JP3138548B2 - Activated manganese dioxide for adsorbent and method for producing the same - Google Patents

Activated manganese dioxide for adsorbent and method for producing the same

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Publication number
JP3138548B2
JP3138548B2 JP04267886A JP26788692A JP3138548B2 JP 3138548 B2 JP3138548 B2 JP 3138548B2 JP 04267886 A JP04267886 A JP 04267886A JP 26788692 A JP26788692 A JP 26788692A JP 3138548 B2 JP3138548 B2 JP 3138548B2
Authority
JP
Japan
Prior art keywords
manganese dioxide
adsorbent
acid
producing
manganese
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
JP04267886A
Other languages
Japanese (ja)
Other versions
JPH0692639A (en
Inventor
貞夫 栗原
敬志 油谷
幸男 松波
洋司 見持
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 JP04267886A priority Critical patent/JP3138548B2/en
Publication of JPH0692639A publication Critical patent/JPH0692639A/en
Application granted granted Critical
Publication of JP3138548B2 publication Critical patent/JP3138548B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、吸着剤用活性化二酸化
マンガンの製造方法に関するものであって、比表面積が
大きく活性な二酸化マンガンについての提案である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing activated manganese dioxide for an adsorbent, and proposes an active manganese dioxide having a large specific surface area.

【0002】上記二酸化マンガンは、比表面積の大きい
特長を生かして、下記の用途に用いられる。 空気浄化用の吸着剤…メルカプタン、アミン類等の悪
臭の除去用吸着剤、二酸化硫黄等有害な気体の吸着剤と
しての効果がある。 有害金属類の吸着剤…Hg, Cr, Pb等の重金属水溶液か
ら、これらの金属を除去するための吸着剤として有効で
ある。 有価金属類の吸着剤…地熱水等や海水等に含まれるL
i, Au等有価金属回収のための吸着剤として有効であ
る。
[0002] The above-mentioned manganese dioxide is used for the following applications by taking advantage of its large specific surface area. Adsorbent for air purification: Effective as an adsorbent for removing odors such as mercaptan and amines, and as an adsorbent for harmful gases such as sulfur dioxide. Adsorbent for harmful metals: Effective as an adsorbent for removing these metals from aqueous solutions of heavy metals such as Hg, Cr, and Pb. Adsorbent for valuable metals: L contained in geothermal water, seawater, etc.
It is effective as an adsorbent for recovering valuable metals such as i and Au.

【0003】[0003]

【従来の技術】従来、二酸化マンガン(粉末状)の製造
方法としては、硫酸マンガン液を電解する方法、酸化マ
ンガンを酸素の存在下で加熱する方法、硝酸マンガンを
加熱する方法などが知られている。しかし、これらの従
来方法は、単に二酸化マンガンを得ることに主眼があ
り、機械的な粉砕や酸化加熱等の処理を経て製造されて
いるために、微粉化が難しく製品粒度に限界があり、ま
た、粒子表面を複雑な形状に加工することも不可能であ
った。その結果として、比表面積(BET値)が30〜40
m/g程度のものが限度とされていた。
2. Description of the Related Art Conventionally, methods for producing manganese dioxide (powder) include a method of electrolyzing a manganese sulfate solution, a method of heating manganese oxide in the presence of oxygen, and a method of heating manganese nitrate. I have. However, these conventional methods mainly focus on simply obtaining manganese dioxide, and are manufactured through processes such as mechanical pulverization and oxidative heating. Also, it was impossible to process the particle surface into a complicated shape. As a result, the specific surface area (BET value) is 30 to 40.
The limit was about m 2 / g.

【0004】これに対して、微細な酸化マンガンを得る
従来技術として、特開昭63−210029号公報では、フェロ
マンガン溶湯に酸素を吹きつける方法を提案している。
ただし、この方法の下で製造された酸化マンガンは、四
三酸化マンガン(MnO)が主体であり、二酸化マンガ
ン(MnO) ではない。そこで、従来、酸化マンガン(Mn
O) を酸化性雰囲気中で加熱処理することにより、
二酸化マンガンにする方法も考慮されてきたが、この方
法では、粒子表面の形状にはあまり変化がなく、粒度的
には満足できても、比表面積(BET値)はせいぜい1
〜5m/g程度の改善にしかならないことが判った。
On the other hand, as a prior art for obtaining fine manganese oxide, Japanese Patent Application Laid-Open No. 63-210029 proposes a method of blowing oxygen into a molten ferromanganese.
However, manganese oxide produced under this method is mainly manganese tetroxide (Mn 3 O 4 ), not manganese dioxide (MnO 2 ). Therefore, conventionally, manganese oxide (Mn
By subjecting 3 O 4 ) to heat treatment in an oxidizing atmosphere,
Although a method of forming manganese dioxide has been considered, in this method, the shape of the particle surface does not change much and the specific surface area (BET value) is at most 1 even though the particle size is satisfactory.
It was found that the improvement was only about 5 m 2 / g.

【0005】[0005]

【発明が解決しようとする課題】結局、上記各従来技術
では、微細でしかも粒子の表面に無数の突起を有する比
表面積の大きな二酸化マンガンを製造することができな
かった。本発明の目的は、特殊なガスや重金属類等の吸
着剤として好適な、いわゆる粒度が小さくて比表面積が
大きい活性な二酸化マンガンの製造方法を提案すること
にある。
As a result, each of the above prior arts could not produce manganese dioxide having a large specific surface area, which is fine and has numerous projections on the surface of the particles. An object of the present invention is to propose a method for producing active manganese dioxide having a small particle size and a large specific surface area, which is suitable as an adsorbent for special gases and heavy metals.

【0006】[0006]

【課題を解決するための手段】上記の目的に対し、本発
明は、次の事項を要旨構成とする二酸化マンガンの製造
方法、すなわち、鉄マンガン合金の溶湯に、酸素または
酸素を含むガスを吹きつけて溶製する際に生成する微細
ほぼ球状の、平均粒径が 0.1〜5μmのマンガン酸化
物に、塩酸、硫酸、硝酸、酢酸および弗酸のいずれか少
なくとも1種以上の酸を加え、Mn2+成分および他の不
純物成分を溶解・除去することにより、 平均粒径が 0.1
〜5μmの主として球状の、表面に溶け残りMn 4+ 成分
からなる無数の突起を有するために比表面積 (BET
値) が50m /g以上である活性化二酸化マンガンを
製造することを特徴とする吸着剤用活性化二酸化マンガ
ンの製造方法を提案する。
In order to solve the above-mentioned problems, the present invention provides a method for producing manganese dioxide having the following features. That is, oxygen or a gas containing oxygen is blown into a molten iron-manganese alloy. Fine particles generated when melted
Substantially spherical in, the manganese oxide having an average particle diameter of 0.1 to 5 [mu] m, hydrochloric acid, sulfuric acid, nitric acid, either at least one or more acids of acetic acid and hydrofluoric acid was added, dissolving the Mn 2+ component and other impurity components・ By removal , the average particle size is 0.1
Mainly spherical Mn 4+ component of ~ 5 μm, remaining on the surface
Specific surface area (BET
Activated manganese dioxide having a value of 50 m 2 / g or more.
A method for producing activated manganese dioxide for an adsorbent, which is characterized by being produced, is proposed.

【0007】[0007]

【作用】本発明は、転炉にて高炭素フェロマンガンから
中・低炭素フェロマンガンを溶製する際に発生する酸化
マンガンなどを原料とし、この酸化マンガン原料を、硫
酸等の酸によってMn2+成分および不純物成分等を溶解
・除去する方法である。即ち、このような原料を使って
製造される本発明にかかる二酸化マンガンの製造方法
は、発明者らが調査し測定したところによれば、製造条
件にかかわらず出発原料の性状に依存して、常に二酸化
マンガンを主成分とし、平均粒径が0.1 〜5μm で、表
面に無数の突起を有するほぼ球状で、しかもその比表面
積(BET値)が50m/g以上の球状微粉が得られる。
According to the present invention, a manganese oxide or the like generated when a medium- to low-carbon ferromanganese is melted from a high-carbon ferromanganese in a converter is used as a raw material, and the manganese oxide raw material is converted into Mn 2+ by an acid such as sulfuric acid. This is a method for dissolving and removing components and impurity components. That is, according to the method for producing manganese dioxide according to the present invention produced using such a raw material, according to the investigation and measurement by the inventors, depending on the properties of the starting material regardless of the production conditions, Spherical fine powder containing manganese dioxide as a main component, an average particle diameter of 0.1 to 5 μm, an almost spherical shape having countless projections on its surface, and a specific surface area (BET value) of 50 m 2 / g or more is obtained.

【0008】このようにして製造される活性化二酸化マ
ンガンは、上記したように、フェロマンガン溶湯に酸素
または酸素を含むガスを吹きつけて生成する酸化マンガ
ンを出発原料とする。このような原料を用いる理由は、
この酸化マンガン原料は、平均粒径が0.1 〜5μm の極
めて微細な球状粒子であること、そして、主成分が四三
酸化マンガンであるために、酸で処理したときに全Mn分
に対し約2/3 相当のMn2+成分のみが溶解し、Mn4+
分が無数の突起を有する粒子となって残る性質を有する
からである。即ち、このことによって二酸化マンガンの
比表面積が大きなものになるのである。しかも、もとも
と微粉であることから、粉砕工程が不要になるため、不
純物の混入するおそれもなく高純度のものが製造でき
る。
As described above, the activated manganese dioxide produced as described above uses, as a starting material, manganese oxide generated by blowing oxygen or a gas containing oxygen onto the molten ferromanganese. The reason for using such raw materials is
This manganese oxide raw material is extremely fine spherical particles having an average particle diameter of 0.1 to 5 μm, and its main component is trimanganese tetroxide. This is because only the Mn 2+ component corresponding to / 3 dissolves, and the Mn 4+ component has the property of remaining as particles having countless projections. That is, this increases the specific surface area of manganese dioxide. In addition, since the powder is originally fine, a pulverizing step is not required, so that a high-purity powder can be produced without the risk of contamination with impurities.

【0009】次に、酸化マンガン原料の溶解に用いる酸
は、1wt%以上で、酸化マンガンと等モル以上の重量の
塩酸、硫酸、硝酸、酢酸、弗酸であればいずれも使用が
可能であり、1種類あるいは2種類以上を混合して用い
ても良く、その濃度も任意に選択できる。この酸処理に
ついては、常温常圧下で1時間程度、好ましくは50℃以
上で4時間以上行う。そして、この酸処理後は、濾過を
したり、さらにアルカリ溶液で中和してもよい。
Next, the acid used for dissolving the manganese oxide raw material is 1 wt% or more, and any of hydrochloric acid, sulfuric acid, nitric acid, acetic acid, and hydrofluoric acid can be used as long as the amount is equal to or more than the mole of manganese oxide. One type or a mixture of two or more types may be used, and the concentration thereof may be arbitrarily selected. This acid treatment is carried out at normal temperature and pressure for about 1 hour, preferably at 50 ° C. or more for 4 hours or more. And after this acid treatment, you may filter and neutralize with an alkali solution further.

【0010】[0010]

【実施例】低炭素フェロマンガンの転炉溶製時に生成し
た酸化マンガン250gに、23%硫酸1250gを徐々に添加
し、攪拌しながら60℃で4時間加熱した後、濾過を行な
った。この濾過後の不溶物に対し、さらにもう一度、23
%硫酸1250gを添加し、同様の操作を繰り返した後、不
溶物をアルカリ溶液で中和し、再び、濾過、洗浄して12
0 ℃で乾燥した。このようにして得られた活性化二酸化
マンガン粉末の、化学成分を表1に、粒度分布を表2
に、そして比重および比表面積(BET値)を表3に示
す。また、原料の酸化マンガンと、ここで得られた活性
化二酸化マンガンの電子顕微鏡写真(×20000)をそれぞ
れ、図1及び図2に示す。
EXAMPLE 1 250 g of 23% sulfuric acid was gradually added to 250 g of manganese oxide produced during the production of a low-carbon ferromanganese converter and heated at 60 ° C. for 4 hours with stirring, followed by filtration. Again, the insoluble matter after filtration is
1250 g of sulfuric acid was added, and the same operation was repeated. The insoluble material was neutralized with an alkaline solution, and then filtered and washed again.
Dried at 0 ° C. Table 1 shows the chemical composition of the activated manganese dioxide powder thus obtained, and Table 2 shows the particle size distribution.
And the specific gravity and specific surface area (BET value) are shown in Table 3. 1 and 2 show electron micrographs (× 20000) of the raw material manganese oxide and the activated manganese dioxide obtained here, respectively.

【0011】[0011]

【表1】 [Table 1]

【0012】[0012]

【表2】 [Table 2]

【0013】[0013]

【表3】 [Table 3]

【0014】[0014]

【発明の効果】以上説明したように、本発明に従って製
造した二酸化マンガンは、超微粒子表面に無数の突起を
有しているために、比表面積が大きく、それ故に、脱臭
等の空気浄化、重金属を含む廃水の無害化処理、地熱水
あるいは海水からのLi, Au等有価金属の回収、その他一
般に吸着剤が有効な分野に好適に用いられる。しかも、
出発原料としてフェロマンガン溶製時に生成する酸化マ
ンガンを使用することから、製造も極めて容易である。
As described above, the manganese dioxide produced according to the present invention has a large specific surface area due to having numerous projections on the surface of the ultrafine particles, and therefore has a large air purification such as deodorization and heavy metal. detoxification of waste water containing, Li from geothermal water or sea water, the recovery of such as Au valuable metals, other general adsorbent is preferably used in the effective of fields. Moreover,
Manufacture is extremely easy because manganese oxide generated during ferromanganese melting is used as a starting material.

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

【図1】原料酸化マンガンの粒子形状を示す電子顕微鏡
写真である。
FIG. 1 is an electron micrograph showing the particle shape of a raw material manganese oxide.

【図2】製品二酸化マンガンの粒子形状を示す電子顕微
鏡写真である。
FIG. 2 is an electron micrograph showing the particle shape of a product manganese dioxide.

フロントページの続き (72)発明者 見持 洋司 茨城県つくば市東光台5丁目9番6号 日本重化学工業株式会社 中央研究所 筑波研究所内 (56)参考文献 特開 昭61−14137(JP,A) 特開 昭62−148326(JP,A) 特開 昭63−210029(JP,A) (58)調査した分野(Int.Cl.7,DB名) C01G 45/02 CA(STN)Continuation of the front page (72) Inventor Yoji Michi 5-9-1-6 Tokodai, Tsukuba-shi, Ibaraki Nippon Heavy Chemical Industry Co., Ltd. Central Research Laboratory Tsukuba Research Laboratory (56) References JP-A-61-14137 (JP, A) JP-A-62-148326 (JP, A) JP-A-63-210029 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C01G 45/02 CA (STN)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 鉄マンガン合金の溶湯に、酸素または酸
素を含むガスを吹きつけて溶製する際に生成する微細
ほぼ球状の、平均粒径が 0.1〜5μmのマンガン酸化物
に、塩酸、硫酸、硝酸、酢酸および弗酸のいずれか少な
くとも1種以上の酸を加え、Mn2+成分および他の不純
物成分を溶解・除去することにより、平均粒径が 0.1〜
5μmの主として球状の、表面に溶け残りMn 4+ 成分か
らなる無数の突起を有するために比表面積 (BET値)
が50m /g以上である活性化二酸化マンガンを製造
することを特徴とする吸着剤用活性化二酸化マンガンの
製造方法。
1. A fine , substantially spherical manganese oxide having an average particle size of 0.1 to 5 μm, which is produced when smelting a molten iron-manganese alloy by blowing oxygen or a gas containing oxygen. Is added with at least one of hydrochloric acid, sulfuric acid, nitric acid, acetic acid and hydrofluoric acid to dissolve and remove the Mn 2+ component and other impurity components, so that the average particle size is 0.1 to 0.1 %.
5μm predominantly spherical, undissolved Mn 4+ component on the surface
Specific surface area (BET value) due to having numerous projections
There method of manufacturing an adsorbent for activated manganese dioxide, characterized by producing <br/> activated manganese dioxide is 50 m 2 / g or more.
JP04267886A 1992-09-11 1992-09-11 Activated manganese dioxide for adsorbent and method for producing the same Expired - Lifetime JP3138548B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04267886A JP3138548B2 (en) 1992-09-11 1992-09-11 Activated manganese dioxide for adsorbent and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04267886A JP3138548B2 (en) 1992-09-11 1992-09-11 Activated manganese dioxide for adsorbent and method for producing the same

Publications (2)

Publication Number Publication Date
JPH0692639A JPH0692639A (en) 1994-04-05
JP3138548B2 true JP3138548B2 (en) 2001-02-26

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Country Link
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