JPS6330323A - Production method of β-manganese dioxide - Google Patents
Production method of β-manganese dioxideInfo
- Publication number
- JPS6330323A JPS6330323A JP17177386A JP17177386A JPS6330323A JP S6330323 A JPS6330323 A JP S6330323A JP 17177386 A JP17177386 A JP 17177386A JP 17177386 A JP17177386 A JP 17177386A JP S6330323 A JPS6330323 A JP S6330323A
- Authority
- JP
- Japan
- Prior art keywords
- mno2
- nitric acid
- present
- heat
- product
- 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.)
- Pending
Links
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は固体コンデンサ、触媒等に有用なβ−二酸化マ
ンガン(以下、β−MnO2と記述する)の製造法、特
に純度の高いβ−Mn02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 β-manganese dioxide (hereinafter referred to as β-MnO2) useful for solid capacitors, catalysts, etc. The present invention relates to a method for manufacturing.
(従来の技術および本発明が解決すべき問題点)一般的
に知られているβ−Mn02の製造法のひとつに、硝酸
マンガン
(Mn (NO3)2−6H20)を熱分解する方法が
ある。(Prior Art and Problems to be Solved by the Present Invention) One of the generally known methods for producing β-Mn02 is a method of thermally decomposing manganese nitrate (Mn (NO3)2-6H20).
しかし、この製造法では、マクロ的にはマンガン低級酸
化物である三酸化マンガン(Mn203 )が不純物と
して生成されてしまうという問題があり、ミクロ的には
硝酸根(以下、NO3−と記述する)がβ−M n O
2粒子へ巻き込み、熱水洗処理をしてもNO3−が残っ
てしまうという問題があるため、純度の高いβ−MnO
2を得ることは困難であった。However, this manufacturing method has the problem that manganese trioxide (Mn203), which is a lower manganese oxide, is produced as an impurity from a macroscopic perspective, and from a microscopic perspective, it produces nitrate radicals (hereinafter referred to as NO3-). is β-M n O
Since there is a problem that NO3- remains even if it is rolled up into two particles and washed with hot water, highly pure β-MnO
It was difficult to obtain 2.
また、この方法で得られるβ−MnO2は、焼結した固
い塊状物であり、粉砕が容易ではなかった。Furthermore, the β-MnO2 obtained by this method was a sintered hard lump and was not easy to crush.
本発明は、以上の問題を解消し、純度の高いβ−MnO
2を得ることが可能なβ−Mn02の製造法を提供する
ものである。The present invention solves the above problems and provides highly pure β-MnO
The purpose of the present invention is to provide a method for producing β-Mn02 capable of obtaining β-Mn02.
(問題点を解決するための手段)
本発明者らは、上記の目的を達成するため鋭意検討を行
った結果、水和酸化マンガン(以下Mn0OHと記述す
る)を原料として用い、酸化剤として硝酸または硝酸マ
ンガンを用いることにより、純度の高いβ−MnO2が
得られるという知見を得て、本発明を完成するに至った
。(Means for Solving the Problems) As a result of intensive studies to achieve the above object, the present inventors used hydrated manganese oxide (hereinafter referred to as Mn0OH) as a raw material and nitric acid as an oxidizing agent. Alternatively, the present invention was completed based on the knowledge that highly pure β-MnO2 can be obtained by using manganese nitrate.
すなわち本発明は、Mn0OHに硝酸または硝酸マンガ
ンを加えて加熱処理することを特徴とするβ−MnOz
の製造法に関するものである。That is, the present invention provides β-MnOz, which is characterized by adding nitric acid or manganese nitrate to Mn0OH and heat-treating it.
This relates to a manufacturing method.
本発明で用いる硝酸または硝酸マンガンの通は、Mn0
OHに対して、濃硝酸または硝酸マンガン6水塩で10
〜ioo重量%であることが好ましい。これより多いと
生成物中のN O3−の含有量が高くなるので好ましく
ない。The standard of nitric acid or manganese nitrate used in the present invention is Mn0
10 with concentrated nitric acid or manganese nitrate hexahydrate for OH
~ioo weight % is preferred. If the amount is more than this, the content of N O3- in the product becomes high, which is not preferable.
熱分解の温度については100℃〜400℃の間であれ
ば特に限定はしないが、好ましくは、150℃〜400
℃である。The thermal decomposition temperature is not particularly limited as long as it is between 100°C and 400°C, but preferably between 150°C and 400°C.
It is ℃.
(実施例)
以下、実施例で本発明を説明するが、本発明はそれらに
何ら限定されるものではない。(Example) The present invention will be described below with reference to Examples, but the present invention is not limited thereto.
実施例1
磁製蒸発皿に市販のMn0OH(東洋曹達製:マンガナ
イト)100Qと濃硝酸(比重1.3)1011r1を
入れて、200℃の電気炉中で8時間加熱処理したとこ
ろ、海綿状の生成物が得られた。Example 1 Commercially available Mn0OH (manganite manufactured by Toyo Soda) 100Q and concentrated nitric acid (specific gravity 1.3) 1011r1 were placed in a porcelain evaporating dish and heated in an electric furnace at 200°C for 8 hours, resulting in a spongy shape. of product was obtained.
その模、この生成物をメノウ乳鉢で解砕し、熱水洗処理
をした。For this purpose, this product was crushed in an agate mortar and washed with hot water.
この生成物の化学分析の結果を表−1に、拡大倍率10
,000倍の電子顕微鏡写真を図1に、X線回折図を図
2(b)にそれぞれ示す。The results of the chemical analysis of this product are shown in Table 1, at a magnification of 10
An electron micrograph at a magnification of 1,000 times is shown in FIG. 1, and an X-ray diffraction diagram is shown in FIG. 2(b).
図2(b)において、図2(a)で示される市販のMn
0OHのX線回折図に基づく回折線が消失している。ま
た、図2(b)に示すようにASTMカード24−73
5に一致するβ−Mn02が高純度で生成していること
が明らかである。In FIG. 2(b), commercially available Mn shown in FIG. 2(a)
The diffraction lines based on the X-ray diffraction diagram of 0OH have disappeared. In addition, as shown in Figure 2(b), ASTM card 24-73
It is clear that β-Mn02 corresponding to 5 is produced with high purity.
また、化学分析の結果においても、β−MnOzが高純
度に生成していることが明らかである。Furthermore, it is clear from the results of chemical analysis that β-MnOz is produced with high purity.
実施例2
磁製蒸発皿に市販のMn0OH10C1と濃硝酸60−
を入れ、380℃の電気炉で8時間加熱処理をし、その
後、実施例1と同じ処理を行った。Example 2 Commercially available Mn0OH10C1 and concentrated nitric acid 60-
was heated in an electric furnace at 380° C. for 8 hours, and then the same treatment as in Example 1 was performed.
得られた生成物は、化学分析の結果を示した表−1のよ
うな高純度のβ−Mn02:であった。The obtained product was highly purified β-Mn02 as shown in Table 1 showing the results of chemical analysis.
実施例3
磁製蒸発皿ニ市販のMn0OH1oooと60%硝酸マ
ンガン20gを入れ、150℃の電気炉中で12時間加
熱処理し、その後、実施例1と同じ処理を行った。Example 3 A porcelain evaporating dish was charged with commercially available Mn0OH1ooo and 20 g of 60% manganese nitrate, heated in an electric furnace at 150° C. for 12 hours, and then subjected to the same treatment as in Example 1.
得られた生成物は、化学分析の結果を示した表−1のよ
うな高純度のβ−Mn02であった。The obtained product was highly purified β-Mn02 as shown in Table 1 showing the results of chemical analysis.
比較例
磁製蒸発皿に硝酸マンガン(Mn(NOs)2・6H2
0)を300Q入れ、380℃で8時間熱分解し、その
後、実施例1と同じ処理を行った。Comparative Example: Manganese nitrate (Mn(NOs)2.6H2) was placed in a porcelain evaporating dish.
300Q of 0) was added and thermally decomposed at 380°C for 8 hours, and then the same treatment as in Example 1 was performed.
得られた生成物は、化学分析、X線回折の結果より、N
o3−およびMn2O3の混入したβ−MnO2であっ
た。According to the results of chemical analysis and X-ray diffraction, the obtained product was N
It was β-MnO2 mixed with o3- and Mn2O3.
化学分析の結果を表−1に、X線回折図を図2(C)に
それぞれ示す。The results of chemical analysis are shown in Table 1, and the X-ray diffraction diagram is shown in FIG. 2(C).
(本発明の効果)
本発明によれば、純度の高いβ−Mn02を製造するこ
とが可能である。(Effects of the present invention) According to the present invention, it is possible to produce highly pure β-Mn02.
更に、本発明・では従来技術と比較して、加熱処理温度
が低いため、得られる生成物は海綿状または粉状で、結
晶構造は棒状なので、解砕を容易に行うことができる。Furthermore, in the present invention, since the heat treatment temperature is lower than in the prior art, the obtained product is spongy or powder-like and has a rod-like crystal structure, so it can be easily crushed.
図1は、拡大倍率10,000倍の走査型電子顕微鏡写
真による実施例1で得られた生成物の結晶構造である。
図2(a)は、市販のMn0OH(東洋費達製:マンガ
ナイト)のX線回折図である。
図2(b)は、実施例1で得られたβ−MnOzのX線
回折図である。
図2(C)は、比較例の硝酸マンガンの熱分解により得
られたβ−Mn02のX線回折図である。
表1
図2FIG. 1 shows the crystal structure of the product obtained in Example 1 as a scanning electron micrograph at a magnification of 10,000 times. FIG. 2(a) is an X-ray diffraction diagram of commercially available Mn0OH (manganite manufactured by Toyo Kashitatsu). FIG. 2(b) is an X-ray diffraction diagram of β-MnOz obtained in Example 1. FIG. 2(C) is an X-ray diffraction diagram of β-Mn02 obtained by thermal decomposition of manganese nitrate in a comparative example. Table 1 Figure 2
Claims (1)
ガンを加え、加熱処理することを特徴とするβ−二酸化
マンガンの製造法。A method for producing β-manganese dioxide, which comprises adding nitric acid or manganese nitrate to hydrated manganese oxide (MnOOH) and heat-treating the mixture.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17177386A JPS6330323A (en) | 1986-07-23 | 1986-07-23 | Production method of β-manganese dioxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17177386A JPS6330323A (en) | 1986-07-23 | 1986-07-23 | Production method of β-manganese dioxide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6330323A true JPS6330323A (en) | 1988-02-09 |
Family
ID=15929412
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17177386A Pending JPS6330323A (en) | 1986-07-23 | 1986-07-23 | Production method of β-manganese dioxide |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6330323A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6517803B2 (en) * | 1998-10-15 | 2003-02-11 | Fmc Corporation | Highly crystalline Mn2O3 or Mn3O4 manganese oxides |
-
1986
- 1986-07-23 JP JP17177386A patent/JPS6330323A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6517803B2 (en) * | 1998-10-15 | 2003-02-11 | Fmc Corporation | Highly crystalline Mn2O3 or Mn3O4 manganese oxides |
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