JP2008280242A - Manganese compound - Google Patents
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- Y—GENERAL 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
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Abstract
Description
本発明は環境汚染物質の吸着もしくは酸化による除去のために使用されるマンガン化合物及びその製造方法並びにその利用に関する。具体的には、臭気成分、ＮＯｘやＳＯｘ、ＶＯＣ、更には、燃焼排ガスの不完全燃焼による未燃焼成分として発生する炭化水素やアルデヒド類等の吸着及び酸化除去に用いられるマンガン化合物及びその製造方法並びにその利用に関する。 The present invention relates to a manganese compound used for removing environmental pollutants by adsorption or oxidation, a method for producing the same, and use thereof. Specifically, odor components, NO x and SO x, VOC, further, manganese compounds and their use in the adsorption and oxidation removal of hydrocarbons and aldehydes like generated as unburned components due to incomplete combustion of the combustion exhaust gas The present invention relates to a manufacturing method and use thereof.
従来、環境汚染物質の除去、たとえば建物や自動車の室内などにおけるタバコ臭や、生ごみから発生する臭気の除去には、活性炭やゼオライトなどの吸着剤が使用されていた。これらの吸着剤による臭気の除去は、一般的に、臭気物質が吸着剤内に取り込まれることによる物理吸着によるものが主体であった。 Conventionally, adsorbents such as activated carbon and zeolite have been used to remove environmental pollutants, for example, tobacco odors in buildings and automobile interiors, and odors generated from garbage. The removal of odors by these adsorbents is generally based on physical adsorption by the odor substance being taken into the adsorbent.
マンガン化合物を主成分とした除去剤について、特開平３−１８６３１７号公報（特許文献１）には、過マンガン酸カリウム水溶液と硫酸を含有する硫酸マンガン水溶液とを混合し、強酸性の条件下で反応させることによる酸化マンガン（表面積２４０ｍ２／ｇ）が硫黄化合物を捕捉、除去することが開示されている。 About the removal agent which has a manganese compound as a main component, Unexamined-Japanese-Patent No. 3-186317 (patent document 1) mixes potassium permanganate aqueous solution and manganese sulfate aqueous solution containing a sulfuric acid, and is on the condition of strong acidity. It is disclosed that manganese oxide (surface area 240 m 2 / g) by reacting captures and removes sulfur compounds.
更に、特開平８−１７３７９５号公報（特許文献２）には、炭酸マンガンを熱分解し、次いで硝酸処理する酸化マンガン（表面積８４〜１８５ｍ２／ｇ）及び過マンガン酸カリウム水溶液と硝酸マンガン水溶液を混合、反応させる酸化マンガン（表面積２０４ｍ２／ｇ）が吸着剤として硫黄化合物系の悪臭を除去することが開示されている。 Further, JP-A-8-173895 (Patent Document 2) discloses manganese oxide (surface area of 84 to 185 m 2 / g) for thermally decomposing manganese carbonate and then treating with nitric acid, potassium permanganate aqueous solution and manganese nitrate aqueous solution. It is disclosed that manganese oxide (surface area 204 m 2 / g) to be mixed and reacted removes a sulfur compound-based odor as an adsorbent.
しかしながら、吸着剤を環境汚染物質の除去のために使用する場合、その吸着容量には限界があるため吸着剤の交換などの工程が更に必要となるという欠点がある。また、温度や圧力などの条件変動により、物理吸着された物質が脱離するという欠点もある。 However, when the adsorbent is used for removal of environmental pollutants, there is a disadvantage that a further step such as replacement of the adsorbent is required because its adsorption capacity is limited. In addition, there is a drawback in that a physically adsorbed substance is desorbed due to fluctuations in conditions such as temperature and pressure.
一方、吸着とは別の方法、すなわち、酸化触媒としてマンガン化合物、特に酸化マンガンを使用することが知られていた。この触媒は常温付近の温度でも作用する性能を有しており、通常、高表面積であることが好ましいことも知られていた。 On the other hand, it has been known that a method different from adsorption, that is, using a manganese compound, particularly manganese oxide, as an oxidation catalyst. It has also been known that this catalyst has a performance that works even at temperatures near room temperature, and that it is usually preferable to have a high surface area.
しかしながら、上記のような従来のマンガン化合物を環境汚染物質の除去のために使用した場合、その除去効果が未だ充分なものではないため、より高性能を示す除去剤の開発が望まれていた。 However, when the conventional manganese compounds as described above are used for removing environmental pollutants, the removal effect is not yet sufficient, and therefore development of a removal agent exhibiting higher performance has been desired.
そこで、本発明の目的は、従来よりも著しく高い環境汚染物質除去能を有するマンガン化合物を提供することである。 Accordingly, an object of the present invention is to provide a manganese compound having a significantly higher ability to remove environmental pollutants than before.
本発明者らは、上記目的を達成するためには、酸化マンガンを高表面積状態にすることが必要であると勘案し、従来にはない高表面積のマンガン化合物を調製する方法について鋭意検討を行った。 In order to achieve the above-mentioned object, the present inventors have taken into consideration that it is necessary to make manganese oxide into a high surface area state, and have intensively studied a method for preparing a manganese compound with a high surface area that has not existed before. It was.
その結果、アルカリ性物質を物質構造の中に１〜１０％の量取り込むことで、ＢＥＴ表面積が３００ｍ２／ｇ以上としたマンガン化合物であれば、高い吸着能及び酸化触媒性能を有することを見出した。 As a result, it was found that a manganese compound having a BET surface area of 300 m 2 / g or more by incorporating an alkaline substance into the material structure in an amount of 1 to 10% has high adsorption ability and oxidation catalyst performance. .
更に、本発明のマンガン化合物は、アルカリ化合物と過マンガン酸塩とを、攪拌下にある二価のマンガン塩の水溶液に混合し、反応させることにより沈殿を生成させ、この沈殿物を充分洗浄した後漉過し、次いで乾燥させることからなる製造方法において、混合するアルカリ化合物の量が、過マンガン酸塩に対して化学量論より多いことを特徴とするマンガン化合物の製造方法により製造することが可能であることを見出した。 Furthermore, the manganese compound of the present invention was prepared by mixing an alkali compound and permanganate with an aqueous solution of a divalent manganese salt under stirring and reacting them, and the precipitate was thoroughly washed. In the manufacturing method comprising the subsequent filtration and then drying, the manufacturing method of a manganese compound characterized in that the amount of the alkali compound to be mixed is greater than the stoichiometric amount relative to the permanganate. I found it possible.
また、得られたマンガン化合物に環境汚染物質を含有するガスを流通、接触させることでガス中の該物質を除去する方法により除去試験を行ったところ、本発明のマンガン化合物は高い除去性能を有していることを見出し、本発明を完成した。 Further, when a removal test was performed by a method of removing the substance in the gas by circulating and contacting a gas containing an environmental pollutant to the obtained manganese compound, the manganese compound of the present invention has high removal performance. As a result, the present invention has been completed.
本発明は、新規なマンガン化合物に関するものであり、そのＢＥＴ表面積が３００ｍ２／ｇ以上、好ましくは３５０ｍ２／ｇ以上であることを特徴とするマンガン化合物である。また、本発明のマンガン化合物中のアルカリ性物質の含有量は化合物全重量に対して１〜１０％の範囲で、より好ましくは３〜９％の範囲である。 The present invention relates to a novel manganese compound, which is a manganese compound characterized in that its BET surface area is 300 m 2 / g or more, preferably 350 m 2 / g or more. Further, the content of the alkaline substance in the manganese compound of the present invention is in the range of 1 to 10%, more preferably in the range of 3 to 9% with respect to the total weight of the compound.
更に本発明は、マンガン化合物の製造方法に関するものであり、具体的には、たとえば、二価のマンガン塩の水溶液（Ａ液）及び過マンガン酸に対して化学量論以上のアルカリ化合物を加えた過マンガン酸アルカリ水溶液（Ｂ液）を準備し、攪拌下にあるＡ液にＢ液を混合、反応させることにより沈殿を生成させ、この沈殿物を充分洗浄した後漉過し、次いで１００℃〜２００℃の範囲内で乾燥させることを特徴としている。 Furthermore, the present invention relates to a method for producing a manganese compound. Specifically, for example, an alkali compound having a stoichiometric amount or more is added to an aqueous solution (liquid A) of a divalent manganese salt and permanganic acid. An alkaline permanganate aqueous solution (liquid B) was prepared, and liquid B was mixed and reacted with liquid A under stirring. A precipitate was produced by thoroughly washing the precipitate, and then filtered, and then filtered at 100 ° C to It is characterized by drying within a range of 200 ° C.
ここで、二価のマンガン塩としては、硝酸塩、硫酸塩、塩化物などを用いるのが好ましく、過マンガン酸塩としては、ナトリウム塩、カリウム塩などを用いるのが好ましい。又、過マンガン酸に対して化学量論以上のアルカリが存在するようにするためのアルカリ化合物としてはナトリウム、カリウム、リチウム等の水酸化物或いは炭酸塩を用いるのが好ましい。 Here, it is preferable to use nitrate, sulfate, chloride, etc. as the divalent manganese salt, and it is preferable to use sodium salt, potassium salt, etc. as the permanganate. Moreover, it is preferable to use hydroxides or carbonates such as sodium, potassium, lithium, etc. as the alkali compound for allowing alkali of a stoichiometric amount or more to permanganic acid.
またここで、過マンガン酸塩に対するアルカリ化合物の添加量は過マンガン酸アルカリ１モルに対するモル比で表示すると、１．０より高く４．０以下の範囲であることが好ましい。この比が１．０以下の場合、アルカリ化合物の量が少なすぎて、最終的に高表面積のマンガン化合物を得ることができず、又、４より高い場合もまた、高表面積の化合物を得ることができない。尚、Ａ液と混合するための過マンガン酸塩及びアルカリ化合物はあらかじめ水溶液の状態で混合準備しておく必要は無く、たとえば、必要量の過マンガン酸塩とアルカリ化合物との混合粉末をＡ液の攪拌下に添加してもよい。 Here, the addition amount of the alkali compound relative to the permanganate is preferably in the range of higher than 1.0 and 4.0 or lower when expressed as a molar ratio with respect to 1 mole of alkali permanganate. When this ratio is 1.0 or less, the amount of the alkali compound is too small to finally obtain a high surface area manganese compound, and when it is higher than 4, a high surface area compound is obtained. I can't. The permanganate and alkali compound to be mixed with the liquid A do not need to be mixed in advance in the form of an aqueous solution. For example, a mixed powder of a permanganate and an alkali compound in a required amount is mixed with the liquid A. It may be added with stirring.
また更に、乾燥温度は、１００〜２００℃が好ましく、より好適には１２０〜１７０℃が良い。乾燥温度が１００℃より低い場合は乾燥に長時間を要するので実用的でなく、又２００℃より高い場合はマンガン化合物の表面積低下が起こるので好ましくない。 Furthermore, the drying temperature is preferably 100 to 200 ° C, and more preferably 120 to 170 ° C. When the drying temperature is lower than 100 ° C., it takes a long time to dry, which is not practical. When the drying temperature is higher than 200 ° C., the surface area of the manganese compound is decreased, which is not preferable.
このようにして得られたマンガン化合物は、ＢＥＴ表面積が３００ｍ２／ｇ以上であった。なお、本発明のマンガン化合物を化学分析したところ、多量のアルカリが含有されていることが判明した。反応物を充分水洗した後漉過乾燥することによって本発明のマンガン化合物を得ていることから、アルカリは不純物として混入しているのではなく、物質構造の中に取り込まれていることが分った。従って、本発明のマンガン化合物はマンガン酸化物というよりはむしろ一種のアルカリ、マンガン、酸素を構成成分とする化合物と考えられる。 The manganese compound thus obtained had a BET surface area of 300 m 2 / g or more. A chemical analysis of the manganese compound of the present invention revealed that a large amount of alkali was contained. Since the manganese compound of the present invention is obtained by thoroughly washing the reaction product with water and then drying by filtration, it is understood that the alkali is not incorporated as an impurity but is incorporated into the material structure. It was. Therefore, the manganese compound of the present invention is considered to be a compound containing a kind of alkali, manganese, and oxygen as constituents rather than manganese oxide.
更に本発明は、本発明のマンガン化合物に環境汚染物質を含有するガスを流通、接触させることによるガス中の環境汚染物質除去方法に関するものである。なお、環境汚染物質としてはアンモニア、硫化水素、メルカプタン類、アルデヒド類、一酸化炭素等を挙げることができる。 Furthermore, the present invention relates to a method for removing environmental pollutants in gas by circulating and contacting a gas containing environmental pollutants with the manganese compound of the present invention. Examples of environmental pollutants include ammonia, hydrogen sulfide, mercaptans, aldehydes, and carbon monoxide.
環境汚染物質の除去は一般的には流通式反応装置により実施されるが、その他の方法でも良い。更に、環境汚染物質の除去は本発明のマンガン化合物を反応管に充填して装置に設置し、次いで環境汚染物質を含有するガスを反応管に導入して接触除去する方法により実施される。環境汚染物質除去性能は反応管出口側の環境汚染物質濃度を測定し、入り口側濃度に対する低下率を算出することにより算定される。本発明のマンガン化合物について環境汚染物質除去率を測定し、既知の方法によって得られた酸化マンガンの環境汚染物質除去率と比較したところ、既知酸化物よりも顕著に高い除去率を示すことを確認し、本発明を完成した。 Removal of environmental pollutants is generally carried out by a flow reactor, but other methods may be used. Furthermore, the removal of environmental pollutants is carried out by a method in which the manganese compound of the present invention is filled in a reaction tube and installed in an apparatus, and then a gas containing environmental pollutants is introduced into the reaction tube and removed by contact. The environmental pollutant removal performance is calculated by measuring the environmental pollutant concentration on the outlet side of the reaction tube and calculating the rate of decrease relative to the inlet side concentration. The manganese pollutant removal rate of the present invention was measured and compared with the manganese pollutant removal rate of manganese oxide obtained by a known method, and it was confirmed that the removal rate was significantly higher than that of known oxides. The present invention has been completed.
以下、本発明の具体的な構成と効果を示す実施例について説明するが、本発明はこれになんら制約されるものではない。 Hereinafter, examples showing specific configurations and effects of the present invention will be described, but the present invention is not limited thereto.
イオン交換水１０Ｌを収容した沈殿槽に硫酸マンガン４水和物を７００ｇ加えて、攪拌して硫酸マンガン溶液を得た。また、別途イオン交換水２３Ｌを収容した沈殿槽に過マンガン酸カリウムを４００ｇと苛性カリウム４６０ｇを加え、攪拌して過マンガン酸カリウム溶液を得た。そして、前記過マンガン酸カリウム溶液を、３０℃に保温した前記硫酸マンガン溶液に攪拌しながら添加した後２時間反応させ、沈殿物を生じさせた。この沈殿物を濾過し、イオン交換水で洗浄し、１２０℃にて１４時間乾燥することでマンガン化合物を得た。得られたマンガン化合物の比表面積は、４２０ｍ２／ｇで、カリウムの含有量は７．８％であった。 700 g of manganese sulfate tetrahydrate was added to a precipitation tank containing 10 L of ion-exchanged water and stirred to obtain a manganese sulfate solution. Further, 400 g of potassium permanganate and 460 g of caustic potassium were added to a precipitation tank separately containing 23 L of ion exchange water, and stirred to obtain a potassium permanganate solution. The potassium permanganate solution was added to the manganese sulfate solution kept at 30 ° C. with stirring and reacted for 2 hours to produce a precipitate. The precipitate was filtered, washed with ion exchange water, and dried at 120 ° C. for 14 hours to obtain a manganese compound. The specific surface area of the obtained manganese compound was 420 m 2 / g, and the potassium content was 7.8%.
実施例１において、苛性カリウムの添加量を２３０ｇとした以外は実施例１と同様の方法にてマンガン化合物を得た。得られたマンガン化合物の比表面積は３５０ｍ２／ｇで、カリウムの含有量は３．１％であった。 In Example 1, a manganese compound was obtained in the same manner as in Example 1 except that the amount of caustic potassium added was 230 g. The specific surface area of the obtained manganese compound was 350 m 2 / g, and the potassium content was 3.1%.
実施例１において、硫酸マンガン４水和物７００ｇの代わりに硝酸マンガン９００ｇを使用した以外は実施例１と同様の方法にてマンガン化合物を得た。得られたマンガン化合物の比表面積は、３４０ｍ２／ｇで、カリウムの含有量は３．５％であった。 In Example 1, a manganese compound was obtained in the same manner as in Example 1 except that 900 g of manganese nitrate was used instead of 700 g of manganese sulfate tetrahydrate. The specific surface area of the obtained manganese compound was 340 m 2 / g, and the potassium content was 3.5%.
実施例１において、苛性カリウム４６０ｇの代わり苛性ソーダ２３０ｇを使用した以外は実施例１と同様の方法にてマンガン化合物を得た。得られたマンガン化合物の比表面積は３２０ｍ２／ｇで、ナトリウム含有量は２．２％であった。 In Example 1, a manganese compound was obtained in the same manner as in Example 1 except that 230 g of caustic soda was used instead of 460 g of caustic potassium. The specific surface area of the obtained manganese compound was 320 m 2 / g, and the sodium content was 2.2%.
試薬炭酸マンガンを空気中にて３５０℃で５時間焼成した。得られた焼成物２００ｇを０．１ｍｏｌ／Ｌ硝酸水溶液１Ｌに投入し、攪拌することで酸処理を行った。濾過、イオン交換水での洗浄の後、比較例１のマンガン酸化物を得た。得られたマンガン酸化物の比表面積は１５０ｍ２／ｇであった。 The reagent manganese carbonate was calcined in air at 350 ° C. for 5 hours. The obtained fired product (200 g) was charged into 1 L of a 0.1 mol / L nitric acid aqueous solution and stirred for acid treatment. After filtration and washing with ion exchange water, the manganese oxide of Comparative Example 1 was obtained. The specific surface area of the obtained manganese oxide was 150 m 2 / g.
実施例１において、過マンガン酸カリウム水溶液に苛性カリウムを加えない以外は実施例１と同じ方法にて、比較例２のマンガン酸化物を得た。得られたマンガン化合物の比表面積は２３０ｍ２／ｇであった。 In Example 1, the manganese oxide of Comparative Example 2 was obtained in the same manner as in Example 1 except that caustic potassium was not added to the aqueous potassium permanganate solution. The specific surface area of the obtained manganese compound was 230 m 2 / g.
環境汚染物質の除去性能評価
本発明のマンガン化合物の性能評価は空気中の環境汚染物質の除去性能を測定することによって行った。すなわち、以下のガス組成のガスを以下の測定条件にて測定を行った。環境汚染物質除去率は下記式によって求めた。また、マンガン化合物は、１〜２ｍｍの顆粒に整粒したものを評価に使用した。
Evaluation of performance for removing environmental pollutants Performance evaluation of the manganese compounds of the present invention was performed by measuring the performance of removing environmental pollutants in the air. That is, a gas having the following gas composition was measured under the following measurement conditions. The environmental pollutant removal rate was calculated by the following formula. Moreover, the manganese compound used for evaluation what adjusted the granule of 1-2 mm.
試験条件
ガス組成
アンモニア ： ２０ｐｐｍ
硫化水素 ： ２０ｐｐｍ
メルカプタン ： ２０ｐｐｍ
アセトアルデヒド ： ２０ｐｐｍ
ホルムアルデヒド ： ２０ｐｐｍ
一酸化炭素 ： ２０ｐｐｍ
空気 ： バランス
試験温度 ： ２５℃
ガス空間速度（ＳＶ） ： １００，０００ｈ−１ Test condition Gas composition Ammonia: 20ppm
Hydrogen sulfide: 20ppm
Mercaptan: 20ppm
Acetaldehyde: 20ppm
Formaldehyde: 20ppm
Carbon monoxide: 20ppm
Air: Balance Test temperature: 25 ° C
Gas space velocity (SV): 100,000 h −1
環境汚染物質除去率の算出
除去率＝｛（Ａ−Ｂ）／Ａ｝×１００（％）
なお、上記Ａ及びＢは以下の通りである
Ａ：反応管入り口側の環境汚染物質濃度
Ｂ：反応管出口側の環境汚染物質濃度
Calculated removal rate of environmental pollutant removal rate = {(A−B) / A} × 100 (%)
A and B are as follows: A: Environmental pollutant concentration at the reaction tube inlet side B: Environmental pollutant concentration at the reaction tube outlet side
得られた結果は［表１］に示した通り、本発明によるマンガン化合物は既知の酸化マンガンと比較して環境汚染物質除去性能の優位性は顕著である。 The obtained results are shown in [Table 1], and the manganese compound according to the present invention has a significant environmental pollutant removal performance compared with known manganese oxide.
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| JP2004524081A Division JP4364798B2 (en) | 2002-07-26 | 2002-07-26 | Method for producing manganese compound and method for using the same |
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| JP5086191B2 JP5086191B2 (en) | 2012-11-28 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108744910A (en) * | 2018-08-02 | 2018-11-06 | 海泉风雷新能源发电股份有限公司 | A kind of desulfuring and denitrifying apparatus |
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| JPS6357535A (en) * | 1986-08-29 | 1988-03-12 | Mitsui Toatsu Chem Inc | Improved production of amide compound |
| JPH0368447A (en) * | 1989-08-08 | 1991-03-25 | Mitsubishi Gas Chem Co Inc | Production of nitrile hydration catalyst |
| JPH03186317A (en) * | 1989-12-14 | 1991-08-14 | Tokyo Gas Co Ltd | Method for removal of sulfur compound in gas and desulfurization agent therefor |
| JPH07118019A (en) * | 1993-08-27 | 1995-05-09 | Mitsui Toatsu Chem Inc | Production of manganese dioxide |
| JPH08173796A (en) * | 1994-09-02 | 1996-07-09 | Sakai Chem Ind Co Ltd | Nitrogen oxide oxidizing adsorbent and nitrogen oxide removing method |
| JPH0924275A (en) * | 1995-07-12 | 1997-01-28 | Daicel Chem Ind Ltd | Manufacture of manganese dioxide catalyst and prepation of carboxylic acid amide |
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Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6357535A (en) * | 1986-08-29 | 1988-03-12 | Mitsui Toatsu Chem Inc | Improved production of amide compound |
| JPH0368447A (en) * | 1989-08-08 | 1991-03-25 | Mitsubishi Gas Chem Co Inc | Production of nitrile hydration catalyst |
| JPH03186317A (en) * | 1989-12-14 | 1991-08-14 | Tokyo Gas Co Ltd | Method for removal of sulfur compound in gas and desulfurization agent therefor |
| JPH07118019A (en) * | 1993-08-27 | 1995-05-09 | Mitsui Toatsu Chem Inc | Production of manganese dioxide |
| JPH08173796A (en) * | 1994-09-02 | 1996-07-09 | Sakai Chem Ind Co Ltd | Nitrogen oxide oxidizing adsorbent and nitrogen oxide removing method |
| JPH0924275A (en) * | 1995-07-12 | 1997-01-28 | Daicel Chem Ind Ltd | Manufacture of manganese dioxide catalyst and prepation of carboxylic acid amide |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108744910A (en) * | 2018-08-02 | 2018-11-06 | 海泉风雷新能源发电股份有限公司 | A kind of desulfuring and denitrifying apparatus |
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| JP5086191B2 (en) | 2012-11-28 |
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