JPH0647274A - Air cleaning material and its production - Google Patents

Air cleaning material and its production

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Publication number
JPH0647274A
JPH0647274A JP4203608A JP20360892A JPH0647274A JP H0647274 A JPH0647274 A JP H0647274A JP 4203608 A JP4203608 A JP 4203608A JP 20360892 A JP20360892 A JP 20360892A JP H0647274 A JPH0647274 A JP H0647274A
Authority
JP
Japan
Prior art keywords
iron
yttrium
gas
salt
air cleaning
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.)
Withdrawn
Application number
JP4203608A
Other languages
Japanese (ja)
Inventor
Tamio Noda
多美夫 野田
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP4203608A priority Critical patent/JPH0647274A/en
Publication of JPH0647274A publication Critical patent/JPH0647274A/en
Withdrawn legal-status Critical Current

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

Abstract

PURPOSE:To provide the air cleaning material which efficiently purifies the contaminated air containing malodorous gas represented by ammonia or hydrogen sulfide, etc., by forming composite oxide of iron and yttrium on the surface of the carrier consisting of an iron molding body. CONSTITUTION:The iron molding body is allowed to contact with the aq. soln. of yttrium salt and allowed to react under the atmosphere, and hear-treated at 200-350 deg.C under the condition in which reactional product coexists with unreacted metallic iron. Preferably, basic materials (e.g. calcium hydroxide) and iron salt (e.g. iron nitrate) are added to the aq. soln. of yttrium salt. The deodorizing filter 3 is made by using the air cleaning material obtained in this way and provided on the holder 7 of the sealed vessel 1 provided with the gas inlet 4 and gas outlet 5, and gas is circulated with the circulation fan 2. Thus the deodorizing filter having eliminating performance of hydrogen sulfide is obtained by convenient process.

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、アンモニアや硫化水素
等に代表される悪臭ガス類を含有する汚染空気を浄化す
る空気清浄化物およびその製造方法に関する。本発明の
空気清浄化物は、例えば家庭用の脱臭剤、乗物の脱臭剤
として用いることができる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air purification product for purifying contaminated air containing odorous gases such as ammonia and hydrogen sulfide, and a method for producing the same. The air-purified product of the present invention can be used as, for example, a household deodorant or a vehicle deodorant.

【0002】[0002]

【従来の技術】従来、空気中の悪臭ガスの処理法として
は、例えば活性炭を用いる吸着法、他の香料を用いるマ
スキング法、悪臭ガスを化学反応させる化学的方法で除
去あるいは不快感の軽減が行われている。しかしなが
ら、活性炭を用いる吸着法は、脱臭性能が短期間で劣化
するという問題がある。他の香料を用いるマスキング法
では香料が新たな不快感を与えることがあり、根本的な
解決策とならない。化学反応により悪臭ガスを変化させ
る化学的方法では、例えばオゾンにより、悪臭ガスを酸
化分解する方法等があるが、過剰なオゾンが人体に有害
である為に新たな害を引き起こす危険性が高い、即ち、
悪臭ガスとちょうど反応してくれる化学物質の量を制御
することが困難な為に不要な化学物質を発生させること
になり、根本的な解決と成りがたい。
2. Description of the Related Art Conventionally, as a method for treating malodorous gas in the air, for example, an adsorption method using activated carbon, a masking method using other fragrance, or a chemical method for chemically reacting the malodorous gas can be used to remove or alleviate discomfort. Has been done. However, the adsorption method using activated carbon has a problem that the deodorizing performance deteriorates in a short period of time. The masking method using other fragrances may not be a fundamental solution because the fragrance may cause new discomfort. In a chemical method of changing a malodorous gas by a chemical reaction, for example, by ozone, there is a method of oxidizing and decomposing the malodorous gas, but there is a high risk of causing new harm because excessive ozone is harmful to the human body. That is,
Since it is difficult to control the amount of chemical substances that react with the malodorous gas, unnecessary chemical substances are generated, and it is difficult to make a fundamental solution.

【0003】それらの問題点を解決する技術として繊維
学会誌(繊維と工業)Vol.42,No.12(19
86)P18〜26には第一鉄化合物とアスコルビン酸
とを水溶液状態で反応させて得られた錯体化合物が窒素
化合物系臭気ガスに対して脱臭力を有することが述べら
れている。しかし、本発明者等の知見ではこの錯体化合
物は硫黄化合物系の臭気ガスに対する脱臭力が弱いとい
う問題点があり、またこの錯体化合物は脱臭力が比較的
短期間で劣化するという問題点もあった。
As a technique for solving these problems, the Institute of Fiber Science (Fiber and Industry), Vol. 42, No. 12 (19
86) P18-26 states that a complex compound obtained by reacting a ferrous compound and ascorbic acid in an aqueous solution has a deodorizing power for a nitrogen compound-based odorous gas. However, according to the findings of the present inventors, there is a problem that this complex compound has a weak deodorizing power for sulfur compound-based odor gas, and that this complex compound has a problem that the deodorizing power deteriorates in a relatively short period of time. It was

【0004】本発明者等は鉄、マンガン等の金属にアス
コルビン酸等を接触させてできる反応生成物を未反応の
鉄、マンガン等と共存させた組成物を特開平3−188
939号(特願平1−280776号)で提案した。こ
の組成物は安価に製造でき、空気清浄力の劣化が極めて
小さく、従来技術の問題点を大巾に解消するものであっ
た。
The inventors of the present invention have disclosed a composition in which a reaction product obtained by contacting a metal such as iron or manganese with ascorbic acid or the like is allowed to coexist with unreacted iron or manganese or the like.
No. 939 (Japanese Patent Application No. 1-2807776). This composition can be manufactured at a low cost, and the deterioration of the air cleaning power is extremely small, and the problems of the prior art were largely solved.

【0005】[0005]

【発明が解決しようとする課題】本発明は、アンモニア
はもとより、特に脱硫化水素速度の改善、及び脱硫化水
素性能を長期間にわたって発揮する新たな空気清浄化物
およびその製造方法を提供することを課題としている。
DISCLOSURE OF THE INVENTION The present invention aims to provide not only ammonia but also a new air-purified product which improves the desulfurization rate and particularly exhibits a desulfurization performance over a long period of time, and a method for producing the same. It is an issue.

【0006】[0006]

【課題を解決するための手段】本発明の第1の態様は、
鉄の成形体を担持体とし、該担持体の表面に鉄とイット
リウムの複合酸化物を形成したことを特徴とする空気清
浄化物である。
The first aspect of the present invention is as follows.
It is an air-purified product characterized in that an iron molded body is used as a carrier and a complex oxide of iron and yttrium is formed on the surface of the carrier.

【0007】また本発明の第2の態様は、鉄の成形体を
イットリウム塩水溶液と接触させて大気中で反応させ、
その反応生成物が未反応の金属鉄と共存している状態で
200℃〜350℃に加熱処理することを特徴とする空
気清浄化物の製造方法である。
A second aspect of the present invention is to contact an iron molding with an aqueous yttrium salt solution to cause reaction in the atmosphere,
In the method for producing an air-purified product, the reaction product is heat-treated at 200 ° C. to 350 ° C. in the state of coexisting with unreacted metallic iron.

【0008】また本発明の第3の態様は、第2の態様に
おいて、前記イットリウム塩水溶液に塩基性物質及び鉄
塩を添加することを特徴とする空気清浄化物の製造方法
である。
A third aspect of the present invention is the method for producing an air-purified product according to the second aspect, wherein a basic substance and an iron salt are added to the yttrium salt aqueous solution.

【0009】[0009]

【作用】本発明者等の研究によればアンモニア(N
3 )やトリメチルアミン((CH 3 3 N)等の塩基
性ガスの脱臭性能は多塩基酸と金属の反応生成物である
金属錯体に非常に良く吸着するが硫化水素(H2 S)ガ
スの吸着力が弱い、その一つの解決方法は、本発明者等
が特願昭63−273195号に記述しているような固
体塩基を配する方法である。しかし、その後の研究で硫
化水素等の酸性ガスの吸着力の強い物質は金属鉄が水溶
液に溶解して生成する水酸化鉄及び酸化第二鉄であるこ
とを突き止めた。更に水酸化鉄を効果的に生成せしめ、
長期に安定して効果を継続する為には金属鉄と水酸化
鉄、酸化第二鉄、マグネタイトが共存する状態を形成さ
せる必要があることも突き止めた。具体的な製造プロセ
スでは、常温付近で製造した酸化鉄を200〜300℃
に加熱して一部の結晶水を分解除去することにより酸化
鉄の比表面積を増加させ、硫化水素吸着性能を大幅に改
善できることも見出した。
According to the research conducted by the present inventors, ammonia (N
H3) And trimethylamine ((CH 3)3N) and other bases
Deodorizing performance of volatile gas is a reaction product of polybasic acid and metal
Adsorbs very well to metal complexes, but hydrogen sulfide (H2S) Mo
The present inventors have found that one solution to the problem
Is described in Japanese Patent Application No. 63-273195.
This is a method of arranging body bases. However, in subsequent research
Metallic iron is water-soluble for substances that strongly adsorb acidic gases such as hydrogen fluoride
It should be iron hydroxide and ferric oxide formed by dissolving in liquid.
I found out. Furthermore, it effectively produces iron hydroxide,
Metallic iron and hydroxide for stable and long-lasting effect
A state in which iron, ferric oxide, and magnetite coexist is formed.
I also found out that it was necessary to make them. Concrete manufacturing process
In the case of iron, the iron oxide produced near room temperature is heated to 200-300 ° C.
Oxidation by heating to room temperature to decompose and remove some water of crystallization
The specific surface area of iron has been increased, and the hydrogen sulfide adsorption performance has been significantly improved.
I also found that I can do good.

【0010】本発明者等は更に改善研究を進めた結果、
触媒担体としての鉄の成形体の表面および細孔に鉄とイ
ットリウムの複合酸化物を形成させることにより、鉄酸
化物のみの組成物よりも優れた脱硫化水素能力を保持す
る組成物を得た。
As a result of further improvement studies conducted by the present inventors,
By forming a complex oxide of iron and yttrium on the surface and pores of an iron molded body as a catalyst carrier, a composition having a desulfurization ability superior to that of a composition containing only iron oxide was obtained. .

【0011】上記鉄の成形体としては、鉄を0.1〜1
mmの粒子に加工したもの、微細鉄粒子に粘結剤、糊料等
を配合混練してシート状とかハニカム状に成形加工後、
焼成して焼結させたもの、あるいは上記混練物を樹脂製
多孔体に塗布した後、焼成して焼結させたもの等が使用
できる。また鉄の成形体の表面および細孔に形成させた
鉄とイットリウムの複合酸化物の量は0.05〜0.2
g/gとすることが好ましい。
As the iron molding, 0.1 to 1 of iron is used.
mm processed into particles, fine iron particles with a binder, a paste, etc. mixed and kneaded, and then processed into a sheet or honeycomb shape,
It is possible to use a product obtained by firing and sintering, or a product obtained by applying the above-mentioned kneaded product to a resin porous body and then firing and sintering. The amount of iron-yttrium complex oxide formed on the surface and pores of the iron compact is 0.05 to 0.2.
It is preferably g / g.

【0012】上記鉄の成形体をイットリウム塩水溶液、
例えば硝酸イットリウム、塩化イットリウム、硫酸イッ
トリウム等を主成分とし、必要に応じてL−アスコルビ
ン酸を添加した水溶液と接触させる。このイットリウム
塩水溶液中において接触させた鉄は一部溶出し鉄イオン
が共存することとなる。上記接触の態様としては一般的
には浸漬法が採用されるが、散布、塗布等であっても両
者が充分に接触する限りにおいて制限はない。鉄の成形
体をイットリウム塩水溶液に、例えば30〜120秒浸
漬後取り出し、大気中で反応させる。
[0012] The above-mentioned iron molding is treated with an yttrium salt aqueous solution,
For example, it is brought into contact with an aqueous solution containing yttrium nitrate, yttrium chloride, yttrium sulfate or the like as a main component, and L-ascorbic acid added if necessary. Part of the iron contacted in this yttrium salt aqueous solution is eluted and iron ions coexist. A dipping method is generally adopted as a mode of the above-mentioned contact, but there is no limitation even in the case of spraying, coating or the like as long as the two are sufficiently in contact with each other. The iron molded body is immersed in an aqueous solution of yttrium salt for 30 to 120 seconds, taken out, and then allowed to react in the atmosphere.

【0013】上記鉄の成形体の表面において、その反応
生成物が未反応の金属鉄と共存している状態で200℃
〜350℃に加熱処理することにより、成形体の表面に
生成している水酸化物は1μ以下のクラスター状の、鉄
とイットリウム複合酸化物を生成する。
On the surface of the iron molding, the reaction product coexists with unreacted metallic iron at 200 ° C.
By heat treatment at up to 350 ° C., the hydroxide formed on the surface of the molded body forms a cluster of iron and yttrium oxide having a size of 1 μm or less.

【0014】上記加熱処理温度が200℃未満である
と、酸化物の生成、結晶水の分解除去が不充分となり、
硫化水素吸着性能があまり向上しない。一方、加熱処理
温度が350℃を越えると上記複合酸化物の結晶が大き
くなり、複合酸化物の比表面積が逆に低下し、硫化水素
吸着表面の低下をもたらす。
If the heat treatment temperature is less than 200 ° C., the formation of oxides and the decomposition and removal of water of crystallization become insufficient,
Hydrogen sulfide adsorption performance does not improve so much. On the other hand, when the heat treatment temperature exceeds 350 ° C., the crystal size of the composite oxide becomes large, and the specific surface area of the composite oxide decreases, which causes a decrease in the hydrogen sulfide adsorption surface.

【0015】前記イットリウム塩水溶液に、例えば水酸
化カルシウム、水酸化ナトリウム、水酸化カリウム等の
塩基性物質および硝酸鉄、塩化鉄、硫化鉄等の鉄塩を添
加することにより、イットリウム塩水溶液の水酸基濃度
を高めると共に鉄イオンを共存させることができるの
で、短時間の接触で必要量の水酸化物を生成でき、ある
いは鉄とイットリウム複合酸化物の量を増加させること
ができる。前記塩基性物質の添加量はイットリウム塩水
溶液を中和する程度までとすることが好ましい。また鉄
塩の添加量は、前記塩基性物質の添加に伴ってイットリ
ウム塩水溶液中への鉄の溶出抑制を補足する程度とする
ものである。
By adding a basic substance such as calcium hydroxide, sodium hydroxide or potassium hydroxide and an iron salt such as iron nitrate, iron chloride or iron sulfide to the aqueous solution of yttrium salt, the hydroxyl group of the aqueous solution of yttrium salt is added. Since it is possible to increase the concentration and allow iron ions to coexist, it is possible to generate a necessary amount of hydroxide in a short time of contact, or to increase the amounts of iron and yttrium composite oxide. The addition amount of the basic substance is preferably such that the yttrium salt aqueous solution is neutralized. The amount of the iron salt added is such that the elution suppression of iron in the yttrium salt aqueous solution is complemented with the addition of the basic substance.

【0016】[0016]

【実施例】目の粗さが20PPI のウレタンフォームに1
0μアンダーの微細銑鉄粉末を塗着して非酸化性雰囲気
中で1150℃、2時間焼成して鉄多孔体を製造した。
1個のサイズは約90mm×80mm×10mmで重量は約4
5gであった。
[Example] 1 for urethane foam with a coarseness of 20 PPI
A fine iron powder having a thickness of 0 μ was applied and baked at 1150 ° C. for 2 hours in a non-oxidizing atmosphere to produce a porous iron body.
One size is about 90mm x 80mm x 10mm and the weight is about 4
It was 5 g.

【0017】その鉄多孔体を硝酸イットリウム、塩化イ
ットリウムを主成分とし、硝酸鉄、塩化鉄等の鉄塩、水
酸化カルシウム等の塩基性物質、塩化セシウム等の触媒
性能活性化剤等を添加した水溶液に1分間浸漬して取り
出し、乾燥機に入れて120℃で2時間乾燥した。一部
の試料は更に250℃〜350℃で2時間加熱処理し更
に経時変化の影響を避ける為に室温に4週間放置した後
脱硫化水素性能を評価した。具体的な配合比については
代表的な例を表1に示し、それらに対応した水溶液のpH
と脱臭性能評価結果については表2に示す。
The iron porous body was mainly composed of yttrium nitrate and yttrium chloride, and iron salts such as iron nitrate and iron chloride, basic substances such as calcium hydroxide, and catalyst performance activators such as cesium chloride were added. It was immersed in the aqueous solution for 1 minute, taken out, put in a dryer and dried at 120 ° C. for 2 hours. Some of the samples were further heat-treated at 250 ° C. to 350 ° C. for 2 hours and left at room temperature for 4 weeks to avoid the influence of aging, and then the desulfurization performance was evaluated. Typical examples of specific mixing ratios are shown in Table 1, and the pH values of the corresponding aqueous solutions.
Table 2 shows the evaluation results of deodorizing performance.

【0018】脱硫化水素性能は、1m3 の密封容器に4
00L/分の送風能力を持つ循環ファンを設置してなる
図1に示した構造の脱臭試験装置で評価した。即ち、ガ
ス導入口4及びガス排出口5を備えた密封容器1に脱臭
フィルター(空気清浄化剤)3を、ホルダー7にセット
し、その下流域に循環ファン2を設け矢印の方向にガス
を循環させ、該脱臭フィルターをファンの入側に設置し
て硫化水素の除去性能を調べた。
The desulfurization performance is 4 in a 1 m 3 sealed container.
The deodorization test device having the structure shown in FIG. 1 in which a circulation fan having a blowing capacity of 00 L / min was installed was used for evaluation. That is, the deodorizing filter (air cleaning agent) 3 is set in the holder 7 in the sealed container 1 having the gas inlet 4 and the gas outlet 5, and the circulation fan 2 is provided in the downstream region of the deodorizing filter 3 to supply the gas in the direction of the arrow. It was circulated and the deodorizing filter was installed on the inlet side of the fan to examine the hydrogen sulfide removal performance.

【0019】初期値は10ppm に設定して各10分後〜
30分後の残存濃度を測定し除去率を脱臭率として求め
た。30分後の残存濃度が検知管で検知不能、即ち脱臭
率100%の場合にはすぐに同じ試験を繰り返し、30
分後に残存濃度が認められた時点で吸着容量に達したも
のと判定してそれまでの吸着した硫化水素重量を脱臭フ
ィルターの重量で除し、単位重量当りの吸着重量(mg/
g)を求めた。
The initial value is set to 10 ppm and after 10 minutes each
The residual concentration after 30 minutes was measured and the removal rate was determined as the deodorization rate. If the residual concentration after 30 minutes cannot be detected by the detector tube, that is, the deodorization rate is 100%, repeat the same test immediately.
After a minute, when the residual concentration was observed, it was judged that the adsorption capacity had been reached, and the weight of the adsorbed hydrogen sulfide up to that point was divided by the weight of the deodorizing filter, and the adsorption weight per unit weight (mg / mg /
g) was determined.

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【表2】 [Table 2]

【0022】[0022]

【比較例】比較のため、市販活性炭(3種類を用意し、
下記表3の中ではそれぞれ市販品A,BおよびCとし
た)についても、不織布で製造した100mm×80mm×
10mmの箱に40gの活性炭をならして入れて脱臭フィ
ルターを作り、脱臭性能を求め、該脱臭性能評価結果に
ついて表3に示した。
[Comparative Example] For comparison, commercially available activated carbon (3 types were prepared,
In Table 3 below, commercial products A, B, and C) are also made of non-woven fabric, and are 100 mm x 80 mm x
40 g of activated carbon was leveled in a 10 mm box to prepare a deodorizing filter, the deodorizing performance was determined, and the results of the deodorizing performance evaluation are shown in Table 3.

【0023】[0023]

【表3】 [Table 3]

【0024】[0024]

【発明の効果】本発明により、脱硫化水素性能の高い空
気清浄化物である脱臭フィルターが簡便な工程で製造で
きる。
EFFECTS OF THE INVENTION According to the present invention, a deodorizing filter which is an air-purified product having high desulfurization performance can be manufactured in a simple process.

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

【図1】脱臭性能を評価する試験装置の概要説明図。FIG. 1 is a schematic explanatory diagram of a test device for evaluating deodorizing performance.

【符号の説明】 1…密閉容器 2…循環ファン 3…脱臭フィルター 4…ガス導入口 5…ガスサンプル採取口 6…ガス循環の方向[Explanation of Codes] 1 ... Airtight container 2 ... Circulation fan 3 ... Deodorizing filter 4 ... Gas inlet 5 ... Gas sample collection port 6 ... Direction of gas circulation

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 鉄の成形体を担持体とし、該担持体の表
面に鉄とイットリウムの複合酸化物を形成したことを特
徴とする空気清浄化物。
1. An air-purified product, characterized in that an iron molding is used as a carrier, and a complex oxide of iron and yttrium is formed on the surface of the carrier.
【請求項2】 鉄の成形体をイットリウム塩水溶液と接
触させて大気中で反応させ、その反応生成物が未反応の
金属鉄と共存している状態で200℃〜350℃に加熱
処理することを特徴とする空気清浄化物の製造方法。
2. A method of contacting an iron molding with an aqueous solution of yttrium salt to cause a reaction in the atmosphere, and heat-treating the reaction product at 200 ° C. to 350 ° C. in the state where the reaction product coexists with unreacted metallic iron. And a method for producing an air-purified product.
【請求項3】 前記イットリウム塩水溶液に塩基性物質
及び鉄塩を添加することを特徴とする請求項2記載の空
気清浄化物の製造方法。
3. The method for producing an air-purified product according to claim 2, wherein a basic substance and an iron salt are added to the yttrium salt aqueous solution.
JP4203608A 1992-07-30 1992-07-30 Air cleaning material and its production Withdrawn JPH0647274A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4203608A JPH0647274A (en) 1992-07-30 1992-07-30 Air cleaning material and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4203608A JPH0647274A (en) 1992-07-30 1992-07-30 Air cleaning material and its production

Publications (1)

Publication Number Publication Date
JPH0647274A true JPH0647274A (en) 1994-02-22

Family

ID=16476862

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4203608A Withdrawn JPH0647274A (en) 1992-07-30 1992-07-30 Air cleaning material and its production

Country Status (1)

Country Link
JP (1) JPH0647274A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011235244A (en) * 2010-05-11 2011-11-24 Masanobu Nakamura Hydrogen sulfide gas removing agent, method of detecting hydrogen sulfide gas using the same, and hydrogen sulfide gas removing apparatus
JP2012051967A (en) * 2010-08-31 2012-03-15 Jfe Mineral Co Ltd Cleaning material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011235244A (en) * 2010-05-11 2011-11-24 Masanobu Nakamura Hydrogen sulfide gas removing agent, method of detecting hydrogen sulfide gas using the same, and hydrogen sulfide gas removing apparatus
JP2012051967A (en) * 2010-08-31 2012-03-15 Jfe Mineral Co Ltd Cleaning material

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Effective date: 19991005