JP2001300251A - Device for cleaning foul gas and cleaning method - Google Patents

Device for cleaning foul gas and cleaning method

Info

Publication number
JP2001300251A
JP2001300251A JP2000116594A JP2000116594A JP2001300251A JP 2001300251 A JP2001300251 A JP 2001300251A JP 2000116594 A JP2000116594 A JP 2000116594A JP 2000116594 A JP2000116594 A JP 2000116594A JP 2001300251 A JP2001300251 A JP 2001300251A
Authority
JP
Japan
Prior art keywords
gas
packed bed
nitrogen oxide
nitrogen
adsorbing
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Withdrawn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
JP2000116594A
Other languages
Japanese (ja)
Inventor
Tatsuo Nakatani
龍男 中谷
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP2000116594A priority Critical patent/JP2001300251A/en
Priority to IDP20010330D priority patent/ID29840A/en
Publication of JP2001300251A publication Critical patent/JP2001300251A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

PROBLEM TO BE SOLVED: To provide a device for cleaning a foul gas which securely maintains a high removing performance of a pollutant such as an exhaust gas by making treatment conditions suitable for the purpose and reducing the degree or contamination in soil or underground water by efficiently converting a nitrogen component to a nitrogen gas as well as a cleaning method using the device. SOLUTION: This cleaning device has a layer filled with an adsorbent which adsorbs and removes the injurious substance of the foul gas as a device for cleaning the foul gas. The device comprises a filled layer for blowing the foul gas thereinto through a blowing means, a filled layer for adsorbing/removing hydrocarbons which adsorbs/removes hydrocarbon pollutans contained in the foul gas, including soil, and the like, and a filled layer for adsorbing a nitrogen oxide which adsorbs the nitrogen oxide contained in the foul gas formed sequentially on the filled layer for the foul gas to be blown into, a water spray means which sprays water to the surface of the filled layer for adsorbing the nitrogen oxide and a filled layer for removing the nitrogen oxide which is formed at the lower part of the filled layer for the foul gas to be blown into and decomposes/removes the nitrogen oxide absorbed into water, including the soil, and the like.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は汚染ガスの浄化装置
および浄化方法に関し、さらに詳しくは窒素酸化物や炭
化水素等を含有する自動車排ガスや燃焼排ガスなどによ
って汚染された空気を浄化するのに好適な汚染ガスの浄
化装置および浄化方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for purifying polluted gas, and more particularly to a method for purifying air polluted by automobile exhaust gas or combustion exhaust gas containing nitrogen oxides and hydrocarbons. The present invention relates to an apparatus and a method for purifying a contaminated gas.

【0002】[0002]

【従来の技術】自動車排ガス中に含まれる窒素酸化物、
炭化水素、浮遊粉塵等は、大気汚染の元凶物質としてそ
の対策が要望されている。従来より、アンモニアや硫黄
酸化物などの悪臭物質を除去する方法としては、土壌や
コンポスト中に生息する微生物を活用する方法が多用さ
れているが、近年、この微生物を活用した悪臭物質除去
方法を自動車排ガスに適用する試みがなされている。例
えば、特開平10−128043号公報には、一定割合
の細礫分と活性炭を含む土壌粒子に、自動車排ガス中の
有害成分を吸着させ、該土壌中の微生物により分解除去
する自動車排ガスの浄化方法が提案されている。しか
し、窒素酸化物、炭化水素、浮遊粉塵等の自動車排ガス
中の有害物質の中には、生物的に分解されるものが存在
する一方で、分解されないものも存在する。また、土壌
が生物分解性を有していたとしても分解にかかわる微生
物の特性は様々である。例えば、窒素酸化物は、脱窒菌
により酸素のない嫌気的状態で、さらに有機物のような
水素供与体が存在する環境下で還元されて窒素ガスとし
て大気中に放散される。また炭化水素は、酸素存在下で
微生物により水と二酸化炭素に分解されて除去される。
従って、微生物が生息する環境によっては有害物質の除
去等の目的が達成できない場合があった。
2. Description of the Related Art Nitrogen oxides contained in automobile exhaust gas,
Hydrocarbons, suspended dust and the like are required as countermeasures for air pollution. Conventionally, as a method for removing malodorous substances such as ammonia and sulfur oxides, a method utilizing microorganisms living in soil or compost has been frequently used.In recent years, a method for removing malodorous substances utilizing this microorganism has been used. Attempts have been made to apply it to automotive exhaust. For example, Japanese Unexamined Patent Publication No. Hei 10-128043 discloses a method of purifying automobile exhaust gas in which harmful components in automobile exhaust gas are adsorbed to soil particles containing a certain percentage of fine gravel and activated carbon and decomposed and removed by microorganisms in the soil. Has been proposed. However, some harmful substances in automobile exhaust gas, such as nitrogen oxides, hydrocarbons, and suspended dust, are biodegradable, while others are not. Furthermore, even if the soil has biodegradability, the characteristics of microorganisms involved in the degradation are various. For example, nitrogen oxides are reduced by denitrifying bacteria in an anaerobic state without oxygen and further in an environment in which a hydrogen donor such as an organic substance is present, and are released into the atmosphere as nitrogen gas. Hydrocarbons are removed by being decomposed into water and carbon dioxide by microorganisms in the presence of oxygen.
Therefore, depending on the environment where the microorganisms live, the purpose of removing harmful substances may not be achieved.

【0003】[0003]

【発明が解決しようとする課題】本発明の課題は、上記
従来技術の問題点を解決し、自動車排ガスや燃焼排ガス
等の各種の汚染物質に対して処理条件を適性化すること
によって高い除去性能を確保するとともに、硝酸、亜硝
酸の形で存在する窒素成分を高い割合で窒素ガスに変換
して土壌や地下水の汚染を低減させることができる汚染
ガスの浄化装置および浄化方法を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art and to achieve high removal performance by optimizing treatment conditions for various pollutants such as automobile exhaust gas and combustion exhaust gas. To provide a pollutant gas purifying apparatus and a purifying method capable of converting nitrogen components present in the form of nitric acid and nitrous acid into nitrogen gas at a high rate and reducing soil and groundwater pollution. is there.

【0004】[0004]

【課題を解決するための手段】本発明者らは、上記課題
に鑑み、鋭意検討した結果、自動車排ガスや燃焼排ガス
中に含まれる有害物質のそれぞれの特性を考慮し、個々
の有害物質に適した処理条件を組合わせて自動車排ガス
や燃焼排ガスを処理することにより、上記課題を達成で
きることを見出し、本発明に到達したものである。すな
わち、本願で特許請求される発明は以下の通りである。
Means for Solving the Problems In view of the above problems, the present inventors have conducted intensive studies and as a result, considered the characteristics of each of the harmful substances contained in automobile exhaust gas and combustion exhaust gas, and made it suitable for each harmful substance. It has been found that the above problems can be achieved by treating automobile exhaust gas and combustion exhaust gas by combining the above-described treatment conditions, and have reached the present invention. That is, the invention claimed in the present application is as follows.

【0005】(1)汚染ガス中の有害物質を吸着除去す
る吸着剤の充填層を有する汚染ガスの浄化装置であっ
て、吹込み手段を介して汚染ガスが吹き込まれる汚染ガ
ス吹込み用充填層と、該汚染ガス吹込み用充填層上に順
に形成され、かつ土壌および/またはコンポストを含
む、前記汚染ガスに含まれる炭化水素系汚染物質を吸着
除去する炭化水素吸着除去用充填層および該汚染ガスに
含まれる窒素酸化物を吸着する窒素酸化物吸着用充填層
と、該窒素酸化物吸着用充填層の表面に水を散布する散
水手段と、前記汚染ガス吹込み用充填層の下部に形成さ
れ、かつ土壌および/またはコンポストを含む、前記水
に吸収された窒素酸化物を分解除去する窒素酸化物除去
用充填層とを設置したことを特徴とする汚染ガスの浄化
装置。 (2)前記窒素酸化物吸着用充填層および炭化水素吸着
除去用充填層に疎水性粒子を混合したことを特徴とする
(1)に記載の汚染ガスの浄化装置。 (3)前記窒素酸化物除去用充填層に生分解性プラスチ
ックを混合したことを特徴とする(1)または(2)に
記載の汚染ガスの浄化装置。
(1) A pollutant gas purifying apparatus having a packed bed of an adsorbent for adsorbing and removing harmful substances in a polluted gas, wherein the packed bed for injecting the polluted gas through a blowing means. And a hydrocarbon adsorbing and removing packing layer formed in order on the contaminated gas injecting filling layer and adsorbing and removing hydrocarbon contaminants contained in the contaminant gas, including soil and / or compost, and the contaminant. A filling layer for adsorbing nitrogen oxides contained in a gas, a watering means for spraying water on the surface of the filling layer for adsorbing nitrogen oxides, and a lower part of the filling layer for blowing the contaminated gas. And a nitrogen oxide removal packed bed that decomposes and removes nitrogen oxides absorbed in the water, including soil and / or compost. (2) The contaminated gas purifying apparatus according to (1), wherein hydrophobic particles are mixed in the nitrogen oxide adsorption packed bed and the hydrocarbon adsorption removal packed bed. (3) The pollutant gas purifying apparatus according to (1) or (2), wherein a biodegradable plastic is mixed in the nitrogen oxide removing packed bed.

【0006】(4)(1)〜(3)のいずれかに記載の
汚染ガスの浄化装置を用いて汚染ガスを浄化するに際
し、吹込み手段により汚染ガス吹込み用充填層に供給し
た汚染ガスを、炭化水素吸着除去用充填層および窒素酸
化物吸着用充填層に順に通過させ、該炭化水素吸着除去
用充填層により汚染ガス中の炭化水素系汚染物質を吸着
分解し、該窒素酸化物吸着用充填層により汚染ガス中の
窒素酸化物を吸着して清浄なガスを該窒素酸化物吸着用
充填層の上部から系外に放出するとともに、前記窒素酸
化物吸着用充填層の表面に散水手段により水を散布し、
該窒素酸化物吸着用充填層および前記炭化水素吸着除去
用充填層を通過する水に、前記汚染ガスに含まれる窒素
酸化物および各層に吸着された窒素酸化物を吸収させ、
該吸収された窒素酸化物を前記汚染ガス吹込み用充填層
の下部に設けられた窒素酸化物除去用充填層で還元除去
した後、排水として系外に排出することを特徴とする汚
染ガスの浄化方法。
(4) When purifying the contaminated gas using the contaminated gas purifying apparatus according to any one of (1) to (3), the contaminated gas supplied to the contaminated gas injection packed bed by the blowing means. Are sequentially passed through a hydrocarbon adsorbing and removing packed bed and a nitrogen oxide adsorbing packed bed, and the hydrocarbon adsorbing and removing packed bed adsorbs and decomposes hydrocarbon-based pollutants in the polluted gas to form the nitrogen oxide adsorbent. The nitrogen oxides in the polluted gas are adsorbed by the packing layer for adsorbing, and a clean gas is released from the upper part of the packing layer for adsorbing nitrogen oxides to the outside of the system. Spray water with
Water passing through the nitrogen oxide adsorption packed bed and the hydrocarbon adsorption removal packed bed absorbs the nitrogen oxides contained in the contaminated gas and the nitrogen oxides adsorbed on each layer,
After reducing the absorbed nitrogen oxides by a nitrogen oxide removal packed bed provided below the polluted gas injection packed bed, the nitrogen oxides are discharged out of the system as wastewater. Purification method.

【0007】[0007]

【発明の実施の形態】図1は、本発明の一実施例を示す
汚染空気の浄化装置の説明図である。図1において、こ
の浄化装置は、吹込み装置6を介して汚染空気が吹き込
まれる汚染空気吹込み用充填層1と、該汚染ガス吹込み
用充填層1の上部に順に形成された、汚染空気に含まれ
る炭化水素系汚染物質を吸着除去する炭化水素吸着除去
用充填層2および該汚染空気に含まれる窒素酸化物を吸
着するNOx吸着用充填層(窒素酸化物吸着用充填層)
3と、該NOx吸着用充填層3の表面に水を散布する散
水装置5と、前記汚染空気吹込み用充填層1の下部に形
成された、水に溶解した窒素酸化物を分解除去するNO
x除去用充填層(窒素酸化物除去用充填層)4とを有す
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is an explanatory view of a polluted air purifying apparatus showing one embodiment of the present invention. In FIG. 1, this purifying apparatus includes a contaminated air blowing packed layer 1 into which contaminated air is blown through a blowing device 6, and a contaminated air formed on an upper portion of the contaminated gas blowing packed layer 1. Packing layer 2 for adsorbing and removing hydrocarbon pollutants contained in water and packing bed for NOx adsorbing nitrogen oxides contained in the polluted air (filling layer for adsorbing nitrogen oxides)
3, a water spray device 5 for spraying water on the surface of the NOx adsorption packed bed 3, and a NO for decomposing and removing nitrogen oxides dissolved in water formed below the contaminated air blowing packed bed 1.
x removing filling layer (nitrogen oxide removing filling layer) 4.

【0008】このような構成において、汚染空気は、吹
込み装置6を介して汚染空気吹込み用充填層1の内部に
吹き込まれ、炭化水素吸着除去用充填層2およびNOx
吸着用充填層2を順に上昇して通過し、炭化水素吸着除
去用充填層2の通過時に汚染ガス中の炭化水素系汚染物
質が吸着分解され、さらに窒素酸化物吸着用充填層3の
通過時に汚染ガス中の窒素酸化物が吸着され、該窒素酸
化物吸着用充填層3の上部から清浄な空気が系外に放出
される。汚染空気としては、沿道やトンネル内の窒素酸
化物、炭化水素系化合物、浮遊粉塵などを含む排ガスに
富んだ汚染空気や燃焼排ガスが挙げられる。吹込み装置
5としては、例えば、集気装置やブロワー等が用いられ
る。汚染空気吹込み用充填層1には、砕石等が充填さ
れ、かつその内部に吹き込まれた汚染空気の偏流を防ぐ
ために汚染空気吹込み管(図示せず)が導入されてい
る。なお、汚染空気吹込み用充填層1はこのような構成
に限定されず、その上部に形成された炭化水素吸着除去
用充填層2の全面に均等に汚染空気を吹き込むことがで
きるものであればよい。
In such a configuration, the contaminated air is blown into the contaminated air blowing packed bed 1 through the blowing device 6, and the hydrocarbon adsorbed and removed packed bed 2 and the NOx
The hydrocarbon-based pollutants in the pollutant gas are adsorbed and decomposed when passing through the packed bed 2 for adsorption and removal of hydrocarbons, and pass through the packed bed 2 for adsorption of hydrocarbons. Nitrogen oxides in the contaminated gas are adsorbed, and clean air is released from the upper part of the nitrogen oxide adsorption packed bed 3 to the outside of the system. Examples of the polluted air include polluted air and combustion exhaust gas that are rich in exhaust gas containing nitrogen oxides, hydrocarbon compounds, suspended dust and the like in roadsides and in tunnels. As the blowing device 5, for example, an air collecting device or a blower is used. The contaminated air blowing filling layer 1 is filled with crushed stones and the like, and a contaminated air blowing pipe (not shown) is introduced to prevent the contaminated air blown into the inside thereof from drifting. In addition, the contaminated air blowing filling layer 1 is not limited to such a configuration, as long as the contaminated air can be blown uniformly over the entire surface of the hydrocarbon adsorption and removal filling layer 2 formed thereon. Good.

【0009】炭化水素吸着除去用充填層2には、土壌お
よび/またはコンポストが充填されており、汚染空気中
の炭化水素系汚染物質は、これらの土壌等に捕捉、吸着
され、さらに土壌等に生息する炭化水素分解微生物によ
って酸素の存在下に水と二酸化炭素に分解除去される。
土壌としては、黒ぼく土などの天然土やこれを主体とし
てパーライトなどの土壌改良材として加えた混合土が用
いられる。またコンポストとしては、例えば、下水汚泥
コンポスト等が用いられる。
The soil and / or compost is filled in the packing layer 2 for removing and absorbing hydrocarbons, and the hydrocarbon-based pollutants in the contaminated air are captured and adsorbed on these soils and the like, and are further absorbed by the soils and the like. It is decomposed into water and carbon dioxide in the presence of oxygen by inhabiting hydrocarbon-degrading microorganisms.
As the soil, a natural soil such as Kuroboku soil or a mixed soil mainly containing this as a soil improving material such as perlite is used. As compost, for example, sewage sludge compost or the like is used.

【0010】これらの土壌および/またはコンポストに
は疎水性粒子を5〜50容積%の割合で混合するのが好
ましい。疎水性粒子の混合により、汚染空気中の炭化水
素系汚染物質が疎水性粒子に選択的に吸着されやすくな
り、土壌やコンポスト等の親水性材料に比較して炭化水
素系汚染物質の捕捉性が著しく向上する。また疎水性粒
子の混入によって通気性が改善される。疎水性粒子とし
ては、表面を疎水処理した無機物粒子、フッ素樹脂等の
有機性疎水粒子、炭素粒子等を用いることができる。無
機物粒子には、例えば、シリカ、アルミナ、カオリン、
タルク、酸化鉄、酸化チタン、酸化亜鉛などが使用さ
れ、該無機物粒子の疎水処理方法としては、例えば、金
属アルコキシドおよび疎水基を有する金属アルコキシド
の脱アルコール反応を伴う脱水縮合により無機物粒子表
面に疎水基を導入する方法が挙げられる。
It is preferable to mix hydrophobic particles in the soil and / or compost in a ratio of 5 to 50% by volume. By mixing the hydrophobic particles, the hydrocarbon contaminants in the contaminated air are more likely to be selectively adsorbed to the hydrophobic particles, and the trapping property of the hydrocarbon contaminants is higher than that of hydrophilic materials such as soil and compost. Significantly improved. In addition, air permeability is improved by mixing hydrophobic particles. As the hydrophobic particles, inorganic particles having a surface subjected to hydrophobic treatment, organic hydrophobic particles such as fluororesin, carbon particles, and the like can be used. Inorganic particles include, for example, silica, alumina, kaolin,
Talc, iron oxide, titanium oxide, zinc oxide and the like are used. Examples of the hydrophobic treatment method of the inorganic particles include, for example, a method in which the surface of the inorganic particles becomes hydrophobic by dehydration condensation accompanied by a dealcoholization reaction of metal alkoxide and metal alkoxide having a hydrophobic group. A method for introducing a group may be mentioned.

【0011】NOx吸着用充填層3には上記した土壌お
よび/またはコンポストが充填されており、汚染空気中
のNOx(窒素酸化物)やSOx(硫黄酸化物)が、こ
れらの充填物に吸着されるとともに、後述するようにN
Ox吸着用充填層3の表面に散水された水に吸収、溶解
されて下部層に移行する。上記土壌等には疎水性粒子を
混合することができる。疎水性粒子を混合することによ
ってNOx吸着用充填層3の通気性が改善されるが、疎
水性粒子の混合割合が高くなると該吸着用充填層の保水
能力が低下し、吸着されたNOx等の水への吸収量が低
減するため、疎水性粒子の混合割合は3〜30容積%程
度とするのが好ましい。汚染空気中の浮遊粒子状物質
は、炭化水素吸着除去用充填層2およびNOx吸着用充
填層3の各層内の粒子による吸着または濾過作用によっ
て汚染空気から除去される。この結果、NOx吸着用充
填層3の上部から汚染物質が除去された清浄な空気が大
気中に放出される。
The NOx adsorbing packed bed 3 is filled with the above-mentioned soil and / or compost, and NOx (nitrogen oxide) and SOx (sulfur oxide) in contaminated air are adsorbed by these packings. And N as described later.
It is absorbed and dissolved in the water sprinkled on the surface of the Ox adsorption packed layer 3 and moves to the lower layer. Hydrophobic particles can be mixed with the soil and the like. By mixing the hydrophobic particles, the air permeability of the NOx adsorption packed layer 3 is improved. However, when the mixing ratio of the hydrophobic particles increases, the water retention capacity of the adsorption packed layer decreases, and the adsorbed NOx and the like are reduced. In order to reduce the amount of absorption in water, the mixing ratio of the hydrophobic particles is preferably about 3 to 30% by volume. The suspended particulate matter in the contaminated air is removed from the contaminated air by adsorption or filtration by particles in each of the hydrocarbon adsorbing and removing packed bed 2 and the NOx adsorbing packed bed 3. As a result, clean air from which contaminants have been removed is released into the atmosphere from the upper portion of the NOx adsorption packed bed 3.

【0012】一方、NOx吸着用充填層3の表面に散水
装置5により散布された水は、NOx吸着用充填層3お
よび炭化水素吸着除去用充填層2を通過し、該NOx吸
着用充填層3の通過時に該NOx吸着用充填層3に吸着
されたNOx等を吸収、溶解し、さらにその下層の炭化
水素吸着除去用充填層2および汚染空気吹込み用充填層
1を通過して汚染空気中に含まれるNOx等を吸収、溶
解しつつ、さらに下層のNOx除去用充填層4に至る。
NOx除去用充填層4には土壌および/またはコンポス
トが充填されており、上記水に溶解したNOxが、該N
Ox除去用充填層4に生息する脱窒菌により分解され
る。該NOx除去用充填層4には空気が供給されず、嫌
気的な状態が維持されているため、NOxが該土壌等に
生息する脱窒菌によって還元され易く、高効率で窒素ガ
スに変換される。また脱窒菌によるNOxの還元の際に
は、水素供与体として有機物の存在が必要であることか
ら、コンポストの混合割合を高めるのが好ましい。また
上記土壌等には疎水性粒子を混合させてもよい。
On the other hand, water sprayed on the surface of the NOx adsorbing packed layer 3 by the water spray device 5 passes through the NOx adsorbing packed layer 3 and the hydrocarbon adsorbing and removing packed layer 2 and becomes water. Absorbs and dissolves NOx and the like adsorbed on the NOx adsorbing packed layer 3 when passing through, and further passes through the hydrocarbon adsorbing and removing packing layer 2 and the contaminated air blowing packed layer 1 below the NOx adsorbing packed layer 3 so as to absorb contaminated air. While absorbing and dissolving the NOx and the like contained in the NOx, and further reaches the NOx removal filling layer 4 below.
The NOx removal packed bed 4 is filled with soil and / or compost, and the NOx dissolved in the water
It is decomposed by denitrifying bacteria that inhabit the Ox removal filling layer 4. Since no air is supplied to the NOx removal packed bed 4 and an anaerobic state is maintained, NOx is easily reduced by denitrifying bacteria living in the soil and the like, and is converted to nitrogen gas with high efficiency. . In the case of reducing NOx by denitrifying bacteria, it is preferable to increase the mixing ratio of compost because an organic substance is required as a hydrogen donor. Further, hydrophobic particles may be mixed with the above soil and the like.

【0013】また水素供与体として、微生物によって徐
々に分解される生分解性プラスチックを上記NOx除去
用充填層4に混合してもよい。このような生分解性プラ
スチックとしては、脂肪族ポリエステル、ポリ乳酸、ポ
リカプロラクトン等の合成系のポリマーや、澱粉等の天
然系ポリマーが用いられる。生分解性プラスチックをN
Ox除去用充填層4に混合することにより、該生分解性
プラスチックが徐々に生分解されるため、長期にわたっ
て水素供与体としての機能を維持することができる。こ
のように水に吸収されたNOxは、NOx除去用充填層
4によって窒素ガスに効率よく変換されるため、NOx
除去用充填層4から土壌に排出される水のNOx濃度を
低く抑えることができ、土壌や地下水の汚染が著しく軽
減される。
As the hydrogen donor, a biodegradable plastic which is gradually decomposed by microorganisms may be mixed with the NOx removal packed layer 4. As such a biodegradable plastic, synthetic polymers such as aliphatic polyester, polylactic acid, and polycaprolactone, and natural polymers such as starch are used. N biodegradable plastic
By mixing with the Ox removal filling layer 4, the biodegradable plastic is gradually biodegraded, so that the function as a hydrogen donor can be maintained for a long time. The NOx absorbed in the water as described above is efficiently converted into nitrogen gas by the NOx removal packed bed 4, so that the NOx
The NOx concentration of water discharged to the soil from the removal packed bed 4 can be kept low, and the pollution of soil and groundwater is significantly reduced.

【0014】[0014]

【実施例】以下、本発明を実施例によりさらに詳しく説
明するが、本発明はこれらに限定されるものではない。
なお、空気中の窒素酸化物、炭化水素および浮遊粉塵の
濃度の測定は、それぞれ化学発光法測定装置、ガスクロ
マトグラフィー法測定装置、光散乱法測定装置により、
さらに排水中の亜硝酸イオンおよび硝酸イオンの濃度は
イオンクロマトグラフィー法測定装置により測定した。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the invention is limited thereto.
In addition, the measurement of the concentration of nitrogen oxides, hydrocarbons and suspended dust in the air was performed by a chemiluminescence measuring device, a gas chromatography measuring device, and a light scattering measuring device, respectively.
Further, the concentrations of nitrite ion and nitrate ion in the wastewater were measured by an ion chromatography measuring device.

【0015】実施例1 図1の汚染空気の浄化装置を用いて自動車排ガスの浄化
処理を行った。NOx吸着用充填層、炭化水素吸着除去
用充填層およびNOx除去用充填層には、黒ぼく土、コ
ンポスト、パーライトおよび疎水性粒子(粒子表面に有
機性官能基が付加された疎水性シリカ)を表1に示す配
合割合でそれぞれ充填した。また汚染空気吹込み用充填
層には砕石を充填し、その内部に汚染空気吹込み管を導
入して浄化装置内に汚染空気が分散して供給されるよう
にした。また図1の浄化装置は、床面積が1m2 であ
り、NOx吸着用充填層の高さが0.18m、炭化水素
吸着除去用充填層の高さが0.42m、NOx除去用充
填層の高さが0.7mである。また排ガス処理量は0.
72m3 /分とし、NOx吸着用充填層の上部から7リ
ットル/日の水を散水した。処理前の入口空気および処
理後の出口空気の性状を調べ、その結果を表2に示し
た。表2から、汚染空気の窒素酸化物、炭化水素および
浮遊粉塵が、いずれも高い除去率で除去されることがわ
かる。また、NOx除去用充填層の下部から流出する排
水の窒素成分を分析した結果、亜硝酸イオンは11mg/
l、硝酸イオンは19mg/lであった。
Example 1 Purification processing of automobile exhaust gas was performed using the apparatus for purifying contaminated air shown in FIG. The bed for NOx adsorption, the bed for hydrocarbon adsorption removal and the bed for NOx removal contain black clay, compost, perlite and hydrophobic particles (hydrophobic silica with an organic functional group added to the particle surface). Each was filled in the mixing ratio shown in Table 1. In addition, the packed bed for injecting contaminated air was filled with crushed stone, and a contaminated air injecting pipe was introduced therein so that the contaminated air was dispersed and supplied into the purification device. 1 has a floor area of 1 m 2 , the height of the packed bed for NOx adsorption is 0.18 m, the height of the packed bed for hydrocarbon adsorption and removal is 0.42 m, and the height of the packed bed for NOx removal is The height is 0.7 m. In addition, the exhaust gas treatment amount is 0.
Water was sprinkled from the upper part of the packed bed for NOx adsorption at 7 liters / day at 72 m 3 / min. The properties of the inlet air before the treatment and the outlet air after the treatment were examined, and the results are shown in Table 2. From Table 2, it can be seen that nitrogen oxides, hydrocarbons and suspended dust in the contaminated air are all removed at a high removal rate. Also, as a result of analyzing the nitrogen component of the wastewater flowing out from the lower part of the NOx removal packed bed, nitrite ions were found to be 11 mg /
1 and nitrate ion were 19 mg / l.

【0016】[0016]

【表1】 [Table 1]

【0017】[0017]

【表2】 [Table 2]

【0018】実施例2 実施例1において、NOx吸着用充填層、炭化水素吸着
除去用充填層およびNOx除去用充填層のぞれぞれの充
填物を表3に示す配合割合とした以外は実施例1と同様
の方法で自動車排ガスの浄化処理を行った。処理前の入
口空気および処理後の出口空気の性状を調べ、その結果
を表4に示した。表4から、汚染空気の窒素酸化物、炭
化水素および浮遊粉塵が、いずれも高い除去率で除去さ
れることがわかる。また、NOx除去用充填層の下部か
ら流出する排水の窒素成分を分析した結果、亜硝酸イオ
ンは18mg/l、硝酸イオンは25mg/lであった。
Example 2 The procedure of Example 1 was repeated except that the fillers in the bed for NOx adsorption, the bed for adsorption and removal of hydrocarbons and the bed for NOx removal had the mixing ratios shown in Table 3. Purification treatment of automobile exhaust gas was performed in the same manner as in Example 1. The properties of the inlet air before the treatment and the outlet air after the treatment were examined, and the results are shown in Table 4. From Table 4, it can be seen that nitrogen oxides, hydrocarbons and suspended dust in the contaminated air are all removed at a high removal rate. Further, as a result of analyzing the nitrogen component of the wastewater flowing out from the lower part of the packed bed for NOx removal, nitrite ion was 18 mg / l and nitrate ion was 25 mg / l.

【0019】[0019]

【表3】 [Table 3]

【0020】[0020]

【表4】 [Table 4]

【0021】実施例3 実施例1において、NOx吸着用充填層、炭化水素吸着
除去用充填層およびNOx除去用充填層のそれぞれの充
填物を表5に示す充填物および配合割合とした以外は実
施例1と同様の方法で自動車排ガスの浄化処理を行っ
た。なお、疎水性微粒子としては活性炭を用い、生分解
性プラスチックとしては脂肪族ポリエステル系ポリマー
を用いた。処理前の入口空気および処理後の出口空気の
性状を調べ、その結果を表6に示した。表6から、汚染
ガスの窒素酸化物、炭化水素、浮遊粉塵がいずれも高い
除去率で除去されることがわかる。また、NOx除去用
充填層の下部から流出する排水の窒素成分を分析した結
果、亜硝酸イオンは13mg/l、硝酸イオンは16mg/
lであった。
Example 3 The procedure of Example 1 was repeated except that the packings for the NOx adsorbing packed bed, the hydrocarbon adsorbing and removing packed bed and the NOx removing packed bed were changed to the packings and the compounding ratios shown in Table 5. Purification treatment of automobile exhaust gas was performed in the same manner as in Example 1. Activated carbon was used as the hydrophobic fine particles, and aliphatic polyester-based polymer was used as the biodegradable plastic. The properties of the inlet air before the treatment and the outlet air after the treatment were examined, and the results are shown in Table 6. From Table 6, it can be seen that nitrogen oxides, hydrocarbons and suspended dust of the pollutant gas are all removed at a high removal rate. Also, as a result of analyzing the nitrogen component of the wastewater flowing out from the lower part of the packed bed for NOx removal, 13 mg / l of nitrite ions and 16 mg / liter of nitrate ions were analyzed.
l.

【0022】[0022]

【表5】 [Table 5]

【0023】[0023]

【表6】 [Table 6]

【0024】比較例1 床面積が1m2 、層高が0.6mである浄化装置に、黒
ぼく土、コンポストおよびパーライトを表7に示す配合
割合で充填し、自動車排ガスを含む汚染空気の浄化処理
を実施した。汚染空気は、浄化層下部に砕石を充填した
汚染空気吹込み用充填層に導入した汚染空気吹込み管を
介して浄化装置内部に分散するように供給した。またN
Ox吸着用充填層上部から7リットル/日の水を散水し
た。その処理結果を表8に示したが、汚染空気中の炭化
水素の除去率が著しく低下するものであった。また、汚
染空気浄化層下部より流出する水中の窒素成分を分析し
た結果、亜硝酸イオンは109mg/l、硝酸イオンは2
43mg/lであり、排水中の窒素成分が多く、土壌等や
地下水が汚染され易いことがわかった。
Comparative Example 1 Purification equipment having a floor area of 1 m 2 and a layer height of 0.6 m was filled with black clay, compost and pearlite at the compounding ratio shown in Table 7 to purify contaminated air containing automobile exhaust gas. Processing was performed. The contaminated air was supplied so as to be dispersed inside the purification device via the contaminated air blowing pipe introduced into the contaminated air blowing packed bed filled with crushed stone at the lower part of the purification bed. Also N
7 l / day of water was sprinkled from the top of the packed bed for Ox adsorption. The results of the treatment are shown in Table 8, which showed that the removal rate of hydrocarbons in the contaminated air was significantly reduced. Also, as a result of analyzing the nitrogen component in the water flowing out from the lower part of the contaminated air purification layer, nitrite ion was 109 mg / l and nitrate ion was 2 mg / l.
It was 43 mg / l, indicating that the wastewater contained a large amount of nitrogen components, and soil and groundwater were easily contaminated.

【0025】[0025]

【表7】 [Table 7]

【0026】[0026]

【表8】 [Table 8]

【0027】[0027]

【発明の効果】本発明の浄化装置および浄化方法によれ
ば、自動車排ガスや燃焼排ガス等の各種の汚染物質に対
して処理条件を適性化することができるため、高い除去
性能が確保できるとともに、硝酸、亜硝酸等の形で存在
する窒素成分を高い割合で窒素ガスに変換して土壌や地
下水の汚染を低減させることができる。
According to the purifying apparatus and the purifying method of the present invention, it is possible to optimize treatment conditions for various pollutants such as automobile exhaust gas and combustion exhaust gas, so that high removal performance can be ensured. Nitrogen components existing in the form of nitric acid, nitrous acid and the like can be converted into nitrogen gas at a high rate to reduce soil and groundwater contamination.

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

【図1】本発明の一実施例を示す汚染空気の浄化装置の
説明図。
FIG. 1 is an explanatory view of a polluted air purifying apparatus showing one embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…汚染空気吹込み用充填層、2…炭化水素吸着除去用
充填層、3…NOx吸着用充填層、4…NOx除去用充
填層、5…散水装置、6…吹込み装置。
DESCRIPTION OF SYMBOLS 1 ... Packing layer for blowing contaminated air, 2 ... Packing layer for removing and adsorbing hydrocarbons, 3 ... Packing layer for adsorbing NOx, 4 ... Packing layer for removing NOx, 5 ... Sprinkler, 6 ... Blower.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // C08K 3/00 C08L 101/16 Fターム(参考) 3G091 AA02 AB00 AB09 AB10 AB15 BA14 BA15 CA15 GB00Y HA07 4D002 AA12 AA33 AA34 BA03 BA04 BA06 BA14 BA17 CA01 CA07 DA47 DA58 DA70 EA03 EA07 4J002 CF031 CF181 CF191 DM006 FD206 GT00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (reference) // C08K 3/00 C08L 101/16 F term (reference) 3G091 AA02 AB00 AB09 AB10 AB15 BA14 BA15 CA15 GB00Y HA07 4D002 AA12 AA33 AA34 BA03 BA04 BA06 BA14 BA17 CA01 CA07 DA47 DA58 DA70 EA03 EA07 4J002 CF031 CF181 CF191 DM006 FD206 GT00

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 汚染ガス中の有害物質を吸着除去する吸
着剤の充填層を有する汚染ガスの浄化装置であって、吹
込み手段を介して汚染ガスが吹き込まれる汚染ガス吹込
み用充填層と、該汚染ガス吹込み用充填層上に順に形成
され、かつ土壌および/またはコンポストを含む、前記
汚染ガスに含まれる炭化水素系汚染物質を吸着除去する
炭化水素吸着除去用充填層および該汚染ガスに含まれる
窒素酸化物を吸着する窒素酸化物吸着用充填層と、該窒
素酸化物吸着用充填層の表面に水を散布する散水手段
と、前記汚染ガス吹込み用充填層の下部に形成され、か
つ土壌および/またはコンポストを含む、前記水に吸収
された窒素酸化物を分解除去する窒素酸化物除去用充填
層とを設置したことを特徴とする汚染ガスの浄化装置。
An apparatus for purifying a pollutant gas having a packed layer of an adsorbent for adsorbing and removing harmful substances in the polluted gas, comprising: A hydrocarbon adsorbing and removing packing layer formed in order on the contaminated gas injecting filling layer and adsorbing and removing hydrocarbon contaminants contained in the contaminant gas, including soil and / or compost; and the contaminant gas A filling layer for adsorbing nitrogen oxides contained in, a watering means for spraying water on the surface of the filling layer for nitrogen oxide adsorption, and a lower part of the filling layer for blowing the contaminated gas. And a nitrogen oxide removing packed bed that decomposes and removes nitrogen oxides absorbed in the water, including soil and / or compost.
【請求項2】 前記窒素酸化物吸着用充填層および炭化
水素吸着除去用充填層に疎水性粒子を混合したことを特
徴とする請求項1に記載の汚染ガスの浄化装置。
2. The pollutant gas purifying apparatus according to claim 1, wherein hydrophobic particles are mixed in the nitrogen oxide adsorption packed bed and the hydrocarbon adsorption removal packed bed.
【請求項3】 前記窒素酸化物除去用充填層に生分解性
プラスチックを混合したことを特徴とする請求項1また
は2に記載の汚染ガスの浄化装置。
3. The pollutant gas purifying apparatus according to claim 1, wherein a biodegradable plastic is mixed into the nitrogen oxide removing packed bed.
【請求項4】 請求項1〜3のいずれかに記載の汚染ガ
スの浄化装置を用いて汚染ガスを浄化するに際し、吹込
み手段により汚染ガス吹込み用充填層に供給した汚染ガ
スを、炭化水素吸着除去用充填層および窒素酸化物吸着
用充填層に順に通過させ、該炭化水素吸着除去用充填層
により汚染ガス中の炭化水素系汚染物質を吸着分解し、
該窒素酸化物吸着用充填層により汚染ガス中の窒素酸化
物を吸着して清浄なガスを該窒素酸化物吸着用充填層の
上部から系外に放出するとともに、前記窒素酸化物吸着
用充填層の表面に散水手段により水を散布し、該窒素酸
化物吸着用充填層および前記炭化水素吸着除去用充填層
を通過する水に、前記汚染ガスに含まれる窒素酸化物お
よび各層に吸着された窒素酸化物を吸収させ、該吸収さ
れた窒素酸化物を前記汚染ガス吹込み用充填層の下部に
設けられた窒素酸化物除去用充填層で還元除去した後、
排水として系外に排出することを特徴とする汚染ガスの
浄化方法。
4. When purifying a pollutant gas using the pollutant gas purifier according to any one of claims 1 to 3, the pollutant gas supplied to the polluted gas injection packed bed by the blowing means is carbonized. Pass through the packed bed for hydrogen adsorption and removal and the packed bed for nitrogen oxide adsorption in order, and the hydrocarbon-based contaminants in the polluted gas are adsorbed and decomposed by the packed bed for hydrocarbon adsorption and removal,
The nitrogen oxide-absorbing packed bed absorbs nitrogen oxides in the polluted gas and releases a clean gas from the upper part of the nitrogen oxide-absorbing packed bed to the outside of the system. Water is sprayed on the surface of the substrate by water spraying means, and the water passing through the nitrogen oxide adsorption packed bed and the hydrocarbon adsorption removal packed bed contains nitrogen oxides contained in the contaminated gas and nitrogen adsorbed on each layer. After absorbing the oxides, the absorbed nitrogen oxides are reduced and removed by a nitrogen oxide removal packed bed provided below the contaminated gas injection packed bed,
A method for purifying pollutant gas, which is discharged outside the system as wastewater.
JP2000116594A 2000-04-18 2000-04-18 Device for cleaning foul gas and cleaning method Withdrawn JP2001300251A (en)

Priority Applications (2)

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IDP20010330D ID29840A (en) 2000-04-18 2001-04-18 GENES OF GENES

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JP2001300251A true JP2001300251A (en) 2001-10-30

Family

ID=18628036

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2001300251A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100568699B1 (en) * 2004-02-23 2006-04-11 정하영 The purifier and method for the filert off smoke gas
JP2006218364A (en) * 2005-02-09 2006-08-24 Taisei Corp Purification apparatus and purifying method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100568699B1 (en) * 2004-02-23 2006-04-11 정하영 The purifier and method for the filert off smoke gas
JP2006218364A (en) * 2005-02-09 2006-08-24 Taisei Corp Purification apparatus and purifying method
JP4718199B2 (en) * 2005-02-09 2011-07-06 大成建設株式会社 Purification device and purification method

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