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JPH0639334B2 - Production method of β-manganese dioxide - Google Patents
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JPH0639334B2 - Production method of β-manganese dioxide - Google Patents

Production method of β-manganese dioxide

Info

Publication number
JPH0639334B2
JPH0639334B2 JP59018924A JP1892484A JPH0639334B2 JP H0639334 B2 JPH0639334 B2 JP H0639334B2 JP 59018924 A JP59018924 A JP 59018924A JP 1892484 A JP1892484 A JP 1892484A JP H0639334 B2 JPH0639334 B2 JP H0639334B2
Authority
JP
Japan
Prior art keywords
mno
manganese dioxide
heat treatment
nitric acid
electrolytic
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
Application number
JP59018924A
Other languages
Japanese (ja)
Other versions
JPS60166229A (en
Inventor
曉 上平
資子 新中
英雅 田村
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.)
Sony Corp
Original Assignee
Sony 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 Sony Corp filed Critical Sony Corp
Priority to JP59018924A priority Critical patent/JPH0639334B2/en
Publication of JPS60166229A publication Critical patent/JPS60166229A/en
Publication of JPH0639334B2 publication Critical patent/JPH0639334B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/48Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/50Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
    • 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

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Description

【発明の詳細な説明】 本発明はリチウムマンガン電池(Li-MnO2電池)や固体
電解コンデンサ、各種触媒等に用いられるβ−二酸化マ
ンガンに製法に関し、特に高純度のβ−二酸化マンガン
の製法に関するものである。
The present invention relates to a method for producing β-manganese dioxide used in lithium manganese batteries (Li-MnO 2 batteries), solid electrolytic capacitors, various catalysts, etc., and particularly to a method for producing high-purity β-manganese dioxide. It is a thing.

マンガンの代表的な酸化物である二酸化マンガン(Mn
O2)は、その結晶構造の違い等から、α−二酸化マンガ
ン(α−MnO2)、β−二酸化マンガン(β−MnO2)、γ
−二酸化マンガン(γ−MnO2)等が知られており、例え
ばLi-MnO2電池の正極活物質として用いられる二酸化マ
ンガンとしては、従来、硫酸マンガンや塩化マンガンの
酸性浴からの電解酸化によって得られる電解二酸化マン
ガンや中性硫酸マンガンの沸騰溶液に過マンガン酸アル
カリ溶液を添加して得られる化学合成二酸化マンガン等
のγ−MnO2が使用されている。
Manganese dioxide (Mn
O 2 ), α-manganese dioxide (α-MnO 2 ), β-manganese dioxide (β-MnO 2 ), γ
-Manganese dioxide (γ-MnO 2 ) and the like are known, and, for example, manganese dioxide used as a positive electrode active material of a Li-MnO 2 battery is conventionally obtained by electrolytic oxidation of manganese sulfate or manganese chloride from an acidic bath. Γ-MnO 2 such as chemically synthesized manganese dioxide obtained by adding an alkaline solution of permanganate to a boiling solution of electrolytic manganese dioxide or neutral manganese sulfate is used.

ところで、上述の電解酸化や化学合成で得られるγ−Mn
O2は、かなりの量の水分を含んでいることが知られてお
り、また、化学量論的にもずれが生じていると言われて
いる。すなわち、上記電解二酸化マンガンあるいは化学
合成二酸化マンガンをMnOxとしたときに、x=2.0では
なくx=1.95前後であると言われている。そして、この
x=2.0からのずれは、三二酸化マンガン(Mn2O3)等の
存在によるものと考えられている。
By the way, γ-Mn obtained by the above-mentioned electrolytic oxidation or chemical synthesis
O 2 is known to contain a considerable amount of water, and is also said to have a stoichiometric deviation. That is, when the electrolytic manganese dioxide or the chemically synthesized manganese dioxide is MnOx, it is said that x = 1.95 instead of x = 2.0. The deviation from x = 2.0 is considered to be due to the presence of manganese trioxide (Mn 2 O 3 ).

このように、γ−MnO2が水分を含んだり不純物であるMn
2O3を含んでいるために、このγ−MnO2を使用する上で
種々の欠点が問題となっている。
In this way, γ-MnO 2 contains Mn
Since it contains 2 O 3 , various defects have been problems in using this γ-MnO 2 .

例えば、Li-MnO2電池においては、負極活物質として金
属リチウムを用いているので水分を極端に嫌い、もしも
上記γ−MnO2中に水分が存在すると、この水が上記金属
リチウムと反応して電池罐の腐蝕や漏液を引き起こし保
存特性が悪くなってしまう。また、γ−MnO2の不純物で
あるMn2O3はLi-MnO2電池においては活物質ではないの
で、このMn2O3が混入すると利用できるγ−MnO2の量が
かなり少なくなって電池の寿命が低下したり、電池の電
気抵抗が増加する等、電池の性能を著しく劣化してしま
う。あるいは、上記γ−MnO2を固体電解コンデンサに使
用した場合には、このγ−MnO2中の水分により耐電圧、
漏電流、経時変化等の問題が生じ、また不純物であるMn
2O3により電気抵抗の増加、耐圧信頼性、周波数特性等
に問題が生じている。さらに、上記γ−MnO2を触媒とし
て用いる場合にも、上記Mn2O3の存在は好ましいもので
はない。
For example, in a Li-MnO 2 battery, since metallic lithium is used as the negative electrode active material, it is extremely disliked by water.If water is present in the γ-MnO 2 , the water reacts with the metal lithium. Corrosion of the battery canister or leakage will occur, resulting in poor storage characteristics. Further, since Mn 2 O 3 which is an impurity of γ-MnO 2 is not an active material in a Li-MnO 2 battery, the amount of γ-MnO 2 that can be used when this Mn 2 O 3 is mixed is considerably reduced and the battery is considerably reduced. The life of the battery is shortened, the electric resistance of the battery is increased, and the battery performance is significantly deteriorated. Alternatively, when the γ-MnO 2 is used in a solid electrolytic capacitor, the withstand voltage due to the water content in the γ-MnO 2 ,
Problems such as leakage current and changes over time occur, and impurities such as Mn
2 O 3 causes problems in increase of electric resistance, reliability of breakdown voltage, frequency characteristics, and the like. Furthermore, even when γ-MnO 2 is used as a catalyst, the presence of Mn 2 O 3 is not preferable.

そこで従来は、上述のγ−MnO2を350〜450℃程度
の条件で熱処理し、含有する水分を除去して使用してい
る。しかしながら、このような熱処理によっても上記水
分を完全に除去することは難かしく、本発明者等が電解
二酸化マンガンを350〜450℃で熱処理した生成物
について熱分析によりその組成を分析したところ、残存
水分が1.2〜1.8重量%、Mn2O3と考えられる不純物が7
〜18重量%存在することが判明した。さらに、上記水
分の除去という観点からは上記熱処理温度をより高温と
なしまた長時間に亘って処理することが好ましいが、こ
の場合にはγ−MnO2のMn2O3への分解が始まり不純物の
混入量が多くなってしまう。
Therefore, conventionally, the above-mentioned γ-MnO 2 is heat-treated under the condition of about 350 to 450 ° C. to remove the contained water before use. However, it is difficult to completely remove the above moisture even by such heat treatment, and the present inventors analyzed the composition by thermal analysis of the product obtained by heat treating electrolytic manganese dioxide at 350 to 450 ° C. The water content is 1.2 to 1.8% by weight, and the impurities considered to be Mn 2 O 3 are 7
It was found to be present at -18% by weight. Further, from the viewpoint of removing the water content, it is preferable that the heat treatment temperature is not higher and the treatment is performed for a long time, but in this case, decomposition of γ-MnO 2 into Mn 2 O 3 is started and impurities are started. The amount of mixed in will increase.

このため、水分をほとんど含まず熱力学的に安定なβ−
MnO2が注目されている。このβ−MnO2の製法としては、
通常は硝酸マンガン(Mn(NO3)2・6H2O)を熱分解すると
いう方法が行なわれており、例えば固体電解コンデンサ
の製造工程においては、タンタルTaやアルミニウムA
等のバルブ金属上にホウ酸、ホウ酸アンモニウム、リ
ン酸アンモニウム等の電解質溶液から陽極酸化法により
金属酸化物被膜を形成させて、さらにこの上に硝酸マン
ガンを浸漬(ディッピング)やスプレーによる吹付け等
の手段により付着し、熱分解してβ−MnO2層を形成して
いる。
Therefore, the thermodynamically stable β-
MnO 2 is attracting attention. As a method for producing this β-MnO 2 ,
Usually, a method of thermally decomposing manganese nitrate (Mn (NO 3 ) 2 .6H 2 O) is performed. For example, in the manufacturing process of a solid electrolytic capacitor, tantalum Ta or aluminum A is used.
A metal oxide film is formed on the valve metal, such as boric acid, ammonium borate, ammonium phosphate, etc., by an anodic oxidation method, and manganese nitrate is further dipped on it or sprayed by spraying. And the like, and thermally decomposed to form a β-MnO 2 layer.

しかしながら、上述のような硝酸マンガンの熱分解によ
って得られるβ−MnO2においてもMn2O3の混入はさけら
れずβ−MnO2の品質を低下してしまうばかりか、原料と
なる硝酸マンガンの価格が高いので、安価に大量に供給
することが困難である。
However, even in β-MnO 2 obtained by thermal decomposition of manganese nitrate as described above, mixing of Mn 2 O 3 is not avoided and not only the quality of β-MnO 2 is deteriorated, but also manganese nitrate as a raw material Since the price is high, it is difficult to supply in large quantities at a low price.

さらにまた、先の電解二酸化マンガンや化学合成二酸化
マンガン等のγ−MnO2を高温で熱処理してβ−MnO2に相
転移させることも考えられるが、この場合にも上記熱処
理温度が高温であるために生成するβ−MnO2がさらに分
解し酸素を放出してMn2O3の如き不純物が生成してしま
い、実用するに至っていない。
Furthermore, it is possible to heat-process γ-MnO 2 such as electrolytic manganese dioxide or chemically synthesized manganese dioxide at a high temperature to cause a phase transition to β-MnO 2 , but in this case also, the heat treatment temperature is high. Therefore, β-MnO 2 thus generated is further decomposed and oxygen is released to generate impurities such as Mn 2 O 3 , which is not practical.

そこで、本発明は、上述の従来の方法の有する欠点を解
消するために提案されたものであり、安価で入手の容易
な電解二酸化マンガンや化学合成二酸化マンガンを原料
として高純度なβ−MnO2を得ることが可能なβ−MnO2
製法を提供することを目的とする。
Therefore, the present invention has been proposed in order to eliminate the drawbacks of the above-mentioned conventional method, high-purity β-MnO 2 using electrolytic manganese dioxide or chemically synthesized manganese dioxide that is inexpensive and easily available as a raw material. An object of the present invention is to provide a method for producing β-MnO 2 capable of obtaining

本発明者等は、上記目的を達成せんものと鋭意検討の結
果、あらかじめ電解二酸化マンガンや化学合成二酸化マ
ンガンを高温で熱処理してβ−MnO2とMn2O3との混合物
に変換しておき、さらにこの混合物に硝酸を加えて熱処
理することにより純度の高いβ−MnO2が得られることを
見出し本発明を完成したものであって、電解二酸化マン
ガンあるいは化学合成二酸化マンガンを熱処理して得ら
れるβ−二酸化マンガンと三二酸化マンガンの混合生成
物に硝酸を加えて熱処理することを特徴とするものであ
る。
The present inventors, as a result of earnest studies to achieve the above-mentioned object, previously heat-treated electrolytic manganese dioxide or chemically synthesized manganese dioxide at a high temperature to convert it into a mixture of β-MnO 2 and Mn 2 O 3. The present invention has been completed by further discovering that highly pure β-MnO 2 can be obtained by adding nitric acid to this mixture and subjecting it to heat treatment, which is obtained by heat treating electrolytic manganese dioxide or chemically synthesized manganese dioxide. It is characterized in that nitric acid is added to a mixed product of β-manganese dioxide and manganese trioxide to perform heat treatment.

すなわち、本発明においては、電解二酸化マンガンある
いは化学合成二酸化マンガン等のγ−MnO2を出発原料と
して準備し、先ずこのγ−MnO2を420〜650℃の温
度条件で熱処理する。
That is, in the present invention, γ-MnO 2 such as electrolytic manganese dioxide or chemically synthesized manganese dioxide is prepared as a starting material, and this γ-MnO 2 is first heat-treated at a temperature of 420 to 650 ° C.

この熱処理による生成物は、上記γ−MnO2の相転移によ
るβ−MnO2と、熱分解により生成するMn2O3との混合物
である。
The product of this heat treatment is a mixture of the above and γ-MnO β-MnO 2 by phase transition 2, and Mn 2 O 3 produced by pyrolysis.

次いで、上記熱処理によって生成するβ−MnO2とMn2O3
の混合物に硝酸を加えて再び加熱し熱処理を行なう。
Then, β-MnO 2 and Mn 2 O 3 produced by the above heat treatment
Nitric acid is added to the mixture and heated again to perform heat treatment.

上記硝酸による熱処理温度としては、170〜500℃
であることが好ましい。この熱処理温度が500℃を越
えると、生成するβ−MnO2がさらに分解し不純物である
Mn2O3を生ずる虞れがある。また、上記熱処理時に加え
る硝酸の添加量としては、上記γ−MnO2の熱処理による
生成物(β−MnO2とMn2O3との混合物)1.00gあたり1
3規定のものを0.4m以上、すなわち0.52グラム当量
以上であることが好ましい。硝酸の添加量が0.52グラム
当量未満であると、酸化が不足して不純物であるMn2O3
が残存する虞れがある。
The heat treatment temperature with the nitric acid is 170 to 500 ° C.
Is preferred. When the heat treatment temperature exceeds 500 ° C., β-MnO 2 produced is further decomposed and is an impurity.
May produce Mn 2 O 3 . The amount of nitric acid added during the heat treatment is 1 per 1.00 g of the product (mixture of β-MnO 2 and Mn 2 O 3 ) of the above γ-MnO 2 heat treatment.
It is preferable that the value of 3 normal is 0.4 m or more, that is, 0.52 gram equivalent or more. If the amount of nitric acid added is less than 0.52 gram equivalent, oxidation is insufficient and Mn 2 O 3 which is an impurity
May remain.

上記硝酸を加えた熱処理は、1回であってもよいが、必
要に応じて2回以上繰り返し行なってもよい。
The heat treatment to which nitric acid is added may be performed once, or may be repeated twice or more as necessary.

以上の製法により極めて純度の高いβ−MnO2が製造され
る。このβ−MnO2を熱分析により分析したところ、熱分
解前の重量がβ−MnO2100%としたときの理論量とよ
く一致し、不純物や水分をほとんど含まないこが確認さ
れた。また、この熱分析の結果、得られるβ−MnO2は5
00℃付近まで安定で、したがってたとえ若干の水分を
含有していたとしても高温での熱処理によりこの水分を
ほとんど完全に除去することが可能であることも判明し
た。
By the above production method, β-MnO 2 with extremely high purity is produced. When this β-MnO 2 was analyzed by thermal analysis, it was confirmed that the weight before thermal decomposition was in good agreement with the theoretical amount when β-MnO 2 was 100%, and that it contained almost no impurities or water. In addition, as a result of this thermal analysis, β-MnO 2 obtained was 5
It has also been found that it is stable up to around 00 ° C., so that even if it contains some water, it is possible to almost completely remove this water by heat treatment at high temperature.

このように、本発明によれば、電解二酸化マンガンや化
学合成二酸化マンガン等の安価なγ−MnO2を原料として
水分や不純物をほとんど含まない純度の高いβ−MnO2
製造することが可能である。
Thus, according to the present invention, it is possible to produce highly pure β-MnO 2 containing almost no water or impurities from inexpensive γ-MnO 2 such as electrolytic manganese dioxide or chemically synthesized manganese dioxide as a raw material. is there.

以下、本発明の具体的な実施例について説明するが、本
発明がこれら実施例に限定されるものでないことは言う
までもない。
Hereinafter, specific examples of the present invention will be described, but it goes without saying that the present invention is not limited to these examples.

実施例1 先ず、市販の電解二酸化マンガンを525℃で2時間熱
処理した。
Example 1 First, commercially available electrolytic manganese dioxide was heat-treated at 525 ° C. for 2 hours.

上記電解二酸化マンガンの回折X線スペクトルを第1図
に、また上記熱処理による生成物の回折X線スペクトル
を第2図にそれぞれ示す。この第1図より、上記電解二
酸化マンガンの回折X線スペクトルはASTM(The Am
erican Society for Tezting Materials)カード14−
644と一致し結晶性の悪いγ−MnO2であることが分か
る。また、第2図より、上記熱処理による生成物は、A
STMカード24−735に一致するβ−MnO2とAST
Mカード10−69に一致するMn2O3との混合物である
ことが分かる。
The diffraction X-ray spectrum of the electrolytic manganese dioxide is shown in FIG. 1, and the diffraction X-ray spectrum of the product obtained by the heat treatment is shown in FIG. From FIG. 1, the diffraction X-ray spectrum of the electrolytic manganese dioxide can be determined by ASTM (The Am
erican Society for Tezting Materials) Card 14-
It is found that it is γ-MnO 2 having a poor crystallinity in agreement with 644. Further, from FIG. 2, the product obtained by the heat treatment is A
Β-MnO 2 and AST matching STM card 24-735
It can be seen that it is a mixture with Mn 2 O 3 corresponding to M-card 10-69.

次いで、上記熱処理による生成物であるβ−MnO2とMn2O
3との混合物50gを磁製るつぼ中に取り、濃硝酸(1
3規定)40mを加えて電気炉中に入れた。そして、
1時間当り12℃の割合で280℃まで昇温し、さらに
この温度に2時間保持して熱処理を施した。
Then, β-MnO 2 and Mn 2 O, which are products of the above heat treatment,
50 g of the mixture with 3 is placed in a porcelain crucible and concentrated nitric acid (1
(3N) 40 m was added and placed in an electric furnace. And
The temperature was raised to 280 ° C. at a rate of 12 ° C. per hour, and this temperature was maintained for 2 hours for heat treatment.

得られた生成物の回折X線スペクトルを第3図に示す。
この第3図より、上記硝酸を加えた熱処理によってMn2O
3に基づく回折ピークが消失し、ASTMカード24−
735に一致するβ−MnO2が高純度に生成していること
が分かる。
The diffraction X-ray spectrum of the obtained product is shown in FIG.
From FIG. 3, it can be seen that Mn 2 O
The diffraction peak based on 3 disappeared, and the ASTM card 24-
It can be seen that β-MnO 2 corresponding to 735 is produced in high purity.

さらに、本実施例により得られた生成物について熱重量
分析を行なってその組成を考察した。
Furthermore, the product obtained in this example was subjected to thermogravimetric analysis to examine its composition.

第4図は1分間当り10℃の割合で昇温して熱重量分析
を行なった結果を示すグラフであり、図中aは市販の電
解二酸化マンガンの熱分解曲線、bは本実施例の最初の
熱処理によって得られる生成物の熱分解曲線、cは硝酸
を加えた熱処理によって得られるβ−MnO2の熱分解曲線
をそれぞれ示す。なお、この第4図において、縦軸は最
終的に得られるMn2O3の量から逆算することによって求
められるMnO2の理論量を100%としたときの相対重量
を示す。
FIG. 4 is a graph showing the results of thermogravimetric analysis at a temperature rise of 10 ° C. per minute, where a is a thermal decomposition curve of commercially available electrolytic manganese dioxide, and b is the beginning of this example. Shows the thermal decomposition curve of the product obtained by the heat treatment of, and c shows the thermal decomposition curve of β-MnO 2 obtained by the heat treatment with addition of nitric acid. In FIG. 4, the vertical axis represents the relative weight when the theoretical amount of MnO 2 obtained by back-calculating from the amount of Mn 2 O 3 finally obtained is 100%.

この第4図より、本実施例の原料となる電解二酸化マン
ガンにあっては昇温前は理論量を大幅に上回り、昇温す
るに従って重量が著しく減少して300℃以上では理論
量を下回っている。これは、上記電解二酸化マンガンが
多量の水分を含んでおりこれら水分を加熱により徐々に
放出すること、また不純物としてMn2O3の如き物質を含
んでいることによるものと考えられる。また、この電解
二酸化マンガンを525℃で熱処理した生成物にあって
は、第4図中bで示すように水分の放出による重量の減
少は見られないものの、熱分解前の重量がMnO2100%
の場合に対して大幅に下回り、相当量がMn2O3となって
β−MnO2とMn2O3との混合物となっていることが分か
る。これに対して、硝酸を加えた熱処理によって得られ
る本実施例の最終生成物は、第4図中cに示すように、
熱分解前(500℃以下)での重量がMnO2100%の理
論量とよく一致し極めて安定したものであるので、不純
物であるMn2O3や水分をほとんど含まず、また熱力学的
にも極めて安定していることが分かる。
From FIG. 4, it can be seen that the electrolytic manganese dioxide, which is the raw material of this example, greatly exceeds the theoretical amount before the temperature rises, remarkably decreases in weight as the temperature rises, and falls below the theoretical amount at 300 ° C. or higher. There is. It is considered that this is because the electrolytic manganese dioxide contains a large amount of water and gradually releases the water by heating, and also contains a substance such as Mn 2 O 3 as an impurity. In addition, in the product obtained by heat-treating this electrolytic manganese dioxide at 525 ° C., although the weight loss due to the release of water was not observed as shown by b in FIG. 4, the weight before thermal decomposition was MnO 2 100. %
It is significantly lower than that of the above case, and it can be seen that a considerable amount becomes Mn 2 O 3 and is a mixture of β-MnO 2 and Mn 2 O 3 . On the other hand, the final product of this example obtained by the heat treatment with addition of nitric acid is as shown in FIG.
Since the weight before thermal decomposition (500 ° C or less) is in good agreement with the theoretical amount of MnO 2 100% and is extremely stable, it contains almost no impurities such as Mn 2 O 3 and water, and thermodynamically It turns out that is also very stable.

以上のX線回折や熱重量分析の結果より、本実施例にお
いては高純度のβ−MnO2が得られたことが明白である。
From the results of the above X-ray diffraction and thermogravimetric analysis, it is clear that highly pure β-MnO 2 was obtained in this example.

また、本実施例により得られた生成物の走査型電子顕微
鏡写真を第5図に示す。なお、この第5図において白く
観察される線は、長さの基準となるマーカであって、1
μmを示すものである。
A scanning electron micrograph of the product obtained in this example is shown in FIG. The line observed in white in FIG. 5 is a marker that serves as a reference for the length, and
It shows μm.

実施例2 先の実施例1と同様の市販の電解二酸化マンガンを57
5℃で2時間熱処理した。
Example 2 A commercially available electrolytic manganese dioxide similar to that used in Example 1 was used.
It heat-processed at 5 degreeC for 2 hours.

得られる生成物の回折X線スペクトルを第6図に示す。
この第6図より上記生成物はASTMカード24−73
5に一致するβ−MnO2とASTMカード10−69に一
致するMn2O3の混合物であることが分かる。
The diffraction X-ray spectrum of the product obtained is shown in FIG.
As shown in FIG. 6, the product is ASTM card 24-73.
It can be seen that it is a mixture of β-MnO 2 matching 5 and Mn 2 O 3 matching ASTM card 10-69.

次いで、上記混合物50gを磁製るつぼ中に取り、濃硝
酸(13規定)40mを加えて電気炉中に入れ、1時
間当り12℃の昇温速度で280℃まで昇温し熱処理し
た。
Next, 50 g of the above mixture was placed in a porcelain crucible, 40 m of concentrated nitric acid (13 normal) was added, and the mixture was placed in an electric furnace and heated to 280 ° C. at a heating rate of 12 ° C. per hour for heat treatment.

さらに、濃硝酸40mを加えて上記熱処理を再度行な
った。
Further, 40 m of concentrated nitric acid was added and the above heat treatment was performed again.

得られた生成物の回折X線スペクトルを第7図に示す。
この第7図より、上記生成物においてはMn2O3の回折ピ
ークが消失し、β−MnO2単相となっていることが分か
る。
The diffraction X-ray spectrum of the obtained product is shown in FIG.
From FIG. 7, it can be seen that in the above product, the diffraction peak of Mn 2 O 3 disappeared and the product became a β-MnO 2 single phase.

また、最初の熱処理により得られる混合物と最終的に得
られる生成物の熱分解曲線を、第8図中にそれぞれd及
びeで示す。この第8図より、上記混合物にあっては半
量近くがMn2O3となっていることが分かり、また最終生
成物は熱分解前の重量がMnO2100%の理論量と一致し
水分や不純物であるMn2O3をほとんど含まないことが分
かる。
The thermal decomposition curves of the mixture obtained by the first heat treatment and the product finally obtained are shown by d and e in FIG. 8, respectively. From FIG. 8, it can be seen that nearly half the amount of the above mixture is Mn 2 O 3, and the final product has a weight before pyrolysis of 100% of MnO 2, which is in agreement with the theoretical amount of water and water. It can be seen that it contains almost no impurities Mn 2 O 3 .

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

第1図ないし第5図は本発明を適用した一実施例を示す
ものであって、第1図は原料となる電解二酸化マンガン
の回折X線スペクトル、第2図は電解二酸化マンガンの
熱処理によって得られる生成物の回折X線スペクトル、
第3図は硝酸を加えた熱処理によって得られる生成物の
回折X線スペクトル、第4図は得られるβ−MnO2の熱分
解曲線を電解二酸化マンガンの熱分解曲線と比較して示
すグラフ、第5図は得られるβ−MnO2の結晶を写真で示
す図である。 第6図ないし第8図は本発明の他の実施例を示すもので
あり、第6図は原料である電解二酸化マンガンを熱処理
して得られる生成物の回折X線スペクトル、第7図は硝
酸を加えた熱処理によって得られる生成物の回折X線ス
ペクトル、第8図は得られるβ−MnO2の熱分解曲線を示
すグラフである。
1 to 5 show an embodiment to which the present invention is applied. FIG. 1 is a diffraction X-ray spectrum of electrolytic manganese dioxide as a raw material, and FIG. 2 is obtained by heat treatment of electrolytic manganese dioxide. X-ray spectrum of the product obtained,
FIG. 3 is a diffraction X-ray spectrum of the product obtained by the heat treatment with addition of nitric acid, and FIG. 4 is a graph showing the thermal decomposition curve of β-MnO 2 obtained in comparison with the thermal decomposition curve of electrolytic manganese dioxide. FIG. 5 is a photograph showing the obtained β-MnO 2 crystal. 6 to 8 show another embodiment of the present invention. FIG. 6 is a diffracted X-ray spectrum of a product obtained by heat treatment of electrolytic manganese dioxide as a raw material, and FIG. 7 is nitric acid. FIG. 8 is a graph showing the thermal decomposition curve of β-MnO 2 obtained by the diffracted X-ray spectrum of the product obtained by the heat treatment with addition of.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】電解二酸化マンガンあるいは化学合成二酸
化マンガンを熱処理して得られるβ−二酸化マンガンと
三二酸化マンガンの混合生成物に硝酸を加えて熱処理す
ることを特徴とするβ−二酸化マンガンの製法。
1. A method for producing β-manganese dioxide, which comprises adding nitric acid to a mixed product of β-manganese dioxide and manganese trioxide obtained by heat-treating electrolytic manganese dioxide or chemically synthesized manganese dioxide, and then heat-treating.
JP59018924A 1984-02-04 1984-02-04 Production method of β-manganese dioxide Expired - Lifetime JPH0639334B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59018924A JPH0639334B2 (en) 1984-02-04 1984-02-04 Production method of β-manganese dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59018924A JPH0639334B2 (en) 1984-02-04 1984-02-04 Production method of β-manganese dioxide

Publications (2)

Publication Number Publication Date
JPS60166229A JPS60166229A (en) 1985-08-29
JPH0639334B2 true JPH0639334B2 (en) 1994-05-25

Family

ID=11985166

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH0639334B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4604336A (en) * 1984-06-29 1986-08-05 Union Carbide Corporation Manganese dioxide and process for the production thereof
JPH0420256U (en) * 1990-06-11 1992-02-20
CN101786666B (en) * 2010-02-10 2012-02-22 彭天剑 lithium manganate anode material and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59128218A (en) * 1983-01-10 1984-07-24 Chuo Denki Kogyo Kk Manufacture of modified manganese dioxide
JPS6086030A (en) * 1983-10-18 1985-05-15 Sony Corp Production of beta-manganese dioxide

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