JPH0824667A - Carrier and filter using the same - Google Patents

Carrier and filter using the same

Info

Publication number
JPH0824667A
JPH0824667A JP6163801A JP16380194A JPH0824667A JP H0824667 A JPH0824667 A JP H0824667A JP 6163801 A JP6163801 A JP 6163801A JP 16380194 A JP16380194 A JP 16380194A JP H0824667 A JPH0824667 A JP H0824667A
Authority
JP
Japan
Prior art keywords
carrier
filter
alloy
oxidized film
gas
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
Application number
JP6163801A
Other languages
Japanese (ja)
Inventor
Keizo Harada
敬三 原田
Masayuki Ishii
正之 石井
Seisaku Yamanaka
正策 山中
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.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries 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 Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP6163801A priority Critical patent/JPH0824667A/en
Publication of JPH0824667A publication Critical patent/JPH0824667A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a carrier which can utilize more efficiently an active component such as a catalyst by forming the carrier from a three dimensional porous metal body of A1 or A1-alloy having specified communicating pores, and making the surface of the carrier have a finely uneven oxidized film formed by alumite treatment. CONSTITUTION:The carrier for an active component is formed from a three dimensional porous metal body of A1 or A1-alloy having communicating pores and porosity of 80% or more, and the surface has a finely uneven oxidized film. The oxidized film has a large number of pores several hundreds Angstrom in diameter so that the specific surface area is large and further increased by the unevenness on the surface the pores. In this way, the contact area with gas increases for reactions or separation, contributing largely to the improvement of decomposition and recovery efficiency. The oxidized film is also effective to protect the porous metal body from corrosion due to corrosive gas contained slightly in exhaust gas.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本願発明は、触媒等の活性成分を
担持する担体、とくに近年問題となっている工場や発電
所あるいは自動車からの排気ガス中に含まれる大気汚染
物質あるいは地球温暖化の原因となっている炭酸ガス等
の大気への放散を防止するためのフィルタ用担体及びそ
れを用いたフィルタに関する。
BACKGROUND OF THE INVENTION The present invention relates to a carrier for supporting an active component such as a catalyst, and particularly to an air pollutant contained in exhaust gas from a factory, a power plant, or an automobile, which has been a problem in recent years, or global warming. The present invention relates to a filter carrier for preventing the emission of carbon dioxide gas, which is the cause, to the atmosphere, and a filter using the same.

【0002】[0002]

【従来の技術】発電所や工場等の大量の炭酸ガスを排出
する固定発生源から排出される炭酸ガスは濃度が比較的
高く回収が容易と考えられることから、資源再利用技術
の対象となっている。炭酸ガスの再資源化技術として
は、例えば特開平5−337334に示されるように、
炭酸ガスをアミン系吸収液などの有幾化学品中に固定す
るなどがある。また、炭酸ガスを吸着・脱離方法とし
て、活性炭などの固体の吸着剤を用いて加圧下において
炭酸ガスを吸着させた後減圧下において脱離させること
により炭酸ガスを多量に含んだ排出ガスから効率的に炭
酸ガスの分離を行う方法などもある。また、鉄酸化物触
媒を板状アルミナに担持させた分解体により炭酸ガスを
分解処理する方法(特開平4−135621号)、アル
ミナ、チタニア等に担持させた硫化モリブデン触媒によ
り炭酸ガスを還元する方法(特開平4−363142
号)も提案されている。
2. Description of the Related Art Carbon dioxide emitted from a fixed source that emits a large amount of carbon dioxide, such as a power plant or a factory, has a relatively high concentration and is considered to be easily recovered. ing. As a technology for recycling carbon dioxide gas, for example, as disclosed in JP-A-5-337334,
For example, carbon dioxide is fixed in a number of chemical products such as amine-based absorbents. As a method for adsorbing / desorbing carbon dioxide, a solid adsorbent such as activated carbon is used to adsorb carbon dioxide under pressure and then desorb it under reduced pressure to remove carbon dioxide from a large amount of exhaust gas. There is also a method of efficiently separating carbon dioxide gas. Further, a method of decomposing carbon dioxide gas with a decomposed material in which an iron oxide catalyst is supported on plate-like alumina (JP-A-4-135621), and carbon dioxide gas is reduced by a molybdenum sulfide catalyst supported on alumina, titania or the like. Method (JP-A-4-363142)
No.) is also proposed.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、炭酸ガ
スの吸着・脱離を利用する方法では、吸着剤の再生は可
能であるが、ガス処理塔のような膨大な処理設備が必要
となり大量の排出ガスをリアルタイムに処理するには不
向きもしくは経済的ではない。また、前記の分解触媒を
利用する方法ではガス処理塔のような設備は不要である
が、使用するアルミナ等の触媒担体は薄板形状や単なる
微粉末状で触媒成分の効率的利用を図る上では未だ不十
分である。本発明は、こうした状況の下に触媒等の活性
成分をより効率的に利用するための担体を提供すること
を目的とするものであり、とくに排気ガス中の汚染物質
や炭酸ガス等の大気へ放散することが好ましくない物質
を効率的に除去するためのフィルタ担体及びそれを用い
たフィルタ、とりわけ固定発生源からの大量の炭酸ガス
等のガスを効率的にかつ経済的に分離回収するに好適な
フィルタ担体及びそれを用いたフィルタを提供すること
を目的とするものである。
However, although the method utilizing the adsorption / desorption of carbon dioxide gas can regenerate the adsorbent, it requires a huge amount of treatment equipment such as a gas treatment tower, and a large amount of exhaust gas is discharged. It is not suitable or economical to process gas in real time. Further, in the method utilizing the above-mentioned decomposition catalyst, equipment such as a gas treatment tower is not necessary, but the catalyst carrier such as alumina used is in the form of a thin plate or simply fine powder in order to efficiently utilize the catalyst components. It is still insufficient. The present invention aims to provide a carrier for more efficiently utilizing an active component such as a catalyst under such a situation, and particularly to a carrier such as pollutants in exhaust gas or carbon dioxide gas. A filter carrier for efficiently removing substances that are not desirable to be released and a filter using the same, especially suitable for efficiently and economically separating and recovering a large amount of gas such as carbon dioxide gas from a fixed source Another object of the present invention is to provide a simple filter carrier and a filter using the same.

【0004】[0004]

【課題を解決するための手段】本発明者は、鋭意検討し
た結果、特定の構造を有するAlまたはAl合金の多孔
体を担体として利用することが有効であることを見出
し、本発明に至った。すなわち、本発明は、(1)気孔
率80%以上の連通孔を有するAlもしくはAl合金よ
りなる金属3次元多孔体からなり、かつその表面がアル
マイト処理により微細な表面凹凸のある酸化皮膜を有し
ている活性成分用担体、(2)上記(1)項記載の担体
の酸化皮膜表面に特定成分を吸着・吸収もしくは分解し
得る成分を担持しているフィルタをその要旨とするもの
である。上記のように本発明の担体においてはAlもし
くはAl合金よりなり80%以上の気孔率を持つ連通孔
を有する金属多孔体を使用する。ここでAlもしくはA
l合金を素材とするのはフィルタ等の軽量化に貢献する
ことに加え、以下に述べるようにアルマイト処理により
容易に微細孔を有する酸化皮膜を形成することが可能で
あるためである。
As a result of intensive studies, the present inventors have found that it is effective to use a porous body of Al or Al alloy having a specific structure as a carrier, and have arrived at the present invention. . That is, the present invention comprises (1) a three-dimensional metal porous body made of Al or an Al alloy having continuous pores having a porosity of 80% or more, and having an oxide film whose surface has fine surface irregularities by alumite treatment. The gist of the present invention is a carrier for active ingredients, (2) a filter carrying a component capable of adsorbing, absorbing or decomposing a specific component on the surface of an oxide film of the carrier described in (1) above. As described above, in the carrier of the present invention, a porous metal body made of Al or an Al alloy and having communicating pores having a porosity of 80% or more is used. Where Al or A
The reason why the l-alloy is used as a material is that, in addition to contributing to weight reduction of filters and the like, an oxide film having fine pores can be easily formed by alumite treatment as described below.

【0005】本発明に使用するAl合金としては、例え
ばAl/S;Al/Mg;Al/Cu;Al/Ni等が
ある。またフィルタ等として適用するためには被処理流
体の通気抵抗を小さくする必要があることから、80%
以上の気孔率を持つ連通孔を有している多孔体構造とす
る。本発明に使用するこのようなAlもしくはAl合金
よりなる金属多孔体は、公知の方法により製造すること
ができる。例えば、特公昭38−17554に記載され
ているような方法を用いることができる。この方法に従
って例えば発泡構造を有するポリウレタンフォーム上に
Al粉末、結合剤としてフェノール樹脂、希釈剤として
アルコール、添加剤としてカルボキシルメチルセルロー
スをそれぞれ40,10,48,2重量%混合した塗料
をスプレー等で均一に塗布する。この塗布物を室温で1
0分間及び120℃で10分間乾燥後380℃で50分
間焼成する。ついで水素気流中において630℃にて2
時間焼成することによりAl多孔体が形成される。
Examples of the Al alloy used in the present invention include Al / S; Al / Mg; Al / Cu; Al / Ni. Moreover, in order to apply it as a filter, it is necessary to reduce the ventilation resistance of the fluid to be treated, so 80%
A porous body structure having communication holes having the above porosity is used. The metal porous body made of such Al or Al alloy used in the present invention can be manufactured by a known method. For example, the method described in JP-B-38-17554 can be used. According to this method, for example, by spraying a paint, etc., on a polyurethane foam having a foamed structure, Al powder, phenol resin as a binder, alcohol as a diluent, and carboxymethyl cellulose as an additive at 40, 10, 48 and 2% by weight, respectively, are sprayed. Apply to. Apply this coating at room temperature for 1
Dry for 0 minutes and 120 ° C. for 10 minutes, and then bake at 380 ° C. for 50 minutes. Then, in a hydrogen stream at 630 ° C, 2
By firing for a time, an Al porous body is formed.

【0006】次に上記のAlもしくはAl合金よりなる
金属多孔体にアルマイト処理により酸化皮膜を形成す
る。この酸化皮膜は数百Åの微細孔が多数存在すること
により大きな表面凹凸を有する。従って、本来多孔体構
造であるためその比表面積が大きいのに加え、さらにそ
の比表面積は大きくなり、反応あるいは分離、回収を目
的とするガスとの接触面積が増大することで分解回収効
率の向上に大きく寄与する。さらにこの酸化皮膜は排出
ガス中に微量含まれる腐蝕性のガスによる多孔体金属の
腐蝕を防止する働きもする。ここで酸化皮膜を形成する
ためのアルマイト処理自体は公知の方法により行うこと
ができる。例えば一般的な硫酸電解液を用いる方法など
で行うことができる。また、酸化皮膜の厚みとしては、
好ましくは0.1μm以上10μm以下とする。0.1
μmより薄いと表面凹凸が小さいことに加え耐食性にも
問題があり、10μmを越える厚みになると金属多孔体
としての曲げ、屈曲等の加工性が悪くなるためフィルタ
形状に制限が生じるためである。
Next, an oxide film is formed on the porous metal body made of Al or Al alloy by alumite treatment. This oxide film has large surface irregularities due to the presence of many hundreds of Å micropores. Therefore, in addition to having a large specific surface area because it is a porous structure by nature, its specific surface area is further increased, and the contact area with the gas for the purpose of reaction, separation, or recovery is increased, and the decomposition recovery efficiency is improved. Greatly contribute to. Further, this oxide film also functions to prevent the corrosion of the porous metal by the corrosive gas contained in the exhaust gas in a trace amount. The alumite treatment itself for forming the oxide film can be performed by a known method. For example, it can be performed by a method using a general sulfuric acid electrolyte. Also, as the thickness of the oxide film,
The thickness is preferably 0.1 μm or more and 10 μm or less. 0.1
This is because when the thickness is less than 10 μm, the surface irregularities are small, and in addition, there is a problem in corrosion resistance, and when the thickness exceeds 10 μm, the workability such as bending and bending of the porous metal body deteriorates, and the filter shape is restricted.

【0007】本発明の担体は、今まで述べてきたことか
ら明らかなように、通気抵抗が小さく、かつ比表面積が
著しく大きく、軽量でしかも成形加工性にも優れてお
り、一般の反応用触媒担体として有用であり、また流体
中の特定成分を分離、除去するためのフィルタ用担体と
しても好適である。例えば火力発電所や工場の排気ガス
からのSOx、NOx等の有害成分の除去あるいは自動車
排気ガスのフィルタとして有用である。しかし、本発明
の担体は、その骨格表面に炭酸ガスを吸着・吸収もしく
は分解可能な材料を担持させることにより排出ガスから
炭酸ガスを効率よく分離もしくは分解を可能とするフィ
ルタにとくに好適である。ここで炭酸ガスを吸着もしく
は分解させる物質としては、例えばまたIIa属金属もし
くはその酸化物などにより炭酸ガスを吸着させることが
可能である。また、特開平4−135621に記載され
ているような酸素欠陥マグネタイトや、特開平4−36
3142に記載されている硫化モリブデン等の触媒物質
を用いることができる。
As is clear from what has been described so far, the carrier of the present invention has a small air flow resistance, a remarkably large specific surface area, is lightweight, and is excellent in molding processability. It is useful as a carrier, and is also suitable as a carrier for a filter for separating and removing a specific component in a fluid. For example, it is useful as a filter for automobile exhaust gas, or removal of harmful components such as SO x and NO x from exhaust gas of thermal power plants and factories. However, the carrier of the present invention is particularly suitable for a filter capable of efficiently separating or decomposing carbon dioxide gas from exhaust gas by supporting a material capable of adsorbing / absorbing or decomposing carbon dioxide gas on its skeleton surface. Here, as the substance that adsorbs or decomposes carbon dioxide, for example, it is also possible to adsorb carbon dioxide with a Group IIa metal or its oxide. Further, oxygen-defective magnetite as described in JP-A-4-135621 and JP-A-4-36
Catalytic materials such as molybdenum sulfide described in 3142 may be used.

【0008】またこれらの物質を金属多孔体の骨格表面
に担持させる方法としては、微粉末をバインダーととも
に吹き付け塗着させる方法やゾルゲル法もしくはメッキ
法などによる被膜の形成あるいは真空蒸着、スパッタリ
ング、イオンプレーティング、CVD、プラズマCVD
法などの気相法による膜形成方法を用いても可能であ
る。本発明の金属多孔体を用いたフィルタ構造において
は、切断、曲げなどの機械加工が容易であることから炭
酸ガス等の排出設備に合わせて所望の形状のフィルタ構
造が容易かつ安価に実現可能である。さらに炭酸ガス等
を吸着・吸収あるいは分解した後のフィルターは加熱処
理や水素などの還元ガス中での加熱処理により容易に再
生可能であり、これらの再生過程において再放出される
高濃度の炭酸ガスや炭化水素ガスは再資源利用すること
も可能である。
Further, as a method for supporting these substances on the skeleton surface of the metal porous body, a method of spraying and applying fine powder together with a binder, a film formation by a sol-gel method or a plating method, vacuum deposition, sputtering, ion plating, etc. Coating, CVD, plasma CVD
It is also possible to use a film forming method by a vapor phase method such as a method. In the filter structure using the porous metal body of the present invention, it is possible to easily and inexpensively realize a filter structure having a desired shape in accordance with a discharge facility such as carbon dioxide gas, since machining such as cutting and bending is easy. is there. Furthermore, the filter after adsorbing, absorbing or decomposing carbon dioxide, etc. can be easily regenerated by heat treatment or heat treatment in a reducing gas such as hydrogen. High concentration carbon dioxide gas re-released during these regeneration processes. It is also possible to reuse hydrocarbon gas and hydrocarbon gas.

【0009】[0009]

【実施例】【Example】

実施例1 厚さ2mmのポリウレタン発泡体に、平均粒径8μmの
Al合金(Mg1wt%)粉末50重量部をバインダー
樹脂としてのアクリル樹脂を10重量部、さらに希釈剤
としてベンジルアルコールを38重量部、分散剤として
カルボキシルメチルセルロースを2重量部混合したスラ
リー液を塗布後室温で乾燥した後、還元雰囲気で620
℃で熱処理することにより形成したAl合金多孔体(気
孔率91%)を下記の条件でアルマイト処理を行った。 電解液 10%硫酸 液温度 2℃ 電流密度 1A/dm2 時間 20分 この時の酸化皮膜の厚みは約6μmであった。
Example 1 In a polyurethane foam having a thickness of 2 mm, 50 parts by weight of an Al alloy (Mg 1 wt%) powder having an average particle size of 8 μm, 10 parts by weight of an acrylic resin as a binder resin, and 38 parts by weight of benzyl alcohol as a diluent, A slurry liquid prepared by mixing 2 parts by weight of carboxymethyl cellulose as a dispersant was applied, dried at room temperature, and then 620 in a reducing atmosphere.
The Al alloy porous body (porosity 91%) formed by heat treatment at ℃ was anodized under the following conditions. Electrolyte solution 10% sulfuric acid solution temperature 2 ° C. current density 1 A / dm 2 hours 20 minutes At this time, the thickness of the oxide film was about 6 μm.

【0010】この酸化皮膜を有するAl多孔体に酸化カ
ルシウム微粉末を50g/cm2の割合でアクリル樹脂
をバインダーとして吹き付け塗着させた後脱気乾燥し
た。こうして得られた多孔体を巾1m、長さ15mに切
り、これを図1に示すように円筒状に巻き、仕上げ直径
20cmのアルマイト処理したアルミニウム円筒に納め
た。中心部と外筒の隙間はアルマイト処理したアルミニ
ウム板で埋めた。出来上がったフィルタを用いて吸着実
験を行った。その実験に使用した装置の概要を図2に示
す。処理用ガス10%CO2を含むairを1リットル
/minの流量で流し、フィルタ後のガスをサンプリン
グし、市販のCO2濃度検知管(2%濃度以上を検知)
を用いてCO2の存在確認をした。airを流しはじめ
てから約21時間後よりCO2が検知され始めた。実験
終了後、フィルタを真空下500℃で加熱して、CO2
を回収して再生した。再生したフィルタを再度実験に供
したところ、初期とほぼ同じ結果が得られた。
A fine powder of calcium oxide was sprayed on the Al porous body having the oxide film at a rate of 50 g / cm 2 by using an acrylic resin as a binder to apply the powder, followed by degassing and drying. The thus-obtained porous body was cut into a width of 1 m and a length of 15 m, which was wound into a cylindrical shape as shown in FIG. 1 and placed in an anodized aluminum cylinder having a finished diameter of 20 cm. The gap between the center and the outer cylinder was filled with an alumite-treated aluminum plate. An adsorption experiment was conducted using the finished filter. The outline of the apparatus used for the experiment is shown in FIG. Air containing processing gas 10% CO 2 is flowed at a flow rate of 1 liter / min, the gas after the filter is sampled, and a commercially available CO 2 concentration detection tube (2% concentration or more is detected)
Was used to confirm the presence of CO 2 . Approximately 21 hours after the start of air flow, CO 2 started to be detected. After the experiment was completed, the filter was heated at 500 ° C. under vacuum to remove CO 2
Was recovered and regenerated. When the regenerated filter was subjected to the experiment again, almost the same result as the initial result was obtained.

【0011】比較例 実施例1においてアルマイト処理を施さないAl多孔体
を、同様にフィルタとしての特性を評価したところ、a
irを流し始めてから2時間後にCO2が検知され始め
た。
Comparative Example The characteristics of the Al porous body not subjected to the alumite treatment in Example 1 as a filter were evaluated in the same manner.
CO 2 started to be detected 2 hours after starting the flow of ir.

【0012】[0012]

【発明の効果】以上説明したように、本発明の活性成分
用担体は、その比表面積が従来の担体に比べて顕著に増
大しているため担持した活性成分を効率的に利用でき
る。また、これを使用したフィルタにより大掛かりな設
備を設置することになく効率的、かつ経済的に炭酸ガス
等を分離、回収しあるいは汚染物質を除去することがで
きる。
As described above, the carrier for active ingredient of the present invention has a remarkably increased specific surface area as compared with the conventional carrier, so that the loaded active ingredient can be efficiently utilized. Further, a filter using this can efficiently and economically separate and recover carbon dioxide gas or remove pollutants without installing large-scale equipment.

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

【図1】本発明のAl又はAl合金多孔体からなる活性
成分用担体を円筒状に巻いたフィルタの説明図、
FIG. 1 is an explanatory view of a filter in which a carrier for an active ingredient comprising an Al or Al alloy porous body of the present invention is wound in a cylindrical shape,

【図2】実施例に使用した実験装置の概略図。FIG. 2 is a schematic diagram of an experimental apparatus used in Examples.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01J 37/02 ZAB 301 K ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location B01J 37/02 ZAB 301 K

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 気孔率80%以上の連通孔を有するAl
もしくはAl合金よりなる金属3次元多孔体からなり、
かつその表面がアルマイト処理により微細な表面凹凸の
ある酸化皮膜を有していることを特徴とする活性成分用
担体。
1. Al having communication holes with a porosity of 80% or more
Or, it consists of a metal three-dimensional porous body made of Al alloy,
A carrier for an active ingredient, characterized in that its surface has an oxide film having fine surface irregularities by anodizing.
【請求項2】 酸化皮膜の厚みが0.1μm以上10μ
m以下であることを特徴とする請求項1記載の活性成分
用担体。
2. The thickness of the oxide film is 0.1 μm or more and 10 μm.
The carrier for an active ingredient according to claim 1, which is less than or equal to m.
【請求項3】 請求項1記載の担体の酸化皮膜表面に特
定成分を吸着・吸収もしくは分解し得る成分を担持して
いることを特徴とするフィルタ。
3. A filter, wherein the oxide film surface of the carrier according to claim 1 carries a component capable of adsorbing, absorbing or decomposing a specific component.
【請求項4】 酸化皮膜の厚みが0.1μm以上10μ
m以下であることを特徴とする請求項3記載のフィル
タ。
4. The oxide film has a thickness of 0.1 μm or more and 10 μm.
The filter according to claim 3, wherein the filter is m or less.
JP6163801A 1994-07-15 1994-07-15 Carrier and filter using the same Pending JPH0824667A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6163801A JPH0824667A (en) 1994-07-15 1994-07-15 Carrier and filter using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6163801A JPH0824667A (en) 1994-07-15 1994-07-15 Carrier and filter using the same

Publications (1)

Publication Number Publication Date
JPH0824667A true JPH0824667A (en) 1996-01-30

Family

ID=15780966

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6163801A Pending JPH0824667A (en) 1994-07-15 1994-07-15 Carrier and filter using the same

Country Status (1)

Country Link
JP (1) JPH0824667A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006055692A (en) * 2004-08-17 2006-03-02 Ishikawajima Harima Heavy Ind Co Ltd Catalyst product and production method therefor
CN100395028C (en) * 2005-11-03 2008-06-18 安泰科技股份有限公司 Porous catalytic filtering metal material and its prepn
JP2008212844A (en) * 2007-03-05 2008-09-18 Shimadzu Corp Adsorption element and adsorption apparatus for carbon dioxide

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006055692A (en) * 2004-08-17 2006-03-02 Ishikawajima Harima Heavy Ind Co Ltd Catalyst product and production method therefor
CN100395028C (en) * 2005-11-03 2008-06-18 安泰科技股份有限公司 Porous catalytic filtering metal material and its prepn
JP2008212844A (en) * 2007-03-05 2008-09-18 Shimadzu Corp Adsorption element and adsorption apparatus for carbon dioxide
JP4730842B2 (en) * 2007-03-05 2011-07-20 株式会社島津製作所 Carbon dioxide adsorption element and adsorption device

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