記載
の公知のメッキ浴である。これらの試験片について、メ
ッキ層断面中のクラック数をメッキしたままの状態と3
50°Cに加熱した後冷却した状態で測定し、得られた
結果を表2に示した。さらに、メッキしたままの状態の
各試験片を組成がNaz S4である溶融多硫化ナトリ
ウム中に浸漬して通電試験を行った後、各試験片の重量
減少量を測定した。しかる後、各試験片の比重を用いて
直径の減少J!(減厚i)を算出し、得られた結果を表
2に示した。
In this test, first, the surface of an aluminum alloy round bar with a diameter of 5 cm and a length of 3011s+ was plated with chrome in the metal coating bath listed in Table 1, and the test pieces listed in Table 2 were prepared. Plating bath No. 1.2 described in No. 1 is a known plating bath described on page 216 of "Plating Technology Handbook" published by Nikkan Kogyo Shimbun. In addition, plating bath No. 3 was released on August 12, 1986.
This is a known plating bath described in Japanese Patent Application Laid-open No. 179890/1989 published on 1986. Regarding these test pieces, the number of cracks in the cross section of the plated layer was determined between the as-plated state and 3.
Measurements were made after heating to 50°C and cooling, and the results are shown in Table 2. Further, each test piece in the as-plated state was immersed in molten sodium polysulfide having a composition of Naz S4 and subjected to an electrical current test, and then the amount of weight loss of each test piece was measured. After that, the specific gravity of each specimen is used to calculate the decrease in diameter J! (Thickness reduction i) was calculated and the obtained results are shown in Table 2.

通電試験は窒素雰囲気中で、350℃に加熱した多硫化
ナトリウム中に各試験片を浸漬した後、各試験片に電流
密度:100mA/−の電流を500時間流して行った
。
The current test was performed by immersing each test piece in sodium polysulfide heated to 350° C. in a nitrogen atmosphere, and then passing a current at a current density of 100 mA/− through each test piece for 500 hours.

表2 クラックの単位二ケ/■ 表2記載の結果から明らかなように、試!’IN0゜1
〜3の試験片は多硫化ナトリウムによる1z帥か大きい
。これは、試@No、1〜3の試験片のクロムメツ−]
?層は、メッキのままの状態で、すでにメッキ層中に多
数のクラックが存在するとともに、350℃への加熱に
よりクラック密度がさらに増加しているためである。な
お、ここでいう、クラック密度はクロムメッキ層断面の
単位長さ(1cll)当りの貫通りラック数である。ま
た、試験N。
Table 2 Crack unit 2/■ As is clear from the results listed in Table 2, the test! 'IN0゜1
-3 test specimens are 1 z or more large with sodium polysulfide. This is the chrome metal of test @ No. 1 to 3 test pieces]
? This is because a large number of cracks already exist in the plated layer in the plated state, and the crack density further increases due to heating to 350°C. Note that the crack density referred to here is the number of racks penetrated per unit length (1 cll) of the cross section of the chrome plating layer. Also, test N.

4〜6の試験片では、メッキ厚さが厚くなるにつれてク
ラック数が減少するとともに、多硫化ナトリウムによる
腐蝕が減少する。この傾向は、メッキ厚さが10μmの
試験片(No、6)において特に顕著である。さらにま
た、試験N017〜12の試験片のうち、試験N088
〜11の試験片において、多硫化ナトリウムによる腐蝕
が著しく減少した。これは、試験No、8〜11の試験
片のクロムメッキ層は、メッキのままの状態でクラック
密度が小さいうえ、腐蝕試験温度である350℃へ加熱
してもクラック密度が大きく増大しないためである、し
かし、このメッキ層は、厚さが5μm未満ではクラック
密度が小さくても(試fiNo、7)−多硫化ナトリウ
ムによる腐蝕量が大きい、また、メッキ厚さが大きくな
りすぎて、50μmを越えるとクラック密度の増加が起
こり(試験No、12>、耐食性が低下する。このよう
に、試験No、7〜12のメッキ層はメッキ厚さが5μ
m未満と50μm以上では、多硫化ナトリウムに対する
耐蝕性がメッキ厚さ5μm〜50μmの場合に比べて明
らかに劣っている。
In test specimens 4 to 6, as the plating thickness increases, the number of cracks decreases and corrosion due to sodium polysulfide decreases. This tendency is particularly remarkable in the test piece (No. 6) with a plating thickness of 10 μm. Furthermore, among the test pieces of Tests N017 to 12, Test No.
Sodium polysulfide corrosion was significantly reduced in ~11 specimens. This is because the chromium plating layer of test pieces No. 8 to 11 has a small crack density in the as-plated state, and the crack density does not increase significantly even when heated to 350°C, which is the corrosion test temperature. However, if the thickness of this plating layer is less than 5 μm, even if the crack density is small (Test fi No. 7) - the amount of corrosion due to sodium polysulfide is large, and the plating thickness becomes too large, If the thickness exceeds 5 μm, the crack density will increase (Test No. 12>, corrosion resistance will decrease.)
When the plating thickness is less than 50 μm or more than 50 μm, the corrosion resistance against sodium polysulfide is clearly inferior to that when the plating thickness is 5 μm to 50 μm.

表2の結果にもとづき、各試験片の多硫化ナトリウムに
対する耐蝕性を、クロムメッキ層中のクラック密度とメ
ッキ厚さとの関係で考察すると、メッキ層断面中のクラ
ック密度が1ケ/am以下(No、7)ならびに25ケ
/cs以上(No、12)では、多硫化ナトリウム中で
の腐食試験後の減厚量が増加しているので、これらの試
験片ではクロムメッキ層の耐蝕性が低下していることが
わかる。
Based on the results in Table 2, when considering the corrosion resistance of each test piece against sodium polysulfide in terms of the relationship between the crack density in the chrome plating layer and the plating thickness, it is found that the crack density in the cross section of the plating layer is 1 ke/am or less ( For No. 7) and 25 pieces/cs or more (No. 12), the amount of thickness reduction after the corrosion test in sodium polysulfide increases, so the corrosion resistance of the chrome plating layer decreases in these test pieces. I know what you're doing.

クラック密度は、前述したように多すぎても逆に少なす
ぎても良くない、クラック密度が小さすぎる場合には、
メッキ層中に残留しているt着応力の緩和が不十分なこ
とが多い、この場合には、電池作動温度への昇温時にア
ルミニウムとクロムの熱膨張係数の差により発生ずる熱
応力と上記残留電着応力のため、メッキ層に多数のクラ
ックが発生し、耐蝕性を低下させる。一方、クラック密
度が多すぎる場合には、メッキ層の防蝕被膜としての作
用が低下し、耐食性が低下する。
As mentioned above, the crack density is neither too high nor too low.If the crack density is too low,
The relaxation of the adhesion stress remaining in the plating layer is often insufficient.In this case, the thermal stress generated due to the difference in the thermal expansion coefficients of aluminum and chromium when the temperature is raised to the battery operating temperature and the above-mentioned Due to residual electrodeposition stress, many cracks occur in the plating layer, reducing corrosion resistance. On the other hand, if the crack density is too high, the action of the plating layer as a corrosion-preventing film will be reduced, and the corrosion resistance will be reduced.

なお、試@No、9.10のクロムメッキ層の組成分析
と結晶構造の解析を行い、これらのメツ−1rJttl
が非晶質で、しかもクロムと炭素から構成されているこ
とが確認された。このことから、ナトリウム−硫黄電池
の陽極活物質を収容する陽極容器の内表面にクロムと炭
素からなる非晶質のクロムメッキ層を形成することが好
ましいことがわかる。 次に、防蝕被膜の厚さとその電
池容量の関係について実験した。
In addition, we analyzed the composition and crystal structure of the chromium plating layer of test @ No. 9.10, and these results
was confirmed to be amorphous and composed of chromium and carbon. This shows that it is preferable to form an amorphous chromium plating layer made of chromium and carbon on the inner surface of the anode container housing the anode active material of the sodium-sulfur battery. Next, we conducted an experiment to determine the relationship between the thickness of the corrosion-resistant coating and its battery capacity.

外径:38mm、内径=36浦で有底のアルミニウム合
金(J I 5−A5003)製のパイプ内面に、クロ
ムメッキを行い、表3記載のメッキ厚さとクラック密度
を有するパイプを作製した。また。
The inner surface of an aluminum alloy (J I 5-A5003) pipe with an outer diameter of 38 mm and an inner diameter of 36 pores and a bottom was plated with chrome to produce a pipe having the plating thickness and crack density shown in Table 3. Also.

比較のため、メッキ厚さとクラック密度が本発明の範囲
外のパイプを作製した。該パイプを使用して固体電解質
管がナトリウムイオン、陽極活物質がグラファイトに含
浸させた硫黄、陰極活物質が溶融ナトリウムからなるナ
トリウム−硫黄電池を作製した。この電池を使用して作
動温度:350℃で1000サイクルの充放電試験を繰
り返し、電池容量の変化を測定した結果を表3に示す。
For comparison, a pipe was produced whose plating thickness and crack density were outside the range of the present invention. Using this pipe, a sodium-sulfur battery was fabricated in which the solid electrolyte tube is sodium ions, the anode active material is sulfur impregnated with graphite, and the cathode active material is molten sodium. Using this battery, a charge/discharge test was repeated for 1000 cycles at an operating temperature of 350° C., and changes in battery capacity were measured. Table 3 shows the results.

この表3から明らかなごとく、厚さが5μm〜50μm
、クラック密度が2ケ/ c m〜10ゲ/cmである
メッキ層を有する容器で組み立てた電池では、1000
サイクルの充放電試験後も80%以上の高い電池容量を
有しており、陽極活物質が電池反応に有効に活用されて
いる。
As is clear from Table 3, the thickness is 5 μm to 50 μm.
, for a battery assembled in a container with a plating layer with a crack density of 2 ge/cm to 10 ge/cm, 1000
The battery has a high battery capacity of more than 80% even after a cycle charge-discharge test, and the anode active material is effectively utilized for battery reactions.

これに対し、厚さとクラック密度が本発明の範囲外であ
るメッキ層を有する容器で組み立てた比較例の電池では
、1000サイクルの充放電試験後の電池容量の低下が
大きい、これは比較例の電池では、容器の腐蝕が起こり
、陽極活物質が容器の腐蝕反応に消費され、陽極活1勿
質が減少したためである。
On the other hand, in a comparative example battery assembled with a container having a plating layer whose thickness and crack density are outside the range of the present invention, the battery capacity decreased significantly after 1000 cycles of charge/discharge test. This is because the container of the battery corrodes, and the anode active material is consumed by the corrosion reaction of the container, resulting in a decrease in the anode active material.

表3 (以下余白) [発明の効果] 以上詳述したように、この発明は陽極容器の耐蝕性を向
上して、陽極容器が腐蝕により破口して陽極活物質が漏
出する事故を未然に防止することができるとともに、陽
極活物質を!効に利用して電池効率を向上することがで
きる効果がある。
Table 3 (blank space below) [Effects of the invention] As detailed above, this invention improves the corrosion resistance of the anode container and prevents accidents in which the anode container ruptures due to corrosion and the anode active material leaks. Can be prevented along with the anode active material! This has the effect that battery efficiency can be improved by using it effectively.

また、クロムと炭素からなるクロムメッキ層は多硫化ナ
トリウムに対する耐蝕性に優れ、組成中の炭素はクロム
メッキ層中のクラ:・iりの低減とクロムメッキ層の非
晶質化を促進し耐久性を向上することができる効果があ
る。
In addition, the chrome plating layer, which is composed of chromium and carbon, has excellent corrosion resistance against sodium polysulfide, and the carbon in the composition promotes the reduction of cracks in the chrome plating layer and the amorphization of the chrome plating layer, making it durable. It has the effect of improving sex.

また、前記防蝕被膜のクラック密度、を2ゲ/cm〜1
0ケ/ c mにすると、電池加熱時の膨張収縮による
応力の吸収が適正に行われ、クロムメッキ層の剥離や耐
腐蝕性を向上することができる。
In addition, the crack density of the corrosion-resistant coating is 2ge/cm to 1
When it is 0 pieces/cm, the stress caused by expansion and contraction during battery heating can be properly absorbed, and the peeling and corrosion resistance of the chromium plating layer can be improved.

さらに、防蝕被膜の厚さを、5〜50μmにすると、耐
蝕性が向上し、長期間の使用に耐えることができる効果
がある。
Furthermore, when the thickness of the corrosion-resistant coating is set to 5 to 50 μm, corrosion resistance is improved and the product can withstand long-term use.

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

第1図は各種の金属材料と平均腐蝕減摩量との関係を示
すグラフ、第2図は従来のナトリウム−硫黄電池の一例
を示す中央部縦断面図である。 1・・・陽極容器、2・・・絶縁リング、3・・・陰極
容器、4・・・固体電解質管、M・・・陽極用導電材、
R1・・・n庫室、R2・・・陽極室。 特許出願人     日本硝子 株式会社代理人 弁理
士   恩1)博宣
FIG. 1 is a graph showing the relationship between various metal materials and the average amount of corrosion and friction reduction, and FIG. 2 is a longitudinal sectional view of the central part of an example of a conventional sodium-sulfur battery. DESCRIPTION OF SYMBOLS 1... Anode container, 2... Insulating ring, 3... Cathode container, 4... Solid electrolyte tube, M... Conductive material for anode,
R1...n storage room, R2...anode room. Patent applicant Nippon Glass Co., Ltd. Agent Patent attorney On 1) Hironobu

Claims (1)

【特許請求の範囲】 1、アルカリイオン伝導性を有する固体電解質管により
陽極室と陰極室を区画形成し、陽極室内には溶融硫黄を
収容し、陰極室内にはナトリウムを収容したナトリウム
−硫黄電池において、前記陽極室を形成する陽極容器を
アルミニウム−マンガン−クロム合金又はアルミニウム
−マンガン合金などのアルミニウム合金により形成し、
該陽極容器の内表面に対し、クロムメッキ層からなる防
蝕被膜を設けたことを特徴とするナトリウム−硫黄電池
。 2、前記防蝕被膜は、非晶質のクロムメッキ層である請
求項1記載のナトリウム−硫黄電池。 3、前記防蝕被膜は非晶質のクロムと炭素からなるメッ
キ層である請求項1又は請求項2記載のナトリウム−硫
黄電池。 4、前記防蝕被膜のクラック密度が2ケ/cm〜10ケ
/cmである請求項1〜請求項3のいづれかに記載のナ
トリウム−硫黄電池。 5、前記防蝕被膜の厚さは、5〜50μmである請求項
1〜請求項4のいづれかに記載のナトリウム−硫黄電池
。
[Claims] 1. A sodium-sulfur battery in which an anode chamber and a cathode chamber are partitioned by solid electrolyte tubes having alkali ion conductivity, the anode chamber contains molten sulfur, and the cathode chamber contains sodium. wherein the anode container forming the anode chamber is formed of an aluminum alloy such as an aluminum-manganese-chromium alloy or an aluminum-manganese alloy;
A sodium-sulfur battery characterized in that an anti-corrosion coating consisting of a chrome plating layer is provided on the inner surface of the anode container. 2. The sodium-sulfur battery according to claim 1, wherein the anti-corrosion coating is an amorphous chromium plating layer. 3. The sodium-sulfur battery according to claim 1 or 2, wherein the anti-corrosion coating is a plating layer made of amorphous chromium and carbon. 4. The sodium-sulfur battery according to any one of claims 1 to 3, wherein the corrosion-resistant coating has a crack density of 2 cracks/cm to 10 cracks/cm. 5. The sodium-sulfur battery according to any one of claims 1 to 4, wherein the corrosion-resistant coating has a thickness of 5 to 50 μm.
JP63295847A 1988-11-22 1988-11-22 Sodium-sulfur battery Expired - Lifetime JP2574016B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63295847A JP2574016B2 (en) 1988-11-22 1988-11-22 Sodium-sulfur battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63295847A JP2574016B2 (en) 1988-11-22 1988-11-22 Sodium-sulfur battery

Publications (2)

Publication Number Publication Date
JPH02142066A true JPH02142066A (en) 1990-05-31
JP2574016B2 JP2574016B2 (en) 1997-01-22

Family

ID=17825957

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63295847A Expired - Lifetime JP2574016B2 (en) 1988-11-22 1988-11-22 Sodium-sulfur battery

Country Status (1)

Country Link
JP (1) JP2574016B2 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51124635A (en) * 1975-04-18 1976-10-30 Stauffer Chemical Co Plated metal product and production method therefor
JPS542228A (en) * 1977-06-03 1979-01-09 Ford Motor Co Method of plating lighttweigh metal capable of improving corrosion resistivity in transverse direction
JPS5646233A (en) * 1979-09-20 1981-04-27 Canon Inc Preparation of photoconductor particle

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51124635A (en) * 1975-04-18 1976-10-30 Stauffer Chemical Co Plated metal product and production method therefor
JPS542228A (en) * 1977-06-03 1979-01-09 Ford Motor Co Method of plating lighttweigh metal capable of improving corrosion resistivity in transverse direction
JPS5646233A (en) * 1979-09-20 1981-04-27 Canon Inc Preparation of photoconductor particle

Also Published As

Publication number Publication date
JP2574016B2 (en) 1997-01-22

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