KR20050023272A - Manganese compound, process for producing the same, and method of utilization of the same - Google Patents

Manganese compound, process for producing the same, and method of utilization of the same Download PDF

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KR20050023272A
KR20050023272A KR10-2004-7019051A KR20047019051A KR20050023272A KR 20050023272 A KR20050023272 A KR 20050023272A KR 20047019051 A KR20047019051 A KR 20047019051A KR 20050023272 A KR20050023272 A KR 20050023272A
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manganese
manganese compound
compound
environmental pollutants
alkali
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하야시노부요시
시오야야스시
와다히로시
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즈도케미 쇼쿠바이 가부시키가이샤
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G45/00Compounds of manganese
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/112Metals or metal compounds not provided for in B01D2253/104 or B01D2253/106
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/20Metals or compounds thereof
    • B01D2255/207Transition metals
    • B01D2255/2073Manganese
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/12Surface area

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  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

종래의 산화망간보다도 높은 환경오염물질 제거능을 발휘하는 망간 화합물의 제공. 2가의 망간염 수용액과 화학양론 이상의 알칼리를 함유하는 과망간산알칼리 수용액을 혼합·반응시킴으로서 망간 화합물을 얻는다. 이 망간 화합물은 기지의 망간 산화물과 비교하면, 비표면적의 대폭적인 증대가 인정되고, 환경오염물질 제거능 향상이 현저하다. 본 발명에 의한 망간 화합물은, 비표면적값이 크고, 환경오염물질 제거능이 크고, 각 공장에서 배출된 악취 성분, NOX나 SOX, VOC, 또한, 불완전 연소에 의해 발생하는 탄화수소나 알데히드류 등의 미연소 성분의 흡착 및 산화 제거에 유용하다.Providing a manganese compound that exhibits a higher ability to remove environmental pollutants than conventional manganese oxide. A manganese compound is obtained by mixing and reacting a bivalent manganese aqueous solution and an aqueous alkali permanganate solution containing more than stoichiometric alkali. Compared with a known manganese oxide, this manganese compound is recognized that the specific surface area is greatly increased, and the improvement of the ability to remove environmental pollutants is remarkable. The manganese compounds according to the present invention have a large specific surface area, a high ability to remove environmental pollutants, odorous components emitted from each plant, NO X , SO X , VOC, hydrocarbons and aldehydes generated by incomplete combustion, and the like. It is useful for adsorption and oxidation removal of unburned components.

Description

망간 화합물 및 그 제조 방법과 그 이용 방법{MANGANESE COMPOUND, PROCESS FOR PRODUCING THE SAME, AND METHOD OF UTILIZATION OF THE SAME} Manganese compound, its manufacturing method, and its manufacturing method {MANGANESE COMPOUND, PROCESS FOR PRODUCING THE SAME, AND METHOD OF UTILIZATION OF THE SAME}

본 발명은 환경 오염 물질의 흡착 또는 산화에 의한 제거를 위해 사용되는 망간 화합물 및 그 제조 방법과 그 이용 방법에 관한 것이다. 구체적으로는, NOX나 SOX, VOC, 또한, 연소 배기 가스의 불완전 연소에 의한 미연소 성분으로서 발생하는 탄화수소나 알데히드류 등의 흡착 및 산화 제거에 이용되는 망간 화합물 및 그 제조 방법과 그 이용에 관한 것이다.The present invention relates to a manganese compound used for removal by adsorption or oxidation of environmental pollutants, a method for producing the same, and a method for using the same. Specifically, NO X or SO X, VOC, also, the absorption and the manganese compound and a method of manufacturing the same for use in removing oxides such as hydrocarbons, aldehydes occurring as unburned components due to incomplete combustion of the combustion exhaust gas and use thereof It is about.

종래, 환경 오염 물질의 제거, 예를 들어, 건물이나 자동차 실내 등에서의 담배 냄새, 쓰레기에서 발생하는 악취의 제거에는, 활성탄이나 제올라이트 등의 흡착제가 사용되어 왔다. 이들 흡착제에 의한 악취의 제거는, 일반적으로, 악취 물질을 흡착제 내로 거두어 들이는 물리 흡착에 의한 것이 주체였다. Background Art Conventionally, adsorbents such as activated carbon and zeolite have been used to remove environmental pollutants, for example, to remove odors generated from cigarette smells and garbage in buildings and automobile interiors. In general, the removal of malodor by these adsorbents was mainly caused by physical adsorption of the malodorous substance into the adsorbent.

망간 화합물을 주성분으로 한 제거제에 대하여, 특개평 3-186317 호 공보에는, 과망간산칼륨 수용액과 황산을 함유하는 황산망간 수용액을 혼합하고, 강산성의 조건 하에서 반응시킴으로서 생성된 산화 망간(표면적 240m2/g)이 황 화합물을 포착, 제거하는 것이 개시되어 있다.For a remover based on manganese compounds, Japanese Patent Application Laid-Open No. 3-186317 discloses manganese oxide (surface area 240m 2 / g) produced by mixing an aqueous solution of potassium permanganate and an aqueous solution of manganese sulfate containing sulfuric acid and reacting under strong acidic conditions. ) Traps and removes sulfur compounds.

그리고, 특개평 8-173765 호 공보에는, 산화망간을 열분해하고, 계속하여 초산 처리한 산화망간(표면적 84-185m2/g) 및 과망간산칼륨 수용액과 초산망산 수용액을 혼합, 반응시킨 산화망간(표면적 204m2/g)이 흡착제로서 황 화합물계의 악취를 제거하는 것이 개시되어 있다.Further, Japanese Patent Application Laid-Open No. 8-173765 discloses manganese oxide (surface area) by thermally decomposing manganese oxide, followed by mixing and reacting manganese oxide (surface area 84-185 m 2 / g) and aqueous potassium permanganate solution with aqueous manganese acetate solution. It is disclosed that 204 m 2 / g) is used as an adsorbent to remove odors of sulfur compounds.

그러나, 흡착제를 환경 오염 물질의 제거를 위해 사용한은 경우, 그 흡착 용량에는 한계가 있기 때문에 흡착제 교환 등의 공정이 더 필요하게 된다고 하는 결점이 있다. 또한, 온도나 압력 등의 조건 변동에 의해, 물리 흡착된 물질이 탈리한다고 하는 결점도 있다. However, when the adsorbent is used for the removal of environmental pollutants, there is a disadvantage that the adsorption capacity is limited, so that further steps such as adsorbent exchange are required. In addition, there is a drawback that the substance physically adsorbed is released due to a change in conditions such as temperature and pressure.

한편, 흡착과는 별도의 방법, 즉, 산화 촉매로서 망간 화합물, 특히 산화망간을 사용하는 것이 알려져 있었다. 이 촉매는 상온 부근의 온도에서도 작용하는 성능을 가지고 있으며, 통상, 고표면적인 것이 바람직한 것으로 알려져 있었다.On the other hand, it is known to use a manganese compound, especially manganese oxide, as a method separate from adsorption, that is, as an oxidation catalyst. This catalyst has the performance of acting even at a temperature near room temperature, and it is generally known that a high surface area is preferable.

그러나, 상기와 같은 종래의 망간 화합물을 환경 오염 물질의 제거를 위해 사용하는 경우, 그 제거 효과가 아직 충분치 않기 때문에, 보다 고성능을 나타내는 제거제의 개발이 요청되고 있다. However, when the above-mentioned conventional manganese compounds are used for the removal of environmental pollutants, the removal effect thereof is not yet sufficient, and therefore, there is a demand for the development of a removal agent exhibiting higher performance.

따라서, 본 발명의 목적은, 종래보다 현저히 높은 환경 오염 물질 제거능을 가진 망간 화합물을 제공하는 것이다.Accordingly, it is an object of the present invention to provide a manganese compound having a significantly higher ability to remove environmental pollutants than before.

본 발명자들은, 상기 목적을 달성하기 위하여, 산화망간을 고표면적 상태로 할 필요가 있음을 감안하여, 종래에는 없었던 고표면적의 망간 화합물을 제조하는 방법에 대하여 예의 검토를 행하였다. MEANS TO SOLVE THE PROBLEM In order to achieve the said objective, the present inventors earnestly examined about the method of manufacturing the manganese compound of the high surface area which has not existed conventionally, considering that it is necessary to make a manganese oxide a high surface area state.

그 결과, 알칼리성 물질을 물질 구조 중에 1-10%의 양으로 포함하여, BET 표면적이 300m2/g이상으로 된 망간 화합물이라면, 높은 흡착능 및 산화 촉매 성능을 가짐을 발견하였다.As a result, it was found that the manganese compound having an alkaline substance in an amount of 1-10% in the material structure and having a BET surface area of 300 m 2 / g or more has high adsorption capacity and oxidation catalyst performance.

그리고, 본 발명의 망간 화합물은, 알칼리 화합물과 과망간산염을, 교반 하에 있는 2 가의 망간염의 수용액에 혼합하고, 반응시킴으로서 침전을 생성시키고, 이 침전물을 충분히 세정한 후 여과하고, 계속하여 건조시키는 것으로 이루어지는 제조 방법에 있어서, 혼합하는 알칼리 화합물의 양이, 과망간산염에 대하여 화학 양론보다 많은 것을 특징으로 하는 망간 화합물의 제조 방법에 의해 제조할 수 있음을 발견하였다. And the manganese compound of this invention mixes an alkali compound and a permanganate salt with the aqueous solution of the divalent manganese salt under stirring, and makes it react, produces | generates a precipitate, wash | cleans this deposit sufficiently, and it filters and continues to dry. In the manufacturing method which consists of these, it discovered that the quantity of the alkali compound to mix can manufacture by the manufacturing method of the manganese compound characterized by more than stoichiometry with respect to permanganate.

또한, 얻어진 망간 화합물에 환경 오염 물질을 함유하는 가스를 유통·접촉시켜 가스 중의 상기 물질을 제거하는 방법에 의해 제거 시험을 행하였는 바, 본 발명의 망간 화합물이 높은 제거 성능을 가지고 있음을 발견하고, 본 발명을 완성하였다.In addition, when the removal test was conducted by the method of removing the said substance in gas by flowing and contacting the gas containing environmental pollutants to the obtained manganese compound, it discovered that the manganese compound of this invention has high removal performance, The present invention has been completed.

본 발명은, 신규한 망간 화합물에 관한 것으로, 그 BET 표면적이 300m2/g이상, 바람직하게는 350m2/g이상인 것을 특징으로 하는 망간 화합물이다. 또한, 본 발명의 망간 화합물 중의 알칼리성 물질의 함유량은 화합물 전 중량에 대하여 1-10%의 범위이고, 보다 바람직하게는 3-9%의 범위이다.The present invention relates to a novel manganese compound, wherein the BET surface area is at least 300 m 2 / g, preferably at least 350 m 2 / g. Moreover, content of the alkaline substance in the manganese compound of this invention is 1-10% of range with respect to the compound total weight, More preferably, it is 3-9% of range.

그리고 본 발명은, 망간 화합물의 제조 방법에 관한 것으로, 구체적으로는, 예를 들어, 2가의 망간염의 수용액(A액) 및 과망간산에 대하여 화학양론 이상의 알칼리 화합물을 가한 과망간산알칼리 수용액(B액)을 준비하고, 교반 하에 있는 A액에 B액을 혼합, 반응시킴으로서 침전을 생성시키고, 이 침전물을 충분히 세정한 후 여과하고, 계속하여 100℃-200℃의 범위 내에서 건조시킴을 특징으로 하고 있다. And this invention relates to the manufacturing method of a manganese compound, Specifically, For example, Alkali permanganate aqueous solution (B liquid) which added the stoichiometric or more alkali compound to the aqueous solution (A liquid) of divalent manganese salt and permanganic acid. To prepare a precipitate by mixing and reacting the liquid B with the liquid A under stirring, and sufficiently washing the precipitate, followed by filtration, followed by drying in the range of 100 ° C to 200 ° C. .

여기서, 2가의 망간염으로서는, 초산염, 황산염, 염화물 등을 사용함이 바람직하고, 과망간산염으로서는, 나트륨염, 칼륨염 등을 사용함이 바람직하다. 또, 과망간산에 대하여 화학 양론 이상의 알칼리가 존재하도록 하기 위한 알칼리 화합물로서 나트륨, 칼륨, 리튬 등의 수산화물 또는 탄산염을 사용함이 바람직하다. Here, it is preferable to use acetate, sulfate, chloride, etc. as a divalent manganese salt, and it is preferable to use sodium salt, potassium salt, etc. as a permanganate salt. Moreover, it is preferable to use hydroxides or carbonates, such as sodium, potassium, and lithium, as an alkali compound for making alkali or more stoichiometric alkali exist with respect to permanganic acid.

또한 여기서, 과망간산염에 대한 알칼리 화합물의 첨가량은 과망간산알칼리 1 몰에 대한 몰비로 표시하면, 1.0보다 높고 4.0 이하의 범위임이 바람직하다. 이 비가 1.0 이하인 경우, 알칼리 화합물의 양이 작아지게 되어, 최종적으로 고표면적의 망간 화합물을 얻을 수 없고, 또, 4 보다 큰 경우에도 또한, 고표면적의 화합물을 얻을 수 없다. 또한, A액과 혼합하기 위한 과망간산염 및 알칼리 화합물은 사전에 수용액의 상태로 혼합 준비하여 둘 필요가 없고, 예를 들어, 필요량의 과망간산염과 알칼리 화합물의 혼합 분말을 A액의 교반 하에 첨가하여도 좋다.Here, the addition amount of the alkali compound to the permanganate is preferably expressed in a molar ratio with respect to 1 mole of alkali permanganate, which is higher than 1.0 and less than 4.0. When this ratio is 1.0 or less, the quantity of an alkali compound becomes small, and finally, a manganese compound of high surface area cannot be obtained, and even if it is larger than 4, a compound of high surface area cannot be obtained. In addition, the permanganate and the alkali compound for mixing with the liquid A do not need to be prepared in advance in the form of an aqueous solution, for example, by adding a necessary amount of the mixed powder of the permanganate and the alkaline compound under stirring of the liquid A Also good.

더 나아가, 건조 온도는, 100-200℃가 바람직하고, 보다 바람직하게는 120-170℃가 좋다. 건조 온도가 100℃보다 낮은 경우는 건조에 장시간을 요하므로 실용적이지 않고, 또 200℃보다 높은 경우는 망간 화합물의 표면적 저하가 일어나므로 바람직하지 않다. Furthermore, as for drying temperature, 100-200 degreeC is preferable, More preferably, 120-170 degreeC is preferable. If the drying temperature is lower than 100 ° C, it is not practical because drying takes a long time, and if it is higher than 200 ° C, the surface area of the manganese compound is lowered, which is not preferable.

이와 같이 하여 얻어진 망간 화합물은, BET 표면적 300m2/g 이상이었다. 또, 본 발명의 망간 화합물을 화학 분석하였는 바, 다량의 알칼리가 함유되어 있음이 판명되었다. 반응물을 충분히 수세한 후 여과 건조함으로서 본 발명의 망간 화합물을 얻을 수 있으므로, 알칼리는 불순물로서 혼입되어 있는 것이 아니고, 물질 구조 중에 포함되어 있음을 알 수 있다. 따라서, 본 발명의 망간 화합물은 망간산화물 이라기 보다는 오히려 일종의 알칼리, 망간, 산소를 구성 성분으로 하는 화합물로 생각된다.The manganese compound thus obtained had a BET surface area of 300 m 2 / g or more. In addition, when the manganese compound of the present invention was chemically analyzed, it was found that a large amount of alkali was contained. Since the manganese compound of the present invention can be obtained by washing the reactant sufficiently with water and filtering and drying, it can be seen that alkali is not incorporated as an impurity but is contained in the substance structure. Therefore, the manganese compound of the present invention is considered to be a compound having a kind of alkali, manganese, and oxygen as a constituent rather than manganese oxide.

그리고, 본 발명은, 본 발명의 망간 화합물에 환경 오염 물질을 함유하는 가스를 유통, 접촉시킴에 의한 가스 중의 환경 오염 물질 제거 방법에 관한 것이다. 또, 환경 오염 물질로서는 암모니아, 황화수소, 메르캅탄산, 알데히드류, 일산화탄소 등을 들 수 있다. The present invention also relates to a method for removing environmental pollutants in a gas by circulating and contacting a gas containing an environmental pollutant in a manganese compound of the present invention. Examples of environmental pollutants include ammonia, hydrogen sulfide, mercaptanic acid, aldehydes, carbon monoxide, and the like.

환경 오염 물질의 제거는 일반적으로 유통식 반응 장치에 의해 실시되나, 그 외의 다른 방법이어도 좋다. 그리고, 환경 오염 물질의 제거는 본 발명의 망간 화합물을 반응관에 충전하여 장치에 설치하고, 계속하여 환경 오염 물질을 함유하는 가스를 반응관에 도입하여 접촉 제거하는 방법에 의해 실시된다. 환경 오염 물질 제거 성능은 반응관 출구 측의 환경 오염 물질 농도를 측정하고, 입구 측 농도에 대한 저하율을 산출함으로서 산정된다. 본 발명의 망간 화합물에 대하여 환경 오염 물질 제거율을 측정하고, 기지의 방법에 따라 얻어진 산화망간의 환경 오염 물질 제거율과 비교하였는 바, 기지 산화물보다도 현저히 높은 제거율을 나타냄을 확인하고, 본 발명을 완성하였다. Removal of environmental pollutants is generally carried out by a flow-type reactor, but other methods may be used. The removal of environmental pollutants is carried out by a method in which a manganese compound of the present invention is filled in a reaction tube, installed in an apparatus, and then a gas containing environmental pollutants is introduced into the reaction tube to remove contact therewith. The environmental pollutant removal performance is estimated by measuring the environmental pollutant concentration at the outlet side of the reaction tube and calculating the rate of decrease for the concentration at the inlet side. The removal rate of environmental pollutants of the manganese compounds of the present invention was measured, and compared with the removal rate of environmental pollutants of manganese oxide obtained according to a known method, it was confirmed that the removal rate was significantly higher than that of a known oxide. .

이하, 본 발명의 구체적인 구성과 효과를 나타내는 실시예에 대하여 설명하나, 본 발명은 이에 하등 제약되는 것은 아니다. Hereinafter, an embodiment showing a specific configuration and effects of the present invention will be described, but the present invention is not limited thereto.

[실시예 1]Example 1

이온 교환수 10L를 수용한 침전조에 황산 망간 4 수화물을 700g 가하고, 교반하여 황산망간 용액을 얻었다. 또한, 별도의 이온 교환수 23L를 수용한 침전조에 과망간산칼륨 400g과 가성 칼륨 460g을 가하고, 교반하여 과망간산칼륨 용액을 얻었다. 그리고, 상기 과망간산칼륨 용액을, 30℃로 보온한 상기 황산망간 용액에 교반하면서 첨가한 후 2 시간 반응시켜, 침전물을 생성시켰다. 이 침전물을 여과하고, 이온 교환수로 세정하고, 120℃로 14 시간 건조하여 망간 화합물을 얻었다. 얻어진 망간 화합물의 비표면적은, 420m2/g이고, 칼륨의 함유량은 7.8% 였다.700 g of manganese sulfate tetrahydrate was added to a precipitation tank containing 10 L of ion-exchanged water, followed by stirring to obtain a manganese sulfate solution. Furthermore, 400 g of potassium permanganate and 460 g of caustic potassium were added to a precipitation tank containing 23 L of ion-exchanged water, followed by stirring to obtain a potassium permanganate solution. Then, the potassium permanganate solution was added to the manganese sulfate solution kept at 30 ° C. with stirring, followed by reaction for 2 hours to produce a precipitate. This precipitate was filtered, washed with ion exchanged 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 content of potassium was 7.8%.

[실시예 2]Example 2

실시예 1에 있어서, 가성 칼륨의 첨가량을 230g으로 한 이외는 실시예 1과 같은 방법으로 망간 화합물을 얻었다. 얻어진 망간 화합물의 비표면적은 350m2/g이고, 칼륨의 함유량은 3.1%였다.In Example 1, a manganese compound was obtained in the same manner as in Example 1 except that the addition amount of caustic potassium was 230 g. The specific surface area of the obtained manganese compound was 350 m 2 / g, and the content of potassium was 3.1%.

[실시예 3]Example 3

실시예 1에 있어서, 황산망간 4 수화물 700g 대신 초산망간 900g을 사용한 이외는 실시예 1과 같은 방법으로 망간 화합물을 얻었다. 얻어진 망간 화합물의 비표면적은 340m2/g이고, 칼륨의 함유량은 3.5%였다.In Example 1, a manganese compound was obtained in the same manner as in Example 1 except that 900 g of manganese acetate 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 content of potassium was 3.5%.

[실시예 4]Example 4

실시예 1에 있어서, 가성 칼륨 460g 대신 가성 소다 230g을 사용한 이외는 실시예 1과 같은 방법으로 망간 화합물을 얻었다. 얻어진 망간 화합물의 비표면적은 320m2/g이고, 나트륨의 함유량은 2.2%였다.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 content of sodium was 2.2%.

[비교예 1]Comparative Example 1

시약 탄산망간을 공기 중에 350℃로 5 시간 소성하였다. 얻어진 소성물 200g을 0.1mol/L 초산수용액 1L에 투입하고, 교반하여 산처리를 행하였다. 여과, 이온 교환수로의 세정 후, 비교예 1의 망간산화물을 얻었다. 얻어진 망간산화물의 비표면적은 150m2/g이었다.The reagent manganese carbonate was calcined at 350 ° C. for 5 hours in air. 200 g of the obtained fired product was put into 1 L of 0.1 mol / L acetic acid aqueous solution, and stirred to perform acid treatment. After filtration and washing with ion-exchanged water, the manganese oxide of Comparative Example 1 was obtained. The specific surface area of the obtained manganese oxide was 150 m 2 / g.

[비교예 2]Comparative Example 2

실시예 1에 있어서, 과망간산칼륨 수용액에 가성 칼륨을 가하지 않는 이외는 실시예 1과 같은 방법으로, 비교예 2의 망간 산화물을 얻었다. 얻어진 망간 화합물의 비표면적은 230m2/g이었다.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.

[시험예 1] <<환경오염물질의 제거성능평가>>[Test Example 1] << Evaluation of Removal Performance of Environmental Pollutants >>

본 발명의 망간 화합물의 성능 평가는 공기 중의 환경오염물질의 제거 성능을 측정함으로서 행하였다. 즉, 이하의 가스 조성의 가스를 이하의 측정 조건으로 측정을 행하였다. 환경오염물질 제거율은 하기 식에 의해 구하였다. 또한, 망간 화합물은, 1-2mm의 과립으로 정립한 것을 평가에 사용하였다. The performance evaluation of the manganese compound of this invention was performed by measuring the removal performance of the environmental pollutant in air. That is, the gas of the following gas compositions was measured on the following measurement conditions. The environmental pollutant removal rate was calculated | required by the following formula. In addition, the manganese compound used for evaluation evaluated what was granulated in the granule of 1-2 mm.

<<시험 조건>><< test condition >>

가스 조성Gas composition

암모니아: 20ppmAmmonia: 20 ppm

황화수소: 20ppmHydrogen sulfide: 20ppm

메르캅탄: 20ppmMercaptan: 20 ppm

아세트알데히드: 20ppmAcetaldehyde: 20 ppm

포름알데히드: 20ppmFormaldehyde: 20ppm

일산화탄소: 20ppmCarbon Monoxide: 20ppm

공기: 밸런스Air: balance

시험온도: 25℃Test temperature: 25 ℃

가스공간속도(SV): 100,000h-1 Gas Space Velocity (SV): 100,000h -1

<<환경오염물질제거율의 산출>><< Calculation of environmental pollutant removal rate >>

제거율 = {(A-B)/A}×100 (%)Removal Rate = {(A-B) / A} × 100 (%)

또, 상기 A 및 B는 이하와 같다. In addition, said A and B are as follows.

A: 반응관 입구 측의 환경오염물질농도A: Environmental pollutant concentration at the inlet of the reaction tube

B: 반응관 출구 측의 환경오염물질농도B: environmental pollutant concentration at the exit of the reaction tube

[표 1] 환경오염물질제거율 측정결과[Table 1] Result of environmental pollutant removal rate

환경오염물질 제거율(%)Environmental pollutant removal rate (%) 암모니아ammonia 황화수소Hydrogen sulfide 메틸메르캅탄Methyl mercaptan 아세토알데히드Acetoaldehyde 포름알데히드Formaldehyde 일산화탄소carbon monoxide 실시예 1Example 1 9090 7575 6060 6565 8585 3535 실시예 2Example 2 8989 7070 5757 6363 8181 3232 실시예 3Example 3 8484 7070 5555 6262 7575 2828 실시예 4Example 4 8585 6868 5353 6060 7373 2424 비교예 1Comparative Example 1 5050 3030 2020 3535 5252 99 비교예 2Comparative Example 2 5858 3636 2828 4141 5555 44

얻어진 결과는 [표 1]에 나타난 바와 같이, 본 발명에 의한 망간 화합물은 기지의 산화망간과 비교하여 환경오염물질 제거성능의 우수성이 현저하다.As shown in Table 1, the manganese compound according to the present invention is remarkably excellent in removing environmental pollutants compared with known manganese oxide.

Claims (5)

알칼리성 물질을 물질 구조 중에 1-10%의 양으로 포함하여, BET 표면적이 300m2/g 이상인 망간 화합물.A manganese compound having an BET surface area of at least 300 m 2 / g, comprising an alkaline substance in an amount of 1-10% in the material structure. 알칼리 화합물과 과망간산염을, 교반 하에 있는 2 가의 망간염의 수용액에 혼합하고, 반응시킴으로서 침전을 생성시키고, 이 침전물을 충분히 세정한 후 여과하고, 계속하여 건조시키는 것으로 이루어지는 망간 화합물의 제조 방법에 있어서, 알칼리 화합물의 양이, 과망간산염에 대하여 화학양론보다 많은 것을 특징으로 하는 망간 화합물의 제조 방법.In the manufacturing method of the manganese compound which consists of mixing an alkali compound and a permanganate salt in the aqueous solution of the divalent manganese salt under stirring, and making it react, generating a precipitate, after wash | cleaning this deposit sufficiently, filtering and continuing to dry. The amount of the alkali compound is greater than the stoichiometry for the permanganate salt. 제 2 항에 있어서, 과망간산염에 대한 알칼리 화합물의 첨가량은 과망간산알칼리 1 몰에 대한 몰비로 표시하면, 1.0보다 높고 4.0 이하의 범위인 것을 특징으로 하는 망간 화합물의 제조 방법.The method for producing a manganese compound according to claim 2, wherein the amount of the alkali compound added to the permanganate is in the range of higher than 1.0 and lower than 4.0 when expressed in molar ratio with respect to 1 mol of alkali permanganate. 제 2 항에 있어서, 건조 온도가 100-200℃인 것을 특징으로 하는 망간 화합물의 제조 방법.The process for producing a manganese compound according to claim 2, wherein the drying temperature is 100-200 ° C. 제 1 항에 기재된 망간 화합물에 환경오염물질을 함유하는 가스를 유통시키는 것에 의한 가스 중의 환경오염물질 제거방법. A method for removing environmental pollutants in gas by circulating a gas containing environmental pollutants in the manganese compound according to claim 1.
KR10-2004-7019051A 2004-11-24 2002-07-26 Manganese compound, process for producing the same, and method of utilization of the same KR20050023272A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100840721B1 (en) * 2007-04-02 2008-06-23 아주대학교산학협력단 Preparing method of catalyst for removing nox and catalyst for removing nox prepared thereform
CN117383617A (en) * 2023-10-20 2024-01-12 广州南科高新材料科技有限公司 Efficient active manganese preparation method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100840721B1 (en) * 2007-04-02 2008-06-23 아주대학교산학협력단 Preparing method of catalyst for removing nox and catalyst for removing nox prepared thereform
CN117383617A (en) * 2023-10-20 2024-01-12 广州南科高新材料科技有限公司 Efficient active manganese preparation method
CN117383617B (en) * 2023-10-20 2024-03-19 广州南科高新材料科技有限公司 Efficient active manganese preparation method

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