JPH0596158A - Method for producing composition having air cleaning power - Google Patents

Method for producing composition having air cleaning power

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Publication number
JPH0596158A
JPH0596158A JP3160754A JP16075491A JPH0596158A JP H0596158 A JPH0596158 A JP H0596158A JP 3160754 A JP3160754 A JP 3160754A JP 16075491 A JP16075491 A JP 16075491A JP H0596158 A JPH0596158 A JP H0596158A
Authority
JP
Japan
Prior art keywords
iron
aqueous solution
composition
gas
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Withdrawn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
JP3160754A
Other languages
Japanese (ja)
Inventor
Tamio Noda
多美夫 野田
Yozo Takemura
洋三 竹村
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 JP3160754A priority Critical patent/JPH0596158A/en
Publication of JPH0596158A publication Critical patent/JPH0596158A/en
Withdrawn legal-status Critical Current

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  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Gas Separation By Absorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

(57)【要約】 【目的】 本発明は、NH3 やH2 S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材の
製造方法を提供する。 【構成】 鉄または鉄と酸化鉄または鉄と酸化鉄と鉄化
合物と、タンニン酸または没食子酸またはそれらの混合
物を水溶液状態で反応させてpH5以上にした後、その
水溶液に硫化水素ガスを吹き込んで反応させる。鉄分が
0.05〜2mol/lと、没食子酸換算で算出するタ
ンニン酸または没食子酸の量を0.05〜2mol/l
の割合で水と混合させ、水の温度を80℃以上に上げて
反応させ、室温付近まで冷却した後でその水溶液に添加
する硫化水素ガスの吹き込み量が鉄分に対する硫黄分の
量としてモル比で0.005〜0.1とする。
(57) [Summary] [Object] The present invention provides a method for producing an air purification material for purifying contaminated air containing malodorous gases represented by NH 3 and H 2 S. [Composition] Iron or iron and iron oxide or iron and iron oxide and iron compound are reacted with tannic acid or gallic acid or a mixture thereof in an aqueous solution state to adjust the pH to 5 or more, and then hydrogen sulfide gas is blown into the aqueous solution. React. Iron content is 0.05 to 2 mol / l, and the amount of tannic acid or gallic acid calculated in terms of gallic acid is 0.05 to 2 mol / l.
Of water, the temperature of water is raised to 80 ° C. or higher to react, and after cooling to near room temperature, the amount of hydrogen sulfide gas blown into the aqueous solution is a molar ratio as the amount of sulfur to iron. It is set to 0.005 to 0.1.

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、NH3 やH2 S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
清浄化材に関する。本発明の空気清浄化材は、例えば家
庭用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 material for purifying polluted air containing offensive odor gases such as NH 3 and H 2 S. The air cleaning material of the present invention can be used, for example, as a household deodorant.

【0002】[0002]

【従来の技術】空気中の悪臭ガスに対しては、活性炭を
用いる吸着法や、他の香料を用いるマスキング法や、臭
気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。
2. Description of the Related Art A malodorous gas in the air is removed by an adsorption method using activated carbon, a masking method using another fragrance, or a chemical method for chemically reacting an odor, or reducing unpleasant sensation. ing.

【0003】しかし、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り、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。
However, the adsorption method using activated carbon has a problem that the deodorizing performance deteriorates in a short period of time, and the masking method using other fragrances may give a new discomfort to the fragrance. I won't.

【0004】化学反応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。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。
As a chemical method of chemically reacting, for example, there is a method of oxidizing and decomposing a malodorous gas with ozone, but excessive ozone is harmful to the human body and causes new harm. In other words, it is difficult to control the amount of chemical substances that react with the malodorous gas, so unnecessary chemical substances are generated, and it is difficult to make a fundamental solution.

【0005】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(1
986)、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。
As a technique for solving these problems, the Journal of the Textile Society of Japan (Fiber and Industry), Vol. 42, No. 12 (1
986), P18-26, it is stated that a complex compound obtained by reacting a ferrous compound and ascorbic acid in an aqueous solution has a deodorizing power for nitrogen compound-based odorous gas.

【0006】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
という問題点がある。また本発明者等の知見によればこ
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。
However, the inventors of the present invention have found that this complex compound has a problem that it has a weak deodorizing power for sulfur compound type odorous gas. According to the findings of the present inventors, there is also a problem that the deodorizing power of this complex compound deteriorates in a relatively short period of time.

【0007】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発明し、先に特
願平1―280776号で特許出願した。この組成物は
安価に製造できるし、空気清浄力の劣化が極めて小さ
く、従来技術の問題点を解決するものであった。
The inventors of the present invention have invented 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. A patent application was filed under No. 1-2780776. This composition can be manufactured at low cost, and the deterioration of the air cleaning power is extremely small, which solves the problems of the prior art.

【0008】本発明者等の研究によれば、NH3 や(C
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、C
3 SH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。
According to the research conducted by the present inventors, NH 3 and (C
The deodorizing performance of basic gas such as H 3 ) 3 N is very well adsorbed on a metal complex which is a reaction product of a polybasic acid and a metal.
The adsorption power of H 3 SH gas is weak. One solution is
This is a method of disposing a solid base as described in Japanese Patent Application No. 63-273195 by the present inventors.

【0009】しかし、その後の研究で、H2 S等の酸性
ガスの吸着力の強い物質は、金属が水溶液に溶解して生
成する金属水酸化物及び金属酸化物であることを突き止
めた。更に、水酸化物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、金属と水酸化物、金属酸
化物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。
However, in the subsequent research, it was found that the substances having a strong adsorptive power for acidic gas such as H 2 S are metal hydroxides and metal oxides produced by dissolving metal in an aqueous solution. Furthermore, they have also found that it is necessary to form a state in which a metal and a hydroxide or a metal oxide coexist in order to effectively generate a hydroxide and continue the effect stably for a long period of time.

【0010】脱H2 S性能が良くなると脱CH3 SH性
能も良くなるのは―SH基のHがH2 Sと同様な性質を
持つ為と考えられる。従って金属水酸化物を効果的に生
成せしめることが有効であることが推察できる。しか
し、脱H2 S性能が良いことが脱CH3 SH性能も良い
ことの充分条件ではないことが、本発明者等の研究で判
明した。
The reason why the de-CH 3 SH performance improves as the de-H 2 S performance improves is considered to be that H of the --SH group has the same properties as H 2 S. Therefore, it can be inferred that it is effective to effectively generate the metal hydroxide. However, studies by the present inventors have revealed that good de-H 2 S performance is not a sufficient condition for good de-CH 3 SH performance.

【0011】例えば、鉄とL―アスコルビン酸水溶液を
空気中で接触させ、生成した錯塩と鉄の共存物を150
℃で24時間加熱処理した反応生成物は極めて脱H2
性能が良いが、脱CH3 SH性能がやや劣る。
For example, iron and L-ascorbic acid aqueous solution are brought into contact with each other in the air, and the complex salt produced and the coexisting substance of iron are mixed in an amount of 150.
The reaction product heat-treated at 24 ° C for 24 hours was extremely free of H 2 S.
Good performance, but slightly inferior CH 3 SH performance.

【0012】脱CH3 SH性能を改善する為に種々の対
策を調査研究した結果、比較的薄い酸の水溶液に接触さ
せて大気中に放置した鉄表面には水酸化鉄、酸化第二
鉄、マグネタイトが生じ、極めて脱H2S性能の優れた
組成物が生じるが、それに硫化水素が吸着すると硫化水
素を吸着させる前の組成物に比較して極めて脱CH3
H性能の優れた組成物に変化することを突き止めた。
As a result of investigating various countermeasures for improving the de-CH 3 SH performance, iron hydroxide, ferric oxide, Magnetite is generated, and a composition having extremely excellent dehydrogenation of H 2 S is generated. However, when hydrogen sulfide is adsorbed on it, it is extremely deCH 3 S depleted as compared with the composition before adsorbing hydrogen sulfide.
It was found that the composition changed to an excellent H performance.

【0013】この硫化水素吸着によって生成する脱CH
3 SH性能の優れた組成物について詳細に調べた結果、
硫化鉄が主な効果を発揮していることを突き止めた。
De-CH generated by this hydrogen sulfide adsorption
3 As a result of detailed investigation of the composition having excellent SH performance,
We have found that iron sulfide has a major effect.

【0014】さらに、事前に硫黄含有量の高い金属を使
用して酸の水溶液と空気中で反応させることにより、同
様の成果が得られることをも見出し、先に本発明者等が
特願平3―16815号等で記述した方法で解決でき
た。
Further, it was also found that similar results can be obtained by reacting a metal having a high sulfur content in advance with an aqueous solution of an acid in the air. It could be solved by the method described in 3-16815.

【0015】[0015]

【発明が解決しようとする課題】本発明者等の特願平3
―16815号の組成物を更に広範囲に研究して、更に
簡単な工程でかつ安全な新たな方法で空気清浄力を有す
る材料を提供することを課題としている。特に、製造工
程でH2Sが発生して作業者がガス中毒を起こす心配の
無い製造工程を提供することが望まれている。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
It is an object of the present invention to further extensively study the composition of No. -16815 to provide a material having an air cleaning power in a new process that is simpler and safer. In particular, it is desired to provide a manufacturing process in which H 2 S is not generated in the manufacturing process and an operator is not concerned with gas poisoning.

【0016】[0016]

【課題を解決するための手段】本発明は、(1)鉄また
は鉄と酸化鉄または鉄と酸化鉄と鉄化合物と、タンニン
酸または没食子酸またはそれらの混合物を水溶液状態で
反応させてpH5以上にした後、その水溶液に硫化水素
ガスを吹き込んで反応させることを特徴とする空気清浄
力を有する組成物の製造方法である。
According to the present invention, (1) iron or iron and iron oxide or iron and iron oxide and an iron compound are reacted with tannic acid or gallic acid or a mixture thereof in an aqueous solution state to have a pH of 5 or more. After that, the method for producing a composition having an air cleaning power is characterized in that hydrogen sulfide gas is blown into the aqueous solution to react.

【0017】また、(2)(1)の鉄分が0.05〜2
mol/lと、没食子酸換算で算出するタンニン酸また
は没食子酸の量を0.05〜2mol/lの割合で水と
混合させ、水の温度を80℃以上に上げて反応させ、室
温付近まで冷却した後でその水溶液に添加する硫化水素
ガスの吹き込み量が鉄分に対する硫黄分の量としてモル
比で0.005〜0.1であることを特徴とする空気清
浄力を有する組成物の製造方法である。
The iron content of (2) (1) is 0.05 to 2
mol / l and the amount of tannic acid or gallic acid calculated in terms of gallic acid are mixed with water at a ratio of 0.05 to 2 mol / l, the temperature of water is raised to 80 ° C. or higher to react, and the temperature is kept around room temperature. A method for producing a composition having an air cleaning power, characterized in that the amount of hydrogen sulfide gas blown into the aqueous solution after cooling is 0.005 to 0.1 in terms of the amount of sulfur to iron Is.

【0018】また、(3)(1)のH2 Sガスが10p
pm以下に空気で希釈されているか、または濃縮H2
ガスが大気圧を保って自由に体積を変えられる容器に封
入され、容器の出口が鉄または鉄と酸化鉄または鉄と酸
化鉄と鉄化合物とタンニン酸または没食子酸またはそれ
らの混合物を水溶液状態で反応させてpH5以上にした
水溶液中に接続する構造で反応させることを特徴とする
空気清浄力を有する組成物の製造方法である。
Further, (3) (1) H 2 S gas is 10 p
Air diluted below pm or concentrated H 2 S
The gas is enclosed in a container whose volume can be freely changed while maintaining the atmospheric pressure, and the outlet of the container is iron or iron and iron oxide or iron and iron oxide and iron compounds and tannic acid or gallic acid or a mixture thereof in an aqueous state. It is a method for producing a composition having an air cleaning power, which comprises reacting in a structure of being connected to an aqueous solution having a pH of 5 or more.

【0019】また、(4)(1)の組成物がFe、N
i、Cr、Mn、Co、Cu、Znから選ばれる1また
は2以上の金属またはその硫化物と共存する組成物であ
ることを特徴とする空気清浄力を有する組成物の製造方
法である。
Further, the composition of (4) (1) contains Fe, N
A method for producing a composition having an air cleaning power, which is a composition coexisting with one or more metals selected from i, Cr, Mn, Co, Cu and Zn or a sulfide thereof.

【0020】[0020]

【作用】H2 Sガスが健康障害を起こさない濃度は10
ppm以下と言われている。従ってH2 Sガスを予め空
気で10ppm以下に希釈して使用すれば、万一H2
ガスが流出しても安全である。
[Function] The concentration of H 2 S gas that causes no health hazard is 10
It is said to be below ppm. Therefore, if used by diluting 10ppm or less in advance air H 2 S gas, event H 2 S
It is safe even if gas flows out.

【0021】しかし低濃度のガスを使用すれば安全では
あるがそれだけ使用するガスの体積が増えて効率が良く
ない。H2 Sガス100%のガスやそれに近い高濃度の
2 Sガスを使用する場合には、酸化鉄に吸収されない
余分なガスが洩れ出さない工夫が必要となる。
However, although it is safe to use a low concentration gas, the volume of the gas used increases by that much, and the efficiency is not good. When a 100% H 2 S gas or a high concentration H 2 S gas close to the H 2 S gas is used, it is necessary to devise an extra gas that is not absorbed by iron oxide to leak out.

【0022】それを具体的に説明すれば、図1に示した
構造の機能を持つ装置を用い、反応を進めれば良い。即
ち、鉄または鉄と酸化鉄または鉄と酸化鉄と鉄化合物
と、タンニン酸または没食子酸またはそれらの混合物を
水溶液状態で反応させてpH5以上にした水溶液を用意
する。
More specifically, the reaction may be advanced using an apparatus having the function of the structure shown in FIG. That is, iron or iron and iron oxide or iron and iron oxide and iron compound are reacted with tannic acid or gallic acid or a mixture thereof in an aqueous solution state to prepare an aqueous solution having a pH of 5 or more.

【0023】H2 Sガスは弁4及び出入管5のついたテ
ドラーパック3のような内容ガスの体積に応じて大気圧
を保ちながら形状が変化する容器3に入れる。H2 Sガ
スの量は多過ぎると万一流出した場合の危険性が高まる
し、少な過ぎるとFeSの生成量が少なくて脱臭性能が
劣化するので、水溶液中の鉄分に対するS量がモル比で
0.05程度に調整するのが好ましい。
The H 2 S gas is placed in a container 3 such as a Tedlar pack 3 equipped with a valve 4 and an inlet / outlet pipe 5, the shape of which changes while maintaining the atmospheric pressure according to the volume of the content gas. If the amount of H 2 S gas is too large, the risk in case of outflow increases, and if it is too small, the amount of FeS produced is small and the deodorizing performance deteriorates. It is preferably adjusted to about 0.05.

【0024】水溶液1中にテドラーパック3の出入管5
を浸漬し、水溶液を攪拌しながら弁4を開くとH2 Sガ
スは水溶液中の酸化鉄と反応して徐々に消費される。目
的の量が吸収されたら弁4を閉じて作業を終了する。
An inlet / outlet pipe 5 for the Tedlar pack 3 in the aqueous solution 1.
When the valve 4 is opened while immersing the H 2 S and stirring the aqueous solution, the H 2 S gas reacts with the iron oxide in the aqueous solution and is gradually consumed. When the target amount is absorbed, the valve 4 is closed and the work is finished.

【0025】それらの目的を達成する鉄分、タンニン酸
または没食子酸の配合量は、それぞれ0.05〜2mo
l/lとする。この配合量が少ないと効果が小さく、配
合量が多すぎると溶液の粘性が高くなり過ぎて製造作業
が困難になり実用的でない。
The amount of iron, tannic acid or gallic acid to achieve these purposes is 0.05 to 2 mo, respectively.
1 / l. If the blending amount is too small, the effect is small, and if the blending amount is too large, the viscosity of the solution becomes too high and the manufacturing work becomes difficult, which is not practical.

【0026】適切な作業効率、性能を同時に達成する具
体的な方法は、ほぼ等モルの鉄と有機酸水溶液を熱湯状
態に加熱して反応させ、しかる後に硫化水素を吸着させ
る方法である。
A specific method for simultaneously achieving appropriate work efficiency and performance is a method in which substantially equimolar iron and an aqueous solution of an organic acid are heated in a hot water state for reaction, and then hydrogen sulfide is adsorbed.

【0027】鉄と有機酸水溶液を熱湯状態に加熱して反
応させることにより鉄と有機酸の錯体を生成するだけで
なくH2 Sガスと極めて反応が速い酸化鉄を生じる。H
2 Sガスは酸化鉄と反応して硫化鉄と水を生じる為、H
2 Sガスが大気中に逃げ出すことは無い。テドラーパッ
ク内に残っている未反応の過剰のH2 Sガスは出口が水
溶液で封鎖されているので大気中に逃げ出すことはなく
ない。
By heating iron and an aqueous solution of an organic acid in a hot water state to react with each other, not only a complex of iron and an organic acid is produced, but also iron oxide which reacts extremely rapidly with H 2 S gas is produced. H
2 S gas reacts with iron oxide to produce iron sulfide and water.
2 S gas does not escape into the atmosphere. The unreacted excess H 2 S gas remaining in the Tedlar pack does not escape to the atmosphere because the outlet is sealed with the aqueous solution.

【0028】鉄と有機酸水溶液を混合して室温付近で長
期間保持する方法でもある程度の酸化鉄やマグネタイト
は生成する為、熱湯状態で反応させた場合の数分の1程
度の効果は得られるが生成する酸化鉄の量が少なく万全
ではないので、できるだけ水溶液の温度を上げて反応さ
せることが好ましい。
Even when iron and an aqueous solution of an organic acid are mixed and kept at room temperature for a long period of time, iron oxide and magnetite are produced to some extent, and therefore, an effect which is about a fraction of that in the case of reacting in hot water can be obtained. Since the amount of iron oxide produced in (1) is small and not perfect, it is preferable to raise the temperature of the aqueous solution as much as possible to react.

【0029】また、このようにして製造した空気清浄力
を持つ物質はFe、Ni、Cr、Mn、Co、Cu、Z
n等の金属と共存することにより、時間経過とともに新
たな酸化金属を形成する効果により脱臭性能を発揮する
寿命期間が長くなる効果がある。
The substances having the air cleaning power produced in this manner are Fe, Ni, Cr, Mn, Co, Cu and Z.
By coexisting with a metal such as n, there is an effect that a life period for exhibiting deodorizing performance is extended due to an effect of forming a new metal oxide with the passage of time.

【0030】次に本発明の実施例について述べる。Next, examples of the present invention will be described.

【0031】[0031]

【実施例】【Example】

【0032】[0032]

【実施例1】カルボニル鉄粉1.2mol/lとタンニ
ン酸を没食子酸換算で同じく1.2mol/l添加した
水溶液を100℃に加熱して10分間攪拌しながら反応
させて室温まで冷却した。その水溶液1lに濃度90%
のH2 Sガスを100cc吸収させて脱臭材溶液を製造
した。
Example 1 An aqueous solution containing 1.2 mol / l of carbonyl iron powder and 1.2 mol / l of tannic acid in terms of gallic acid was heated to 100 ° C., reacted with stirring for 10 minutes, and cooled to room temperature. 90% concentration in 1 liter of the aqueous solution
The deodorizing agent solution was produced by absorbing 100 cc of H 2 S gas.

【0033】その水溶液中に目の粗さが20PPIのウ
レタンフォームを浸漬して反応生成物を塗着して室温で
24時間乾燥し、脱臭フィルターを製造した。脱臭フィ
ルターのサイズは約80mm×100mm×12mmで
重量は約15gであった。
A urethane foam having a coarseness of 20 PPI was dipped in the aqueous solution to apply the reaction product and dried at room temperature for 24 hours to produce a deodorizing filter. The deodorizing filter had a size of about 80 mm × 100 mm × 12 mm and a weight of about 15 g.

【0034】その脱臭性能を図2に示した構造の試験装
置を使って評価した。試験装置の内容積は40l、循環
ファンの風量は約400l/分であった。
The deodorizing performance was evaluated using a test apparatus having the structure shown in FIG. The internal volume of the test apparatus was 40 l, and the air volume of the circulation fan was about 400 l / min.

【0035】まず、最初に脱CH3 SH性能を評価し、
引続き脱NH3 性能、脱H2 S性能を評価した。その評
価結果を表1に示した。
First, the de-CH 3 SH performance is evaluated first,
Subsequently, the NH 3 removal performance and the H 2 S removal performance were evaluated. The evaluation results are shown in Table 1.

【0036】[0036]

【実施例2】目の粗さが20PPIのウレタンフォーム
に10μアンダーの微細銑鉄粉末を塗着し、非酸化雰囲
気で1150℃×2時間焼成して製造した鉄多孔体を実
施例1と同様にして製造した鉄粉、タンニン酸、H2
ガスの反応水溶液に浸漬し、室温で2時間放置して乾燥
し脱臭フィルターを製造した。できあがった脱臭フィル
ターのサイズは約80mm×90mm×10mmで重量
は約40gであった。
Example 2 A porous iron body produced by applying fine 10 μ-under powder of pig iron to urethane foam having a coarseness of 20 PPI and firing in a non-oxidizing atmosphere at 1150 ° C. for 2 hours was the same as in Example 1. Produced iron powder, tannic acid, H 2 S
A deodorizing filter was manufactured by immersing in a reaction aqueous solution of gas and leaving it for 2 hours at room temperature to dry. The resulting deodorizing filter had a size of about 80 mm × 90 mm × 10 mm and a weight of about 40 g.

【0037】その脱臭性能を図2に示した構造の試験装
置を使って評価した。試験装置の内容積は40l、循環
ファンの風量は約400l/分であった。まず、最初に
脱CH3 SH性能を評価し、引続き脱NH3 性能、脱H
2 S性能を評価した。その評価結果を表2に示した。
The deodorizing performance was evaluated using a test apparatus having the structure shown in FIG. The internal volume of the test apparatus was 40 l, and the air volume of the circulation fan was about 400 l / min. First, the de-CH 3 SH performance is evaluated first, followed by the de-NH 3 performance and de-H treatment.
2 S performance was evaluated. The evaluation results are shown in Table 2.

【0038】[0038]

【実施例3】実施例2と同様にして10%の硫黄と20
%のMnを含有する合金鉄多孔体を製造した。その合金
鉄多孔体を使用して実施例1と同様にして製造した鉄
粉、タンニン酸、H2 Sガスの反応水溶液に浸漬し、室
温で2週間放置して乾燥し脱臭フィルターを製造した。
できあがった脱臭フィルターのサイズは約85mm×9
5mm×10mmで重量は約50gであった。
Example 3 Similar to Example 2, 10% sulfur and 20%
A ferroalloy porous body containing 10% Mn was produced. Using the alloyed iron porous body, it was immersed in a reaction aqueous solution of iron powder, tannic acid, and H 2 S gas produced in the same manner as in Example 1, and allowed to stand at room temperature for 2 weeks for drying to produce a deodorizing filter.
The size of the finished deodorizing filter is about 85 mm x 9
It was 5 mm × 10 mm and weighed about 50 g.

【0039】その脱臭性能を図1に示した構造の試験装
置を使って評価した。試験装置の内容積は40l、循環
ファンの風量は約400l/分であった。まず、最初に
脱CH3 SH性能を評価し、引続き脱NH3 性能、脱H
2 S性能を評価した。その評価結果を表3に示した。
The deodorizing performance was evaluated using a test apparatus having the structure shown in FIG. The internal volume of the test apparatus was 40 l, and the air volume of the circulation fan was about 400 l / min. First, the de-CH 3 SH performance is evaluated first, followed by the de-NH 3 performance and de-H treatment.
2 S performance was evaluated. The evaluation results are shown in Table 3.

【0040】[0040]

【表1】 [Table 1]

【0041】[0041]

【表2】 [Table 2]

【0042】[0042]

【表3】 [Table 3]

【0043】[0043]

【発明の効果】本発明により、脱NH3 性能、脱H2
性能、脱酸(CH3)3 N性能が良くて、更に脱CH3
H性能も極めて優れた空気清浄化物が安全に効率良く製
造できる。
INDUSTRIAL APPLICABILITY According to the present invention, NH 3 removal performance and H 2 S removal
Performance, deoxidized (CH 3 ) 3 N performance is good, and further de-CH 3 S
An air-purified product with excellent H performance can be manufactured safely and efficiently.

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

【図1】本発明に係わる水溶液にH2 Sガスを吸着、反
応させる装置の構造を示す説明図である。
FIG. 1 is an explanatory view showing the structure of an apparatus for adsorbing and reacting H 2 S gas with an aqueous solution according to the present invention.

【図2】脱臭性能を評価する試験装置の構造を示す説明
図である。
FIG. 2 is an explanatory view showing the structure of a test device for evaluating deodorizing performance.

【符号の説明】 1 水溶液 2 攪拌機 3 テドラーパック(容器) 4 弁 5 出入管 6 密閉容器 7 循環ファン 8 脱臭フィルター 9 ガス導入口 10 ガスサンプル採取口 11 ガス循環の方向[Explanation of symbols] 1 aqueous solution 2 stirrer 3 Tedlar pack (container) 4 valve 5 inlet / outlet pipe 6 closed container 7 circulation fan 8 deodorizing filter 9 gas inlet port 10 gas sample collection port 11 gas circulation direction

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B01D 53/34 131 6953−4D C09K 3/00 S 9049−4H ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Office reference number FI technical display location B01D 53/34 131 6953-4D C09K 3/00 S 9049-4H

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 鉄または鉄と酸化鉄または鉄と酸化鉄と
鉄化合物と、タンニン酸または没食子酸またはそれらの
混合物を水溶液状態で反応させてpH5以上にした後、
その水溶液に硫化水素ガスを吹き込んで反応させること
を特徴とする空気清浄力を有する組成物の製造方法。
1. After reacting iron or iron and iron oxide or iron and iron oxide and iron compound with tannic acid or gallic acid or a mixture thereof in an aqueous solution to adjust the pH to 5 or more,
A method for producing a composition having an air cleaning power, which comprises reacting by blowing hydrogen sulfide gas into the aqueous solution.
【請求項2】 請求項1の鉄分が0.05〜2mol/
lと、没食子酸換算で算出するタンニン酸または没食子
酸の量を0.05〜2mol/lの割合で水と混合さ
せ、水の温度を80℃以上に上げて反応させ、室温付近
まで冷却した後でその水溶液に添加する硫化水素ガスの
吹き込み量が鉄分に対する硫黄分の量としてモル比で
0.005〜0.1であることを特徴とする空気清浄力
を有する組成物の製造方法。
2. The iron content of claim 1 is 0.05 to 2 mol /
1, and the amount of tannic acid or gallic acid calculated in terms of gallic acid were mixed with water at a ratio of 0.05 to 2 mol / l, the temperature of water was raised to 80 ° C. or higher to react, and cooled to around room temperature. A method for producing a composition having an air cleaning power, characterized in that the amount of hydrogen sulfide gas to be added later to the aqueous solution is 0.005 to 0.1 in terms of a molar ratio as a sulfur content to an iron content.
【請求項3】 請求項1のH2 Sガスが10ppm以下
に空気で希釈されているか、または濃縮H2 Sガスが大
気圧を保って自由に体積を変えられる容器に封入され、
容器の出口が鉄または鉄と酸化鉄または鉄と酸化鉄と鉄
化合物とタンニン酸または没食子酸またはそれらの混合
物を水溶液状態で反応させてpH5以上にした水溶液中
に接続する構造で反応させることを特徴とする空気清浄
力を有する組成物の製造方法。
3. The H 2 S gas of claim 1 is diluted with air to 10 ppm or less, or the concentrated H 2 S gas is enclosed in a container whose volume can be freely changed while maintaining atmospheric pressure,
When the outlet of the container is made to react with iron or iron and iron oxide or iron and iron oxide and iron compound and tannic acid or gallic acid or a mixture thereof in an aqueous solution state and connected to an aqueous solution whose pH is 5 or more, the reaction is performed. A method for producing a composition having a characteristic air cleaning power.
【請求項4】 請求項1の組成物がFe、Ni、Cr、
Mn、Co、Cu、Znから選ばれる1または2以上の
金属またはその硫化物と共存する組成物であることを特
徴とする空気清浄力を有する組成物の製造方法。
4. The composition of claim 1 comprising Fe, Ni, Cr,
A method for producing a composition having air cleaning power, which is a composition coexisting with one or more metals selected from Mn, Co, Cu and Zn or a sulfide thereof.
JP3160754A 1991-06-06 1991-06-06 Method for producing composition having air cleaning power Withdrawn JPH0596158A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3160754A JPH0596158A (en) 1991-06-06 1991-06-06 Method for producing composition having air cleaning power

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3160754A JPH0596158A (en) 1991-06-06 1991-06-06 Method for producing composition having air cleaning power

Publications (1)

Publication Number Publication Date
JPH0596158A true JPH0596158A (en) 1993-04-20

Family

ID=15721744

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3160754A Withdrawn JPH0596158A (en) 1991-06-06 1991-06-06 Method for producing composition having air cleaning power

Country Status (1)

Country Link
JP (1) JPH0596158A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0523380A (en) * 1991-07-25 1993-02-02 Matsushita Electric Works Ltd Deodorant and preparation thereof
JP2016539799A (en) * 2013-12-12 2016-12-22 北京博源恒升高科技有限公司Beijing Boyuan−Hengsheng High−Technology Co., Ltd. Method for removing SOx in gas with ethylene glycol complex solution

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0523380A (en) * 1991-07-25 1993-02-02 Matsushita Electric Works Ltd Deodorant and preparation thereof
JP2016539799A (en) * 2013-12-12 2016-12-22 北京博源恒升高科技有限公司Beijing Boyuan−Hengsheng High−Technology Co., Ltd. Method for removing SOx in gas with ethylene glycol complex solution
US9815017B2 (en) 2013-12-12 2017-11-14 Beijing Boyuan Hengsheng High-Technology Co., Ltd. Method for removing SOx from gas using ethylene glycol composite solution

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Effective date: 19980903