JPS60189832A - Preparation of alkaline-earth carbonate - Google Patents

Preparation of alkaline-earth carbonate

Info

Publication number
JPS60189832A
JPS60189832A JP4397184A JP4397184A JPS60189832A JP S60189832 A JPS60189832 A JP S60189832A JP 4397184 A JP4397184 A JP 4397184A JP 4397184 A JP4397184 A JP 4397184A JP S60189832 A JPS60189832 A JP S60189832A
Authority
JP
Japan
Prior art keywords
carbonate
alkaline earth
solution
crystal
alkaline
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
JP4397184A
Other languages
Japanese (ja)
Other versions
JPH0445451B2 (en
Inventor
Sadao Matsumoto
松本 貞雄
Katsuhiro Shimura
志村 勝弘
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP4397184A priority Critical patent/JPS60189832A/en
Publication of JPS60189832A publication Critical patent/JPS60189832A/en
Publication of JPH0445451B2 publication Critical patent/JPH0445451B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J9/00Apparatus or processes specially adapted for the manufacture, installation, removal, maintenance of electric discharge tubes, discharge lamps, or parts thereof; Recovery of material from discharge tubes or lamps
    • H01J9/02Manufacture of electrodes or electrode systems
    • H01J9/04Manufacture of electrodes or electrode systems of thermionic cathodes
    • H01J9/042Manufacture, activation of the emissive part

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

PURPOSE:To obtain alkaline-earth carbonate which has needle crystal and is capable of controlling crystal grain size by dissolving salt containing ammonium ions in an alkaline-earth nitrate solution and thereafter allowing it to react with a carbonate solution. CONSTITUTION:A given amount of salt containing ammonium ions such as ammonium nitrate is mingled to dissolve in three kinds of soluble alkaline-earth nitrate solution composed of Ba, Sr and Ca. The mingled solution is heated while being stirred, and a soluble carbonate solution such as ammonium carbonate is added to react and subsequently crystal maturation is carried out. At this time, when an additive amount of ammonium salt is increased, crystal grains size is enlarged. By this method, it is possible to effectively obtain alkaline-earth carbonate in the state of needle crystal suitable for an oxide-coated cathode for an electron that.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明はアルカリ土類炭酸塩の製造方法に係シ、特に電
子管用ば化物陰極に使用するアルカリ土類炭酸塩の製造
方法に関するものでちる。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for producing an alkaline earth carbonate, and more particularly to a method for producing an alkaline earth carbonate for use in a bride cathode for an electron tube.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

現在の電子管用酸化物陰極は、はとんどアルカリ土類炭
酸塩を真空中で加熱分解し酸化物としている。
Current oxide cathodes for electron tubes are made by thermally decomposing alkaline earth carbonates in vacuum to form oxides.

従ってアルカリ土類炭酸塩の性質は極めて重要であ多、
電子管としての種々な特性に関係する。
Therefore, the properties of alkaline earth carbonates are extremely important.
It is related to various characteristics as an electron tube.

即ち、初期のエミッション、加熱分解によるコーティン
グの収量率、コーティングのはがれ、及びエミッション
ライフfj:、どである。これらは勿論、酸化物への転
化条件によっても陰極としての性質が左右されるが、こ
のときの条件は陰極以外の要素によって支配され、制御
し得る範囲は極めて狭いのが普通である。また炭酸塩の
性質は陰極の装造上にも影響することが大きい。即、塗
布液の粘度、コーティング層の密度および表面の粗さな
どでらる。
That is, the initial emission, the yield rate of the coating by thermal decomposition, the peeling off of the coating, and the emission life fj:, etc. Of course, the properties of these as a cathode are also influenced by the conditions for conversion to an oxide, but the conditions at this time are controlled by elements other than the cathode, and the controllable range is usually extremely narrow. Furthermore, the properties of the carbonate have a large effect on the construction of the cathode. That is, the viscosity of the coating liquid, the density of the coating layer, the roughness of the surface, etc.

したがって、今までにもアルカリ土類炭酸塩の製造条件
と、その性質については、数多くの検討が行なわれ、ア
ルカリ土類炭酸塩の組成比と、エミツ7ヨンの関係もか
なシ解明されている。
Therefore, many studies have been carried out on the production conditions and properties of alkaline earth carbonates, and the relationship between the composition ratio of alkaline earth carbonates and the concentration has also been elucidated. .

また、このアルカリ土類炭酸塩の製造方法にもいろいろ
おるが、いずれも水溶液中でのアルカリ土類金属イオン
と炭酸イオンとの反応に基づいている。そして、このア
ルカリ土類金属イオンとしては硝酸塩、炭酸イオンとし
ては炭酸ナトリウムまたは炭酸アンモニウムが主として
使用されている。また特vc電子放射特性の良好なもの
としてはアルカリ土類硝酸塩がバリウムを最大とし、ス
トロンチウム、カルシウムの順に少なくなる3種類の可
溶性アルカリ土類硝酸塩混合溶液が多く用いられている
There are various methods for producing alkaline earth carbonates, but all of them are based on the reaction between alkaline earth metal ions and carbonate ions in an aqueous solution. As the alkaline earth metal ion, nitrate is mainly used, and as the carbonate ion, sodium carbonate or ammonium carbonate is mainly used. Also, as a solution having good vc electron emission characteristics, a mixed solution of three types of soluble alkaline earth nitrates is often used, in which the alkaline earth nitrate contains the largest amount of barium, and the amount of strontium and calcium decreases in that order.

一般的なアルカリ土類炭酸塩の製造方法としてはアルカ
リ土類硝酸塩溶液、例えばパリウA33wt%、ストロ
ンチウム4Q wt%、カルク94フ加熱しながら攪拌
し、このアルカリ土類硝酸塩溶液に同じ温度に加熱した
炭酸ナトリウム溶液を所定の添加速度で添カロしアルカ
リ土類炭酸塩を沈澱させる。次に、この反応が終了した
後、不純物を除去するために温水による洗浄を繰返し、
最後に脱水、乾燥を行ない、アルカリ土類炭酸塩の粉体
を得る方法がある。
A general method for producing alkaline earth carbonates is to stir an alkaline earth nitrate solution, such as Pariu A 33wt%, strontium 4Q wt%, Calc 94, while heating, and then heat the alkaline earth nitrate solution to the same temperature. A sodium carbonate solution is added at a predetermined addition rate to precipitate alkaline earth carbonates. Then, after this reaction is finished, washing with hot water is repeated to remove impurities.
Finally, there is a method of dehydrating and drying to obtain alkaline earth carbonate powder.

このようにして得られたアルカリ土類炭酸塩の結晶形状
及び結晶粒度は、反応液の濃度、反応温度、炭酸塩の添
加速度、さらには反応中の攪拌などに影響され、種々の
結晶が得られるが、結晶形状を同じくして結晶粒度のみ
を変化させることは前述したような反応条件の変更では
困難でちる〇酸化物陰極に用いられるアルカリ土類炭酸
塩の結晶形状としては陰極のコーティング特性、即ち陰
極コーティング層内の付着力、ポロシティ、及び、加熱
分解後の収縮によるコーティング層のひび割れなどから
針状の結晶形状が有利であると言われておシ、この針状
の結晶形状が多用されている。
The crystal shape and grain size of the alkaline earth carbonate thus obtained are affected by the concentration of the reaction solution, reaction temperature, carbonate addition rate, and stirring during the reaction, and various crystals may be obtained. However, it is difficult to change only the crystal grain size while keeping the crystal shape the same by changing the reaction conditions as described above. The crystal shape of the alkaline earth carbonate used in the oxide cathode depends on the coating characteristics of the cathode. In other words, it is said that an acicular crystal shape is advantageous due to adhesion and porosity within the cathode coating layer, and cracks in the coating layer due to shrinkage after thermal decomposition, and this acicular crystal shape is often used. has been done.

しかし、種々の電子管特性、つまシ陰他コーティング表
面のスムース度、高密度なコーティング層などを要求さ
れる電子管には針状の結晶形状で結晶粒度の細かいアル
カリ土類炭酸塩が望まれている。
However, alkaline earth carbonates with needle-like crystal shapes and fine crystal grains are desired for electron tubes that require various electron tube characteristics, smoothness of the coating surface, high density coating layer, etc. .

現在のアルカリ土類炭酸塩の反応条件でも針状の結晶形
状をほぼ同じくして結晶粒度のみを変化させる反応条件
は、ある税関可能であるが、この反応条件は反応両度を
非常に薄くする必要がちシ量産性、経済性に欠ける。こ
のため経済性にすぐれ、種々の電子管に要求される針状
の結晶状態で結状粒度のみをコントロールするアルカリ
土類炭酸塩の製造方法が要望されている。
Even under the current reaction conditions for alkaline earth carbonates, it is possible to create a reaction condition in which the acicular crystal shape is almost the same and only the crystal grain size is changed, but this reaction condition makes the reaction rate very thin. It is not necessary for mass production and is not economical. Therefore, there is a need for a method for producing alkaline earth carbonates that is highly economical and that controls only the particle size of the crystals in the acicular crystalline state required for various electron tubes.

〔発明の目的〕[Purpose of the invention]

本発明は上述した問題点及び要望に鑑みなされたもので
おり、種々な電子管用陰極特性に有利な針状の結晶状態
でちゃ、かつそれぞれの電子管陰極に要求される結晶粒
度をコントロールすることが可能なアルカリ土類炭酸塩
の製造方法を提供することを目的としている。
The present invention was made in view of the above-mentioned problems and demands, and it is possible to obtain an acicular crystalline state that is advantageous for various electron tube cathode characteristics, and to control the crystal grain size required for each electron tube cathode. The present invention aims to provide a possible method for producing alkaline earth carbonates.

〔発明の概要〕[Summary of the invention]

次に本発明のアルカリ土類炭酸塩の製造方法の一実施例
を説明する。
Next, an embodiment of the method for producing an alkaline earth carbonate of the present invention will be described.

先ずアルカリ土類硝酸塩としてのバリウム、ストロンチ
ウム、カルシラムラハリラム53 wt %、ストロン
チウム4Q wt%、カルシウム7wt%の1己合比率
で濃度約0.52モル/lの硝酸に溶解した溶 □液の
中に更に硝酸カルシウムの重量を基準としてこの重量の
O乃至10%の例えば硝酸アンモニウムのような塩類を
加えて史(溶解する。
First, a solution of barium, strontium, calciramrahilirum 53 wt%, strontium 4Q wt%, and calcium 7 wt% as alkaline earth nitrates was dissolved in nitric acid at a concentration of about 0.52 mol/l. Further, a salt such as ammonium nitrate in an amount of O to 10% by weight based on the weight of calcium nitrate is added and dissolved.

次に、この溶液を攪拌しながら約87°0に加熱するO 次に例えば濃度1.1モル/lの炭酸アンモニウム溶液
を約87°0に加熱し、この炭酸アンモニウム溶液をア
ルカリ土類硝酸塩溶液の中へアルカリ土類硝酸塩溶液と
同じ温度、即ち、反応温度87°に加熱して、このアル
カリ土類硝酸塩溶液へーにの添加速度で加え両液全反応
させ、反応終了後も反応液の攪拌を約30分間継続し結
晶熟成を行う。
Next, heat this solution to about 87°0 while stirring.Next, for example, heat an ammonium carbonate solution with a concentration of 1.1 mol/l to about 87°0, and add this ammonium carbonate solution to an alkaline earth nitrate solution. The alkaline earth nitrate solution was heated to the same temperature as the alkaline earth nitrate solution, that is, the reaction temperature of 87°, and added to the alkaline earth nitrate solution at the same rate as the alkaline earth nitrate solution, allowing both solutions to fully react, and the reaction solution was stirred even after the reaction was completed. This continues for about 30 minutes to ripen the crystals.

次に沈澱生成したアルカリ土類炭酸塩(Ba 、Sr 
Next, precipitated alkaline earth carbonates (Ba, Sr
.

Oa) 00sを静置し、上溌液を排出して、不純物が
除去されるまで温水洗浄を繰返して行ない、最後に一遠
心脱水等の方法で脱水する。
Oa) 00s is allowed to stand still, the supernatant liquid is discharged, hot water washing is repeated until impurities are removed, and finally, water is dehydrated by a method such as centrifugal dehydration.

この様な製造方法によシ得られたアルカリ土類炭酸塩の
添力0した硝酸アンモニウム量による結晶形状を電子顕
微鏡写真により対比したところ硝酸アンモニウム量を増
加するにつれて結晶粒度は針状の結晶形状を保ちながら
粗大となシ、硝酸アンモニウムの添加量が結晶粒度成長
促進に起因していることが確認できた。
When the crystal shape of the alkaline earth carbonate obtained by such a production method was compared with the amount of ammonium nitrate with zero additive using electron micrographs, it was found that as the amount of ammonium nitrate was increased, the crystal grain size maintained an acicular crystal shape. However, it was confirmed that the amount of ammonium nitrate added was due to the promotion of grain size growth.

≠暗図の曲線(1)は本実施例によって製造したアルカ
リ土類炭酸塩の硝酸アンモニウム添加量と反応生成した
結晶の平均粒度との関係を沈降式粒度分布測定装置で測
定したものである。
≠The dark curve (1) shows the relationship between the amount of ammonium nitrate added to the alkaline earth carbonate produced in this example and the average particle size of the crystals produced by the reaction, measured using a sedimentation type particle size distribution measuring device.

この図より本発明の製造方法によれば硝酸アンモニウム
添加量の増加と共に平均粒度の粗大化が認められ電子M
機銃写真による結果と同様の傾向を示している事がわか
る。
From this figure, it can be seen that according to the production method of the present invention, the average particle size becomes coarser as the amount of ammonium nitrate added increases.
It can be seen that the results show the same tendency as the results from the machine gun photographs.

アンモニウムイオンの結晶粒度への作用は現時点では明
確でないが結晶成長を促進する作用のあることが明らか
になった。
Although the effect of ammonium ions on crystal grain size is not clear at present, it has become clear that they have the effect of promoting crystal growth.

前述した実施例では硝酸アンモニウムの添加量を硝酸カ
ル/ラムをベースにしたが、これに限定されるものでは
なく硝酸塩溶液中に混合させれば同様な効果が得られる
ことは言うまでもない。
In the above embodiments, the amount of ammonium nitrate added was based on Cal/Rum nitrate, but it is not limited to this, and it goes without saying that the same effect can be obtained by mixing it into the nitrate solution.

また実施例では硝酸アンモニウムで説明したが、炭酸塩
らるV−は陰極に悪書の必る塩類以外のアンそニウム塩
類で分解温度が100°C以上で水溶性かつ安定なアン
モニウム塩類を使用しても同様な結果が得られることも
言うまでもない。
In addition, although the explanation was made using ammonium nitrate in the examples, the carbonate Ral V- uses ammonium salts other than salts that require bad writing for the cathode, and is water-soluble and stable ammonium salts with a decomposition temperature of 100°C or higher. Needless to say, similar results can be obtained.

〔発明の効果〕〔Effect of the invention〕

上述のように本発明のアルカリ土類炭酸塩の製造方法に
よれば種々の電子管に個別に要求される結晶粒度を電子
管特性に有利とされている針状の結晶状態を維持したま
までコントロールすることが可能となり、また最も収率
が筒〈経済的な反応条件で沈#させることができ、更に
電子管@極に不純物程度に混入しても、その特性に悪書
のないアンモニウムイオンを使用しているので特性悪化
の心配が全くない。
As mentioned above, according to the method for producing alkaline earth carbonates of the present invention, the crystal grain size individually required for various electron tubes can be controlled while maintaining the acicular crystal state that is said to be advantageous for electron tube characteristics. In addition, the highest yield can be achieved by using ammonium ions, which can be precipitated under economical reaction conditions, and whose characteristics are not bad even if they are mixed into the electron tube @ electrode to the extent of impurities. There is no need to worry about deterioration of characteristics.

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

図は硝酸アンモニウム添加量と平均粒度の関係、を示す
曲線図である。 1・・・硝酸アンモニウム添〃口量と平均粒此の関係を
示す曲線 代理人 弁理士 井 上 −男
The figure is a curve diagram showing the relationship between the amount of ammonium nitrate added and the average particle size. 1...Curve showing the relationship between the amount of ammonium nitrate added and the average particle size Agent Patent attorney Inoue - Male

Claims (2)

【特許請求の範囲】[Claims] (1) バリウム1スト四ンチウム、及びカルシウムか
らなる3種類の可溶性アルカリ土類硝酸塩溶液と、可溶
性炭酸塩溶液とを反応させて、前記バリウム、ストロン
チウム及びカル7クムの複合炭酸塩粉末全生成するに際
し、前記可溶性アルカリ土類硝酸塩浴液に結晶成長を促
進させる作用を有するアンモニウムイオンを含む塩類の
所定量を混合溶解させた後、前記可溶性炭酸塩溶液と反
応させ、生成される前記バリウム、ストロ/チウム及び
カル7クムからなるアルカリ土類炭酸塩粉末の結晶形状
を同じくして結晶粒度を可変にするようにしたことを特
徴とするアルカリ土類炭酸塩の製造方法。
(1) Three types of soluble alkaline earth nitrate solutions consisting of barium, strontium, and calcium are reacted with a soluble carbonate solution to produce a composite carbonate powder of barium, strontium, and calcium. At this time, a predetermined amount of salts containing ammonium ions having the effect of promoting crystal growth is mixed and dissolved in the soluble alkaline earth nitrate bath solution, and then reacted with the soluble carbonate solution to form the barium and strontium. / A method for producing an alkaline earth carbonate, characterized in that the crystal shape of the alkaline earth carbonate powder consisting of thium and calcium is made to be the same and the crystal grain size is variable.
(2) 所定量が1%以下(Oを含まない)であること
を特徴とする特許請求の範囲第1項記載のア
(2) The solution according to claim 1, wherein the predetermined amount is 1% or less (does not include O).
JP4397184A 1984-03-09 1984-03-09 Preparation of alkaline-earth carbonate Granted JPS60189832A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4397184A JPS60189832A (en) 1984-03-09 1984-03-09 Preparation of alkaline-earth carbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4397184A JPS60189832A (en) 1984-03-09 1984-03-09 Preparation of alkaline-earth carbonate

Publications (2)

Publication Number Publication Date
JPS60189832A true JPS60189832A (en) 1985-09-27
JPH0445451B2 JPH0445451B2 (en) 1992-07-24

Family

ID=12678594

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4397184A Granted JPS60189832A (en) 1984-03-09 1984-03-09 Preparation of alkaline-earth carbonate

Country Status (1)

Country Link
JP (1) JPS60189832A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02180713A (en) * 1988-12-29 1990-07-13 Sakai Chem Ind Co Ltd Alkaline earth metal carbonate
JP2010132555A (en) * 1995-10-26 2010-06-17 Solvay Barium Strontium Gmbh Finely divided alkaline earth metal carbonate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02180713A (en) * 1988-12-29 1990-07-13 Sakai Chem Ind Co Ltd Alkaline earth metal carbonate
JP2010132555A (en) * 1995-10-26 2010-06-17 Solvay Barium Strontium Gmbh Finely divided alkaline earth metal carbonate

Also Published As

Publication number Publication date
JPH0445451B2 (en) 1992-07-24

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