JPH0647246A - Adsorption type air cleaning machine and adsorbent used therefor - Google Patents

Adsorption type air cleaning machine and adsorbent used therefor

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Publication number
JPH0647246A
JPH0647246A JP4204997A JP20499792A JPH0647246A JP H0647246 A JPH0647246 A JP H0647246A JP 4204997 A JP4204997 A JP 4204997A JP 20499792 A JP20499792 A JP 20499792A JP H0647246 A JPH0647246 A JP H0647246A
Authority
JP
Japan
Prior art keywords
filter
air
adsorption
micropores
cleaning machine
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
JP4204997A
Other languages
Japanese (ja)
Inventor
Keiichi Chiba
佳一 千葉
Koji Mishima
弘次 三嶋
Tomoyo Inoue
智代 井上
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.)
Takuma Research and Development Co Ltd
Original Assignee
Takuma Research and Development 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 Takuma Research and Development Co Ltd filed Critical Takuma Research and Development Co Ltd
Priority to JP4204997A priority Critical patent/JPH0647246A/en
Publication of JPH0647246A publication Critical patent/JPH0647246A/en
Pending legal-status Critical Current

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  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To well clean air contg. carbon monoxide by providing an adsorption filter having adsorbents designed to carry metals on carriers having micropores to a passage for treating the air to be cleaned. CONSTITUTION:This adsorption type air cleaning machine is constituted of a means which consists of a cleaning machine body 1 and a suction pipe 2, is provided with a case-shaped truck 1A having a wind path A for treating the air to be cleaned from a connecting port 1a to a discharge port 1b within this cleaning machine body 1 and cleans the air of a wind path A for treatment and a motor-driven fan 1B which sucks and discharges the air. This cleaning means consists of the primary filter F1 which is formed of metallic wires entangled like a scrubbing brush as filter media, the secondary filter F2 which consists of screens made of wire nets as filter media, the tertiary filter F3 for which bag filters made of glass wool are utilized and the quatenary filter F4 which has the adsorbents carrying one or plural metals selected from transition metals on adsorbents and carriers having micropores.

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、アーク溶接・ガス溶接
・レーザー溶接・ガス切断・レーザー切断・プラズマ切
断・電子ビーム加工・放電加工・レーザー加工で代表さ
れる各種加工作業に伴う排ガスで汚染される各種作業
場、自動車の排ガスで汚染される屋内駐車場・交差点、
石油ストーブで代表される燃焼器具の排ガスで汚染され
る各種店舗・スーパーマーケット・百貨店などを浄化対
象域をして、汚染された空気を浄化するための技術で、
詳しくは、浄化対象域から導入した浄化対象空気の処理
用風路に吸着フィルターを浄化対象空気に接触する状態
に設けて、浄化対象空気中の窒素酸化物や亜硫酸ガス・
アンモニアガス・臭気成分等を吸着除去するように構成
してある吸着式空気清浄機と、それに用いる吸着剤とに
関する。
[Field of Industrial Application] The present invention is contaminated by exhaust gas accompanying various processing operations represented by arc welding, gas welding, laser welding, gas cutting, laser cutting, plasma cutting, electron beam machining, electric discharge machining, and laser machining. Various workplaces, indoor parking lots / intersections contaminated by automobile exhaust gas,
A technology for purifying contaminated air by purifying various stores, supermarkets, department stores, etc. that are contaminated with exhaust gas of combustion appliances typified by oil stoves,
Specifically, an adsorption filter is provided in the air passage for treatment of the air to be purified introduced from the area to be purified so that it is in contact with the air to be purified, and nitrogen oxides or sulfur dioxide gas
The present invention relates to an adsorption-type air cleaner configured to adsorb and remove ammonia gas, odorous components, and the like, and an adsorbent used therefor.

【0002】[0002]

【従来の技術】例えば各種作業場に設置される空気清浄
機としては、作業場の全体を浄化対象域とする全体用の
ものと、作業場のうち排ガスが発生する局部箇所を浄化
対象域とする局部用のものとがある。そして、上記のよ
うに各種の箇所で使用される空気清浄機として従来で
は、吸着フィルターとして、活性炭・活性アルミナ・ゼ
オライトなどの吸着剤を備えたものが知られている。
2. Description of the Related Art For example, as an air cleaner installed in various workplaces, an air cleaner for the entire work area is a purification target area, and an air cleaner for a local location in the work area where exhaust gas is generated is a purification target area. There are some. As an air purifier used in various places as described above, conventionally, an adsorption filter provided with an adsorbent such as activated carbon, activated alumina, or zeolite is known.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来技術
によるときは、アンモニアガス・亜硫酸ガス・臭気成分
は吸着フィルターによって吸着除去できる。しかし、上
記した各種作業場を浄化対象域とした場合、前記のアー
ク溶接・ガス溶接・レーザー溶接・ガス切断・レーザー
切断・プラズマ切断・電子ビーム加工・放電加工・レー
ザー加工などに伴い発生する窒素酸化物を除去すること
ができなかった。つまり、活性炭・活性アルミナ・ゼオ
ライトなどの吸着剤は、窒素酸化物のうち二酸化窒素
(NO2 )に対する吸着能は若干有するが、一酸化窒素
(NO)に対する吸着能は殆どない。そして、上記の各
種作業に伴って発生する排ガス中の窒素酸化物は、例え
ばアーク溶接やプラズマ切断に伴う排ガス中では一酸化
窒素が80〜95%であるといったように大部分が一酸
化窒素であり、また、その排ガス中には、一酸化窒素が
5〜60ppm含まれるといったように一酸化窒素が多
量に含有されているから、その一酸化窒素の全部を吸着
除去できず、そのため空気浄化は十分に行えなかった。
要するに、従来には窒素酸化物を除去する技術及び装置
がなかった。本発明の目的は、一酸化窒素を含有する空
気を良好に浄化することができる吸着式空気清浄機と、
それの使用に好適な吸着剤とを提供する点にある。
However, according to the above conventional technique, the ammonia gas, the sulfurous acid gas, and the odorous component can be adsorbed and removed by the adsorption filter. However, when the above-mentioned various workplaces are targeted for purification, the nitrogen oxides that accompany arc welding, gas welding, laser welding, gas cutting, laser cutting, plasma cutting, electron beam machining, electrical discharge machining, laser machining, etc. The thing could not be removed. That is, adsorbents such as activated carbon, activated alumina, and zeolite have some adsorption capacity for nitrogen dioxide (NO 2 ) among nitrogen oxides, but almost no adsorption capacity for nitric oxide (NO). And most of the nitrogen oxides in the exhaust gas generated by the above-mentioned operations are nitric oxide, such as 80 to 95% of nitric oxide in the exhaust gas accompanying arc welding or plasma cutting. In addition, since the exhaust gas contains a large amount of nitric oxide such as 5 to 60 ppm of nitric oxide, it is not possible to adsorb and remove all of the nitric oxide, and therefore air purification is not possible. I couldn't do enough.
In short, heretofore, there has been no technique or apparatus for removing nitrogen oxides. An object of the present invention is an adsorption type air purifier capable of satisfactorily purifying air containing nitric oxide,
And to provide a suitable adsorbent for its use.

【0004】[0004]

【課題を解決するための手段】本発明による吸着式空気
清浄機の特徴は、吸着フィルターとして、ミクロ細孔を
有する担体に金属を担持させた構造の吸着剤を備えたも
のを設けてある点にある。本発明による第1の吸着式空
気清浄機用吸着剤の特徴は、ミクロ細孔を有する活性炭
に、遷移金属のうちから選択した1つ又は複数のものを
担持させてある点にある。本発明による第2の吸着式空
気清浄機用吸着剤の特徴は、ミクロ細孔を有するゼオラ
イトに、遷移金属のうちから選択した1つ又は複数のも
のを担持させてある点にある。本発明による第3の吸着
式空気清浄機用吸着剤の特徴は、ミクロ細孔を有する無
機担体に、遷移金属のうちから選択した1つ又は複数の
ものを担持させてある点にある。前記遷移金属は、銅ヤ
マンガンなどである。詳述すれば、原子の電子配列が不
完全なd軌道を持つ元素又は、不完全なd軌道を持つ陽
イオンを生じる元素で、典型元素以外の元素をさし、具
体的にいうと、第1から第4遷移元素である。第1遷移
元素は、スカンジウム・チタン・バナジウム・クロム・
マンガン・鉄・コバルト・ニッケル・銅であり第2遷移
元素は、イットリウム・ジルコニウム・ニオブ・モリブ
デン・テクネチウム・ルテニウム・ロジウム・パテジウ
ム・銀であり、第3遷移元素は、ランタンなどのランタ
ノイドであり、第4遷移元素は、アクチウムなどのアク
チノイドである。前記無機担体は、アルミナ・シリカ・
シリカアルミナ・酸化チタン・マグネシアなどであり、
可及的表面積が大きいことが好ましい。
The adsorption type air purifier according to the present invention is characterized in that an adsorption filter provided with an adsorbent having a structure in which a metal having micropores is supported is provided. It is in. The feature of the first adsorbent for an adsorption air purifier according to the present invention is that activated carbon having micropores is loaded with one or more selected from transition metals. A feature of the second adsorbent for an adsorption air purifier according to the present invention is that one or more selected from transition metals are supported on zeolite having micropores. The third characteristic of the adsorbent for an adsorption air purifier according to the present invention is that one or more selected from transition metals are carried on an inorganic carrier having micropores. The transition metal is copper yamanganese or the like. More specifically, an element having an d-orbital in which the electronic arrangement of atoms is incomplete or an element that produces a cation having an incomplete d-orbital is an element other than a typical element, and specifically, It is a 1st to 4th transition element. The first transition element is scandium, titanium, vanadium, chromium,
Manganese, iron, cobalt, nickel, copper, the second transition element is yttrium, zirconium, niobium, molybdenum, technetium, ruthenium, rhodium, palladium, silver, and the third transition element is a lanthanoid such as lanthanum, The fourth transition element is an actinide such as actium. The inorganic carrier is alumina / silica /
Silica-alumina, titanium oxide, magnesia, etc.,
It is preferable that the surface area is as large as possible.

【0005】[0005]

【作用】活性炭やゼオライトなどのミクロ細孔を有する
担体に金属を担持させた構造の吸着剤は、一酸化窒素に
対しても化学吸着型ミクロ細孔充填現象を起こし、単に
ミクロ細孔を有する従来の活性炭・活性アルミナ・ゼオ
ライトなどに比較して一酸化窒素に対する吸着能が格段
に優れている。従って上記本発明の吸着式空気清浄機に
よれば、そのような一酸化窒素に対する吸着能に優れた
吸着剤を備えた吸着フィルターを備えているので、一酸
化窒素を十分に吸着除去することができる。第1〜第3
の吸着式空気清浄機用吸着剤によれば、活性炭の60倍
以上のNO吸着能を得ることができる。因みに、第1、
第2の吸着式空気清浄機用吸着剤の吸着能は図3のNO
吸着等温線図に示すようになる。もちろん、本発明に吸
着式空気清浄機及び吸着剤には、従来と同様な一酸化窒
素以外の物質に対する吸着能を有する。
[Function] An adsorbent having a structure in which a metal is supported on a carrier having micropores such as activated carbon or zeolite causes a chemisorption-type micropore filling phenomenon even for nitric oxide, and simply has micropores. Compared to conventional activated carbon, activated alumina, zeolite, etc., its adsorption capacity for nitric oxide is significantly superior. Therefore, according to the adsorption type air cleaner of the present invention described above, since it is provided with the adsorption filter provided with the adsorbent excellent in the adsorption ability for such nitric oxide, it is possible to sufficiently adsorb and remove nitric oxide. it can. First to third
According to the adsorbent for the adsorption-type air purifier, it is possible to obtain the NO adsorption capacity which is 60 times or more that of activated carbon. By the way, first,
The adsorption capacity of the second adsorption-type air cleaner adsorbent is NO in FIG.
As shown in the adsorption isotherm. Needless to say, the adsorption type air cleaner and the adsorbent of the present invention have the same adsorbing ability for substances other than nitric oxide as in the conventional case.

【0006】[0006]

【発明の効果】従って本発明によれば、対象空気が一酸
化窒素を多く含む場合の空気浄化に有用な吸着式空気清
浄機及びそれに好適使用できる吸着剤を提供できるよう
になった。
Therefore, according to the present invention, it is possible to provide an adsorption type air cleaner useful for air purification when the target air contains a large amount of nitric oxide and an adsorbent which can be suitably used for the adsorption type air cleaner.

【0007】[0007]

【実施例】吸着式空気清浄機は、作業員の手元など局部
箇所を浄化対象域として空気浄化を行なうものであっ
て、図1に示すように、移動自在な清浄機本体1と吸込
管2とからなる。前記清浄機本体1は、吸込管2からの
吸い込み空気を対象空気とするものであって、上部に前
記吸込管2との接続口1aと排気口1bとを備えるとと
もに、下部に移動用のキャスター車輪1cを備え、か
つ、内部に前記接続口1aから排気口1bにわたる浄化
対象空気の処理用風路Aを備えたケース状の台車1Aを
設け、その台車1A内つまり処理用風路Aに接続口1a
から取り入れた空気を浄化する浄化手段と、吸込管2か
ら空気を吸い込んで処理用風路Aを通過させたのち排気
口1bから排出するように空気を吸い込み排出するため
のモーター駆動のファン1Bとを設けて構成されてい
る。前記浄化手段は、図2にも示すように、処理用風路
Aに、流動する吸い込み空気に接触して処理する1次フ
ィルターF1,2次フィルターF2,3次フィルターF
3,4次フィルターF4を、上流側から下流側にかけて
その記載順で並置する状態に設けて構成されている。1
次フィルターF1は、たわし状に絡ませた金属線をフィ
ルター材として、吸い込み空気中の火の粉を消す、つま
り、火花が内部に入ることを阻止するためのものであ
る。2次フィルターF2は、金網製のスクリーンをフィ
ルター材として、100μm以上の粗ダストを除去する
ためのものである。3次フィルターF3は、グラスウー
ル製のバグフィルター利用した0.5〜100μmの細
ダストを除去するためのものである。4次フィルターF
4は、吸着剤を備えた吸着フィルターFAであって、吸
着剤、ミクロ細孔(径20Å以下)を有する担体に、遷
移金属のうちから選択した1つ又は複数のものを担持さ
せた構造のものである。前記担体は、活性炭、ゼオライ
ト、無機担体であり、無機担体としては、アルミナ・シ
リカ・シリカアルミナ・酸化チタン・マグネシアなどを
挙げることができ、これらは、可及的表面積が大きいこ
とが好ましい。もちろん、吸着フィルターFAに使用す
る吸着剤は、活性炭を担体とするもの、、ゼオライトを
担体とするもの、無機担体を担体とするもののうちから
1つ又は複数を選択する。前記遷移金属のうち、第1遷
移元素としては、スカンジウム・チタン・バナジウム・
クロム・マンガン・鉄・コバルト・ニッケル・銅等を挙
げることができ、第2遷移元素としては、イットリウム
・ジルコニウム・ニオブ・モリブデン・テクネチウム・
ルテニウム・ロジウム・パテジウム・銀等を挙げること
ができ、第3遷移元素としては、ランタンなどのランタ
ノイド等を挙げることができ、第4遷移元素としては、
アクチウムなどのアクチノイドを挙げることができる。
これら吸着剤は、銅やマンガン等の遷移金属の存在によ
り、一酸化窒素に対しても化学的吸着型ミクロ細孔充填
現象を起こしてその一酸化窒素を吸着する。それらのN
O吸着能を確認するための実験を行った。実験に使用し
た吸着剤は、ミクロ細孔を有するヤシガラ活性炭(直径
3mm、高さ3mmの円柱状のもの)に銅とマンガンと
を担持させた構造の本発明のものAと、同様にミクロ細
孔を有するゼオライト(直径3mm、高さ3mmの円柱
状のもの)に銅とマンガンとを担持させた構造の本発明
のものBと、ヤシガラ活性炭(直径3mm、高さ3mm
の円柱状のもの)のみの従来品である。そして、グリデ
ュア溶接棒65を使用して電流値250Aにてアーク溶
接することで行うショベルローダの爪の肉盛りの際に発
生する煙を処理対象の排ガスとして供給し、出口での排
ガス中のNO濃度を測定した。入口での排ガス中のNO
濃度は55〜65ppmであり、従来品の出口での排ガ
ス中のNO濃度が50〜60ppmであったのに対し、
本発明のA及びBの出口での排ガス中のNO濃度はとも
に0ppmであった。なお、NO濃度測定は、化学発光
法(ケミカル法)によった。図3のNO吸着等温線(a
t25℃)で結果を示す。また、上記吸着剤の再生は、
温度あるいは圧力スイングにより窒素酸化物を脱離し、
脱離した窒素酸化物を別途処理する。前記吸込管2は、
長手方向の複数箇所に、屈曲自在な蛇腹管部2Aを有
し、それら各蛇腹管部2Aでの屈曲と台車1Aに対する
縦軸周りの回転により先端の吸込口2aの位置及び向き
を変更自在なものである。上記構成の吸着型空気清浄機
では、局部箇所から空気を吸い込むように吸込口2aを
セットすることにより、局部箇所の空気中のヒューム・
ダスト・臭気・窒素酸化物を除去することができ、特
に、窒素酸化物については、二酸化窒素はもちろん、一
酸化窒素も吸着除去することができる。なお、図では、
4次フィルターF4《吸着フィルターFA》の後にファ
ン1Bを設置してあるが、1次フィルターF1の手前・
1次フィルターF1と2次フィルターF2との間・2次
フィルターF2と3次フィルターF3との間・3次フィ
ルターF3と4次フィルターF4(FA)との間のいず
れに設置しても良い。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An adsorption type air purifier is for purifying air by using a local area such as a worker's hand as a purifying target area. As shown in FIG. 1, a movable purifier body 1 and a suction pipe 2 are provided. Consists of. The purifier body 1 is intended to use suction air from the suction pipe 2 as a target air, and has a connection port 1a for connecting to the suction pipe 2 and an exhaust port 1b at an upper portion thereof, and a moving caster at a lower portion thereof. A case-shaped truck 1A provided with wheels 1c and internally provided with a treatment air passage A for the air to be purified extending from the connection port 1a to the exhaust port 1b is provided, and is connected to the treatment vehicle air passage A inside the vehicle 1A. Mouth 1a
And a motor-driven fan 1B for sucking and discharging the air so that it is sucked from the suction pipe 2, passed through the processing air passage A, and then discharged from the exhaust port 1b. Is provided. As shown in FIG. 2, the purifying means has a primary filter F1, a secondary filter F2, and a tertiary filter F that process the suction air flowing in the treatment air passage A by contacting the suction air.
The third and fourth-order filters F4 are arranged in the stated order from the upstream side to the downstream side. 1
The next filter F1 uses a metal wire entwined in a scissor-like shape as a filter material to extinguish the sparks in the sucked air, that is, to prevent sparks from entering the inside. The secondary filter F2 is for removing coarse dust of 100 μm or more by using a wire mesh screen as a filter material. The third filter F3 is used for removing fine dust of 0.5 to 100 μm using a bag filter made of glass wool. 4th order filter F
Reference numeral 4 denotes an adsorption filter FA provided with an adsorbent, which has a structure in which one or more selected from transition metals are supported on an adsorbent and a carrier having micropores (diameter 20 Å or less). It is a thing. The carrier is activated carbon, zeolite, or an inorganic carrier, and examples of the inorganic carrier include alumina, silica, silica-alumina, titanium oxide, magnesia, and the like, which preferably have a large surface area. As a matter of course, the adsorbent used in the adsorption filter FA is selected from one or more of those having activated carbon as a carrier, those having zeolite as a carrier, and those having an inorganic carrier as a carrier. Among the above transition metals, the first transition element includes scandium, titanium, vanadium,
Chromium, manganese, iron, cobalt, nickel, copper, etc. can be mentioned, and the second transition elements include yttrium, zirconium, niobium, molybdenum, technetium,
Examples thereof include ruthenium, rhodium, palladium, silver, etc., examples of the third transition element include lanthanoids such as lanthanum, and examples of the fourth transition element include:
Mention may be made of actinides such as actium.
Due to the presence of transition metals such as copper and manganese, these adsorbents also cause a chemical adsorption type micropore filling phenomenon for nitric oxide and adsorb the nitric oxide. Those N
An experiment was conducted to confirm the O adsorption capacity. The adsorbent used in the experiment was the same as that of the present invention A having a structure in which copper and manganese were supported on coconut husk activated carbon (cylindrical having a diameter of 3 mm and a height of 3 mm) having micropores. Zeolite activated carbon (diameter 3 mm, height 3 mm) of the present invention B having a structure in which copper and manganese are supported on a porous zeolite (cylindrical one having a diameter 3 mm and height 3 mm).
It is a conventional product. Then, the smoke generated during the buildup of the claws of the shovel loader by performing arc welding at a current value of 250 A using the gridur welding rod 65 is supplied as the exhaust gas to be treated, and NO in the exhaust gas at the outlet is supplied. The concentration was measured. NO in exhaust gas at the inlet
The concentration is 55 to 65 ppm, whereas the NO concentration in the exhaust gas at the outlet of the conventional product was 50 to 60 ppm,
The NO concentrations in the exhaust gas at the outlets A and B of the present invention were both 0 ppm. The NO concentration was measured by the chemiluminescence method (chemical method). The NO adsorption isotherm (a in FIG.
The results are shown at t25 ° C. Also, the regeneration of the adsorbent,
Desorption of nitrogen oxides by temperature or pressure swing,
Separately treat the desorbed nitrogen oxides. The suction pipe 2 is
A flexible bellows tube portion 2A is provided at a plurality of positions in the longitudinal direction, and the position and direction of the suction port 2a at the tip can be freely changed by bending at each of the bellows tube portions 2A and rotating around the vertical axis with respect to the carriage 1A. It is a thing. In the adsorption-type air cleaner having the above-mentioned configuration, by setting the suction port 2a so as to suck the air from the local location, the fume in the air at the local location
Dust, odor, and nitrogen oxides can be removed, and in particular, nitrogen oxides can be adsorbed and removed as well as nitrogen dioxide. In the figure,
The fan 1B is installed after the fourth-order filter F4 << adsorption filter FA >>, but before the first-order filter F1.
It may be installed anywhere between the first-order filter F1 and the second-order filter F2, between the second-order filter F2 and the third-order filter F3, and between the third-order filter F3 and the fourth-order filter F4 (FA).

【0008】〔別実施例〕上記実施例では、局部箇所を
浄化対象域とする空気清浄機を示したが、本発明は室内
全体を浄化対象域として浄化する空気清浄機にも適用す
ることができる。
[Other Embodiments] In the above embodiments, the air purifier having the local portion as the purification target area is shown, but the present invention can be applied to the air purifier for purifying the entire room as the purification target area. it can.

【0009】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.

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

【図1】一部切り欠き側面図[Figure 1] Side view with partial cutaway

【図2】空気の流れを示すフローチャートFIG. 2 is a flowchart showing the flow of air.

【図3】NO吸着等温線図FIG. 3 NO adsorption isotherm diagram

【符号の説明】[Explanation of symbols]

A 処理用風路 FA 吸着フィルター A treatment air passage FA adsorption filter

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 浄化対象空気の処理用風路(A)に吸着
フィルター(FA)を浄化対象空気に接触する状態に設
けてある吸着式空気清浄機であって、前記吸着フィルタ
ー(FA)として、ミクロ細孔を有する担体に金属を担
持させた構造の吸着剤を備えたものを設けてある吸着式
空気清浄機。
1. An adsorption type air purifier, wherein an adsorption filter (FA) is provided in a treatment air passage (A) for purifying air to be in contact with the purification air, and the adsorption filter (FA) is used as the adsorption filter (FA). An adsorption type air cleaner provided with an adsorbent having a structure in which a metal having micropores is carried on a carrier having micropores.
【請求項2】 ミクロ細孔を有する活性炭に、遷移金属
のうちから選択した1つ又は複数のものを担持させてあ
る吸着式空気清浄機用吸着剤。
2. An adsorbent for an adsorption type air cleaner, wherein one or more selected from transition metals are supported on activated carbon having micropores.
【請求項3】 ミクロ細孔を有するゼオライトに、遷移
金属のうちから選択した1つ又は複数のものを担持させ
てある吸着式空気清浄機用吸着剤。
3. An adsorbent for an adsorption type air cleaner, wherein one or more selected from transition metals is supported on a zeolite having micropores.
【請求項4】 ミクロ細孔を有する無機担体に、遷移金
属のうちから選択した1つ又は複数のものを担持させて
ある吸着式空気清浄機用吸着剤。
4. An adsorbent for an adsorption-type air cleaner, wherein one or more selected from transition metals are supported on an inorganic carrier having micropores.
JP4204997A 1992-07-31 1992-07-31 Adsorption type air cleaning machine and adsorbent used therefor Pending JPH0647246A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4204997A JPH0647246A (en) 1992-07-31 1992-07-31 Adsorption type air cleaning machine and adsorbent used therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4204997A JPH0647246A (en) 1992-07-31 1992-07-31 Adsorption type air cleaning machine and adsorbent used therefor

Publications (1)

Publication Number Publication Date
JPH0647246A true JPH0647246A (en) 1994-02-22

Family

ID=16499753

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4204997A Pending JPH0647246A (en) 1992-07-31 1992-07-31 Adsorption type air cleaning machine and adsorbent used therefor

Country Status (1)

Country Link
JP (1) JPH0647246A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2728806A1 (en) * 1994-12-29 1996-07-05 Inst Francais Du Petrole ADSORBENTS USEFUL IN PROCESSES FOR PURIFYING ATMOSPHERES POLLUTED WITH NITROGEN OXIDE
KR100600514B1 (en) * 2004-08-19 2006-07-13 코아텍주식회사 A Portable Air Cleaning Apparatus using Filter for Dust Removal and Catalyst Material for Decomposition of Various Harmful and Acid Gas in the Air
JP2010253246A (en) * 2009-03-30 2010-11-11 Ando Corp Deodorizing device
EP2465673B1 (en) * 2010-12-14 2017-04-26 Erutec GmbH Device for preparing mineral wool waste
RU200346U1 (en) * 2020-04-08 2020-10-20 Евгения Александровна Колесняк Mobile ventilation unit for flue gas
US11976847B2 (en) 2022-03-22 2024-05-07 Danvita Thermal LLC Air purification system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2728806A1 (en) * 1994-12-29 1996-07-05 Inst Francais Du Petrole ADSORBENTS USEFUL IN PROCESSES FOR PURIFYING ATMOSPHERES POLLUTED WITH NITROGEN OXIDE
BE1010539A3 (en) * 1994-12-29 1998-10-06 Inst Francais Du Petrole Method of treatment of polluted by an atmosphere of nitrogen oxide.
KR100600514B1 (en) * 2004-08-19 2006-07-13 코아텍주식회사 A Portable Air Cleaning Apparatus using Filter for Dust Removal and Catalyst Material for Decomposition of Various Harmful and Acid Gas in the Air
JP2010253246A (en) * 2009-03-30 2010-11-11 Ando Corp Deodorizing device
JP2010253248A (en) * 2009-03-30 2010-11-11 Ando Corp Deodorizing device
JP4651741B2 (en) * 2009-03-30 2011-03-16 安藤建設株式会社 Deodorization device
EP2465673B1 (en) * 2010-12-14 2017-04-26 Erutec GmbH Device for preparing mineral wool waste
RU200346U1 (en) * 2020-04-08 2020-10-20 Евгения Александровна Колесняк Mobile ventilation unit for flue gas
US11976847B2 (en) 2022-03-22 2024-05-07 Danvita Thermal LLC Air purification system

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