JPH08112513A - Method for deodorizing waste gas generated in coating work and deodorizing device - Google Patents

Method for deodorizing waste gas generated in coating work and deodorizing device

Info

Publication number
JPH08112513A
JPH08112513A JP6275796A JP27579694A JPH08112513A JP H08112513 A JPH08112513 A JP H08112513A JP 6275796 A JP6275796 A JP 6275796A JP 27579694 A JP27579694 A JP 27579694A JP H08112513 A JPH08112513 A JP H08112513A
Authority
JP
Japan
Prior art keywords
exhaust gas
coating
waste gas
deodorizing
porous mineral
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
JP6275796A
Other languages
Japanese (ja)
Inventor
Tamio Noda
多美夫 野田
Tatsuo Mukai
達夫 向井
Katsumi Hirano
克己 平野
Takahiro Yamato
崇弘 山戸
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 PAINT PLANT ENG KK
Nippon Steel Corp
Original Assignee
NIPPON PAINT PLANT ENG KK
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 PAINT PLANT ENG KK, Nippon Steel Corp filed Critical NIPPON PAINT PLANT ENG KK
Priority to JP6275796A priority Critical patent/JPH08112513A/en
Publication of JPH08112513A publication Critical patent/JPH08112513A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Details Or Accessories Of Spraying Plant Or Apparatus (AREA)

Abstract

PURPOSE: To effectively deodorize waste gas by removing dust from waste gas generated in a coating process before bringing it into contact with a porous mineral adsorbent carrying hydrazine salts and passing it through an active carbon filter. CONSTITUTION: The temperature of waste gas is adjusted to <=100 deg.C. At first, after dust is removed by a dust collecting filter 41, the waste gas is passed through a bed 42 packed with porous mineral foil carrying hydrazine salts. Then almost all the malodorous materials of aldehydes and a part of the other malodorous materials are adsorbed and removed. Furthermore, when it is passed through a bed 43 packed with granular active carbon, the remaining malodorous materials are adsorbed and removed. After that, it is dissipated in the air as clean air 23 by a suction fan 33. Malodor is removed from waste gas generated in a coating work is inexpensively and surely removed.

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、自動車等の塗装工程で
発生した排気ガスを消臭する方法及び消臭装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and a deodorizing apparatus for deodorizing exhaust gas generated in a painting process for automobiles and the like.

【0002】[0002]

【従来の技術】自動車塗装工程における塗装ブース、セ
ッティングブース及び(焼付)乾燥部塗装工程において
は、塗膜形成のために揮発された溶剤や、塗料に混合さ
れた樹脂から種々の悪臭が発生する。例えば、アクリル
樹脂を含む塗料を用いて塗装を行った場合等は、トルエ
ン、キシレン等の通常用いられる溶剤が塗装排気ガスと
して排出される。また、アクリル酸エステル等の原料の
モノマーやその分解生成物が当該塗料から揮発してく
る。従って、アクリル樹脂を含む塗料を使用した塗装ブ
ースから発生する排気ガスは、アクリル酸エステルに起
因する催涙性をも有している。
2. Description of the Related Art In a coating booth, a setting booth, and a (baking) drying section coating process in an automobile coating process, various odors are generated from a solvent volatilized for forming a coating film and a resin mixed with the coating film. . For example, when coating is performed using a coating material containing an acrylic resin, a commonly used solvent such as toluene or xylene is discharged as coating exhaust gas. Further, raw material monomers such as acrylic acid ester and decomposition products thereof are volatilized from the coating material. Therefore, the exhaust gas generated from the coating booth using the coating material containing acrylic resin also has a tearing property due to the acrylic ester.

【0003】更に、メラミン樹脂を含む塗料を用いて塗
装を行った場合等は、縮重合剤として用いられているホ
ルムアルデヒドが当該塗料から揮発してくる。従って、
メラミン樹脂を含む塗料を使用した塗装工程から発生す
る排気ガスは、ホルムアルデヒドに起因する刺激臭を有
していることになる。
Further, when coating is performed using a paint containing a melamine resin, formaldehyde used as a polycondensation agent is volatilized from the paint. Therefore,
Exhaust gas generated from a coating process using a paint containing a melamine resin has an irritating odor caused by formaldehyde.

【0004】上記ホルムアルデヒド自体は悪臭防止法の
規制物質には含まれていないが発癌性の疑いがあるた
め、労働環境基準は産業衛生学会基準で0.5ppm以
下と定められている。また、目に対する刺激も顕著であ
ることから、塗装排気ガスからこのものを確実に除去す
る方法が求められている。塗装排気ガスで通常含有され
ているトルエン、キシレンの労働環境基準、産業衛生学
会基準では100ppm以下と定められており、この数
値をみれば、ホルムアルデヒド除去は、上記溶媒の除去
よりも極めて低い数値が求められていることが判る。
Although the formaldehyde itself is not included in the regulated substances of the Odor Control Law, it is suspected to be carcinogenic, so the working environment standard is defined as 0.5 ppm or less according to the Japan Society for Occupational Health standards. Further, since the irritation to the eyes is remarkable, there is a demand for a method for surely removing this from the coating exhaust gas. It is stipulated that the standard of working environment of toluene and xylene, which are usually contained in paint exhaust gas, and the standard of Japan Society for Occupational Health is 100 ppm or less. From this figure, formaldehyde removal is much lower than removal of the above solvent. I know what is required.

【0005】アクリル酸、メタクリル酸の誘導体を主成
分とする重合樹脂であるアクリル樹脂については、アク
リルモノマーの種類、組み合わせにより極めて多種のも
のが存在する。これらは、本来は自然乾燥で使われるが
メラミン樹脂などで補強することによって焼付塗装にも
使われ、そのときに分解生成するアルデヒド類が独特の
焦げ臭を持ち悪臭主成分となるものと推定されている。
モノマーの主成分はむしろ刺激臭を持つものが多い。
As for the acrylic resin, which is a polymer resin containing a derivative of acrylic acid or methacrylic acid as a main component, there are a great variety of acrylic resins depending on the type and combination of acrylic monomers. These are originally used for natural drying, but they are also used for baking coating by reinforcing them with melamine resin, and it is estimated that the aldehydes decomposed and generated at that time have a unique burning odor and become the main component of the malodor. ing.
Most of the main components of the monomer have rather a pungent odor.

【0006】環境庁等の調査では焼付工程で反応生成す
るアルデヒド類の中にはイソバレルアルデヒド、ノルマ
ルバレルアルデヒド、ノルマルブチルアルデヒド等の高
分子アルデヒド類が含まれ、それらの閾値は極めて低
く、極低濃度でも臭いを感じることから、特に注意を要
することが指摘されている。例えば、イソバレルアルデ
ヒドは0.003ppmの低濃度でも臭いを感じること
ができるので、極めて精巧な消臭が必要となる。
According to a survey conducted by the Environment Agency and the like, high molecular weight aldehydes such as isovaleraldehyde, normal valeraldehyde, and normal butyraldehyde are included in the aldehydes formed by the reaction in the baking process, and their threshold values are extremely low. It has been pointed out that special attention is required because it smells even at low concentrations. For example, since isovaleraldehyde can smell even at a low concentration of 0.003 ppm, delicate deodorization is required.

【0007】ところで、塗装工程において生じた排気ガ
スの消臭処理を行うために、従来は、排気ガスを高温燃
焼炉に導いて酸化分解させる直接燃焼法、比較的低い温
度で酸化分解させる触媒燃焼法、活性炭に吸着して除去
する吸着法等を用いて消臭処理を行っていた。
By the way, in order to deodorize exhaust gas generated in the painting process, a conventional direct combustion method in which the exhaust gas is introduced into a high temperature combustion furnace for oxidative decomposition, and catalytic combustion for oxidative decomposition at a relatively low temperature have been used. Deodorizing treatment was carried out by using a method, an adsorption method of adsorbing on activated carbon and removing it.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、上記直
接燃焼法は、燃料費が高く、エネルギー消費量も大きい
ことが問題であった。上記触媒燃焼法は、触媒が被毒し
た場合に触媒の交換費用が高く、取り替えに時間が掛か
ることが問題であった。また活性炭による吸着法は、比
較的高分子のガスの吸着容量は優れているが、ホルムア
ルデヒド、アセトアルデヒド等の吸着容量が小さく、頻
繁に活性炭を交換する必要が生じ、費用の増大に繋がる
問題があった。本発明は、上記した状況に鑑み、塗装工
程で生じた排気ガスを低コストで効果的に消臭する方法
及び消臭装置を提供することを目的とするものである。
However, the above direct combustion method has a problem that the fuel cost is high and the energy consumption is large. The above-mentioned catalytic combustion method has a problem that the replacement cost of the catalyst is high when the catalyst is poisoned and it takes a long time to replace the catalyst. In addition, the adsorption method using activated carbon has a relatively high adsorption capacity for high-molecular gas, but it has a small adsorption capacity for formaldehyde, acetaldehyde, etc., and requires frequent replacement of the activated carbon, leading to an increase in cost. It was In view of the above situation, it is an object of the present invention to provide a method and a deodorizing device for effectively deodorizing exhaust gas generated in a coating process at low cost.

【0009】[0009]

【課題を解決するための手段】本発明者らは、上記目的
を達成するため、鋭意検討した結果、塗装工程で生じた
排気ガスを除塵した後にヒドラジン塩類を担持した多孔
質鉱物吸着材に接触させ、その後に活性炭フィルタを通
過させることにより活性炭の交換頻度を大幅に低減させ
ることを見いだし、本発明に到達した。
Means for Solving the Problems The inventors of the present invention have conducted extensive studies to achieve the above object. As a result, the exhaust gas generated in the coating process was removed, and then contacted with a porous mineral adsorbent carrying hydrazine salts. The present invention has been found to significantly reduce the frequency of exchanging activated carbon by allowing the activated carbon to pass through an activated carbon filter after that.

【0010】即ち、本発明は、塗装工程で生じた排気ガ
スを収集する収集工程と、前記収集工程で収集した排気
ガスをフィルタに通過させることにより排気ガス中から
微粒子を除去するフィルタリング工程と、前記フィルタ
リング工程で微粒子が除去された排気ガスをヒドラジン
塩類を担持した多孔質鉱物吸着材に接触させてホルムア
ルデヒド、アセトアルデヒド等のアルデヒド類を除去す
る悪臭物質除去工程とを含む塗装排気ガスの消臭方法及
び消臭装置である。以下、本発明を詳述する。
That is, the present invention includes a collecting step for collecting exhaust gas generated in the coating step, and a filtering step for removing fine particles from the exhaust gas by passing the exhaust gas collected in the collecting step through a filter, A method for deodorizing a coating exhaust gas, which comprises a step of removing odorous substances such as formaldehyde and acetaldehyde by contacting the exhaust gas from which fine particles have been removed in the filtering step with a porous mineral adsorbent supporting hydrazine salts. And a deodorizing device. Hereinafter, the present invention will be described in detail.

【0011】本発明においては、まず、塗装工程で生じ
た排気ガスは、吸引手段によって吸引される(収集工
程)。上記吸引手段で吸引された排気ガスは除塵フィル
タを通過し、ここで排気ガス中から微粒子が除去される
ことになる(フィルタリング工程)。
In the present invention, first, the exhaust gas generated in the painting step is sucked by the suction means (collecting step). The exhaust gas sucked by the suction means passes through the dust filter, and the particulates are removed from the exhaust gas here (filtering step).

【0012】上記除塵フィルタによって微粒子が除去さ
れた排気ガスに、ヒドラジン塩類を担持した多孔質鉱物
吸着材に接触させて、ホルムアルデヒド、アセトアルデ
ヒド、その他のアルキルアルデヒド等のアルデヒド類等
の悪臭物質が除去されることとなる(悪臭物質除去工
程)。
The exhaust gas from which the fine particles have been removed by the dust filter is brought into contact with a porous mineral adsorbent carrying hydrazine salts to remove odorous substances such as aldehydes such as formaldehyde, acetaldehyde and other alkyl aldehydes. It will be (odorous substance removal process).

【0013】上記悪臭物質除去工程における多孔質鉱物
吸着材には、冷気を導入することにより、通過する排気
ガスの温度を100℃以下することが好ましい。これに
より上記多孔質鉱物吸着材の働きが増加する。
It is preferable that the temperature of the exhaust gas passing through the porous mineral adsorbent in the step of removing the malodorous substance is 100 ° C. or less by introducing cold air. This increases the function of the porous mineral adsorbent.

【0014】塗装排気ガスのなかでも、トルエン、キシ
レン等の有機溶剤成分の一部は、本発明の上記塗装排気
ガスの消臭方法により消臭を施した後、必要に応じて、
更に活性炭で吸着除去することにより悪臭物質の殆どを
除去することができる。また塗装排気ガスのなかでも、
ホルムアルデヒド、アセトアルデヒド等のアルデヒド類
の悪臭物質については、活性炭の吸着容量を阻害する
が、本発明の塗装排気ガスの消臭方法により、ヒドラジ
ン塩類を担持した多孔質鉱物吸着材によって事前に除去
されているため、本発明の塗装排気ガスの消臭方法の後
に活性炭による処理を行うにしても、当該活性炭の寿命
を大幅に延ばすことができる。
Among the coating exhaust gases, some of the organic solvent components such as toluene and xylene are deodorized by the above-mentioned coating exhaust gas deodorizing method of the present invention, and then, if necessary,
Furthermore, most of the malodorous substances can be removed by adsorption removal with activated carbon. Also, among the paint exhaust gases,
For odorous substances such as formaldehyde and acetaldehyde, which inhibit the adsorption capacity of activated carbon, they are removed in advance by a hydrazine salt-supporting porous mineral adsorbent by the deodorizing method of the coating exhaust gas of the present invention. Therefore, even if the treatment with activated carbon is performed after the method for deodorizing the coating exhaust gas of the present invention, the life of the activated carbon can be significantly extended.

【0015】上記ヒドラジン塩類を担持した多孔質鉱物
吸着材によって、アルデヒド類の吸着除去ができるメカ
ニズムについては、詳細な解明はできていない。しかし
ながら、基本的には多孔質鉱物の層状結晶の隙間にヒド
ラジン塩類が析出し、それによってヒドラジンが化学的
に安定な状態に保たれ、そこに塗装排気ガス中のアルデ
ヒド類が接触するとアルダジンを作って化学吸着を引き
起こすものと推定される。
The mechanism by which the aldehydes can be adsorbed and removed by the porous mineral adsorbent supporting the hydrazine salts has not been elucidated in detail. However, basically, hydrazine salts are deposited in the interstices of layered crystals of porous minerals, which keeps hydrazine chemically stable, and when aldehydes in the coating exhaust gas come into contact with it, aldazine is formed. It is presumed that it causes chemisorption.

【0016】本発明の消臭方法及び本発明の消臭装置を
図により説明する(図1)。消臭装置11は、排気ガス
吸入口31と、冷気吸入量調整弁32と、吸引ファン3
3とを有し、吸入口31から塗装排気ガス21を吸入
し、その排気ガス温度が100℃を超える場合には冷気
吸引調整弁32を開いて冷気22を混入することにより
排気ガス温度が100℃以下になるように調整する。
The deodorizing method of the present invention and the deodorizing device of the present invention will be described with reference to the drawings (FIG. 1). The deodorizing device 11 includes an exhaust gas intake port 31, a cool air intake amount adjusting valve 32, and a suction fan 3.
3 and sucks the coating exhaust gas 21 from the suction port 31, and when the exhaust gas temperature exceeds 100 ° C., the cool air suction adjusting valve 32 is opened to mix the cool air 22 to bring the exhaust gas temperature to 100. Adjust so that it is below ℃.

【0017】100℃以下に調整された排気ガスは集塵
フィルタ41で除塵され、ヒドラジン塩を担持した多孔
質鉱物箔を充填した層42を通過し、アルデヒド類の悪
臭物質のほとんど及びその他の悪臭物質の一部を吸着除
去した後、更に残りの悪臭物質を吸着除去するため、粒
状活性炭を充填した層43を通過させる。その後、吸引
ファン33によって脱臭装置から清浄空気23として大
気中へ放散される。
Exhaust gas adjusted to a temperature of 100 ° C. or lower is dust-removed by a dust collecting filter 41, passes through a layer 42 filled with a porous mineral foil carrying a hydrazine salt, and most of odorous substances such as aldehydes and other malodorous substances are discharged. After part of the substance is adsorbed and removed, in order to adsorb and remove the remaining malodorous substance, the layer 43 filled with the granular activated carbon is passed through. Then, the suction fan 33 disperses the deodorizing device as clean air 23 into the atmosphere.

【0018】粒状活性炭43は、トルエン、キシレン等
のヒドラジン塩を担持した多孔質鉱物の吸着性能が相対
的に弱い悪臭物質を吸着する材料であれば特に限定され
るものではなく、シリカゲル、ゼオライト等でも良い。
シリカの組成を高めた疎水性合成ゼオライト等を使用し
ても差し支えない。
The granular activated carbon 43 is not particularly limited as long as it is a material capable of adsorbing a malodorous substance having a relatively weak adsorption performance for a porous mineral supporting a hydrazine salt such as toluene or xylene, and silica gel, zeolite or the like. But good.
Hydrophobic synthetic zeolite having an increased silica composition may be used.

【0019】[0019]

【実施例】以下に本発明の実施例を掲げて更に詳しく説
明するが、本発明はこれら実施例に限定されるものでは
ない。
The present invention will be described in more detail below with reference to examples of the present invention, but the present invention is not limited to these examples.

【0020】実施例1 メラミン樹脂の場合 実際に稼働中のメラミン樹脂を使った塗装工場の排気ガ
スの一部を無処理で直接試験装置に吸引して脱臭性能を
評価した。初期性能は全く問題が無く、1ヵ月継続して
試験を行った。実際に稼働した8時間/日×24日間の
テストの最終日の測定結果を表1に示した。
Example 1 In the case of melamine resin A part of the exhaust gas of a coating factory that actually used the melamine resin was sucked directly into the test device without any treatment to evaluate the deodorizing performance. There was no problem with the initial performance, and the test was continued for one month. Table 1 shows the measurement results of the final day of the test of 8 hours / day × 24 days when the test was actually performed.

【0021】評価装置は図1に示した基本構造の装置を
使った。装置の断面積は0.7m2、ヒドラジン塩担持
多孔質鉱物箔の充填量は30kg、粒状活性炭の充填量
は15kgとした。脱臭装置内のガス流速は、0.2m
/秒でフラッディング等の支障はなく、充填層の不均一
化等の問題は生じていない。活性炭及び集塵フィルタは
市販品を用いた。上記ヒドラジン塩担持多孔質鉱物箔
は、ゼオライト微粉末を硫酸アルミニウムとヒドラジン
の混合水溶液で混練し、厚さ0.5mmの箔に圧延して
成型した。それを電子レンジで乾燥し、破砕して20m
m角と3mm角の網で篩分けし整粒することにより製造
したものを用いた。
As the evaluation device, the device having the basic structure shown in FIG. 1 was used. The cross-sectional area of the apparatus was 0.7 m 2 , the filling amount of the hydrazine salt-supporting porous mineral foil was 30 kg, and the filling amount of the granular activated carbon was 15 kg. Gas flow rate in the deodorizer is 0.2m
/ Sec, there is no problem such as flooding, and there is no problem such as uneven filling layer. As the activated carbon and the dust collecting filter, commercially available products were used. The hydrazine salt-supporting porous mineral foil was formed by kneading zeolite fine powder with a mixed aqueous solution of aluminum sulfate and hydrazine and rolling into a foil having a thickness of 0.5 mm. Dry it in the microwave and crush it to 20m.
The product produced by sieving with a m-square and 3 mm-square mesh and sizing was used.

【0022】評価はホルムアルデヒド、アセトアルデヒ
ド、トルエン、キシレンの4成分について検知管を用い
て測定し、また官能評価を6人のパネルによって行っ
た。官能評価は臭気強度2.5以下を○、3.5以上を
×、中間を△として評価した。少なくとも8時間/日×
24日間のテストでは消臭後の排ガスに臭気や目に対す
る刺激は認められず、長期耐用性のあることが確認でき
た。
The evaluation was carried out by measuring the four components of formaldehyde, acetaldehyde, toluene and xylene using a detector tube, and the sensory evaluation was conducted by a panel of 6 people. In the sensory evaluation, the odor intensity of 2.5 or less was evaluated as ◯, 3.5 or more as x, and the middle was evaluated as Δ. At least 8 hours / day ×
In a 24-day test, no odor or eye irritation was observed in the exhaust gas after deodorization, and it was confirmed that the exhaust gas had long-term durability.

【0023】実施例2 アクリル樹脂の場合 実際に稼働中のアクリル樹脂を使った塗装工場の排気ガ
スの一部を無処理で直接試験装置に吸引して脱臭性能を
評価した。初期性能は全く問題がなく、1ヶ月間継続し
て試験を行った。実際に稼働した8時間/日×24日間
のテストの最終日の測定結果を表2に示した。
Example 2 Acrylic Resin A part of the exhaust gas of a coating factory using an acrylic resin that was actually in operation was directly sucked into the test device without treatment to evaluate the deodorizing performance. There was no problem with the initial performance, and the test was continued for one month. Table 2 shows the measurement results of the final day of the test of 8 hours / day × 24 days when the test was actually performed.

【0024】評価装置は図1に示した基本構造の装置を
使ったがメラミン樹脂の工場実験で使用したものより一
回り小型の装置を用意し、活性炭前のガス温度を下げる
目的で活性炭充填層の前に水冷パイプを通して冷却を行
った。装置の断面積は0.04m2 、ヒドラジン塩担持
多孔質鉱物箔の充填量は2kg、粒状活性炭の充填量は
1kgとした。脱臭装置内のガス流速は0.2m/秒で
フラッディング等の支障は無く、充填層の不均一化等の
問題は生じていない。活性炭及び集塵フィルタは市販品
を用いた。上記ヒドラジン塩担持多孔質鉱物箔は、ゼオ
ライト微粉末を硫酸アルミニウムとヒドラジンの混合水
溶液で混練し、厚さ0.5mmの箔に圧延して成型し
た。それを電子レンジで乾燥し、破砕して20mm角と
3mm角の網で篩分けし整粒することにより製造したも
のを用いた。評価は実施例1と同様にして行った。少な
くとも8時間/日×24日間のテストでは消臭後の排ガ
スに臭気や目に対する刺激は認められず、長期耐用性の
あることが確認できた。
As the evaluation apparatus, the apparatus having the basic structure shown in FIG. 1 was used, but an apparatus smaller than the one used in the factory experiment of melamine resin was prepared, and an activated carbon packed bed was prepared for the purpose of lowering the gas temperature before activated carbon. Cooling was performed through a water cooling pipe before. The cross-sectional area of the device was 0.04 m 2 , the filling amount of the hydrazine salt-supporting porous mineral foil was 2 kg, and the filling amount of the granular activated carbon was 1 kg. The gas flow rate in the deodorizing device was 0.2 m / sec, there were no problems such as flooding, and there were no problems such as nonuniformity of the packed bed. As the activated carbon and the dust collecting filter, commercially available products were used. The hydrazine salt-supporting porous mineral foil was formed by kneading zeolite fine powder with a mixed aqueous solution of aluminum sulfate and hydrazine and rolling into a foil having a thickness of 0.5 mm. It was dried in a microwave oven, crushed, sieved through a 20 mm square and a 3 mm square mesh, and sized to prepare a product. The evaluation was performed in the same manner as in Example 1. In a test of at least 8 hours / day × 24 days, no odor or eye irritation was observed in the exhaust gas after deodorization, and it was confirmed that the exhaust gas after long-term durability was durable.

【0025】実施例3 その他の塗料の場合 その他の評価例としてアルキド樹脂塗料を金属に塗装す
る工場の塗装ブースの排気の脱臭試験を行った例を示し
た。塗装ブースの排気ではミストが多く、集塵フィルタ
ーの目詰まりが大きかった為一週間で評価を打ち切った
がその期間の脱臭効率は全く問題がなかった。塗装ブー
ス排気は温度が低く特に清浄空気を導入して温度を下げ
る必要は生じなかった。初期性能は全く問題が無く、一
週間継続して試験を行った。実際に稼働した8時間/日
×6日間のテストの最終日の測定結果を表3に示した。
Example 3 In the case of other paints As another evaluation example, an example in which a deodorization test of exhaust gas from a coating booth of a factory for coating metal with an alkyd resin paint was conducted was shown. There was a lot of mist in the exhaust air of the painting booth, and the clogging of the dust collection filter was large, so the evaluation was terminated in one week, but there was no problem with the deodorizing efficiency during that period. The exhaust air from the coating booth was low, and it was not necessary to introduce clean air to lower the temperature. There was no problem with the initial performance, and the test was continued for one week. Table 3 shows the measurement results of the final day of the test of 8 hours / day × 6 days that were actually operated.

【0026】評価装置は図1に示した基本構造の装置を
使い、アクリル樹脂の工場実験で使用したものと同じ小
型の装置で評価した。アクリル樹脂の工場実験で使用し
た活性炭充填層の前に設置した水冷パイプは排気ガス温
度が低いので使用しなかった。装置の断面積は0.04
2 、ヒドラジン塩担持多孔質鉱物箔の充填量は2k
g、粒状活性炭の充填量は1kgとした。脱臭装置内の
ガス流速は0.2m/秒でフラッディング等の支障は無
く、充填層の不均一化等の問題は生じていない。活性炭
及び集塵フィルタは市販品を用いた。上記ヒドラジン塩
担持多孔質鉱物箔は、ゼオライト微粉末を硫酸アルミニ
ウムとヒドラジンの混合水溶液で混練し、厚さ0.5m
mの箔に圧延して成型した。それを電子レンジで乾燥
し、破砕して20mm角と3mm角の網で篩分けし整粒
することにより製造したものを用いた。評価は実施例1
と同様にして行った。少なくとも8時間/日×6日間の
テストでは消臭後の排ガスに臭気や目に対する刺激は認
められず、脱臭効果のあることが確認できた。
As the evaluation apparatus, the apparatus having the basic structure shown in FIG. 1 was used, and the same small apparatus used in the acrylic resin factory experiment was used for evaluation. The water-cooled pipe installed before the activated carbon packed bed used in the acrylic resin factory experiment was not used because the exhaust gas temperature was low. The cross-sectional area of the device is 0.04
m 2 , filling amount of hydrazine salt-supporting porous mineral foil is 2 k
g, and the filling amount of granular activated carbon was 1 kg. The gas flow rate in the deodorizing device was 0.2 m / sec, there were no problems such as flooding, and there were no problems such as nonuniformity of the packed bed. As the activated carbon and the dust collecting filter, commercially available products were used. The hydrazine salt-supporting porous mineral foil has a thickness of 0.5 m obtained by kneading zeolite fine powder with a mixed aqueous solution of aluminum sulfate and hydrazine.
m foil was rolled and molded. It was dried in a microwave oven, crushed, sieved through a 20 mm square and a 3 mm square mesh, and sized to prepare a product. Evaluation is Example 1
I went in the same way. In a test of at least 8 hours / day × 6 days, no odor or eye irritation was observed in the exhaust gas after deodorization, and it was confirmed that it had a deodorizing effect.

【0027】[0027]

【表1】 [Table 1]

【0028】[0028]

【表2】 [Table 2]

【0029】[0029]

【表3】 [Table 3]

【0030】[0030]

【発明の効果】本発明によれば、塗装排気ガスの悪臭除
去が安価で確実、かつ、装置の維持管理が容易に可能と
なる。また、アルデヒド類で特に問題の多い、印刷工
場、木工工場、食品加工工場等の排気ガスの消臭も同様
に可能である。
According to the present invention, the bad odor of the coating exhaust gas can be removed inexpensively and reliably, and the maintenance of the apparatus can be easily performed. Further, it is also possible to deodorize exhaust gas in a printing plant, a woodworking plant, a food processing plant or the like, which is particularly problematic with aldehydes.

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

【図1】本発明の塗装排気ガスの消臭装置の概略図。FIG. 1 is a schematic view of a coating exhaust gas deodorizing apparatus of the present invention.

【符号の説明】[Explanation of symbols]

11 塗装排気ガスの消臭装置 21 塗装排気ガス 22 冷気 23 消臭処理後の排気ガス 31 吸入口 32 冷気吸入量調整弁 33 吸引ファン 41 集塵フィルタ 42 ヒドラジン塩担持多孔質鉱物箔 43 粒状活性炭 11 Paint Exhaust Gas Deodorizer 21 Paint Exhaust Gas 22 Cold Air 23 Exhaust Gas after Deodorization 31 Intake Port 32 Cool Air Intake Volume Control Valve 33 Suction Fan 41 Dust Collection Filter 42 Hydrazine Salt-Supporting Porous Mineral Foil 43 Granular Activated Carbon

───────────────────────────────────────────────────── 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 B01D 53/81 // B05B 15/12 7310−4F B01D 53/34 117 A (72)発明者 向井 達夫 東京都千代田区大手町二丁目6番3号 新 日本製鐵株式会社内 (72)発明者 平野 克己 大阪市淀川区西中島5丁目5番15号 日本 ペイントプラント・エンジニアリング株式 会社内 (72)発明者 山戸 崇弘 大阪市淀川区西中島5丁目5番15号 日本 ペイントプラント・エンジニアリング株式 会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B01D 53/81 // B05B 15/12 7310-4F B01D 53/34 117 A (72) Inventor Mukai Tatsuo 2-6-3 Otemachi, Chiyoda-ku, Tokyo Inside Nippon Steel Corporation (72) Inventor Katsumi Hirano 5-5-15 Nishinakajima, Yonagawa-ku, Osaka City Japan Paint Plant Engineering Co., Ltd. (72) Inventor Takahiro Yamato 5-5-15 Nishinakajima, Yodogawa-ku, Osaka Japan Paint Plant Engineering Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 塗装工程で生じた排気ガスを収集する収
集工程と、前記収集工程で収集された排気ガスをフィル
タに通過させることにより排気ガス中から微粒子を除去
するフィルタリング工程と、前記フィルタリング工程で
微粒子が除去された排気ガスをヒドラジン塩類を担持し
た多孔質鉱物吸着材に接触させて悪臭物質を除去する工
程とを含むことを特徴とする塗装排気ガスの消臭方法。
1. A collecting step of collecting exhaust gas generated in a coating step, a filtering step of removing fine particles from the exhaust gas by passing the exhaust gas collected in the collecting step through a filter, and the filtering step. And a step of contacting the exhaust gas from which the fine particles are removed with a porous mineral adsorbent carrying a hydrazine salt to remove a malodorous substance, and a deodorizing method for a coating exhaust gas.
【請求項2】 塗装工程で生じた排気ガスを吸引する吸
引手段と、前記吸引手段によって吸引された排気ガス中
から微粒子を除去する集塵フィルタと、ヒドラジン塩類
が担持された多孔質鉱物吸着材とを含むことを特徴とす
る塗装排気ガスの消臭装置。
2. A suction means for sucking the exhaust gas generated in the coating step, a dust collecting filter for removing fine particles from the exhaust gas sucked by the suction means, and a porous mineral adsorbent carrying hydrazine salts. A paint exhaust gas deodorizing device characterized by including and.
【請求項3】 ヒドラジン塩類が担持された多孔質鉱物
吸着材が、これを通過する排気ガスの温度が100℃以
下になるように冷気を導入する機能を有するものである
請求項2記載の塗装排気ガスの消臭装置。
3. The coating according to claim 2, wherein the porous mineral adsorbent supporting hydrazine salts has a function of introducing cold air so that the temperature of the exhaust gas passing therethrough becomes 100 ° C. or lower. Exhaust gas deodorizer.
JP6275796A 1994-10-14 1994-10-14 Method for deodorizing waste gas generated in coating work and deodorizing device Pending JPH08112513A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6275796A JPH08112513A (en) 1994-10-14 1994-10-14 Method for deodorizing waste gas generated in coating work and deodorizing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6275796A JPH08112513A (en) 1994-10-14 1994-10-14 Method for deodorizing waste gas generated in coating work and deodorizing device

Publications (1)

Publication Number Publication Date
JPH08112513A true JPH08112513A (en) 1996-05-07

Family

ID=17560541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6275796A Pending JPH08112513A (en) 1994-10-14 1994-10-14 Method for deodorizing waste gas generated in coating work and deodorizing device

Country Status (1)

Country Link
JP (1) JPH08112513A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005007272A1 (en) * 2002-07-19 2005-01-27 Tateo Uegaki Device and method for eliminating odor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005007272A1 (en) * 2002-07-19 2005-01-27 Tateo Uegaki Device and method for eliminating odor

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