Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0696466B2 - Method for manufacturing β "alumina sintered body - Google Patents
[go: Go Back, main page]

JPH0696466B2 - Method for manufacturing β "alumina sintered body - Google Patents

Method for manufacturing β "alumina sintered body

Info

Publication number
JPH0696466B2
JPH0696466B2 JP1180593A JP18059389A JPH0696466B2 JP H0696466 B2 JPH0696466 B2 JP H0696466B2 JP 1180593 A JP1180593 A JP 1180593A JP 18059389 A JP18059389 A JP 18059389A JP H0696466 B2 JPH0696466 B2 JP H0696466B2
Authority
JP
Japan
Prior art keywords
alumina
sintered body
strength
manufacturing
seed 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 - Fee Related
Application number
JP1180593A
Other languages
Japanese (ja)
Other versions
JPH0345554A (en
Inventor
敬一郎 渡邊
均 樋口
敏之 美馬
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
Tokyo Electric Power Co Holdings Inc
Original Assignee
NGK Insulators Ltd
Tokyo Electric Power Co Inc
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, Tokyo Electric Power Co Inc filed Critical NGK Insulators Ltd
Priority to JP1180593A priority Critical patent/JPH0696466B2/en
Publication of JPH0345554A publication Critical patent/JPH0345554A/en
Publication of JPH0696466B2 publication Critical patent/JPH0696466B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • 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

  • 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β″アルミナ焼結体の製造方法に関するもので
ある。更に詳しくはナトリウム−硫黄電池等に好適なナ
トリウムイオン電導に対して低いイオン伝導抵抗率を有
し、緻密で高強度のβ″アルミナ焼結体を安価に製造し
得る製造方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for producing a β ″ -alumina sintered body. More specifically, it is suitable for sodium-sulfur batteries, etc. The present invention relates to a production method capable of inexpensively producing a dense and high-strength β ″ alumina sintered body having a conductive resistivity.

(従来の技術及びその問題点) ナトリウム−硫黄電池は、300〜350℃で作動する高温型
の二次電池である。溶融ナトリウムを負極活物質、溶融
硫黄または多硫化ナトリウムを正極活物質として使用
し、電解質として、ナトリウムイオン伝導性を有するβ
−アルミナ(Na2O・11Al2O3)、β″−アルミナ(Na2O・5
Al2O3)等の固体電解質からなる焼結体が用いられる。
ナトリウム−硫黄電池では、特に良好な性能と長い使用
寿命が要求されるため、ナトリウム−硫黄電池用固体電
解質焼結体には以下の特性が必要である。
(Prior Art and Its Problems) A sodium-sulfur battery is a high temperature type secondary battery that operates at 300 to 350 ° C. Molten sodium is used as a negative electrode active material, and molten sulfur or sodium polysulfide is used as a positive electrode active material. As an electrolyte, β having sodium ion conductivity is used.
-Alumina (Na 2 O ・ 11Al 2 O 3 ), β ″ -Alumina (Na 2 O ・ 5
A sintered body made of a solid electrolyte such as Al 2 O 3 ) is used.
Since the sodium-sulfur battery requires particularly good performance and long service life, the solid electrolyte sintered body for sodium-sulfur battery needs the following characteristics.

(1)高密度で通気性がないこと (2)機械的強度が高いこと (3)イオン伝導度が良好なこと (4)ベータアルミナ結晶の粒径が均一で100μm以上
の粗大粒子がないこと このような特性を有するβ″アルミナ焼結体を製造する
ため種々の製造法が提案されている。
(1) High density and no air permeability (2) High mechanical strength (3) Good ionic conductivity (4) Beta-alumina crystal grain size is uniform and there are no coarse particles of 100 μm or more Various manufacturing methods have been proposed for manufacturing a β ″ alumina sintered body having such characteristics.

例えば、Li2O安定化β″アルミナ焼結体の製造法として
は、予めNa2CO3とα−Al2O3の混合物を仮焼してβおよ
びβ″アルミナが混じった仮焼物を形成しておき、また
別途Li2O・5Al2O3(ゼータリチウムアルミネート)を混
合・仮焼して作成し、これら二種類の仮焼物をさらにも
う一度有機溶媒中で粉砕・混合し噴霧して原料とするゼ
ータプロセスが特公昭57-15063号で知られている。ゼー
タプロセスでは、安定化剤であるLi2Oの分散性が向上す
るため、粗大粒子の形成が抑制される。
For example, as a method for producing a Li 2 O-stabilized β ″ alumina sintered body, a mixture of Na 2 CO 3 and α-Al 2 O 3 is previously calcined to form a calcined product containing β and β ″ alumina. In addition, separately prepared Li 2 O ・ 5Al 2 O 3 (zetalithium aluminate) was mixed and calcined, and these two calcined products were further crushed and mixed in an organic solvent and sprayed again. The zeta process used as a raw material is known from Japanese Patent Publication No. 57-15063. In the zeta process, the dispersibility of Li 2 O, which is a stabilizer, is improved, so that the formation of coarse particles is suppressed.

しかし、原料調製時に2種類の仮焼物を作成するため、
仮焼の工程が2回必要なこと、および二種類の仮焼物の
粉砕・混合時にβおよびβ″アルミナ仮焼物の水による
分解を抑制するために、有機溶媒を使用する必要がある
ため、工程が複雑で、コスト高になる欠点がある。また
焼成スケジュールも、例えば200℃/min以上急昇温し、1
600℃前後の温度で5〜10分間保持後1500℃以下の温度
で数時間焼鈍するという複雑なもので極めて高度な焼成
技術を要する。
However, because two types of calcined products are created during raw material preparation,
Since the calcination process is required twice and it is necessary to use an organic solvent in order to suppress the decomposition of β and β ″ alumina calcination products with water when pulverizing and mixing two types of calcination products, However, the firing schedule is, for example, 200 ° C / min or more
An extremely advanced firing technique is required because it is a complex one that is held at a temperature of around 600 ° C for 5 to 10 minutes and then annealed at a temperature of 1500 ° C or less for several hours.

一方、ゼータプロセスに対して現在注目されているのが
水溶液噴霧乾燥法である。水溶液噴霧乾燥法は、水溶性
のアルカリ原料種を直接水溶媒中に溶解混合し、スラリ
ー調製したものを噴霧乾燥して成形用顆粒原料を得る製
法で、SSSDプロセス(Slurry Solution Spray Drying)
と呼ばれ、将来のβ″アルミナ袋管量産のため、原料処
理工程の簡略化と低コスト化に有効と考えられる。しか
し、SSSDプロセスによるβ″アルミナ焼結体は、従来は
β″化率がまだ不十分で、イオン伝導抵抗率が高く、こ
れらの特性改良が課題となっていた。
On the other hand, the aqueous solution spray-drying method is currently receiving attention for the zeta process. The aqueous solution spray drying method is a method of directly dissolving and mixing a water-soluble alkaline raw material species in a water solvent, and spray-drying a slurry-prepared product to obtain a granular raw material for molding. SSSD process (Slurry Solution Spray Drying)
It is considered to be effective in simplifying the raw material processing process and reducing costs for mass production of β ″ alumina bag tubes in the future. However, the β ″ alumina sintered body produced by the SSSD process has a β ′ conversion rate in the past. However, the ionic conductivity is high, and improvement of these characteristics has been a problem.

(発明が解決しようとする課題) 本発明の課題は、β″化率が高く、イオン伝導抵抗率を
低くでき、強度も充分なβ″アルミナ焼結体及びその製
造方法を提供することである。
(Problems to be Solved by the Invention) An object of the present invention is to provide a β ″ alumina sintered body having a high β ″ conversion rate, a low ionic conduction resistivity, and sufficient strength, and a method for producing the same. .

(課題を解決するための手段) 本発明は、水溶性アルカリ原料種とアルミナ原料とを水
を用いて混合粉砕した後、噴霧乾燥して造粒し、次いで
成形、焼成を行うβ″アルミナ焼結体の製造方法におい
て、前記混合粉砕後に結晶相の主成分がβ″アルミナ相
からなりかつ平均粒径が1μm以上、9μm以下のβ″
アルミナ種結晶を2重量%以上、45重量%以下添加混合
することを特徴とするβ″アルミナ焼結体の製造方法に
係るものである。
(Means for Solving the Problems) The present invention is a β ″ -alumina calcination in which a water-soluble alkali raw material species and an alumina raw material are mixed and pulverized with water, spray-dried and granulated, and then molded and fired. In the method for producing a bound body, after the mixing and pulverization, the main component of the crystal phase is β ″ alumina phase and the average particle diameter is β ″ of 1 μm or more and 9 μm or less.
The present invention relates to a method for producing a β ″ alumina sintered body, which comprises adding and mixing 2% by weight or more and 45% by weight or less of alumina seed crystals.

(作用) 本発明に係わるβ″アルミナ焼結体の製造方法では、水
溶性のアルカリ原料種とアルミナ原料を水を用いて混合
粉砕した後に、β″アルミナ粉砕物を種結晶として添加
することが、結晶体のβ″化率を向上させ、イオン伝導
抵抗率を低下させるために重要である。
(Operation) In the method for producing a β ″ alumina sintered body according to the present invention, a water-soluble alkali raw material seed and an alumina raw material are mixed and pulverized with water, and then the β ″ alumina pulverized product is added as a seed crystal. , Is important for improving the β ″ conversion of the crystal and reducing the ionic conductivity resistivity.

この際、種結晶の平均粒径を1〜9μmにして、添加量
を2〜45重量%にすると、焼結体中の結晶子が均一に成
長するため、強度が劣化することがない。平均粒径を1
μm未満にすると、マトリックスに吸収されて消失する
種結晶が増えて種結晶が粒成長の核としての働きを発現
しないため、添加効果が不充分となり、部分的な異常粒
成長が起って強度が劣化する。平均粒径が9μmを越え
ると、種結晶の数が不足して異常粒成長が生じ、強度劣
化が起こる。また種結晶の最大径は44μm以下が好まし
く、仮に44μmを越える場合には、粗大な種結晶を中心
にして異常粒成長が起きたり、種結晶の焼結性が不足し
て強度劣化が起こる。種結晶の添加量が2重量%未満で
は、β″化率が不充分で、イオン伝導抵抗率が大きく、
また異常粒成長も起って強度も低下する。さらに種結晶
の添加量が45重量%を越えると成形体の焼結性が低下し
て焼結体強度が低下する。
At this time, when the average grain size of the seed crystal is set to 1 to 9 μm and the addition amount is set to 2 to 45% by weight, the crystallites in the sintered body grow uniformly, so that the strength does not deteriorate. Average particle size is 1
If it is less than μm, the number of seed crystals that are absorbed and disappeared in the matrix increases, and the seed crystals do not function as nuclei for grain growth. Therefore, the effect of addition becomes insufficient, and partial abnormal grain growth occurs and the strength increases. Deteriorates. If the average grain size exceeds 9 μm, the number of seed crystals is insufficient, abnormal grain growth occurs, and strength deterioration occurs. The maximum diameter of the seed crystal is preferably 44 μm or less, and if it exceeds 44 μm, abnormal grain growth occurs around the coarse seed crystal, or the sinterability of the seed crystal is insufficient, resulting in strength deterioration. If the amount of seed crystals added is less than 2% by weight, the β ″ conversion is insufficient and the ionic conductivity is high.
In addition, abnormal grain growth occurs and the strength also decreases. Further, if the amount of seed crystals added exceeds 45% by weight, the sinterability of the molded body is lowered and the strength of the sintered body is lowered.

以上述べたように本発明では、製造コストが安価なβ″
アルミナ焼結体の水溶液噴霧乾燥法製造プロセスにおい
て、高イオン伝導性と高強度性を両立させるためにβ″
アルミナ焼結体粉砕物を適量添加し、β″化率の向上
を、微構造の均一性を実現したものである。
As described above, in the present invention, the manufacturing cost is low, β ″.
Β ″ in order to achieve both high ionic conductivity and high strength in the aqueous solution spray-drying manufacturing process of the alumina sintered body.
By adding an appropriate amount of crushed alumina sintered body, the β ″ conversion rate is improved and the microstructure is made uniform.

上記種結晶の平均粒径は2〜5μmが更に好ましく、種
結晶の添加量は5〜30重量%が更に好ましい。
The average particle size of the seed crystals is more preferably 2 to 5 μm, and the addition amount of the seed crystals is more preferably 5 to 30% by weight.

(実施例) 第1図はβ″アルミナ焼結体の水噴霧乾燥法製造プロセ
スにβ″アルミナ焼結体粉砕物を種結晶として添加する
本発明のフローチャートである。
(Example) FIG. 1 is a flow chart of the present invention in which a pulverized product of a β ″ alumina sintered body is added as a seed crystal to a water spray drying manufacturing process of a β ″ alumina sintered body.

本例では、Al2O3源としてα−Al2O3、Na2O源として水溶
性のNaOH、安定化剤のMgO、Li2O源としてはMg(NO3)2・6H
2O,MgCO3およびLiOHを用いた、また比較のために、ゼー
タプロセス用の原料として、Al2O3源としてα−Al2O3、N
a2O源として、Na2CO3、NaOH安定化剤のMgO、Li2O源とし
てはMgCO3,Li2CO3およびLiOHを用いた。
In this example, Al 2 O 3 source as α-Al 2 O 3, Na 2 O source as the water-soluble NaOH, MgO stabilizer, as the Li 2 O source Mg (NO 3) 2 · 6H
2 O, MgCO 3 and LiOH, and for comparison, α-Al 2 O 3 , N as a source for Al 2 O 3 as a raw material for the zeta process.
Na 2 CO 3 was used as the a 2 O source, MgO as a NaOH stabilizer, and MgCO 3 , Li 2 CO 3 and LiOH were used as the Li 2 O sources.

β″アルミナ種結晶としては、予め種結晶を添加しない
条件で作った粉末から結晶体を作成し、粗砕後、アセト
ン中でアルミナボールミルにより5〜100時間粉砕し
て、平均粒径の異なる種結晶B,C,D,Eを得た。平均粒径
0.8μmの種結晶Aは、同じ粗砕物をアセトン中で振動
ミルにて24時間粉砕して作成した。種結晶のβ″化率は
80%であった。β″化率の決定は、β相の(110)ピー
ク強度Iβとβ″相の(01,11)ピーク強度Iβ″より の式を用いて算出した。
As the β ″ alumina seed crystal, a crystal is prepared from powder that is not made in advance with the addition of seed crystals, and after coarse crushing, crushing is performed in an alumina ball mill for 5 to 100 hours in acetone to obtain seeds with different average particle sizes. Crystals B, C, D and E were obtained.
The 0.8 μm seed crystal A was prepared by crushing the same coarsely crushed product in acetone with a vibration mill for 24 hours. The β ″ ratio of the seed crystal is
It was 80%. The β "conversion rate is determined from the (110) peak intensity I β of the β phase and the (01,11) peak intensity I β" of the β "phase. It calculated using the formula of.

の式を用いて算出した。It calculated using the formula of.

以下、更に具体的な実験例について述べる。Hereinafter, more specific experimental examples will be described.

まず、MgOを安定化剤として含む系についてはNa2O8.9重
量%、MgO2.1重量%、Al2O389.0重量%となるように、
またLi2Oを安定化剤として含む系についてはNa2O9.0重
量%、Li2O0.8重量%、Al2O390.2重量%となるように、
α−アルミナ、水酸化ナトリウム、炭酸ナトリウム、硝
酸マグネシウム、炭酸マグネシウム、水酸化リチウム、
炭酸リチウム等の原料を表1に示す調合割合で調合し
た。
First, Na 2 O8.9% by weight for the systems containing MgO as a stabilizer, MgO2.1 wt%, such that the Al 2 O 3 89.0 wt%,
The Na 2 O9.0% by weight for the systems containing Li 2 O as a stabilizer, Li 2 O0.8 wt%, Al 2 O 3 so as to be 90.2 wt%,
α-alumina, sodium hydroxide, sodium carbonate, magnesium nitrate, magnesium carbonate, lithium hydroxide,
Raw materials such as lithium carbonate were prepared at the mixing ratio shown in Table 1.

次いで、この混合粉末200g〜100gと玉石(φ15Al2O3)1
kgに混合粉末に対して水分60%となるよう蒸留水を加え
3lポット中で20.5時間混合粉砕し、その後各種粒径の
β″アルミナ種結晶を所定量添加し、更に0.5時間混合
した。種結晶は水と反応し分解するため混合時間は2時
間以下にすることが好ましい。次いで、44μm以上の粗
大粒子を除くために350メッシュの篩でふるい分けし、
スプレードライヤーで乾燥、造粒し、100メッシュ篩で
ふるい分けした。次いで、50×50×6の形状に金型プレ
ス(200kg/cm2)成形後、ラバープレス(1000kg/cm2
し、表1に示す所定の焼成条件で焼成した。焼成時のNa
2O成分の蒸発を防ぐために、アルミナるつぼ中に各成形
体と同じ調合粉末を充填して埋焼とした。
Next, 200g-100g of this mixed powder and cobblestone (φ15Al 2 O 3 ) 1
Add distilled water to kg so that the water content is 60% of the mixed powder.
Mix and pulverize in a 3l pot for 20.5 hours, add a predetermined amount of β ″ alumina seed crystals of various particle sizes, and mix for an additional 0.5 hour. Seed crystals react with water and decompose, so the mixing time is 2 hours or less. Then, it is sifted through a 350-mesh sieve to remove coarse particles of 44 μm or more,
It was dried with a spray dryer, granulated, and sieved with a 100 mesh screen. Next, mold press (200 kg / cm 2 ) into a 50 × 50 × 6 shape, then press rubber (1000 kg / cm 2 ).
Then, it was fired under the predetermined firing conditions shown in Table 1. Na during firing
In order to prevent the evaporation of the 2 O component, the same compound powder as that of each molded body was filled in an alumina crucible and subjected to burial.

また、焼成スケジュールとしては、1時間400℃で1500
〜1600℃まで昇温し、最高温度で10〜60分間保持し、1
時間500℃の速さで1400℃まで降温し、1400℃で5時間
保持し、次いで1時間に300℃の速さで降温した。
Also, the firing schedule is 1500 at 400 ° C for 1 hour.
Raise the temperature up to ~ 1600 ℃, hold at the maximum temperature for 10 ~ 60 minutes, and
The temperature was lowered to 1400 ° C. at a rate of 500 ° C., held at 1400 ° C. for 5 hours, and then lowered to a rate of 300 ° C. for 1 hour.

比較例としてのゼータプロセスでの焼成体の作成は次の
手順で行なった。すなわち、「Am.Ceram.Soc.Bull.,5
6,(2).206,(1977)」の“Sintering Processes an
d Heat Treatment Schedules for Conductive Lithia S
tabilized β″−Al2O3”に記載してあるように、2種
類の混合物を作成し、別々に仮焼して2つの化合物を作
成後、それぞれ解砕し、両者を調合してアセトン溶媒に
てポットミル中で21時間粉砕し、できたスラリーにPVB
をバインダーとして添加後、スプレードライヤーで造粒
した。第1の混合物の組成は、Li2O・5.5Al2O3とし、原
料には炭酸リチウムとアルミナを用いた。第2の混合物
の組成は、Al2O3・5Al2O3として原料には炭酸ナトリウム
とアルミナを用いた。それぞれの混合物の仮焼温度は、
1260℃で仮焼時間は2時間とした。
Preparation of a fired body by the zeta process as a comparative example was performed in the following procedure. That is, `` Am.Ceram.Soc.Bull., 5
6 , (2) .206, (1977) ”,“ Sintering Processes an
d Heat Treatment Schedules for Conductive Lithia S
As described in tabilized β ″ -Al 2 O 3 ″, two kinds of mixture are prepared and calcined separately to prepare two compounds, which are then crushed. Is crushed in a pot mill for 21 hours, and the resulting slurry is PVB
Was added as a binder and then granulated with a spray dryer. The composition of the first mixture was Li 2 O.5.5Al 2 O 3, and lithium carbonate and alumina were used as raw materials. The composition of the second mixture was Al 2 O 3 .5Al 2 O 3 , and sodium carbonate and alumina were used as raw materials. The calcination temperature of each mixture is
The calcination time at 1260 ° C. was 2 hours.

以後の成形・焼成の条件は先に述べた水溶液噴霧乾燥法
と同じ条件とした。第2図にゼータプロセスでの製造の
フローチャートを示す。
The subsequent molding and firing conditions were the same as those of the aqueous solution spray drying method described above. FIG. 2 shows a manufacturing flow chart in the zeta process.

上記各例について、β″化率、焼成収縮率、密度(焼結
体見掛密度)、四点曲げ強度、イオン伝導抵抗率を測定
した。結果を表1に示す。
For each of the above examples, the β ″ conversion rate, firing shrinkage rate, density (sintered body apparent density), four-point bending strength, and ionic conduction resistivity were measured. The results are shown in Table 1.

第3図は種結晶の添加量と四点曲強度の関係を示す。種
結晶を2%(重量%、以下同じ)以上、45%以下添加す
るこにより、250MPa以上の強度の焼結体が得られ、ゼー
タプロセスの焼結体と同等の強度となる。2%未満の添
加量では種結晶の量が不足して、異常粒成長が起こり、
強度劣化が生じているものと考えられる。種結晶の添加
量が2%以上、45%以下では種結晶の量が適切なため、
全体に均一な粒成長が起こり、均質な微構造となって高
強度の焼結体となる。種結晶の添加量が45%を越える
と、焼結性が低下して、低密度の焼結体となり強度が低
値を示すようになる。
FIG. 3 shows the relationship between the amount of seed crystals added and the four-point bending strength. By adding the seed crystal in an amount of 2% (wt%, the same applies hereinafter) or more and 45% or less, a sintered body having a strength of 250 MPa or more can be obtained, and the strength is equivalent to that of the zeta process sintered body. If the amount added is less than 2%, the amount of seed crystals will be insufficient, and abnormal grain growth will occur.
It is considered that the strength has deteriorated. Since the amount of seed crystals is appropriate when the amount of seed crystals added is 2% or more and 45% or less,
Uniform grain growth occurs throughout, resulting in a homogeneous microstructure and a high-strength sintered body. If the amount of seed crystals added exceeds 45%, the sinterability will be reduced, and a low-density sintered body will be obtained, and the strength will be low.

第4図に種結晶添加量とβ″化率の関係を示す。β″ア
ルミナ焼結体を製造する時に重要な点は、Naイオン伝導
抵抗率の低いβ″相を充分に生成することである。第4
図から分かるように、結晶相の主成分がβ″相からなる
種結晶を添加することは、β″化率を向上させるために
有効であり、2%以上添加することで、94%以上のβ″
化率のβ″アルミナ結晶体を製造することができる。
Fig. 4 shows the relationship between the amount of seed crystals added and the β "conversion rate. The important point when manufacturing a β" alumina sintered body is that a β "phase with a low Na ion conductivity resistivity is sufficiently formed. Yes, the fourth
As can be seen from the figure, it is effective to add a seed crystal having a β ″ phase as the main component of the crystal phase, and it is effective to improve the β ″ conversion rate. β ″
It is possible to produce a β ″ alumina crystal having a high conversion rate.

第5図に種結晶添加量と300℃でのNaイオン伝導抵抗率
の関係を示す。この図より種結晶を2%以上添加するこ
とにより、300℃でのNaイオン伝導抵抗率が5Ω・cm以
下となり、ナトリウム−硫黄電池用に好適のβ″アルミ
ナ焼結体が得られることが分る。
Fig. 5 shows the relationship between the seed crystal addition amount and the Na ion conduction resistivity at 300 ° C. From this figure, it can be seen that by adding seed crystals of 2% or more, the Na ion conductivity resistivity at 300 ° C becomes 5 Ω · cm or less, and a β ″ alumina sintered body suitable for sodium-sulfur batteries can be obtained. It

第6図にβ″化率と300℃でのNaイオン伝導抵抗率の関
係を示す。この図よりβ″化率の向上がNaイオン伝導抵
抗率の低減に極めて有効であることが分る。また実施例
1〜8と比較例6,7の比較により、ナトリウム源に水溶
性の水酸化ナトリウムを用いた時に本発明の製造方法が
β″化率を向上させるために有効であることが分る。ま
た水溶性の原料を用いない場合、焼結性も低下して低強
度の焼結体しか得られない。
Fig. 6 shows the relationship between the β "conversion rate and the Na ion conduction resistivity at 300 ° C. From this figure, it is clear that the improvement of the β" conversion rate is extremely effective in reducing the Na ion conduction resistivity. From a comparison between Examples 1 to 8 and Comparative Examples 6 and 7, it was found that the production method of the present invention is effective for improving the β ″ conversion rate when water-soluble sodium hydroxide is used as the sodium source. Further, when a water-soluble raw material is not used, the sinterability is lowered and only a low-strength sintered body can be obtained.

さらに第7図に焼成温度と焼結体密度の関係を示す。ゼ
ータプロセスに対して本発明の製造法では、1540℃から
1600℃の広い範囲にわたって特性の安定した焼結体を得
ることができる。またキープ時間についても実施例1〜
8から分るようにゼータプロセスのように10分以下の短
時間でなくとも、キープ時間を伸ばしても粒成長による
特性の劣化が認められない。このため、ゼータプロセス
のように焼結条件を非常に厳密に制御する必要がないた
め、製造上大いなる利点がある。
Further, FIG. 7 shows the relationship between the firing temperature and the sintered body density. In the manufacturing method of the present invention for the zeta process, from 1540 ° C
It is possible to obtain a sintered body with stable characteristics over a wide range of 1600 ° C. In addition, regarding the keep time, Example 1
As can be seen from FIG. 8, even if the time is not as short as 10 minutes or less as in the Zeta process, deterioration of properties due to grain growth is not recognized even if the keeping time is extended. For this reason, it is not necessary to control the sintering conditions very strictly as in the Zeta process, which is a great advantage in manufacturing.

また第8図に種結晶添加量10重量%の場合の、四点曲げ
強度の種結晶平均粒径依存性を示す。種結晶の平均粒径
が1μm未満では、種結晶の大きさが小さ過ぎるため種
結晶が周囲の組織に吸収されてしまい、有効に働かず、
粗大粒の成長が起って強度が劣化し、250MPa以下ととな
る。また種結晶の平均粒径が9μmを超えると、種結晶
の焼結性が低下するため、得られる焼結体の強度が劣化
し、250MPa以下となる。
Further, FIG. 8 shows the dependence of the four-point bending strength on the average grain size of the seed crystal when the seed crystal addition amount is 10% by weight. If the average particle size of the seed crystal is less than 1 μm, the size of the seed crystal is too small, so that the seed crystal is absorbed by the surrounding tissue and does not work effectively.
Coarse grains grow and the strength deteriorates to 250 MPa or less. Further, if the average grain size of the seed crystal exceeds 9 μm, the sinterability of the seed crystal deteriorates, so that the strength of the obtained sintered body deteriorates to 250 MPa or less.

また種結晶中に44μm以上の粗大な種結晶が含まれてい
ても、焼結体の強度劣化の原因となるため、種結晶の添
加後、325メッシュ以上の篩で篩分けしてこのような粗
大種結晶を除去しておくことが望ましい。
Further, even if the seed crystal contains a coarse seed crystal of 44 μm or more, it will cause the strength deterioration of the sintered body. Therefore, after adding the seed crystal, it is sieved with a sieve of 325 mesh or more. It is desirable to remove coarse seed crystals.

(発明の効果) 以上説明した通り、本発明によれば次の効果が奏せられ
る。
(Effects of the Invention) As described above, the present invention has the following effects.

β″アルミナ焼結体の製造法として公知のゼータプロセ
スでは原料調製時に、2種類の混合物に対して仮焼、粉
砕が余分に必要であり、また最終調合物の粉砕時に有機
溶媒を用いる必要がある。これに対して水溶液噴霧乾燥
法では混合粉砕時に水が使用でき、混合粉砕工程も1回
で澄む低コストの製造法であるが、β″化率が低いため
イオン伝導抵抗率が高く、低強度であるという問題があ
った。
In the zeta process known as a method for producing a β ″ alumina sintered body, it is necessary to additionally calcine and pulverize two kinds of mixture when preparing raw materials, and to use an organic solvent when pulverizing the final formulation. On the other hand, the aqueous solution spray-drying method is a low-cost manufacturing method in which water can be used during mixing and crushing, and the mixing and crushing step can be clarified in a single operation, but the β ″ conversion rate is low, so the ionic conductivity is high, There was a problem of low strength.

この水溶液噴霧乾燥法に本発明の製造法により、定めら
れた平均粒径の結晶相の主成分がβ″相からなる種結晶
を所定量添加することにより、β″化率が向上してイオ
ン伝導抵抗率が低下し、しかも均一な粒成長が生じるた
め、結晶体強度も向上してナトリウム−硫黄電池等に好
適なβ″アルミナ焼結体が得られる。さらに焼成温度幅
も、ゼータプロセスに比べて広いため、ゼータプロセス
の急速昇温、高温短時間保持が不要となり、製造上大な
る利点がある。
According to the production method of the present invention, by adding a predetermined amount of a seed crystal having a β ″ phase as a main component of a crystal phase having a determined average particle size to the aqueous solution spray drying method, the β ″ conversion rate is improved. Since the conductivity resistivity is lowered and uniform grain growth occurs, the crystal strength is improved and a β ″ -alumina sintered body suitable for sodium-sulfur batteries etc. can be obtained. Since it is wider than that of the Zeta process, there is no need for rapid temperature rise in the zeta process and for a short time at high temperature, which is a great advantage in manufacturing.

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

第1図は本発明の製造方法を示すフローチャート、 第2図は従来のゼータプロセス示すフローチャート、 第3図は四点曲げ強度とβ″アルミナ種結晶の添加量と
の関係を示すグラフ、 第4図はβ″化率とβ″アルミナ種結晶の添加量との関
係を示すグラフ、 第5図は300℃でのナトリウムイオン伝導抵抗率とβ″
種結晶の添加量との関係を示すグラフ、 第6図は300℃でのNaイオン伝導抵抗率とβ″化率との
関係を示すグラフ、 第7図は本発明の実施例とゼータプロセスとにおける焼
結体密度と焼結温度との関係を示すグラフ、 第8図は四点曲げ強度と種結晶平均粒径との関係を示す
グラフである。
FIG. 1 is a flow chart showing the manufacturing method of the present invention, FIG. 2 is a flow chart showing a conventional zeta process, FIG. 3 is a graph showing the relationship between four-point bending strength and the amount of β ″ alumina seed crystal added, The figure is a graph showing the relationship between the β "conversion rate and the addition amount of β" alumina seed crystals, and Fig. 5 is the sodium ion conductivity resistivity at 300 ° C and β ".
FIG. 6 is a graph showing the relationship between the amount of seed crystals added, FIG. 6 is a graph showing the relationship between the Na ion conductive resistivity at 300 ° C. and the β ″ conversion rate, and FIG. 7 is an example of the present invention and the zeta process. Fig. 8 is a graph showing the relationship between the sintered body density and the sintering temperature in Fig. 8, and Fig. 8 is a graph showing the relationship between the four-point bending strength and the seed crystal average grain size.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】水溶性アルカリ原料種とアルミナ原料とを
水を用いて混合粉砕した後、噴霧乾燥して造粒し、次い
で成形、焼成を行うβ″アルミナ焼結体の製造方法にお
いて、前記混合粉砕後に結晶相の主成分がβ″アルミナ
相からなりかつ平均粒径が1μm以上、9μm以下の
β″アルミナ種結晶を2重量%以上、45重量%以下添加
混合することを特徴とするβ″アルミナ焼結体の製造方
法。
1. A method for producing a β ″ alumina sintered body, which comprises mixing a water-soluble alkali raw material species and an alumina raw material with water, pulverizing, spray-drying, granulating, and then molding and firing. After mixing and pulverizing, β ″ alumina seed crystals having a β ″ alumina phase as a main component of a crystal phase and having an average particle size of 1 μm or more and 9 μm or less are added and mixed in an amount of 2% by weight or more and 45% by weight or less. ″ Method for manufacturing alumina sintered body.
JP1180593A 1989-07-14 1989-07-14 Method for manufacturing β "alumina sintered body Expired - Fee Related JPH0696466B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1180593A JPH0696466B2 (en) 1989-07-14 1989-07-14 Method for manufacturing β "alumina sintered body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1180593A JPH0696466B2 (en) 1989-07-14 1989-07-14 Method for manufacturing β "alumina sintered body

Publications (2)

Publication Number Publication Date
JPH0345554A JPH0345554A (en) 1991-02-27
JPH0696466B2 true JPH0696466B2 (en) 1994-11-30

Family

ID=16085977

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1180593A Expired - Fee Related JPH0696466B2 (en) 1989-07-14 1989-07-14 Method for manufacturing β "alumina sintered body

Country Status (1)

Country Link
JP (1) JPH0696466B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0547412A (en) * 1991-08-12 1993-02-26 Ngk Insulators Ltd Beta-alumina solid electrolyte
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
KR101337407B1 (en) * 2012-03-15 2013-12-06 건국대학교 산학협력단 Fabrication of beta-alumina solid electrolyte with addition of beta-alumina seeds in spray-drying process and the secondary battery using it

Also Published As

Publication number Publication date
JPH0345554A (en) 1991-02-27

Similar Documents

Publication Publication Date Title
EP0328068B1 (en) Preparation of strong beta-aluminum bodies
US5503930A (en) Layer structure oxide
JP4642959B2 (en) Method for producing lithium titanate
JP3307510B2 (en) Layered structure oxide and secondary battery
JP2019102460A (en) Lithium ion conductive composite material containing at least one polymer and lithium ion conductive particle, and manufacturing method of lithium ion conductive body from composite material
CN112851344B (en) Microwave dielectric ceramic with medium dielectric constant and preparation method thereof
JP7241247B2 (en) Method for producing hexagonal boron nitride powder and sintered boron nitride
CN108727022A (en) A kind of ultra-low loss magnesium-niobate lithium system microwave dielectric ceramic materials and preparation method thereof
JP2010132467A (en) Method for producing oxide
CN114477984B (en) Microwave dielectric ceramic material and preparation method thereof
CN112851346B (en) Ultralow-loss zirconium magnesium niobate system microwave dielectric ceramic material and preparation method thereof
JP7618991B2 (en) Positive electrode active material for lithium ion secondary battery, manufacturing method thereof, and lithium ion secondary battery
JPH0696466B2 (en) Method for manufacturing β "alumina sintered body
WO2019126969A1 (en) Dielectric ceramic material and method for preparing same
KR102016916B1 (en) Method for producing LLZO oxide solid electrolyte powder
US2935411A (en) High dielectric constant ceramics
CN115340378A (en) A kind of oxide solid electrolyte and its preparation method and a kind of lithium ion battery
JP2719352B2 (en) Method for manufacturing solid electrolyte tube for sodium-sulfur battery
JPH09221356A (en) Method for producing beta-alumina sintered body
JP3009566B2 (en) Beta alumina electrolyte
JP3586556B2 (en) Method for producing beta alumina electrolyte
JP3131820B2 (en) Method for producing β ″ -alumina sintered body
JP3581620B2 (en) Beta alumina electrolyte and method for producing the same
JPH0214873A (en) Production of beta-alumina ceramic
JPH02120274A (en) Production of solid electrolyte tube for sodium-sulfur battery

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees