JPH04367723A - Decomposition catalyst and decomposition treatment of nox - Google Patents
Decomposition catalyst and decomposition treatment of noxInfo
- Publication number
- JPH04367723A JPH04367723A JP3170515A JP17051591A JPH04367723A JP H04367723 A JPH04367723 A JP H04367723A JP 3170515 A JP3170515 A JP 3170515A JP 17051591 A JP17051591 A JP 17051591A JP H04367723 A JPH04367723 A JP H04367723A
- Authority
- JP
- Japan
- Prior art keywords
- nox
- decomposition catalyst
- exhaust gas
- decomposition
- coal ash
- 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
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は、火力発電所や工場等
から産業廃棄物として排出される石炭灰の利用を目的と
するもので、これを主成分として得られるNOx 分解
触媒と、このNOx 分解触媒を用いて排気ガス中のN
Ox を分解処理する方法に関するものである。[Industrial Application Field] The purpose of this invention is to utilize coal ash discharged as industrial waste from thermal power plants, factories, etc.; N in exhaust gas using a decomposition catalyst
This invention relates to a method for decomposing Ox.
【0002】0002
【従来の技術】近年、大気汚染の進行に伴い、光化学ス
モッグの発生が社会問題化しており、その原因物質であ
る窒素酸化物(NOx )の除去・浄化は、緊急を有す
る課題となっている。[Background Art] In recent years, with the progress of air pollution, the generation of photochemical smog has become a social problem, and the removal and purification of nitrogen oxides (NOx), which is the causative substance, has become an urgent issue. .
【0003】NOx は、自動車やジェット機のエンジ
ン排気ガス、あるいは、火力発電所のボイラや焼却炉の
燃焼排気ガスなどに由来するが、これらのNOx を浄
化するために、近時では、エンジンやボイラの燃焼方法
自体の改良や、触媒を用いて化学的に分解するなどの対
策が考えられている。上記NOx の処理技術としては
、接触還元法と接触分解法があり、前者は、更に選択法
と非選択法とに分けられる。[0003] NOx originates from the engine exhaust gas of automobiles and jet aircraft, or the combustion exhaust gas from boilers and incinerators at thermal power plants. Countermeasures are being considered, such as improving the combustion method itself and chemically decomposing it using catalysts. The above-mentioned NOx treatment techniques include catalytic reduction methods and catalytic decomposition methods, and the former can be further divided into selective methods and non-selective methods.
【0004】このうち、選択法は、処理用ガスにNH3
を用いるもので、装置の大型化、イニシャルコスト並
びにランニングコストの上昇が避けらないため、小型の
機器には適用し難い。一方、非選択法は、小型化が可能
であるが、貴金属系の3元触媒を用いるためコストの上
昇が避けられない。特に、貴金属系の3元触媒を用いる
ものは、ガソリンエンジン用として多用されているが、
5〜15%の未反応酸素を含むディーゼルエンジンの排
ガス処理には使用できない。また、後者の触媒によるN
Ox 処理に関しては、各種の遷移金属化合物で飽和し
た合成ゼオライト触媒を用いる方法が開発されているけ
れども、この方法は、合成ゼオライトが高価につく割に
経済的効果が低いため、一般に普及するに至っていない
。Among these, the selective method uses NH3 as the processing gas.
This method is difficult to apply to small-sized equipment because it inevitably increases the size of the device and increases the initial cost and running cost. On the other hand, the non-selective method allows for miniaturization, but it inevitably increases costs because it uses a three-way catalyst based on noble metals. In particular, those using precious metal three-way catalysts are often used for gasoline engines.
It cannot be used to treat diesel engine exhaust gas, which contains 5-15% unreacted oxygen. In addition, N due to the latter catalyst
Regarding Ox treatment, a method using synthetic zeolite catalysts saturated with various transition metal compounds has been developed, but this method has not become widely used because synthetic zeolite is expensive and the economic effect is low. not present.
【0005】上記のNOx による大気汚染以外にも、
火力発電所、製鉄所や工場からの産業廃棄物である石炭
灰の処理が、環境汚染問題として緊急を要するもう一つ
の課題となりつつある。石炭灰とは、石炭、コークス等
の燃焼残滓で、統計によると、我が国に現存するほぼ4
0数基の大型火力発電所から排出される石炭灰の量は、
年間250万トン以上にものぼる。In addition to the air pollution caused by NOx mentioned above,
The disposal of coal ash, which is industrial waste from thermal power plants, steel mills, and factories, is becoming another urgent environmental pollution problem. Coal ash is the combustion residue of coal, coke, etc. According to statistics, approximately 40% of coal ash currently exists in Japan.
The amount of coal ash discharged from several large thermal power plants is
This amounts to more than 2.5 million tons per year.
【0006】このような石炭灰は、一部セメント原料等
に再利用されているものの、適切な大量処理方法が無く
、他の固体廃棄物と一緒に埋め立て処分されているのが
現状である。しかし、最近ではセメント自体の需要が頭
打ちになっていることや、廃棄場所(埋立地)の確保に
も困難をきたしており、産業廃棄物としての石炭灰が、
社会的にも、また、環境保全の立場からも全国的に大き
な問題を投げかけている。[0006] Although such coal ash is partially reused as raw material for cement, etc., there is currently no suitable large-scale treatment method, and the coal ash is currently disposed of in landfills together with other solid wastes. However, recently, demand for cement itself has peaked, and it has become difficult to secure disposal sites (landfills), so coal ash as industrial waste has
This poses a major problem nationwide, both socially and from an environmental conservation standpoint.
【0007】[0007]
【発明が解決しようとする課題】この発明は、以上のよ
うな課題に応えようとするものであって、石炭灰を主成
分とする使用上の効果の顕著なNOx 分解触媒及びN
Ox 分解処理法を提供するものである。[Problems to be Solved by the Invention] The present invention aims to meet the above-mentioned problems, and provides a NOx decomposition catalyst and N
This provides an Ox decomposition treatment method.
【0008】[0008]
【課題を解決するための手段】即ち、この発明は、石炭
灰とアルカリ溶液とを混合して得られる石炭灰アルカリ
溶融物に、V,Cr,Mn,Fe,Co,Cu,Pd,
Ag,Pt,Ni等から選択した1以上の金属イオンを
担持させてなるNOx 分解触媒、及びこのようなNO
x 分解触媒を排気ガスの排出経路中に介在させること
によりNOx を直接N2 とO2 に分解することを
特徴とするNOx 分解処理法である。[Means for Solving the Problems] That is, in the present invention, V, Cr, Mn, Fe, Co, Cu, Pd,
NOx decomposition catalyst supported with one or more metal ions selected from Ag, Pt, Ni, etc., and such NOx decomposition catalyst
This is a NOx decomposition treatment method characterized by directly decomposing NOx into N2 and O2 by interposing an x decomposition catalyst in the exhaust gas exhaust path.
【0009】[0009]
【実施例】最初に、この発明に係るNOx 分解触媒に
ついて説明する。[Example] First, the NOx decomposition catalyst according to the present invention will be explained.
【0010】原料となる石炭灰とは、前述のように、石
炭を燃料として用いる火力発電所、製鉄所や工場からの
燃焼廃棄物である石炭クリンカーアッシュ、石炭フライ
アッシュ等をいう。[0010] As mentioned above, the raw material coal ash refers to coal clinker ash, coal fly ash, etc., which are combustion waste from thermal power plants, steel mills, and factories that use coal as fuel.
【0011】これをアルカリ溶液と混合し、加熱あるい
は加圧することによって、部分的に結晶化させた結晶性
物質を生じさせ、多孔質の石炭灰アルカリ溶融物を得る
。[0011] By mixing this with an alkaline solution and applying heat or pressure, a partially crystallized crystalline material is produced, and a porous coal ash alkaline melt is obtained.
【0012】この石炭灰アルカリ溶融物に各種金属イオ
ンをイオン交換法により担持させると所望のNOx 分
解触媒を得ることができる。[0012] A desired NOx decomposition catalyst can be obtained by supporting various metal ions on this coal ash alkali melt by an ion exchange method.
【0013】上記の金属イオンとしては、V,Cr,M
n,Fe,Co,Cu,Pd,Ag,Pt,Ni等が挙
げられる。The above metal ions include V, Cr, M
n, Fe, Co, Cu, Pd, Ag, Pt, Ni, etc.
【0014】更に、上記のNOx 分解触媒に対しては
、前掲の金属イオンに加えて、還元作用を有するアンモ
ニアイオン,アミン等の有機イオンもしくは化合物をイ
オン交換法または吸着法により担持させることもできる
。
このようにすることにより、NO2 が、直接NOに還
元されるため、上記金属イオンによる分解効率が一層高
まる。Furthermore, in addition to the above-mentioned metal ions, organic ions or compounds such as ammonia ions and amines having a reducing action can be supported on the NOx decomposition catalyst by an ion exchange method or an adsorption method. . By doing so, NO2 is directly reduced to NO, so that the efficiency of decomposition by the metal ions is further increased.
【0015】以下に、具体的実施例を説明する。A specific example will be explained below.
【0016】まず、上記石炭灰とアルカリ溶液として水
酸化ナトリウム水溶液を80〜160g/l添加し、例
えば、90℃以上の加熱処理を施す。[0016] First, 80 to 160 g/l of an aqueous sodium hydroxide solution as an alkaline solution is added to the above-mentioned coal ash, and heat treatment is performed at, for example, 90°C or higher.
【0017】この反応(加熱処理)後、過剰の水酸化ナ
トリウムを水洗除去し、風乾して粉末状の石炭灰アルカ
リ溶融物を得る。After this reaction (heat treatment), excess sodium hydroxide is removed by washing with water and air-dried to obtain a powdered coal ash alkali melt.
【0018】次に、この石炭灰アルカリ溶融物と、金属
イオンとして酢酸銅溶液とを混合し、所定反応時間攪拌
することによって、銅イオンを石炭灰アルカリ溶融物に
担持させる。Next, this alkali molten coal ash and a copper acetate solution as metal ions are mixed and stirred for a predetermined reaction time, thereby supporting the copper ions in the alkali molten coal ash.
【0019】この金属イオン担持物を水洗し、脱水した
後、風乾してNOx 分解触媒を得る。The metal ion support is washed with water, dehydrated, and then air-dried to obtain a NOx decomposition catalyst.
【0020】以上のようにして得られた、NOx 分解
触媒を用いて、処理能力を調査した結果を図1に示す。FIG. 1 shows the results of investigating the processing capacity of the NOx decomposition catalyst obtained as described above.
【0021】このNOx 分解触媒のNOの分解処理に
関する実験は、次の環境下において行った。NOx 分
解触媒約40gを200ml容のビーカに取り、容積約
1リットルのオートクレーブ内に収容する。上記オート
クレーブ内の空気を排気した後、純度99.7%のNO
を導入し、密閉する。反応自体は、30〜50rpmで
触媒を攪拌しながら、300、400、500、600
℃の各温度で5時間保持した後、NOの残留量及び分解
反応生成物(N2 及びO2 )の量を測定した。[0021] Experiments regarding the NO decomposition process of this NOx decomposition catalyst were conducted under the following environment. Approximately 40 g of NOx decomposition catalyst is placed in a 200 ml beaker and placed in an autoclave having a volume of approximately 1 liter. After exhausting the air in the autoclave, NO with a purity of 99.7%
Introduce and seal. The reaction itself was carried out at 300, 400, 500, 600 rpm while stirring the catalyst at 30-50 rpm.
After holding at each temperature for 5 hours, the residual amount of NO and the amount of decomposition reaction products (N2 and O2) were measured.
【0022】図1に示すように、この発明に係るNOx
分解触媒では、約500℃で92%のNO分解率を示
し、約450℃から約550℃の範囲においても、90
%以上の高い分解率を示した。As shown in FIG. 1, NOx according to the present invention
The decomposition catalyst shows a NO decomposition rate of 92% at about 500°C, and even in the range of about 450°C to about 550°C, it shows a NO decomposition rate of 92%.
It showed a high decomposition rate of more than %.
【0023】このように、この発明に係るNOx 分解
触媒によれば、光化学スモッグ、酸性雨等の大気汚染を
引き起こす原因として挙げられる燃焼排気ガス中のNO
x を高い効率で、無害な窒素と酸素に分解することが
できる。As described above, the NOx decomposition catalyst of the present invention reduces NOx in combustion exhaust gas, which is a cause of atmospheric pollution such as photochemical smog and acid rain.
x can be decomposed into harmless nitrogen and oxygen with high efficiency.
【0024】燃焼排気ガスとしては、ボイラの排ガス、
交通機関、(特に、ディーゼル機関利用のもの)の排気
ガス、火力発電所、焼却炉等の排気ガスが挙げられ、こ
れらに対して有効に応用可能できる。[0024] Examples of combustion exhaust gas include boiler exhaust gas,
Examples include exhaust gas from transportation systems (particularly those using diesel engines), exhaust gas from thermal power plants, incinerators, etc., and it can be effectively applied to these.
【0025】前述のNOx 分解触媒を用いて実際に排
気ガス処理を行うには、上述機器の排気ガスの排出経路
中に適宜の収容空間を設け、この中に数ミリ〜数十ミリ
の粒径に造粒したNOx 分解触媒を収容する他、平板
形状、ハニカム形状等とした成形品、あるいは、粒状、
粉末状のNOx 分解触媒を適宜の通気性を有する容器
に収容したものを配置するのがよい。そのような成形品
を用いるときは、カートリッジ式に着脱自在に構成する
ことにより、保守・点検の便宜が図れる。In order to actually perform exhaust gas treatment using the NOx decomposition catalyst described above, an appropriate accommodation space is provided in the exhaust gas exhaust path of the above-mentioned equipment, and particles with a size of several millimeters to several tens of millimeters are placed in this space. In addition to containing granulated NOx decomposition catalyst, molded products in flat plate shape, honeycomb shape, etc., or granular,
It is preferable to arrange a container containing a powdered NOx decomposition catalyst in a container having appropriate air permeability. When such a molded product is used, maintenance and inspection can be facilitated by constructing it in a cartridge-type manner so that it can be freely attached and removed.
【0026】[0026]
【発明の効果】この発明に係るNOx 分解触媒及びN
Ox 分解処理法によれば、石炭灰の再資源化を図るこ
とができ、これにより、触媒自体のコストを在来のゼオ
ライト触媒と比較すると極めて低コストとすることがで
きると同時に、火力発電所、製鉄所や工場などから多量
に排出される石炭灰を産業廃棄物として廃棄することを
免れ得る。[Effect of the invention] The NOx decomposition catalyst and N
According to the Ox decomposition treatment method, it is possible to recycle coal ash as a resource, and as a result, the cost of the catalyst itself can be extremely low compared to conventional zeolite catalysts, and at the same time, it is possible to reduce the cost of the catalyst itself. , it is possible to avoid disposing of coal ash, which is produced in large quantities from steel mills and factories, as industrial waste.
【0027】さらに、この発明に係るNOx 分解触媒
を、燃焼排気ガス等の浄化処理に用いることにより、N
Ox による光化学スモッグ発生や酸性雨を防止できる
など、大気汚染の防止にも寄与できる。Furthermore, by using the NOx decomposition catalyst according to the present invention for purifying combustion exhaust gas, etc.
It can also contribute to the prevention of air pollution by preventing photochemical smog and acid rain caused by Ox.
【0028】また、この発明によれば、NH3 等の処
理用ガスを用いるものと比べて、処理設備の小型化が可
能であると共に小さな排ガス発生源、例えば、小型ボイ
ラや焼却炉等の小型産業用機器、給湯器やガスレンジ等
の家庭用燃焼機器、自動車や航空機や船舶等の内燃機関
を有する輸送機器等への適用が容易になり、未反応のN
H3 ガスが大気中に洩出することもない。[0028] Furthermore, according to the present invention, it is possible to downsize the processing equipment compared to those using a processing gas such as NH3, and it is also possible to reduce the size of the processing equipment, and also to reduce the size of small exhaust gas generation sources such as small boilers and incinerators for small industries. It can be easily applied to household combustion equipment such as water heaters and gas ranges, and transportation equipment with internal combustion engines such as automobiles, airplanes, and ships.
No H3 gas leaks into the atmosphere.
【0029】しかも、貴金属系の3元触媒を用いるもの
に比べ、排ガス中の未反応酸素量が多い場合においても
窒素酸化物の分解を行えるなど、この分野に多大な貢献
をすることができる。[0029] Furthermore, compared to a catalyst using a noble metal three-way catalyst, nitrogen oxides can be decomposed even when the amount of unreacted oxygen in the exhaust gas is large, making it possible to make a great contribution to this field.
【図1】この発明に係るNOx 分解触媒によるNOの
分解処理能力の実験結果を示す線図である。FIG. 1 is a diagram showing experimental results of the NOx decomposition processing ability of the NOx decomposition catalyst according to the present invention.
Claims (5)
られる石炭灰アルカリ溶融物に、金属イオンを担持させ
てなるNOx 分解触媒。1. A NOx decomposition catalyst comprising a coal ash alkaline melt obtained by mixing coal ash and an alkaline solution and carrying metal ions thereon.
物に、金属イオン並びに有機物を担持させてなるNOx
分解触媒。[Claim 2] NOx produced by making the coal ash alkali melt according to Claim 1 support metal ions and organic substances.
Decomposition catalyst.
が、V,Cr,Mn,Fe,Co,Cu,Pd,Ag,
Pt,Niの何れかを含むことを特徴とするNOx 分
解触媒。3. The metal ion according to claim 1 or 2 is V, Cr, Mn, Fe, Co, Cu, Pd, Ag,
A NOx decomposition catalyst characterized by containing either Pt or Ni.
アイオン、アミン等の還元作用を有する有機イオンもし
くは化合物であることを特徴とするNOx 分解触媒。4. A NOx decomposition catalyst, wherein the organic substance according to claim 2 is an organic ion or compound having a reducing action, such as an ammonia ion or an amine.
Ox 分解触媒を排気ガスの排出経路中に介在させるこ
とによりNOx を直接N2 とO2 とに分解するこ
とを特徴とするNOx 分解処理法。[Claim 5] N according to any one of claims 1 to 4.
A NOx decomposition treatment method characterized by directly decomposing NOx into N2 and O2 by interposing an Ox decomposition catalyst in an exhaust gas exhaust path.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3170515A JPH04367723A (en) | 1991-06-14 | 1991-06-14 | Decomposition catalyst and decomposition treatment of nox |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3170515A JPH04367723A (en) | 1991-06-14 | 1991-06-14 | Decomposition catalyst and decomposition treatment of nox |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04367723A true JPH04367723A (en) | 1992-12-21 |
Family
ID=15906377
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3170515A Pending JPH04367723A (en) | 1991-06-14 | 1991-06-14 | Decomposition catalyst and decomposition treatment of nox |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04367723A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109794258A (en) * | 2019-01-26 | 2019-05-24 | 江西科环工业陶瓷有限公司 | A kind of catalyst and preparation method of waste water by ozone processing |
| US11291950B2 (en) | 2019-11-07 | 2022-04-05 | Massachusetts Institute Of Technology | Treatment of acid gases using molten alkali metal borates and associated methods of separation |
| US11311840B2 (en) | 2018-10-05 | 2022-04-26 | Massachusetts Institute Of Technology | Carbon dioxide removal using sequestration materials that include salts in molten form, and related systems and methods |
| US11577223B2 (en) | 2019-11-07 | 2023-02-14 | Massachusetts Institute Of Technology | Processes for regenerating sorbents, and associated systems |
-
1991
- 1991-06-14 JP JP3170515A patent/JPH04367723A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11311840B2 (en) | 2018-10-05 | 2022-04-26 | Massachusetts Institute Of Technology | Carbon dioxide removal using sequestration materials that include salts in molten form, and related systems and methods |
| CN109794258A (en) * | 2019-01-26 | 2019-05-24 | 江西科环工业陶瓷有限公司 | A kind of catalyst and preparation method of waste water by ozone processing |
| US11291950B2 (en) | 2019-11-07 | 2022-04-05 | Massachusetts Institute Of Technology | Treatment of acid gases using molten alkali metal borates and associated methods of separation |
| US11577223B2 (en) | 2019-11-07 | 2023-02-14 | Massachusetts Institute Of Technology | Processes for regenerating sorbents, and associated systems |
| US11602716B2 (en) | 2019-11-07 | 2023-03-14 | Massachusetts Institute Of Technology | Treatment of acid gases using molten alkali metal borates, and associated methods of separation |
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