JPS63222017A - Production of high-purity manganese compound - Google Patents

Production of high-purity manganese compound

Info

Publication number
JPS63222017A
JPS63222017A JP62054872A JP5487287A JPS63222017A JP S63222017 A JPS63222017 A JP S63222017A JP 62054872 A JP62054872 A JP 62054872A JP 5487287 A JP5487287 A JP 5487287A JP S63222017 A JPS63222017 A JP S63222017A
Authority
JP
Japan
Prior art keywords
manganese
iron
solution
compound
electrolyte
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
JP62054872A
Other languages
Japanese (ja)
Other versions
JPH0457618B2 (en
Inventor
Yoji Kenmochi
洋司 見持
Koichi Yoshioka
吉岡 孝一
Hideaki Honoki
朴木 秀明
Koichi Kanbe
神戸 功一
Kiyoshi Matsuura
松浦 清
Tatsuo Kiyono
清野 達雄
Yoshiyuki Kimura
義行 木村
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.)
Japan Metals and Chemical Co Ltd
Original Assignee
Japan Metals and Chemical Co 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 Japan Metals and Chemical Co Ltd filed Critical Japan Metals and Chemical Co Ltd
Priority to JP62054872A priority Critical patent/JPS63222017A/en
Priority to FR878717776A priority patent/FR2612173B1/en
Priority to NL8703098A priority patent/NL8703098A/en
Priority to DE3805797A priority patent/DE3805797A1/en
Priority to GB8805418A priority patent/GB2204029B/en
Publication of JPS63222017A publication Critical patent/JPS63222017A/en
Priority to US07/361,757 priority patent/US4943418A/en
Publication of JPH0457618B2 publication Critical patent/JPH0457618B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Compounds Of Iron (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

PURPOSE:To readily obtain a high-purity Mn compound, by adding ferromanganese to an aqueous solution containing an electrolyte, adjusting to proper pH, dissolving iron, aging, separating and removing undissolved substances, precipitating Mn and iron and recovering. CONSTITUTION:An electrolyte-containing aqueous solution (e.g. aqueous solution of ammonium chloride) is blended with one or more of ferromanganese and metallic manganese, an acid is added to the solution while stirring, manganese and iron are dissolved by maintaining pH2-9. The solution is aged, undissolved substances are condensed, coarse particles are formed and the undissolved substances are separated and removed. Then manganese and iron in the solution are precipitated and recovered to give a high-purity manganese compound. The prepared manganese compound has low content of impurities such as Si and P and is preferably used as a raw material for ferrite of manganese type.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は高純度マンガン化合物の製造法に関するもので
あって、特にマンガン系フェライト用原料に好適なマン
ガン化合物を製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a high purity manganese compound, and particularly to a method for producing a manganese compound suitable as a raw material for manganese ferrite.

〔従来の技術〕[Conventional technology]

従来高純度のマンガン化合物はマンガン鉱石を硫酸に溶
解し、不純物たる重金属は硫化物法、溶媒抽出法又はア
ルコレート法等で、また鉄は酸化して水酸化物として分
離除去した後、マンガンを各種塩類として回収する方法
が行われている。
Conventionally, high-purity manganese compounds are produced by dissolving manganese ore in sulfuric acid, impurity heavy metals are removed by the sulfide method, solvent extraction method, alcoholate method, etc., and iron is oxidized and separated and removed as hydroxide. Methods are being used to recover it as various salts.

最近では更に高純度のマンガン化合物を製造するために
、マンガン鉱石より不純物元等が少ないフェロマンガン
又は金属マンガンを用い、これらを直接酸で溶解し、前
期従来法と同様重金属及び鉄を分離除去し、さらに再結
晶法を組合せることによって高純度マンガン化合物を精
製する方法がある。
Recently, in order to produce manganese compounds with even higher purity, ferromanganese or metallic manganese, which has fewer impurities than manganese ore, are used, and these are directly dissolved in acid, and heavy metals and iron are separated and removed as in the previous conventional method. There is a method of purifying high-purity manganese compounds by further combining recrystallization.

しかし、前記方法は数工程を要し、かつ複信[な再結晶
法による精製工程を必要とし、処理能率が悪いばかりか
必らずしも高純度のものを得ることができない。
However, the above method requires several steps and a purification step using a multiplex recrystallization method, which not only has poor processing efficiency but also does not necessarily result in a product of high purity.

本出願人は前述従来法の欠点を改善するため、電解質を
含む水溶液にフェロマンガン、金属マンガンの1種又は
2種を加え攪拌しつつ酸を添加しpH2〜9に保持して
未溶解物を分離し、溶液中のマンガン及び鉄を沈澱して
回収することにより高純度のマンガン化合物を得る方法
を提案したく特願昭60−197246号参照)。
In order to improve the drawbacks of the conventional method described above, the present applicant added one or two of ferromanganese and metallic manganese to an aqueous solution containing an electrolyte, added acid while stirring, and maintained the pH at 2 to 9 to remove undissolved substances. (See Japanese Patent Application No. 60-197246) to propose a method for obtaining highly pure manganese compounds by separating, precipitating and recovering manganese and iron in solution.

〔本発明が解決しようとする問題点〕[Problems to be solved by the present invention]

前記特願昭60−1.97246号に記載されている発
明(以下先行技術という)は、処理工程が従来法に比較
して簡単で、しかもCr、 Co、 Ni等の重金属の
ほかP、Si、AA、V等の不純物を除去できるという
効果がある。
The invention described in the above-mentioned Japanese Patent Application No. 60-1.97246 (hereinafter referred to as the prior art) has a simple treatment process compared to the conventional method, and it can treat heavy metals such as Cr, Co, and Ni as well as P and Si. , AA, V, and other impurities can be removed.

しかし、前記先行技術は不純物の除去に有効であるけれ
ども、不純物の除去効率にかなりのバラツキがあり、従
って使用に当り不純物の含有量ごとに仕分けしなげれば
ならず、安定した品質のものを大量に供給することは困
難である。
However, although the above-mentioned prior art is effective in removing impurities, there is considerable variation in impurity removal efficiency, and therefore, it is necessary to sort by impurity content before use, and products of stable quality cannot be obtained. It is difficult to supply in large quantities.

本発明は前述先行技術の欠点を改善するため研究の結果
、フェライト用原料として使用するマンガン化合物の不
純物が極低含有量て、かつバラツキの少ない高純度マン
ガン化合物を安定して製造する方法を提供することにあ
る。
As a result of research to improve the drawbacks of the prior art described above, the present invention provides a method for stably producing a high-purity manganese compound with extremely low impurity content and little variation in manganese compound used as a raw material for ferrite. It's about doing.

〔問題点を解決するための手段〕[Means for solving problems]

本出願の第1の発明は、電解質を含む水溶液にフェロマ
ンガン、金属マンガンノ1種又ハ23一 種を加えて攪拌しつつ酸を添加し、p +−1を2〜9
に保持してマンガン及び鉄を溶解した後、溶液中のマン
ガン及び鉄を沈澱して回収する工程に於て、マンガン及
び鉄を溶解した後、熟成処理し、ついて未溶解物を分離
除去するという構成のものからなる高純度マンガン化合
物の製造法である。
The first invention of the present application is to add ferromanganese, one type of metal manganese, or one type of Ha23 to an aqueous solution containing an electrolyte, add an acid while stirring, and adjust p+-1 to 2 to 9.
In the process of precipitating and recovering the manganese and iron in the solution, after dissolving the manganese and iron, the solution is aged and then the undissolved substances are separated and removed. This is a method for producing a high-purity manganese compound consisting of the following components.

また・、第2の発明は、電解質を含む水溶液にフェロマ
ンガン、金属マンガンの1種又は2種を加えて攪拌しつ
つ酸を添加し、pHを2〜9に保持してマンガン及び鉄
を溶解した後、溶液中のマンガン及び鉄を沈澱して回収
する工程に於て、マンガン及び鉄を溶解した後、未溶解
物を分離除去し、ついてこれに沈澱剤を添加して熟成処
理するという構成からなる高純度マンガン化合物の製造
法である。
In addition, the second invention is to add one or two of ferromanganese and metallic manganese to an aqueous solution containing an electrolyte, add acid while stirring, and maintain the pH at 2 to 9 to dissolve manganese and iron. After that, in the process of precipitating and recovering the manganese and iron in the solution, after dissolving the manganese and iron, undissolved substances are separated and removed, followed by adding a precipitant to the solution and subjecting it to aging treatment. This is a method for producing a high purity manganese compound consisting of:

〔作   用〕[For production]

本発明は以」−の如き構成のものからなり、芸に使用す
る電解質は塩化アンモニウム、硝酸アンモニウム、酢酸
アンモニウム又はアルカリ金属塩等の1種又は2種以」
二である。
The present invention has the following configuration, and the electrolyte used in the art is one or more of ammonium chloride, ammonium nitrate, ammonium acetate, or alkali metal salts.
Two.

また、本発明に云うマンガン化合物とは、マンガン化合
物単独のもののほか、マンガン化合物と鉄化合物との混
合物を含むものとする。
Furthermore, the manganese compound referred to in the present invention includes not only a manganese compound alone but also a mixture of a manganese compound and an iron compound.

本発明の原料たるフェロマンガン、金属マンガン(お粉
砕しく好ましくは60メツシユ下)、これを電解質溶液
中へ添加する。
Ferromanganese and metallic manganese (pulverized, preferably less than 60 mesh), which are the raw materials of the present invention, are added to an electrolyte solution.

前記の如きフェロマンガン、金属マンガンを水に添加す
ると、マンガン、鉄は一部水と反応して水酸化物を生成
し、その液のpHは9.7前後まで上昇する。
When ferromanganese and metallic manganese as described above are added to water, some of the manganese and iron react with the water to produce hydroxide, and the pH of the liquid increases to around 9.7.

一方、塩化アンモニウム等の電解質を含む溶液に、前記
フェロマンガン、金属マンガンを添加すると、マンガン
、鉄は同様に水酸化物を生成するが、前記電解質の緩衝
作用によって溶液のpHが低下する。そのpHの低下す
る程度は電解質の濃度によって異なるが、例えば塩化ア
ンモニウムの2%溶液の場合pH=9.0程度、20%
溶液ては7.8程度となる。
On the other hand, when the ferromanganese and metal manganese are added to a solution containing an electrolyte such as ammonium chloride, manganese and iron similarly produce hydroxides, but the buffering action of the electrolyte lowers the pH of the solution. The degree to which the pH decreases varies depending on the concentration of the electrolyte, but for example, in the case of a 2% solution of ammonium chloride, the pH is about 9.0, 20%
The solution value is about 7.8.

芸で水酸化マンガン(n)又は水酸化鉄(I+)が完全
に沈澱するpHは夫々9以」−18以上程度であるから
、生成した水酸化マンガン及び水酸化鉄は一部溶解し、
他の部分は沈澱した状態となす、他方マンガン、鉄より
イオン化傾向の貴なる元素、即ち重金属元素は未反応の
まま残存する。また、この方法によると、フェロマンガ
ン、金属マンガンに含まれているCao 、 SiO2
゜A I 203. MgO等の酸化物を主体とする非
金属介在物(スラグ成分)は殆んど溶解せず、はぼ完全
に分離てぎる。
The pH at which manganese hydroxide (n) or iron hydroxide (I+) completely precipitates is approximately 9 or higher and 18 or higher, respectively, so the produced manganese hydroxide and iron hydroxide are partially dissolved.
Other parts remain in a precipitated state, while noble elements that tend to ionize more than manganese and iron, ie, heavy metal elements, remain unreacted. In addition, according to this method, Cao, SiO2 contained in ferromanganese and metal manganese
゜AI 203. Nonmetallic inclusions (slag components) mainly composed of oxides such as MgO are hardly dissolved and are almost completely separated.

前記のようにして生成した水酸化マンガン。Manganese hydroxide produced as described above.

水酸化鉄に酸を添加すれば水酸化マンガン、水酸化鉄は
塩となって溶解し、重金属元素を完全に分離てきる。蕊
て使用する酸は塩酸、硫酸。
When acid is added to iron hydroxide, manganese hydroxide and iron hydroxide become salts and dissolve, completely separating heavy metal elements. The acids used for cleaning are hydrochloric acid and sulfuric acid.

酢酸又は硝酸の何れでもよい。Either acetic acid or nitric acid may be used.

而して、電解質を含む溶液ては前記電解質の緩衝作用に
よって酸の添加によるpH変化が小さくなる。そして、
このようなpH領域(少なくともpH= 2以上)ては
未反応物は酸による影響を受けず、従って何等溶解せず
、不純物を完全に分離することができる。
Therefore, in a solution containing an electrolyte, the pH change due to the addition of an acid is reduced due to the buffering effect of the electrolyte. and,
In such a pH range (at least pH=2 or higher), unreacted substances are not affected by the acid and are therefore not dissolved at all, allowing complete separation of impurities.

前記の方法によってP、i、Vその他各種の元素が可成
りの程度除去できるが、その除去率にバラツキがある。
Although various elements such as P, i, and V can be removed to a considerable extent by the above method, there are variations in the removal rate.

特に、Co、 Ca等のように溶解速度の温度依存性が
大きいものとか、P、 Si。
In particular, materials such as Co and Ca, whose dissolution rate is highly dependent on temperature, P and Si.

AI等のように反応系中の未反応物は沈澱に吸着して除
去されるものはその影響が大きい。
This has a large effect on substances such as AI, in which unreacted substances in the reaction system are adsorbed to the precipitate and removed.

本発明はフェロマンガン、金属マンガンの1種又は2種
を電解質を含む水溶液中に添加し、攪拌しつつ酸を添加
し、pHを2〜9に保持してマンガン及び鉄を溶解して
回収する方法において、マンガン及び鉄を溶解した後、
熟成する工程を採用することによって不純物の除去率が
向上し、かつそのバラツキの少ない安定した製品を得る
ことかできる。
The present invention involves adding one or both of ferromanganese and metallic manganese to an aqueous solution containing an electrolyte, adding acid while stirring, and maintaining the pH at 2 to 9 to dissolve and recover manganese and iron. In the method, after dissolving the manganese and iron,
By adopting the aging process, the removal rate of impurities can be improved and a stable product with less variation can be obtained.

即ち、第1の発明はマンガン及び鉄を溶解した後、熟成
するものである。これにより溶解中に溶解している珪酸
分が除々に重合して沈澱し、未溶解物とともに分離でき
る。
That is, in the first invention, manganese and iron are dissolved and then aged. As a result, the silicic acid component dissolved during dissolution gradually polymerizes and precipitates, and can be separated together with undissolved materials.

さらに第1の発明は、前記熟成処理することによって、
未溶解物の濾過分離の際、濾過速度を大巾に改善するこ
とができる。これは水溶液を熟成することによって未溶
解物が徐々に凝縮して粗大粒子を形成するものと考えら
れ、従って、濾過処理が容易になり、工業的に実施する
場合大きな効果がある。
Furthermore, the first invention provides, by the aging treatment,
When undissolved substances are separated by filtration, the filtration rate can be greatly improved. This is thought to be due to the gradual condensation of undissolved substances to form coarse particles as the aqueous solution ages, and therefore the filtration process is facilitated, which is highly effective when carried out industrially.

また、熟成に要する時間は、目的とする製品のSiの許
容量によって適宜選択すればよいが、望ましくは3時間
以上10時間程度とする。
Further, the time required for aging may be appropriately selected depending on the allowable amount of Si in the target product, but is desirably 3 hours or more and about 10 hours.

前記熟成処理を終了した後、溶液中の未溶解−8= 物を分前除去する。After completing the aging process, undissolved −8= Remove things in advance.

第2の発明は、マンガン及び鉄を水溶液中に溶解抽出し
、未溶解物を分離除去した後、これに沈澱剤を添加して
熟成するものである。これにより溶液中に溶出したPが
沈澱剤に吸着されて沈澱し簡単に分離除去てきる。
The second invention involves dissolving and extracting manganese and iron in an aqueous solution, separating and removing undissolved substances, and then adding a precipitant to the solution for ripening. As a result, the P eluted into the solution is adsorbed by the precipitant, precipitated, and easily separated and removed.

芸で使用する沈澱剤は、アルミニウム塩、鉄(III)
塩その他溶液中に溶解抽出することがないものを若干添
加する。この場合、不純物のSiは勿論、Pはほぼ完全
に除去てきる。
The precipitants used in the art are aluminum salts, iron(III)
Add a small amount of salt or other substances that will not be dissolved or extracted into the solution. In this case, not only the impurity Si but also the P can be almost completely removed.

尚、第2の発明においても、熟成時において添加される
沈澱剤が凝集し、濾過速度が向上する。
In addition, also in the second invention, the precipitant added during ripening aggregates, improving the filtration rate.

前述の如き手段によって水溶液中には、実質的にマンガ
ン及び鉄のみが溶解抽出された状態として得られる。
Substantially only manganese and iron are dissolved and extracted in the aqueous solution by the above-mentioned means.

前記水溶液からマンガン及び鉄を回収するには、前記溶
液中のマンガン及び鉄を例えば炭酸塩として沈澱せしめ
た後、炭酸塩を回収すれば、不純物の含有量の極めて少
ないマンガン化合物を回収することができる。
In order to recover manganese and iron from the aqueous solution, manganese and iron in the solution are precipitated, for example, as carbonates, and then the carbonates are recovered, thereby making it possible to recover manganese compounds with an extremely low content of impurities. can.

また、前記炭酸塩は必要によってはこれを800°Cに
焼成すれば簡単にマンガン及び鉄を含む高純度の酸化物
として回収することができる。
Furthermore, if necessary, the carbonate can be easily recovered as a high-purity oxide containing manganese and iron by calcining it at 800°C.

尚、溶液中からマンガン化合物を回収するに当り、必ら
ずしも炭酸塩として回収する必要はなく、溶液から容易
に沈澱分離できるものてあればよい。
Note that when recovering the manganese compound from the solution, it is not necessarily necessary to recover it as a carbonate, as long as it can be easily precipitated and separated from the solution.

〔実 施 例〕〔Example〕

以下実施例をもって本発明を具体的に説明する。 The present invention will be specifically explained below with reference to Examples.

実施例1 10%塩化アンモニウム溶液500 lに、6oメツシ
ユ以下に粉砕したフェロマンガン粉末50gを加えて、
前記溶液を攪拌しながら、かつ前記溶液に1.2M塩酸
を逐次添加してフェロマンガン中のマンガン及び鉄を溶
解抽出した。
Example 1 To 500 liters of 10% ammonium chloride solution, 50 g of ferromanganese powder crushed to 6o mesh or less was added,
While stirring the solution, 1.2M hydrochloric acid was successively added to the solution to dissolve and extract manganese and iron in the ferromanganese.

]、2M塩酸の添加によって、前記溶液のpHは8.5
から逐次低下するが、pHが5になったとぎ、12M塩
酸の添加を中止し反応を終了させた。
], by addition of 2M hydrochloric acid, the pH of the solution was 8.5.
The pH gradually decreased, but when the pH reached 5, the addition of 12M hydrochloric acid was stopped and the reaction was terminated.

ついで、前記反応を終了した溶液(未溶解物を含む)を
別容器に移し、10時間熟成させた。
Then, the solution (containing undissolved materials) after the reaction was transferred to another container and aged for 10 hours.

この場合、経時変化をみるための適宜溶液を採取してS
iの分析を行なった処、第1図に示す通りである。
In this case, collect appropriate solutions to observe changes over time.
The analysis of i is shown in Figure 1.

第1図から明らかなように、溶液中のSiは熟成時間の
経過につれて低下しており、熟成がSiの除去に有効で
あることが認められる。
As is clear from FIG. 1, the Si content in the solution decreases as the aging time progresses, indicating that aging is effective in removing Si.

また、この場合第1の発明と熟成処理しない場合との濾
過速度を比較すると、第1表の通りである。
In addition, in this case, a comparison of the filtration rates between the first invention and the case without aging treatment is as shown in Table 1.

第1表 (註)濾過はフィルタープレスを使用。Table 1 (Note) Use a filter press for filtration.

即ち、第1の発明では濾過速度が熟成処理なしの場合に
比較して犬11に向上しているのが認められ、濾過時間
を短縮できる。
That is, in the first invention, it is recognized that the filtration speed is improved to 11 compared to the case without aging treatment, and the filtration time can be shortened.

実施例2 実施例1と同一の方法で10%塩化アンモニウム溶液中
にマンガン及び鉄を溶解抽出した後、溶液中の未溶解物
を濾過分離し、ついてこれに10%塩化第二鉄溶液を5
00 ml添加混合して10時間熟成し、溶液中のP、
 Siを夫々分析した処、第2表の通りであった。尚、
比較のため熟成処理しない場合の結果を併記する。
Example 2 After dissolving and extracting manganese and iron in a 10% ammonium chloride solution in the same manner as in Example 1, undissolved substances in the solution were separated by filtration, and then 5% of a 10% ferric chloride solution was added.
00 ml was added and mixed and aged for 10 hours, P in the solution,
The analysis of Si was as shown in Table 2. still,
For comparison, the results without aging treatment are also shown.

第2表 〔発明の効果〕 以上の如く本発明はフェロマンガ乙金属マンガンを電解
質水溶液中に添加し、酸を添加しつつpH2〜9に調整
してマンガン及び鉄を溶液中に溶解抽出し回収するに当
り、マンガン及び鉄を溶解した溶液を熟成すること、ま
た未溶解物を分離除去した後、沈澱剤を添加して熟成す
ることによって不純物、特にSi、Pの除去率を向上さ
せることができる。
Table 2 [Effects of the Invention] As described above, the present invention involves adding ferromanganese metal manganese to an electrolyte aqueous solution, adjusting the pH to 2 to 9 while adding an acid, dissolving and extracting manganese and iron in the solution, and recovering them. In this process, it is possible to improve the removal rate of impurities, especially Si and P, by aging a solution in which manganese and iron are dissolved, and by separating and removing undissolved substances and then adding a precipitant and aging. can.

また、熟成処理によって未 物の沈澱を凝集できるため
、未溶解物の濾過処理を改善することができる。
In addition, since the aging treatment allows undissolved precipitates to coagulate, the filtration process for undissolved matters can be improved.

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

図面は熟成時間に対する溶液中のSi含有量との関係を
示すグラフである。
The figure is a graph showing the relationship between the aging time and the Si content in the solution.

Claims (2)

【特許請求の範囲】[Claims] (1)電解質を含む水溶液にフェロマンガン、金属マン
ガンの1種又は2種を加えて覚拌しつつ酸を添加し、p
Hを2〜9に保持してマンガン及び鉄を溶解した後、溶
液中のマンガン及び鉄を沈澱して回収する工程に於て、
マンガン及び鉄を溶解した後、熟成処理し、ついで未溶
解物を分離除去することを特徴とする高純度マンガン化
合物の製造法。
(1) Add one or both of ferromanganese and metal manganese to an aqueous solution containing an electrolyte, add acid while stirring, and p
After dissolving manganese and iron by maintaining H at 2 to 9, in the step of precipitating and recovering manganese and iron in the solution,
A method for producing a high-purity manganese compound, which comprises dissolving manganese and iron, subjecting them to aging treatment, and then separating and removing undissolved substances.
(2)電解質を含む水溶液にフェロマンガン、金属マン
ガンの1種又は2種を加えて攪拌しつつ酸を添加し、p
Hを2〜9に保持してマンガン及び鉄を溶解した後、溶
液中のマンガン及び鉄を沈澱して回収する工程に於て、
マンガン及び鉄を溶解した後、未溶解物を分離除去し、
ついでこれに沈澱剤を添加して熟成処理することを特徴
とする高純度マンガン化合物の製造法。
(2) Add one or both of ferromanganese and metallic manganese to an aqueous solution containing an electrolyte, add acid while stirring, and p
After dissolving manganese and iron by maintaining H at 2 to 9, in the step of precipitating and recovering manganese and iron in the solution,
After dissolving manganese and iron, separating and removing undissolved materials,
A method for producing a high-purity manganese compound, which comprises then adding a precipitant to the compound and subjecting it to aging.
JP62054872A 1987-03-10 1987-03-10 Production of high-purity manganese compound Granted JPS63222017A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP62054872A JPS63222017A (en) 1987-03-10 1987-03-10 Production of high-purity manganese compound
FR878717776A FR2612173B1 (en) 1987-03-10 1987-12-18 PROCESS FOR THE PREPARATION OF HIGH PURITY MANGANESE COMPOUNDS
NL8703098A NL8703098A (en) 1987-03-10 1987-12-22 PROCESS FOR PREPARING HIGH PURITY MANGANES.
DE3805797A DE3805797A1 (en) 1987-03-10 1988-02-24 METHOD FOR PRODUCING HIGHLY PURE MANGANE CONNECTIONS
GB8805418A GB2204029B (en) 1987-03-10 1988-03-08 A method of preparing high-purity manganese compounds
US07/361,757 US4943418A (en) 1987-03-10 1989-05-30 Method of preparing high-purity manganese compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62054872A JPS63222017A (en) 1987-03-10 1987-03-10 Production of high-purity manganese compound

Publications (2)

Publication Number Publication Date
JPS63222017A true JPS63222017A (en) 1988-09-14
JPH0457618B2 JPH0457618B2 (en) 1992-09-14

Family

ID=12982680

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62054872A Granted JPS63222017A (en) 1987-03-10 1987-03-10 Production of high-purity manganese compound

Country Status (1)

Country Link
JP (1) JPS63222017A (en)

Also Published As

Publication number Publication date
JPH0457618B2 (en) 1992-09-14

Similar Documents

Publication Publication Date Title
JP6336469B2 (en) Method for producing scandium-containing solid material with high scandium content
US6113868A (en) Process for treating tungstate solutions to reduce molybdenum impurity and other impurity content
US4724128A (en) Method for purifying molybdenum
JPH09176756A (en) High-purity method for rare earth metal
JPH01153532A (en) Method for purifying acid solution containing ferrous ions
JP3307204B2 (en) Concentration separation and recovery method of rare earth metal
SU793373A3 (en) Method of purifying zinc sulfate solutions
JPS63222017A (en) Production of high-purity manganese compound
JPH0582330B2 (en)
JPS63315521A (en) Method for purifying waste liquor from acid cleaning with hydrochloric acid
US2735760A (en) precipitation from n
JP2994405B2 (en) Purification method of alkali hydroxide
JPH04198017A (en) Purification of scandium oxide
US4943418A (en) Method of preparing high-purity manganese compounds
CN109055775B (en) Regeneration method of complexing precipitator for purifying copper electrolyte
JPS63222016A (en) Production of high-purity manganese compound
JPH035324A (en) Production of iron oxide for rerrite material
JPH0256289B2 (en)
JPH059617A (en) Method for removing tungsten in molybdenum oxide
US3138637A (en) Process for recovering ethylenediamine-tetraacetic acid (edta) from copper-edta-ion exchange effluent solutions
JP3029373B2 (en) Recovery method of zinc chloride from zinc dross
JPH01179712A (en) Treatment of scrap indium-phosphorus compound semiconductor
JPS63183138A (en) Method for refining metallic gallium
JPH01115820A (en) Production of niobium hydroxide of tantalum hydroxide
JPH0375223A (en) Recovery of indium

Legal Events

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