JPH0624149B2 - Beta-alumina solid electrolyte - Google Patents
Beta-alumina solid electrolyteInfo
- Publication number
- JPH0624149B2 JPH0624149B2 JP1301584A JP30158489A JPH0624149B2 JP H0624149 B2 JPH0624149 B2 JP H0624149B2 JP 1301584 A JP1301584 A JP 1301584A JP 30158489 A JP30158489 A JP 30158489A JP H0624149 B2 JPH0624149 B2 JP H0624149B2
- Authority
- JP
- Japan
- Prior art keywords
- alumina
- beta
- solid electrolyte
- sodium
- crystal
- 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
Links
- 229910000873 Beta-alumina solid electrolyte Inorganic materials 0.000 title claims description 37
- 239000002043 β-alumina solid electrolyte Substances 0.000 title claims description 17
- 239000013078 crystal Substances 0.000 claims description 34
- BNOODXBBXFZASF-UHFFFAOYSA-N [Na].[S] Chemical compound [Na].[S] BNOODXBBXFZASF-UHFFFAOYSA-N 0.000 claims description 16
- 229910001415 sodium ion Inorganic materials 0.000 description 19
- 239000011734 sodium Substances 0.000 description 15
- 239000000203 mixture Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 238000010304 firing Methods 0.000 description 8
- 239000002245 particle Substances 0.000 description 8
- RPMPQTVHEJVLCR-UHFFFAOYSA-N pentaaluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Na+].[Al+3].[Al+3].[Al+3].[Al+3].[Al+3] RPMPQTVHEJVLCR-UHFFFAOYSA-N 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 7
- 238000001354 calcination Methods 0.000 description 7
- 238000005259 measurement Methods 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 239000007784 solid electrolyte Substances 0.000 description 6
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 5
- 238000000227 grinding Methods 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 239000002002 slurry Substances 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 238000009472 formulation Methods 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 238000005245 sintering Methods 0.000 description 3
- 239000006183 anode active material Substances 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012212 insulator Substances 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 239000011268 mixed slurry Substances 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000011164 primary particle Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- HYHCSLBZRBJJCH-UHFFFAOYSA-N sodium polysulfide Chemical compound [Na+].S HYHCSLBZRBJJCH-UHFFFAOYSA-N 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000001238 wet grinding Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006182 cathode active material Substances 0.000 description 1
- 238000012669 compression test Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007921 spray 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
- 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
- H01M10/3918—Sodium-sulfur cells characterised by the electrolyte
-
- 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
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Compositions Of Oxide Ceramics (AREA)
- Secondary Cells (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、ナトリウム−硫黄電池用のベータアルミナ固
体電解質に関するものであり、特にベータアルミナ結晶
のC軸方向の結晶配向率を制御することにより、機械的
強度および化学的耐久性が優れ、電気抵抗の低いベータ
アルミナ固体電解質に関する。TECHNICAL FIELD The present invention relates to a beta-alumina solid electrolyte for sodium-sulfur batteries, and in particular, by controlling the crystal orientation ratio of the beta-alumina crystal in the C-axis direction. Relates to a beta-alumina solid electrolyte having excellent mechanical strength and chemical durability and low electric resistance.
[従来の技術] ナトリウム−硫黄電池用の固体電解質として一般的にβ
アルミナあるいはβ″アルミナが知られ、その応用が考
えられている。特にβ″アルミナはその本質的にNaイオ
ン道電率が高い(Naイオン伝導抵抗率が低い)ことか
ら、袋管形状等の構造体でナトリウム硫黄電池に適用さ
れている。[Prior Art] Generally β as a solid electrolyte for sodium-sulfur batteries.
Alumina or β ″ alumina is known, and its application is considered. Especially, β ″ alumina has a high Na ion conductivity (low Na ion conductivity resistivity), so that it can be used in a bag shape or the like. The structure is applied to sodium-sulfur battery.
ナトリウム−硫黄電池は、一方の陰極活物質である溶融
金属ナトリウム、他方には陽極活物質である溶融硫黄を
配し、両者をナトリウムイオンに対して選択的な透過性
を有するベータアルミナ固体電解質で隔離し、300〜
350℃で作動させる高温二次電池である。A sodium-sulfur battery is a beta-alumina solid electrolyte in which molten metal sodium, which is one cathode active material, and molten sulfur, which is an anode active material, are arranged on the other side, and which are both selectively permeable to sodium ions. Isolate, 300 ~
It is a high temperature secondary battery operated at 350 ° C.
このようなナトリウム−硫黄電池の構成は、例えば第3
図に示すように、陽極活物質である溶融硫黄Sを含浸し
たカーボンフェルト等の陽極用導電材1を収容する円筒
状の陽極容器2と、該陽極容器2の上端部と例えばアル
ファアルミナ製の絶縁体リング3を介して連結され且つ
溶融金属ナトリウムNaを貯留する陰極容器4と、前記絶
縁体リング3の内周部に接合され且つナトリウムイオン
Na+を選択的に通過させる機能を有する有低円筒状のベ
ースアルミナ管5とからなっている。また前記陰極容器
4の上蓋6の中央部には、陰極容器4を通して下方向に
ベータアルミナ管5の底部付近まで伸びた陰極管7が貫
通支持されている。The structure of such a sodium-sulfur battery is, for example, the third one.
As shown in the figure, a cylindrical anode container 2 for containing a conductive material 1 for anode such as carbon felt impregnated with molten sulfur S which is an anode active material, an upper end portion of the anode container 2 and, for example, alpha alumina A cathode container 4 that is connected through an insulator ring 3 and stores molten metal sodium Na, and is joined to the inner peripheral portion of the insulator ring 3 and has sodium ions
The base alumina tube 5 has a cylindrical shape with a function of allowing Na + to selectively pass therethrough. A cathode tube 7 extending downward through the cathode container 4 to near the bottom of the beta-alumina tube 5 is penetratingly supported in the central portion of the upper lid 6 of the cathode container 4.
以上のような構成を有するナトリウム−硫黄電池におい
て、放電時には溶融金属ナトリウムは電子を放出してナ
トリウムイオンとなり、これがベータアルミナ固体電解
質中を通過して陽極側に移動し、陽極の硫黄と外部回路
を通ってきた電子と反応して多硫化ナトリウムを生成
し、2ボルト程度の電圧を発生する。充電時には充電と
は逆に多硫化ナトリウムよりナトリウム及び硫黄の生成
反応が起こる。In the sodium-sulfur battery having the above structure, when discharged, molten metal sodium emits electrons to become sodium ions, which pass through the beta-alumina solid electrolyte and move to the anode side, and sulfur of the anode and the external circuit. It reacts with the electrons that have passed through it to produce sodium polysulfide, generating a voltage of about 2 volts. Contrary to charging, the reaction of forming sodium and sulfur from sodium polysulfide occurs during charging.
このようなナトリウム−硫黄電池において、ベータアル
ミナ電解質は極めて重要な役割を果たしているものであ
る。このベータアルミナをナトリウム−硫黄電池に適用
するための種々の研究がなされている。例えば、ナトリ
ウム−硫黄電池は、内部抵抗により電池としての効率が
決まり、内部抵抗の低いほど効率が高く、一般にナトリ
ウム−硫黄電池の内部抵抗に占める固体電解質の寄与は
約40%あると云われている。従って、ナトリウム−硫
黄電池に要するベータアルミナ固体電解質にあっては、
その内部抵抗を低減することが実用上必須である。In such a sodium-sulfur battery, the beta-alumina electrolyte plays a very important role. Various studies have been conducted for applying this beta alumina to a sodium-sulfur battery. For example, in a sodium-sulfur battery, the efficiency as a battery is determined by the internal resistance. The lower the internal resistance, the higher the efficiency. Generally, it is said that the solid electrolyte contributes about 40% to the internal resistance of the sodium-sulfur battery. There is. Therefore, in the beta-alumina solid electrolyte required for the sodium-sulfur battery,
It is practically essential to reduce the internal resistance.
この対策として、従来、電気伝導性の高い組成を探索す
ること、あるいは焼成条件を制御することにより個々の
結晶を大きくすることが行なわれてきた。As a countermeasure against this, conventionally, a search has been made for a composition having high electric conductivity, or an individual crystal has been enlarged by controlling firing conditions.
[発明が解決しようとする課題] しかしながら、上記した電気伝導性の高い組成は不安定
で化学的な耐久性に欠ける。また、個々の結晶粒が大き
くなると機械的強度が低下するなどの問題があった。[Problems to be Solved by the Invention] However, the above-mentioned composition having high electric conductivity is unstable and lacks chemical durability. In addition, there is a problem that the mechanical strength decreases as the size of each crystal grain increases.
[課題を解決するための手段] そこで、本発明者は、上記従来のベータアルミナ固体電
解質における問題を解決し、従来のセラミックスの特性
を維持し機械的強度及び化学的耐久性が優れ、且つ内部
抵抗の低い固体電解質を開発すべく種々検討を重ねた結
果、本発明を完成したものである。[Means for Solving the Problems] Therefore, the present inventor has solved the problems in the above-described conventional beta-alumina solid electrolyte, maintains the characteristics of conventional ceramics, has excellent mechanical strength and chemical durability, and As a result of various studies to develop a solid electrolyte having low resistance, the present invention has been completed.
即ち、本発明によれば、ナトリウム−硫黄電池用のベー
タアルミナ固体電解質において、0.22〜0.44の
範囲に制御されたC軸結晶配向率を有するベータアルミ
ナ固体電解質が提供される。That is, according to the present invention, there is provided a beta-alumina solid electrolyte for a sodium-sulfur battery, the beta-alumina solid electrolyte having a C-axis crystal orientation ratio controlled in the range of 0.22 to 0.44.
[作用] 本発明では、ベータアルミア固体電解質の結晶のC軸配
向率を0.22〜0.44の範囲に制御することを特徴
とする。[Operation] The present invention is characterized by controlling the C-axis orientation ratio of the crystals of the beta-alumina solid electrolyte within the range of 0.22 to 0.44.
このようにベータアルミナ固体電解質の結晶のC軸配向
率を制御することにより、機械的強度および化学的耐久
性が高く、しかも固体電解質の内部抵抗の低い優れた性
質を備えることができる。By controlling the C-axis orientation ratio of the crystals of the beta-alumina solid electrolyte in this manner, excellent properties such as high mechanical strength and chemical durability and low internal resistance of the solid electrolyte can be provided.
ベータアルミナ結晶は結晶形態が六方晶系に属し、第1
図のベータアルミナ固体電解質の単結晶の概要図に示す
如く、単一の結晶ではA軸とB軸で形成される面内(A
B面)にNaイオン導電面を有し、その垂直方向であるC
軸方向には全く導電性を示さない。また、結晶はNaイオ
ン導電面(AB面)で劈開性があるため、C軸方向の引
張に対して機械的強度が低く、一方水分々子はNaイオン
と置換してAB面内へ進入するため、AB面方向の化学
的耐久性が低いという特性を有している。Beta-alumina crystal belongs to hexagonal crystal form and
As shown in the schematic diagram of the single crystal of the beta-alumina solid electrolyte in the figure, the in-plane formed by the A axis and the B axis (A
B surface) has a Na ion conductive surface, which is the vertical direction C
It has no conductivity in the axial direction. Further, since the crystal has a cleavability on the Na ion conductive surface (AB surface), the mechanical strength is low with respect to the tension in the C-axis direction, while the water droplets replace Na ions and enter the AB surface. Therefore, it has a characteristic that the chemical durability in the AB plane direction is low.
また、ナトリウム−硫黄電池を構成するベータアルミナ
固体電解質としては、結晶の成長方向の関係から、これ
らの性質を持った単一結晶を緻密に焼結させた多結晶焼
結体の構造体を用いている。上記のような異方性を持つ
ベータアルミナ結晶の多結晶焼結体を構造体に適用する
場合、構造体としての機械的強度、電気特性あるいは化
学的な耐久性は個々のベータアルミナ結晶の特性が重要
であることは勿論、個々のベータアルミナの結晶の向き
が重要である。In addition, as the beta-alumina solid electrolyte constituting the sodium-sulfur battery, a structure of a polycrystalline sintered body obtained by densely sintering a single crystal having these properties is used because of the relationship of the crystal growth direction. ing. When applying a polycrystalline sintered body of beta-alumina crystals having anisotropy as described above to a structure, the mechanical strength, electrical characteristics or chemical durability of the structure are the characteristics of the individual beta-alumina crystals. Is important, as is the crystal orientation of the individual beta-alumina.
本発明は、これらの結晶の方向を一定範囲内に制御する
ことによって、従来のセラミックスの特性を維持し、且
つ内部抵抗の低いベータアルミナ固体電解質を得るもの
である。The present invention is to obtain a beta-alumina solid electrolyte that maintains the characteristics of conventional ceramics and has a low internal resistance by controlling the directions of these crystals within a certain range.
なお、多結晶構造体のベータアルミナ結晶の方向性は以
下の測定方法で実施した。The orientation of beta-alumina crystals of the polycrystalline structure was measured by the following measuring method.
一定のNa2O,MgO,Al2O3組成となる調合物を後述する実施
例の種々の成形方法で円筒体形状に作成し、一定条件で
焼結し円筒体の焼結体を得た。これらの円筒体焼結体か
ら第2図に示すように同軸円筒体の長手方向に幅1mmで
長さ40mmの試験片を作成し、外面の凹凸の影響を除外す
るため、同軸円筒体の径方向に垂直となるように外表面
を数100 μm研磨した。X線解析装置を用いて上記方法
で作成した試験片の外表面の回析パターンを測定するこ
とにより同軸円筒体の径方向に向いたの各結晶面相対量
を算出した。Formulations of Na 2 O, MgO, and Al 2 O 3 having a constant composition were formed into a cylindrical shape by various molding methods in Examples described later, and sintered under a constant condition to obtain a sintered body of the cylindrical body. . As shown in Fig. 2, a test piece with a width of 1 mm and a length of 40 mm was made in the longitudinal direction of the coaxial cylindrical body from these sintered bodies, and the diameter of the coaxial cylindrical body was changed to exclude the influence of irregularities on the outer surface. The outer surface was polished by several 100 μm so as to be perpendicular to the direction. The relative amount of each crystal plane in the radial direction of the coaxial cylinder was calculated by measuring the diffraction pattern of the outer surface of the test piece prepared by the above method using an X-ray analyzer.
測定はゴニオメーター式X線解析装置を使用した。CuK
α1の特性X線を使用し、加速電圧35kv、陰極電流20mA
で回析パターンをチャートに記録した。測定結果はベー
タアルミナ結晶のC軸と一定角度(0,33.3,60,90゜)を
なす結晶面についてそれぞれのピーク高さを実測し、各
結晶面の占める割合を相対値で表した。ベータアルミナ
結晶の各結晶面の相対量の換算方法を表1に示す。For the measurement, a goniometer type X-ray analyzer was used. CuK
Using characteristic X-ray of α 1 , acceleration voltage 35kv, cathode current 20mA
The diffraction pattern was recorded on a chart. The measurement results were obtained by actually measuring the peak heights of the crystal planes forming a constant angle (0,33.3,60,90 °) with the C axis of the beta-alumina crystal, and expressing the proportion occupied by each crystal plane as a relative value. Table 1 shows a method of converting the relative amount of each crystal face of the beta-alumina crystal.
本発明において、C軸配向率とは上記の表1におけるC
軸と結晶面の角度が0となりC軸に一致するH1の全ピ
ーク高さに占める相対高さをいう。即ち、C軸配向率が
高いことは、ベータアルミナ管のNaイオン導電方向に対
して、ベータアルミナ結晶の非導電面が向くために、ベ
ータアルミナ管としての抵抗が高いことを意味してい
る。 In the present invention, the C-axis orientation rate means C in Table 1 above.
It is the relative height of the total peak height of H 1 that coincides with the C axis when the angle between the axis and the crystal plane becomes 0. That is, a high C-axis orientation ratio means that the resistance of the beta alumina tube is high because the non-conductive surface of the beta alumina crystal faces the Na ion conductive direction of the beta alumina tube.
本発明で述べるベータアルミナとは、β−アルミナ(Na
2O・11Al2O3)とβ″−アルミナ(Na2O・5Al2O3),
β−アルミナ、β′−アルミナを含むものである。Beta alumina described in the present invention means β-alumina (Na
2 O · 11Al 2 O 3 ) and β ″ -alumina (Na 2 O / 5Al 2 O 3 ),
It contains β-alumina and β'-alumina.
[実施例] 以下、本発明を実施例に基き、さらに詳細に説明する
が、本発明はこれら実施例に限られるものではない。[Examples] Hereinafter, the present invention will be described in more detail based on Examples, but the present invention is not limited to these Examples.
(実施例1〜29及び比較例1〜11) 焼結体のベータアルミナ結晶の配向率は、成形体を作成
する際の一次粒子の配列によるものと考えられるため、
一次粒子の大きさ及び成形時の加圧方法を変更した焼結
体を種々作成した。(Examples 1 to 29 and Comparative Examples 1 to 11) The orientation rate of the beta-alumina crystals of the sintered body is considered to be due to the arrangement of the primary particles when forming the molded body,
Various sintered bodies were prepared by changing the size of the primary particles and the pressing method during molding.
[β″−アルミナ多結晶構造体の成形方法A] 原料として、Al2O3源にはα−Al2O3、Na2O源にはNa2CO3、
MgO源にはMgO の所定量を計量し、ボール・ミル中で水
分50% で30分間の湿式混合を実施しβ″−アルミナ組成
の調合物を作成した。[Β ″ -Alumina Polycrystalline Structure Forming Method A] As raw materials, Al 2 O 3 source is α-Al 2 O 3 , Na 2 O source is Na 2 CO 3 , and
A predetermined amount of MgO was measured as the MgO source, and wet mixing was carried out in a ball mill at a water content of 50% for 30 minutes to prepare a β ″ -alumina composition formulation.
混合後の泥漿を乾燥した後、煉瓦質の坩堝に詰め、電気
炉を使用して最高温度1100〜1400℃の空気雰囲
気中で2時間仮焼した。仮焼後の粉体をボール・ミル中
で湿式粉砕を実施し、粉砕時間を変更することにより種
々の平均粒度の泥漿を作成した。After the mixed slurry was dried, it was packed in a brick crucible and calcined for 2 hours in an air atmosphere having a maximum temperature of 1100 to 1400 ° C using an electric furnace. Wet grinding of the powder after calcination was carried out in a ball mill, and slurry having various average particle sizes was prepared by changing the grinding time.
ここで、焼結体のβ″−アルミナ固体電解質の結晶配向
率を変更するため、β″−アルミナ組成調合物の最高仮
焼温度と仮焼粉体の混合粉砕時間を変更した。最高仮焼
温度と混合粉砕時間を変更して得られた仮焼粉末の泥漿
中の平均粒度を表2に示す。平均粒度は50重量%とな
る粒子径で示した。Here, in order to change the crystal orientation ratio of the β ″ -alumina solid electrolyte of the sintered body, the maximum calcination temperature of the β ″ -alumina composition preparation and the mixing and grinding time of the calcined powder were changed. Table 2 shows the average particle size in the slurry of the calcined powder obtained by changing the maximum calcining temperature and the mixing and grinding time. The average particle size is shown by the particle size of 50% by weight.
その後、バインダーとしてエチレングリコールを2%添
加しスプレードヤライヤーで造粒した。得られた造粒粉
体を所定形状のゴム型に装填し、ラバープレスにて加圧
力2t/cm2で加圧成形して所定形状の成形体を得た。 Then, 2% of ethylene glycol was added as a binder and granulated with a spray drier. The obtained granulated powder was loaded into a rubber mold having a predetermined shape and pressure-molded with a rubber press at a pressing force of 2 t / cm 2 to obtain a molded body having a predetermined shape.
この成形体を焼成条件aとして最高温度1500℃、焼
成条件bとして最高温度1575℃、焼成条件cとして
最高温度1650℃で焼成して所定形状の焼結体を得
た。The compact was fired at a maximum temperature of 1500 ° C. as a firing condition a, a maximum temperature of 1575 ° C. as a firing condition b, and a maximum temperature of 1650 ° C. as a firing condition c to obtain a sintered body having a predetermined shape.
[β″−アルミナ多結晶構造体の成形方法B] 原料として、Al2O3源にはα-Al2O3、Na2O源には Na2C
O3、MgO 源にはMgOの所定量を計量し、ボール・ミル中
で水分50%で30分間の湿式混合を実施したβ″−ア
ルミナ組成の調合物を作成した。As a raw material - [beta "molding method B alumina polycrystalline structure, the the Al 2 O 3 source α-Al 2 O 3, Na 2 O source Na 2 C
A predetermined amount of MgO was measured as a source of O 3 and MgO, and wet blending was performed in a ball mill at a water content of 50% for 30 minutes to prepare a β ″ -alumina composition formulation.
混合後の泥漿を乾燥した後、高純度アルミナ煉瓦質の坩
堝に詰め、電気炉を使用した最高温度1100〜140
0℃の空気雰囲気中で2時間仮焼を実施した。仮焼後の
粉体をボール・ミル中で湿式粉砕を実施し、粉砕時間を
変更することにより種々の平均粒度の泥漿を作成した。After the mixed slurry is dried, it is packed in a high-purity alumina brick crucible and the maximum temperature is 1100 to 140 using an electric furnace.
Calcination was performed for 2 hours in an air atmosphere at 0 ° C. Wet grinding of the powder after calcination was carried out in a ball mill, and slurry having various average particle sizes was prepared by changing the grinding time.
ここで、焼結体のβ″結晶配向率を変更するため、β″
−アルミナ組成調合物の最高仮焼温度と仮焼粉砕泥漿の
加圧鋳込み圧力を変更した。最高仮焼温度と混合粉砕時
間を変更して得られた仮焼粉体の泥漿中の平均粒度を表
3に示す。平均粒度は50重量%となる粒子径で示し
た。Here, in order to change the β ″ crystal orientation ratio of the sintered body, β ″
-The maximum calcining temperature of the alumina composition formulation and the pressure pouring pressure of the calcined ground sludge were changed. Table 3 shows the average particle size in the slurry of the calcined powder obtained by changing the maximum calcination temperature and the mixing and grinding time. The average particle size is shown by the particle size of 50% by weight.
その後、エチレングリコールを2%添加し、泥漿水分を
40重量%に調製し、10〜30Kg/cm2の圧力で通気性
樹脂型に加圧鋳込みして所定形状の成形体を作成した。 Then, 2% of ethylene glycol was added to adjust the water content of the slurry to 40% by weight, and the mixture was pressure-cast into a breathable resin mold at a pressure of 10 to 30 kg / cm 2 to prepare a molded product having a predetermined shape.
この成形体を乾燥後、焼成条件aとして最高温度150
0℃、焼成条件bとして最高温度1575℃、焼成条件
cとして最高温度1650℃で焼成し所定形状の焼結体
を得た。After drying this molded body, a maximum temperature of 150 was set as the firing condition a.
The sintered body was fired at 0 ° C., a maximum temperature of 1575 ° C. as the firing condition b, and a maximum temperature of 1650 ° C. as the firing condition c to obtain a sintered body having a predetermined shape.
上記の成形方法A及びBで得られた焼結体の各特性を測
定した。測定結果を表4に示した。Each characteristic of the sintered body obtained by the above-mentioned molding methods A and B was measured. The measurement results are shown in Table 4.
なお、表4において、Naイオン伝導抵抗率、機械的強
度、水分吸着量の測定方法は下記方法によって行なっ
た。また、C軸結晶配向率については前述した通りであ
る。In Table 4, the methods for measuring Na ion conductivity resistivity, mechanical strength, and water adsorption amount were as follows. The C-axis crystal orientation ratio is as described above.
また、表4中の判定欄の○は機械的強度、水分吸着量を
従来レベルに維持し、Naイオン伝導抵抗率の低下が可能
な組合せを、△は機械的強度、水分吸着量が従来に比較
して悪化するもののNaイオン伝導抵抗率が低下する組合
せを、×はNaイオン伝導抵抗率が低下しない組合せを表
わす。In addition, in the judgment column in Table 4, ○ indicates a combination that can maintain the mechanical strength and the amount of adsorbed water at the conventional level and decrease the Na ion conductivity resistivity, and Δ indicates that the mechanical strength and the adsorbed amount of the water are the same. A combination that deteriorates in comparison but decreases in Na ion conduction resistivity, and a cross represents a combination in which Na ion conduction resistivity does not decrease.
[Naイオン伝導抵抗率の測定方法] 上記の方法により、種々の焼成条件で焼結した袋管状即
ち有低円筒体の径方向のNaイオン伝導抵抗率を測定し
た。焼結体の開口端部を切断し長さ180mmの有底円筒
試験体を作成した。[Measurement Method of Na Ion Conductivity Resistivity] The Na ion conduction resistivity in the radial direction of the bag-shaped tubular body, that is, the low pressure cylindrical body sintered under various firing conditions was measured by the above method. The open end of the sintered body was cut to prepare a bottomed cylindrical test body having a length of 180 mm.
不活性雰囲気中で試験体を約350℃の高温に維持し、
内外面の深さ100mmに金属ナトリウムを充填し、該金
属ナトリウム中に通電用の電極及び電圧端子を入れ、定
電流発生装置から10Aの直流電流を供給して、有底円
筒体の内外面の電圧差を測定し、Naイオン伝導抵抗率を
求めた。また、この四端子法による抵抗と表面積、厚み
等の形状因子からNaイオン伝導抵抗率が求められる。測
定は300〜400℃の範囲で昇降温して実施した。Keep the specimen at a high temperature of about 350 ° C in an inert atmosphere,
Metal sodium was filled to a depth of 100 mm on the inner and outer surfaces, electrodes for energization and voltage terminals were placed in the metal sodium, and a direct current of 10 A was supplied from a constant current generator to supply the inner and outer surfaces of the bottomed cylindrical body. The voltage difference was measured and the Na ion conductive resistivity was determined. Further, the Na ion conduction resistivity can be obtained from the resistance by this four-terminal method and the shape factors such as surface area and thickness. The measurement was performed by raising and lowering the temperature in the range of 300 to 400 ° C.
[機械的強度の測定方法] 上記の方法で得た成形体を種々の焼結条件で焼結した同
軸円筒体の圧環強度を測定した。焼結体から幅10〜1
5mmの円環状試験片を切断加工する。切断面のエッジ処
理をした後、充分乾燥し、圧縮試験を実施した。測定は
0.5mm/分の荷重速度で破壊荷重Pを求め、下記の式
1に従って応力換算を行った。[Measurement Method of Mechanical Strength] The radial crushing strength of the coaxial cylindrical body obtained by sintering the molded body obtained by the above method under various sintering conditions was measured. 10 to 1 width from the sintered body
A 5 mm annular test piece is cut and processed. After edge treatment of the cut surface, it was sufficiently dried and a compression test was performed. In the measurement, the breaking load P was obtained at a loading speed of 0.5 mm / min, and the stress was converted according to the following formula 1.
圧環強度σ=P(D-d)/(2ld2)……1 但し、Dは試験片の外径、dは試験片の肉厚、lは試験
片の幅である。Radial crushing strength σ = P (Dd) / (2ld 2 ) ... 1, where D is the outer diameter of the test piece, d is the thickness of the test piece, and 1 is the width of the test piece.
厚環強度の測定結果は、従来例の平均値を100とした
相対値で表現した。The measurement result of the thick ring strength was expressed as a relative value with the average value of the conventional example being 100.
[水分吸着量] 上記のNaイオン伝導抵抗率の測定に用いた試験体と同様
に焼結体の開口端部を切断し、長さ180mmの有底円筒
体の試験体を作成した。[Amount of Moisture Adsorption] The open end of the sintered body was cut in the same manner as the test body used for the measurement of the Na ion conductive resistivity to prepare a test body of a bottomed cylindrical body having a length of 180 mm.
空気中800℃で2時間乾燥した有底円筒体試験体の重
量を測定した後、50℃、相対温度80%の恒温恒湿槽
に200時間放置した。その後、再び試験体の重量を測
定し、単位表面積当りの重量増加を測定した。After measuring the weight of the bottomed cylindrical test body dried in air at 800 ° C. for 2 hours, it was left in a constant temperature and humidity bath at 50 ° C. and a relative temperature of 80% for 200 hours. Then, the weight of the test body was measured again, and the weight increase per unit surface area was measured.
上記の実施例および比較例より、機械的強度、水分吸着
量の性能とNaイオン伝導抵抗率を勘案した結果、C軸結
晶配向率が0.22〜0.44の範囲の実施例1〜29
が好ましいことが明らかである。From the above Examples and Comparative Examples, Examples 1-29 in which the C-axis crystal orientation ratio is in the range of 0.22 to 0.44 as a result of considering the mechanical strength, the performance of the amount of adsorbed water and the Na ion conductive resistivity.
Is clearly preferable.
[発明の効果] 本発明のナトリウム−硫黄電池用ベータアルミナ固体電
解質は、多結晶構造体のC軸方向の結晶配向率を0.2
2〜0.44の範囲になるように制御することによっ
て、固体電解質の内部抵抗が低く、しかも機械的強度と
化学的耐久性が高いという優れた性質を有するため工業
的に有用となる。 [Effect of the Invention] The beta-alumina solid electrolyte for sodium-sulfur batteries of the present invention has a crystal orientation ratio of 0.2 in the C-axis direction of the polycrystalline structure.
By controlling so as to be in the range of 2 to 0.44, the solid electrolyte has excellent internal properties such as low internal resistance and high mechanical strength and chemical durability, and is industrially useful.
第1図はベータアルミナ固体電解質の単結晶の概要図、
第2図はベータアルミナ円筒体の長手方向切断の試験
片、第3図はナトリウム−硫黄電池の断面概要図であ
る。 1……陽極、5……ベータアルミナ管、7……陰極管。FIG. 1 is a schematic diagram of a single crystal of beta-alumina solid electrolyte,
FIG. 2 is a test piece obtained by longitudinally cutting a beta-alumina cylinder, and FIG. 3 is a schematic cross-sectional view of a sodium-sulfur battery. 1 ... Anode, 5 ... Beta-alumina tube, 7 ... Cathode tube.
Claims (1)
固体電解質において、0.22〜0.44の範囲に制御
されたC軸結晶配向率を有することを特徴とするベータ
アルミナ固体電解質。1. A beta-alumina solid electrolyte for sodium-sulfur batteries, which has a C-axis crystal orientation ratio controlled in the range of 0.22 to 0.44.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1301584A JPH0624149B2 (en) | 1989-11-20 | 1989-11-20 | Beta-alumina solid electrolyte |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1301584A JPH0624149B2 (en) | 1989-11-20 | 1989-11-20 | Beta-alumina solid electrolyte |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03163763A JPH03163763A (en) | 1991-07-15 |
| JPH0624149B2 true JPH0624149B2 (en) | 1994-03-30 |
Family
ID=17898709
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1301584A Expired - Lifetime JPH0624149B2 (en) | 1989-11-20 | 1989-11-20 | Beta-alumina solid electrolyte |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0624149B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2856344B2 (en) * | 1994-03-29 | 1999-02-10 | 日本碍子株式会社 | Beta alumina solid electrolyte and method for producing the same |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5197598A (en) * | 1975-02-25 | 1976-08-27 | Beetaa aruminakotaidenkaishitsunarabini sono seizoho | |
| JPS59207838A (en) * | 1983-05-13 | 1984-11-26 | Michihiro Takase | Beta-alumina thin film and its preparation |
-
1989
- 1989-11-20 JP JP1301584A patent/JPH0624149B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03163763A (en) | 1991-07-15 |
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