JP3497718B2 - Contaminated air purification device - Google Patents

Contaminated air purification device

Info

Publication number
JP3497718B2
JP3497718B2 JP00073198A JP73198A JP3497718B2 JP 3497718 B2 JP3497718 B2 JP 3497718B2 JP 00073198 A JP00073198 A JP 00073198A JP 73198 A JP73198 A JP 73198A JP 3497718 B2 JP3497718 B2 JP 3497718B2
Authority
JP
Japan
Prior art keywords
layer
soil
water
activated carbon
container
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.)
Expired - Fee Related
Application number
JP00073198A
Other languages
Japanese (ja)
Other versions
JPH11192413A (en
Inventor
晴男 高野
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.)
Okumura Corp
Original Assignee
Okumura 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 Okumura Corp filed Critical Okumura Corp
Priority to JP00073198A priority Critical patent/JP3497718B2/en
Publication of JPH11192413A publication Critical patent/JPH11192413A/en
Application granted granted Critical
Publication of JP3497718B2 publication Critical patent/JP3497718B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • 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
    • Y02CCAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00Capture or disposal of greenhouse gases
    • Y02C20/40Capture or disposal of greenhouse gases of CO2
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/59Biological synthesis; Biological purification

Landscapes

  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Treating Waste Gases (AREA)
  • Filtering Materials (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

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】この発明は、自動車や工場ま
たはトンネル工事の各種機械から排出される排出ガスに
より汚染された空気を浄化する汚染空気浄化装置に関
し、詳しくは汚染空気中に含まれる炭酸ガス,窒素酸化
物および粉塵等を効果的に除去できる汚染空気浄化装置
に関する。
TECHNICAL FIELD The present invention relates to automobiles and factories or tunnels contaminated air purifying apparatus you purify contaminated air by exhaust gas discharged from the various machines construction, details contained in the polluted air carbon dioxide, on nitrogen oxides and pollution air purifier that can effectively remove dust and the like.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】従
来、汚染空気浄化装置としては、フィルタ式の空気浄化
装置が用いられているが、コストが高く、粉塵によるフ
ィルタの目詰まり処理等に手間がかかるという問題があ
る。また、排出ガス中の窒素酸化物の除去については、
乾式法の接触還元法や無接触還元法または酸化吸収法が
一般に知られているが、これらの方法による処理プラン
トは、建設費やランニングコストが高いため、十分な処
理能力を得るために装置の規模も大きくなり、相当な費
用を要するという問題がある。そこで、この発明の目的
は、低コストで炭酸ガス,窒素酸化物および粉塵等を効
果的に除去できる汚染空気浄化装置を提供することにあ
る。
2. Description of the Related Art Conventionally, a filter type air purifying device has been used as a polluted air purifying device, but the cost is high and it is troublesome to remove the filter from clogging with dust. There is a problem of this. Regarding the removal of nitrogen oxides in exhaust gas,
The dry reduction method, non-contact reduction method or oxidation absorption method is generally known, but the treatment plant by these methods has high construction cost and running cost. There is a problem that the scale becomes large and the cost is considerable. Therefore, an object of the present invention is to provide a polluted air purifying apparatus that can effectively remove carbon dioxide, nitrogen oxides, dust, and the like at low cost.

【0003】[0003]

【課題を解決するための手段】上記目的を達成するた
め、請求項の汚染空気浄化装置は、容器と、上記容器
内に収容され、微生物が繁殖可能でかつ空気が流動可能
な土壌層と、上記容器内に上記土壌層の上側に収容さ
れ、空気が流動可能な活性炭層と、上記土壌層の下方か
ら上記土壌層と上記活性炭層とに汚染空気を通過させる
空気流動部とを備え、上記容器内の上記土壌層の上側に
設けられ、下方に向けて流れるように水を供給する給水
部と、上記容器内の上記土壌層の下側に収容され、気体
と水が流動可能でかつ上記汚染空気中の粉塵が付着する
透水層と、上記容器の底部または上記底部の近傍に設け
られ、上記給水部から上記土壌層と上記透水層とを介し
て流動してきた水を排水する排水部とを備え、上記土壌
層と上記活性炭層との間に、水を通過させずに気体のみ
を通過させる遮水通気層を設けたことを特徴としてい
る。
In order to achieve the above object, the polluted air purifying apparatus according to claim 1 comprises a container, and a soil layer housed in the container, in which microorganisms can propagate and air can flow. , An upper part of the soil layer is housed in the container, an activated carbon layer in which air can flow, and an air flow part for passing contaminated air to the soil layer and the activated carbon layer from below the soil layer , Above the soil layer in the container
Water supply provided to supply water downward
Part and below the soil layer in the container, the gas
And water can flow and dust in the contaminated air adheres
Provided in the water-permeable layer and at the bottom of the container or in the vicinity of the bottom
From the water supply section through the soil layer and the permeable layer.
And a drainage part for draining the flowing water.
Between the bed and the activated carbon bed, only gas without passing water
It is characterized by the provision of a water-permeable ventilation layer that allows water to pass through .

【0004】上記請求項の汚染空気浄化装置によれ
ば、上記空気流動部によって上記土壌層の下方から上記
土壌層と上記活性炭層とに汚染空気を通過させる。そう
すると、上記汚染空気中に含まれる粉塵が上記容器内の
土壌層の土壌粒子に付着すると共に、炭酸ガス等の炭化
物や窒素酸化物等の有害物質を土壌中の微生物により無
害な物質に分解する。また、汚染空気中の窒素酸化物の
うち、土壌層で処理されずに残った窒素酸化物を活性炭
層で吸着させることによって、処理効率を落とすことな
く、窒素酸化物も十分に処理できる。したがって、簡単
な構成で汚染空気中の炭酸ガス,窒素酸化物および粉塵
等を効果的に除去して、低コストで汚染空気を浄化でき
る。
According to the polluted air purifying apparatus of the first aspect , polluted air is passed from below the soil layer to the soil layer and the activated carbon layer by the air flow section. Then, dust contained in the contaminated air adheres to the soil particles in the soil layer in the container, and decomposes harmful substances such as carbon dioxide and other carbides and nitrogen oxides into harmless substances by microorganisms in the soil. . Further, among the nitrogen oxides in the contaminated air, the nitrogen oxides that have not been treated in the soil layer and are left to be adsorbed in the activated carbon layer can sufficiently treat the nitrogen oxides without lowering the treatment efficiency. Therefore, it is possible to purify the contaminated air at low cost by effectively removing carbon dioxide gas, nitrogen oxides, dust and the like in the contaminated air with a simple configuration.

【0005】また、上記土壌層に上記給水部から水を供
給することによって、汚染空気の通過に伴って土壌に含
まれる水が蒸発して乾燥により微生物が減少するという
ことがなく、微生物による有害物質の分解効率の低下を
防ぐ。また、汚染物質に含まれる二酸化窒素が水に溶解
しやすく、水に溶けて亜硝酸や硝酸に変化するので、二
酸化窒素の処理効率が向上する。さらに、汚染空気に含
まれる粉塵が上記透水層や土壌層に付着した後、上記給
水部から土壌層と透水層とを介して流動する水によって
洗い流して、上記排水部により外部に排水できる。
Further, water is supplied to the soil layer from the water supply section.
Supply of soil to the soil as contaminated air passes through.
The water that evaporates evaporates and the microorganisms decrease when dried.
Without decreasing the efficiency of decomposition of harmful substances by microorganisms.
prevent. Also, nitrogen dioxide contained in pollutants dissolves in water
It is easy to do and it dissolves in water and changes to nitrous acid and nitric acid.
The treatment efficiency of nitric oxide is improved. Furthermore, it is included in contaminated air.
After the dust that has accumulated is attached to the permeable layer or soil layer,
By the water flowing from the water part through the soil layer and the permeable layer
It can be washed off and drained to the outside by the drainage part.

【0006】また、上記遮水通気層によって、上記土壌
層側から上記活性炭層に水が入って窒素酸化物等の吸収
効率が低下するのを防止できる。
[0006] Further , the above-mentioned impermeable aeration layer allows the above-mentioned soil
Water enters the activated carbon layer from the layer side to absorb nitrogen oxides, etc.
It is possible to prevent the efficiency from decreasing.

【0007】また、請求項の汚染空気浄化装置は、請
求項の汚染空気浄化装置において、上記活性炭層は、
活性炭に微生物が繁殖可能な土壌を混合した土壌混合活
性炭層であることを特徴としている。
Further, the polluted air purifying apparatus according to claim 2 is the polluted air purifying apparatus according to claim 1 , wherein the activated carbon layer is
It is characterized by a soil-mixed activated carbon layer in which activated carbon is mixed with soil in which microorganisms can reproduce.

【0008】上記請求項の汚染空気浄化装置によれ
ば、上記活性炭層を活性炭に微生物が繁殖可能な土壌を
混合した土壌混合活性炭層とすることによって、窒素酸
化物等の有害物質を活性炭に吸着できると同時に、さら
に、その土壌混合活性炭層の土壌中の微生物で無害な物
質に分解できる。
According to the polluted air purifying apparatus of claim 2 , the activated carbon layer is a soil-mixed activated carbon layer in which activated carbon is mixed with a soil in which microorganisms can grow, so that harmful substances such as nitrogen oxides are activated carbon. At the same time it can be adsorbed, it can be further decomposed into harmless substances by microorganisms in the soil of the soil-mixed activated carbon layer.

【0009】また、請求項の汚染空気浄化装置は、請
求項1または2の汚染空気浄化装置において、上記給水
部から上記土壌層と上記透水層とを介して流動してきた
水を上記透水層で貯留可能なように、上記排水部に開閉
弁を設けたことを特徴としている。
The polluted air purifying apparatus according to claim 3 is the polluted air purifying apparatus according to claim 1 or 2 , wherein the water flowing from the water supply portion through the soil layer and the water permeable layer is used as the water permeable layer. It is characterized in that an opening / closing valve is provided in the drainage section so that it can be stored in.

【0010】上記請求項の汚染空気浄化装置によれ
ば、上記排水部に設けられた上記開閉弁を閉状態にし
て、上記透水層に水を貯留させて、貯留水を適当な期間
で上記開閉弁を開状態にして排出した後、再び上記開閉
弁を閉状態にして水を貯留する。そうして、適当な期間
で貯留水を入れ替えることによって、上記透水層に付着
した粉塵を貯留水に溶かして、上記容器外に排出でき
る。
According to the polluted air purifying apparatus of the third aspect, the on-off valve provided in the drainage section is closed, water is stored in the water permeable layer, and the stored water is stored for an appropriate period. After the on-off valve is opened and discharged, the on-off valve is closed again to store water. Then, by replacing the stored water for an appropriate period, the dust adhering to the water permeable layer can be dissolved in the stored water and discharged outside the container.

【0011】[0011]

【発明の実施の形態】以下、この発明の汚染空気浄化装
置を図示の実施の形態により詳細に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION The polluted air purifying apparatus of the present invention will be described in detail below with reference to the embodiments shown in the drawings.

【0012】図1はこの発明の実施の一形態の汚染空気
浄化装置の断面図であり、1は鋼製の容器、2は上記容
器1内の底部1a上に粒径約40mmの玉砂利が高さ30c
mに敷き詰められた玉砂利層、3は上記玉砂利層3上に
粒径3〜13mmの砂利が高さ20cmに敷き詰められた支
持層、4は上記支持層3上に微生物が繁殖可能な土壌が
高さ50cmに敷き詰められた土壌層、5は上記容器1内
の上記土壌層4上に設けられ、水を通さず気体を通す遮
水通気層、6は上記遮水通気層5上に活性炭が敷き詰め
られた活性炭層である。上記土壌層4は、園芸用土,腐
葉土,油粕および人工軽量骨材を10:1:0.5:1の
容積割合で配合したものである。
FIG. 1 is a cross-sectional view of a polluted air purifying apparatus according to an embodiment of the present invention, in which 1 is a steel container, 2 is a bottom 1a in the container 1, and gravel with a grain size of about 40 mm is high. 30c
The gravel layer 3 spread over the m is a support layer in which the gravel with a particle size of 3 to 13 mm is spread over the gravel layer 3 to a height of 20 cm, and 4 is the support layer 3 in which soil in which microorganisms can grow is high. A soil layer spread over 50 cm, 5 is provided on the soil layer 4 in the container 1, and a water-impermeable gas-permeable gas-permeable layer, and 6 is water-permeable gas-permeable layer 5 having activated carbon spread on it. It is the activated carbon layer. The soil layer 4 is a mixture of horticultural soil, mulch, oil cake and artificial lightweight aggregate in a volume ratio of 10: 1: 0.5: 1.

【0013】また、上記容器1内の玉砂利層2に複数の
送気管13(図1では1つのみを示す)を略水平に配置し
ている。汚染空気をエアーポンプ11により吸い込み、
上記エアーポンプ11により送り出された汚染空気の流
量を流量コントローラ12により制御しながら、上記複
数の送気管13に汚染空気を供給する。上記エアーポン
プ11,流量コントローラ12および送気管13で空気
流動部を構成している。また、上記容器1内の複数の送
気管13には、下側に複数の排気口13aを夫々設けて
おり、上記流量コントローラ13からの汚染空気が複数
の排気口13aから玉砂利層2に排出されて、容器1内
を上方に向かって流れる。また、上記土壌層4の上側に
給水部としての複数の送水管23(図1では1つのみを
示す)を略水平に配置している。上記各送水管23の上
流側の一端を開閉弁22を介して水槽21に接続してい
る。上記水槽21は、容器1内に各送水管23が配置さ
れている位置よりも高い位置に配置している。上記各送
水管23の容器1内の部分には、下側に複数の給水口2
3aを夫々設けており、上記水槽21から水が供給され
て、送水管23の給水口23aから土壌層4に滴下され
る。また、上記容器1の底部1a近傍の側面に、開閉弁
16を有する排水部としての排水管15を設けている。
なお、上記排水管15は、容器1の底部1aに設けても
よい。
Further, a plurality of air supply pipes 13 (only one is shown in FIG. 1) are arranged substantially horizontally in the gravel layer 2 in the container 1. Contaminated air is sucked in by the air pump 11,
The contaminated air is supplied to the plurality of air supply pipes 13 while controlling the flow rate of the contaminated air sent by the air pump 11 by the flow rate controller 12. The air pump 11, the flow rate controller 12, and the air supply pipe 13 constitute an air flow section. Further, the plurality of air supply pipes 13 in the container 1 are respectively provided with a plurality of exhaust ports 13a on the lower side, and the contaminated air from the flow rate controller 13 is discharged to the gravel layer 2 from the plurality of exhaust ports 13a. And flows upward in the container 1. In addition, a plurality of water supply pipes 23 (only one is shown in FIG. 1) as water supply units are arranged substantially horizontally above the soil layer 4. One end of each of the water supply pipes 23 on the upstream side is connected to the water tank 21 via an opening / closing valve 22. The water tank 21 is arranged at a position higher than the position where the water supply pipes 23 are arranged in the container 1. At the inside of the container 1 of each of the water supply pipes 23, a plurality of water supply ports 2 are provided on the lower side.
3a are provided respectively, and water is supplied from the water tank 21 and dripped into the soil layer 4 from the water supply port 23a of the water supply pipe 23. Further, a drainage pipe 15 as a drainage portion having an opening / closing valve 16 is provided on the side surface near the bottom portion 1a of the container 1.
The drain pipe 15 may be provided at the bottom 1a of the container 1.

【0014】図2は図1のII−II線から見た断面図を示
し、容器1内の玉砂利層2に所定の間隔をあけて排気口
13aを有する複数の送気管13を互いに平行に配列し
ている。また、上記土壌層4の上側かつ遮水通気層5の
下側に所定の間隔をあけて給水口23aを有する複数の
送水管23を互いに平行に配列している。上記複数の送
水管23の給水口23aから滴下した水は、容器1内に
ほぼ均一に広がりながら土壌層4,支持層3および玉砂
利層2の順に流動した後、容器1内の下側に貯まり貯留
水14となる。
FIG. 2 is a sectional view taken along the line II--II of FIG. 1, in which a plurality of air supply pipes 13 having exhaust ports 13a are arranged in parallel with each other in the gravel layer 2 in the container 1 at predetermined intervals. is doing. Further, a plurality of water supply pipes 23 having water supply ports 23a are arranged in parallel with each other on the upper side of the soil layer 4 and the lower side of the water-permeable and air-permeable layer 5 at predetermined intervals. The water dripped from the water supply ports 23a of the plurality of water supply pipes 23 flows in the container 1 in the order of the soil layer 4, the support layer 3 and the gravel layer 2 while spreading substantially uniformly, and then accumulates in the lower part of the container 1. It becomes the stored water 14.

【0015】上記構成の汚染空気浄化装置において、エ
アーポンプ11により吸い込まれた汚染空気は、流量コ
ントローラ12により汚染空気の流量が所定量に調整さ
れて、送気管13に送り出され、送気管13の排気口1
3aより容器1内の玉砂利層2に排出される。そうし
て、上記玉砂利層2の玉砂利の隙間を通って汚染空気が
上方に流れ、支持層3の砂利の隙間を通って土壌層4に
流れる。このとき、汚染空気中に含まれる粉塵は、玉砂
利層2,支持層3の砂利に付着すると共に、土壌層4の
下側の土壌粒子に付着する。さらに、上記汚染空気が土
壌層4を通るときに、汚染空気中の炭酸ガス等の炭化物
と窒素酸化物を土壌中の微生物により分解処理する。こ
の場合、炭酸ガスのほとんどが土壌層4で処理されるよ
うに、流量コントローラ12により汚染空気の土壌層4
における通過速度を調整すると、窒素酸化物の未処理分
が残る。そして、汚染空気は、土壌層4から遮水通気層
5を介して活性炭層6を通って上方に出る。このとき、
活性炭層6では、土壌層4で処理されずに残った窒素酸
化物を活性炭に吸着させると共に、土壌中の微生物によ
り分解も行われる。
In the contaminated air purifying apparatus having the above structure, the contaminated air sucked by the air pump 11 is adjusted to a predetermined amount by the flow rate controller 12 and is sent out to the air feeding pipe 13 to be fed to the air feeding pipe 13. Exhaust port 1
It is discharged to the gravel layer 2 in the container 1 from 3a. Then, the contaminated air flows upward through the gaps of the gravel of the gravel layer 2 and flows into the soil layer 4 through the gaps of the gravel of the support layer 3. At this time, the dust contained in the contaminated air adheres to the gravel of the gravel layer 2 and the support layer 3 and also to the soil particles below the soil layer 4. Further, when the contaminated air passes through the soil layer 4, the carbon dioxide and other carbides and nitrogen oxides in the contaminated air are decomposed by microorganisms in the soil. In this case, the flow controller 12 controls the soil layer 4 of the contaminated air so that most of the carbon dioxide gas is treated in the soil layer 4.
Adjusting the passage rate at the temperature leaves an untreated portion of nitrogen oxides. Then, the contaminated air passes through the activated carbon layer 6 from the soil layer 4 through the impermeable aeration layer 5 and exits upward. At this time,
In the activated carbon layer 6, the nitrogen oxide remaining without being treated in the soil layer 4 is adsorbed on the activated carbon, and also decomposed by microorganisms in the soil.

【0016】以下、トンネル工事の坑内において汚染空
気浄化装置を用いた実験について説明する。このトンネ
ル工事の坑内では、ズリ出し作業と吹き付け作業時に長
時間有毒ガスや粉塵が発生する。このトンネル坑内で汚
染空気浄化装置を用いて有毒ガスと粉塵を除去したとき
の有毒ガスと粉塵の除去特性について説明する。この実
験では、上記汚染空気浄化装置の複数の送水管23の給
水口23aより1日に0.5リットルを土壌層4の上部か
ら滴下すると共に、容器1下部の玉砂利層2には、水を
水深15cmに貯留して、2週間毎に入れ換えた。なお、
土壌層4と活性炭層6との間の遮水通気層5はなく、ま
た、活性炭層6の部分が土壌のみの場合と土壌混合活性
炭の場合とを比較した。
An experiment using a polluted air purifying device in a tunnel mine will be described below. In the tunnel mine, toxic gas and dust are generated for a long period of time during the slipping and spraying work. The removal characteristics of toxic gas and dust when the toxic gas and dust are removed using the polluted air purifier in this tunnel pit will be described. In this experiment, 0.5 liters per day was dripped from the upper part of the soil layer 4 from the water supply ports 23a of the plurality of water supply pipes 23 of the above-mentioned polluted air purifying device, and water was added to the gravel layer 2 below the container 1. It was stored at a water depth of 15 cm and replaced every two weeks. In addition,
The water-impermeable and air-permeable layer 5 between the soil layer 4 and the activated carbon layer 6 was not provided, and the case where the portion of the activated carbon layer 6 was only soil and the case of soil-mixed activated carbon were compared.

【0017】まず、図3は線速度(土壌等を汚染空気が
移動する速度)とCO除去率との関係および線速度とC
O濃度差(処理前のCO濃度−処理後のCO濃度)との関
係を示す図である。図3に示すように、線速度が5,1
0,15mm/secの場合のCO濃度差は、約5,3,2pp
m、CO除去率は、約88.6,56.6,41.1%であっ
た。したがって、線速度5mm/secの場合に、実用可能
な除去性能であることを確認した。
First, FIG. 3 shows the relationship between the linear velocity (the velocity at which contaminated air moves through soil etc.) and the CO removal rate, and the linear velocity and C.
It is a figure which shows the relationship with O density | concentration difference (CO density | concentration before processing-CO density | concentration after processing). As shown in FIG. 3, the linear velocity is 5,1.
CO concentration difference at 0,15 mm / sec is about 5,3,2 pp
The m and CO removal rates were about 88.6, 56.6, 41.1%. Therefore, it was confirmed that the removal performance was practical when the linear velocity was 5 mm / sec.

【0018】また、図4は線速度とNO除去率との関係
を示す図である。図4に示すように、活性炭層のない場
合(図4では活性炭無添加のグラフ)に線速度5mm/sec
のときにNO除去率が最大で12.1%であり、土壌層
によるNO除去効果は低い。これに対して、土壌層の表
面から深さ20cmまで粒状活性炭を容積割合で21%混
合して、30日間実験を継続した結果(図4では活性炭
添加のグラフ)、粒状活性炭混合した後のNO除去率
は、すなわち、土壌混合活性炭層とした後のNO除去率
は、いずれの線速度においても95%以上であった。
FIG. 4 is a graph showing the relationship between the linear velocity and the NO removal rate. As shown in Fig. 4, when there is no activated carbon layer (in Fig. 4, the graph without activated carbon added), the linear velocity is 5 mm / sec.
At that time, the NO removal rate was 12.1% at maximum, and the NO removal effect by the soil layer was low. On the other hand, the granular activated carbon was mixed at a volume ratio of 21% from the surface of the soil layer to a depth of 20% and the experiment was continued for 30 days (graph of activated carbon addition in Fig. 4). The removal rate, that is, the NO removal rate after forming the soil-mixed activated carbon layer was 95% or more at any linear velocity.

【0019】また、図5は線速度と粉塵除去率との関係
を示す図である。図5に示すように、いずれの線速度に
おいても高い粉塵除去率が得られた。このとき除去され
た粉塵は、玉砂利層2の空隙の貯留水に移行したり、支
持層3や土壌層4下側に補足されるが、土壌が多孔性の
ために実験期間における土壌層4の圧力損失の増加は見
られなかった。
FIG. 5 is a diagram showing the relationship between the linear velocity and the dust removal rate. As shown in FIG. 5, a high dust removal rate was obtained at any linear velocity. The dust removed at this time migrates to the stored water in the voids of the gravel layer 2 or is trapped under the support layer 3 and the soil layer 4, but because of the porosity of the soil, the dust in the soil layer 4 during the experiment period is No increase in pressure loss was observed.

【0020】このように、汚染空気中に含まれる粉塵が
容器1内の土壌層4の土壌粒子に付着すると共に、炭酸
ガスや窒素酸化物等の有害物質を土壌中の微生物で無害
な物質に分解させ、また、汚染空気中の窒素酸化物のう
ちの土壌層4で処理されずに残った窒素酸化物を活性炭
層6の活性炭に吸着させることによって、処理効率を落
とすことなく、窒素酸化物も十分に処理することができ
る。したがって、簡単な構成で炭酸ガス,窒素酸化物お
よび粉塵等を効果的に除去して、低コストで汚染空気を
浄化することができる。
As described above, the dust contained in the contaminated air adheres to the soil particles in the soil layer 4 in the container 1, and the harmful substances such as carbon dioxide and nitrogen oxides are converted into harmless substances by the microorganisms in the soil. By decomposing and adsorbing, among the nitrogen oxides in the polluted air, the nitrogen oxides that have not been treated in the soil layer 4 and are adsorbed on the activated carbon of the activated carbon layer 6, the nitrogen oxides can be treated without lowering the treatment efficiency. Can also be fully processed. Therefore, it is possible to effectively remove carbon dioxide, nitrogen oxides, dust and the like with a simple configuration, and to purify contaminated air at low cost.

【0021】また、上記土壌層4に送水管23から水を
供給することによって、汚染空気の通過に伴って土壌に
含まれる水が蒸発して乾燥により微生物が減少するのを
防ぎ、微生物による有害物質の分解効率の低下を防止す
ることができる。また、汚染空気に含まれる二酸化窒素
が水に溶解しやすく、水に溶けて亜硝酸や硝酸に変化す
るので、二酸化窒素の処理効率を向上することができ
る。さらに、汚染空気に含まれる粉塵が支持層3と玉砂
利層2の透水層の砂利に付着した後、送水管23から支
持層3と玉砂利層2の透水層を流動する水によって砂利
に付着した粉塵を洗い流すことができる。
Further, by supplying water to the soil layer 4 from the water pipe 23, it is possible to prevent water contained in the soil from evaporating due to the passage of contaminated air and to prevent the microorganisms from being reduced due to drying, thereby preventing harmful effects of the microorganisms. It is possible to prevent degradation of the decomposition efficiency of the substance. Further, since nitrogen dioxide contained in the contaminated air is easily dissolved in water and dissolved in water to be converted into nitrous acid or nitric acid, the treatment efficiency of nitrogen dioxide can be improved. Further, after the dust contained in the contaminated air adheres to the gravel of the permeable layer of the support layer 3 and the gravel layer 2, the dust that adheres to the gravel by the water flowing from the water pipe 23 through the permeable layer of the support layer 3 and the gravel layer 2 Can be washed away.

【0022】また、上記排水管15に設けた開閉弁16
を閉状態にすることによって、玉砂利層2に水を貯留さ
せて、玉砂利層2と支持層3の透水層の砂利に付着した
粉塵を貯留水に溶かして、開閉弁16を開状態にするこ
とによって、容器1外に排出することができる。
An on-off valve 16 provided in the drain pipe 15
Is closed to store water in the gravel layer 2, dissolve the dust adhering to the gravel of the permeable layer of the gravel layer 2 and the support layer 3 into the stored water, and open the on-off valve 16. Can be discharged to the outside of the container 1.

【0023】また、水を通過させずに気体のみを通過さ
せる遮水通気層5を土壌層4と活性炭層6との間に設け
て、送水管23により供給された水が土壌層4側から活
性炭層6に侵入しないようにすることによって、活性炭
による窒素酸化物等の吸収効率が低下するのを防止する
ことができる。
Further, an impermeable aeration layer 5 that allows only gas to pass but not water is provided between the soil layer 4 and the activated carbon layer 6, and the water supplied by the water pipe 23 is fed from the soil layer 4 side. By preventing the activated carbon from entering the activated carbon layer 6, it is possible to prevent the absorption efficiency of nitrogen oxides and the like from being reduced by the activated carbon.

【0024】上記実施の形態では、容器1内の最上部に
活性炭層6を敷き詰めたが、活性炭層は、活性炭に微生
物が繁殖可能な土壌を混合した土壌混合活性炭層でもよ
い。この場合、活性炭に微生物が繁殖可能な土壌を混合
した土壌混合活性炭層によって、窒素酸化物等の有害物
質を土壌混合活性炭層の活性炭に吸着すると共に、その
土壌混合活性炭層の土壌中の微生物で有害物質を無害な
物質にさらに分解することができる。また、土壌混合活
性炭層の土壌と活性炭の混合比は適宜設定してよい。
In the above embodiment, the activated carbon layer 6 is laid on the uppermost part of the container 1, but the activated carbon layer may be a soil-mixed activated carbon layer in which activated carbon is mixed with soil in which microorganisms can grow. In this case, the soil-mixed activated carbon layer in which the soil in which the microorganisms can reproduce can be mixed with the activated carbon adsorbs harmful substances such as nitrogen oxides on the activated carbon in the soil-mixed activated carbon layer, and the microorganisms in the soil in the soil-mixed activated carbon layer Hazardous substances can be further decomposed into harmless substances. Further, the mixing ratio of the soil and the activated carbon in the soil-mixed activated carbon layer may be set appropriately.

【0025】また、上記実施の形態では、トンネル工事
の坑内の汚染空気を浄化する汚染空気消化装置について
説明したが、自動車や工場の各種機械から排出される排
出ガスを浄化するためにこの発明を適用してもよい。
In the above embodiment, the polluted air extinguishing apparatus for purifying the polluted air in the tunnel mine has been described, but the present invention is applied to purify the exhaust gas discharged from various machines in automobiles and factories. You may apply.

【0026】[0026]

【発明の効果】以上より明らかなように、請求項の発
明の汚染空気浄化装置は、容器と、上記容器内に収容さ
れ、微生物が繁殖可能でかつ空気が流動可能な土壌層
と、上記容器内に上記土壌層の上側に収容され、空気が
流動可能な活性炭層とを備え、空気流動部によって上記
土壌層の下方から土壌層と活性炭層とに汚染空気を通過
させるものであり、上記容器内の上記土壌層の上側に設
けられた給水部によって、下方に向けて流れるように水
を供給し、上記容器内の土壌層の下側に収容された気体
と水が流動可能な透水層に上記汚染空気中の粉塵が付着
すると共に、上記容器の底部または上記底部の近傍に設
けられた排水部によって、上記給水部から土壌層と透水
層とを介して流動してきた水を排水するものであり、上
記土壌層と上記活性炭層との間に設けた遮水通気層は、
水を通過させずに気体のみを通過させるものである。
As is clear from the above, the polluted air purifying apparatus according to the invention of claim 1 has a container, a soil layer housed in the container, in which microorganisms can propagate, and air can flow, housed in the upper side of the soil layer into the container, and an air is flowable activated charcoal layer state, and are not passing contaminated air into the soil layer and the activated carbon layer from the bottom of the soil layer by the air flow section, Installed above the soil layer in the container
With the water supply part installed, water flows downward.
The gas stored under the soil layer in the container
The dust in the contaminated air adheres to the water-permeable permeable layer.
And at the bottom of the container or near the bottom.
Soil layer and water permeability from the above water supply section
Drains the water that has flowed through the bed and
The impermeable aeration layer provided between the soil layer and the activated carbon layer,
Ru der lets through only the gas without passing through the water.

【0027】したがって、請求項の発明の汚染空気浄
化装置によれば、上記汚染空気中に含まれる粉塵が上記
容器内の土壌層の土壌粒子に付着すると共に、炭酸ガス
等の炭化物や窒素酸化物等の有害物質を土壌中の微生物
で無害な物質に分解し、さらに、汚染空気中の窒素酸化
物のうち、土壌層で処理されずに残った窒素酸化物を活
性炭層で吸着させることによって、処理効率を落とすこ
となく、炭化物と窒素酸化物の両方を処理できるので、
簡単な構成で炭酸ガス,窒素酸化物および粉塵等を効果
的に除去することができ、低コストで汚染空気を浄化す
ることができる。
Therefore, according to the polluted air purifying apparatus of the first aspect of the present invention, the dust contained in the polluted air adheres to the soil particles in the soil layer in the container, and at the same time, the carbon dioxide and other carbides and nitrogen oxides. By decomposing harmful substances such as substances into harmless substances by microorganisms in the soil, and further adsorbing nitrogen oxides remaining in the polluted air that have not been treated in the soil layer in the activated carbon layer. Since both carbides and nitrogen oxides can be processed without reducing the processing efficiency,
With a simple structure, carbon dioxide, nitrogen oxides, dust, etc. can be effectively removed, and polluted air can be purified at low cost.

【0028】また、上記容器内の上記土壌層の上側に設
けられた給水部によって、下方に向けて流れるように水
を供給し、上記容器内の土壌層の下側に収容された気体
と水が流動可能な透水層に上記汚染空気中の粉塵が付着
すると共に、上記容器の底部または上記底部の近傍に設
けられた排水部によって、上記給水部から土壌層と透水
層とを介して流動してきた水を排水するので、上記給水
部からの水の供給により、汚染空気の通過に伴って土壌
層に含まれる水が蒸発して乾燥により微生物が減少する
ということがなく、微生物による有害物質の分解効率の
低下を防ぐと共に、汚染物質に含まれる二酸化窒素が水
に溶解しやすく、水に溶けて亜硝酸や硝酸に変化するの
で、二酸化窒素の処理効率が向上し、さらに、汚染空気
に含まれる粉塵が透水層や土壌層に付着した後、上記給
水部から土壌層と透水層とを介して流動する水によって
粉塵を洗い流して、排水部より外部に排水することがで
きる。
In addition, it is installed above the soil layer in the container.
With the water supply part installed, water flows downward.
The gas stored under the soil layer in the container
The dust in the contaminated air adheres to the water-permeable permeable layer.
And at the bottom of the container or near the bottom.
Soil layer and water permeability from the above water supply section
The water flowing through the bed is drained, so
Supply of water from some parts of the soil
The water contained in the layer evaporates and the microorganisms decrease due to drying
Of the efficiency of decomposition of harmful substances by microorganisms
In addition to preventing deterioration, nitrogen dioxide contained in pollutants
Easily dissolves in water and dissolves in water to change to nitrous acid or nitric acid
It improves the treatment efficiency of nitrogen dioxide,
After the dust contained in is attached to the permeable layer or soil layer,
By the water flowing from the water part through the soil layer and the permeable layer
Dust can be washed out and drained from the drainage unit to the outside.
Wear.

【0029】さらに、上記土壌層と上記活性炭層との間
に設けた遮水通気層は、水を通過させずに気体のみを通
過させるので、上記給水部により供給された水が上記土
壌層側から上記活性炭層に染み込むのを防いで、活性炭
による窒素酸化物等の吸収効率が低下するのを防止する
ことができる。
Further, between the soil layer and the activated carbon layer
The impermeable ventilation layer provided on the
The water supplied by the water supply section
The activated carbon is prevented from seeping into the activated carbon layer from the loam layer side.
To prevent the absorption efficiency of nitrogen oxides, etc. from decreasing due to
be able to.

【0030】また、請求項の発明の汚染空気浄化装置
は、請求項の汚染空気浄化装置において、上記活性炭
層は、活性炭に微生物が繁殖可能な土壌を混合した土壌
混合活性炭層であるので、窒素酸化物等の有害物質を活
性炭に吸着できると同時に、その土壌混合活性炭層の土
壌中の微生物で無害な物質にさらに分解することができ
る。
Further, the polluted air purifying apparatus of the invention of claim 2 is the polluted air purifying apparatus of claim 1 , wherein the activated carbon layer is a soil-mixed activated carbon layer in which activated carbon is mixed with soil in which microorganisms can propagate. It is possible to adsorb harmful substances such as nitrogen oxides on activated carbon, and at the same time, further decompose them into substances harmless by microorganisms in the soil of the soil-mixed activated carbon layer.

【0031】また、請求項の発明の汚染空気浄化装置
は、請求項1または2の汚染空気浄化装置において、上
記給水部から上記土壌層と上記透水層とを介して流動し
てきた水を上記透水層で貯留可能なように、上記排水部
に開閉弁を設けたので、上記開閉弁の閉状態にすること
によって、上記透水層に水を貯留させて、上記透水層に
付着した粉塵を貯留水に溶かし、上記開閉弁の開状態に
することによって、上記容器外に排出することができ
る。
Further, the polluted air purifying apparatus of the invention of claim 3 is the polluted air purifying apparatus of claim 1 or 2 , wherein the water flowing from the water supply section through the soil layer and the permeable layer is Since the on-off valve is provided in the drainage portion so that the water can be stored in the water-permeable layer, by closing the on-off valve, water is stored in the water-permeable layer and dust adhering to the water-permeable layer is stored. It can be discharged to the outside of the container by dissolving it in water and opening the on-off valve.

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

【図1】 図1はこの発明の実施の一形態の汚染空気浄
化装置の断面図である。
FIG. 1 is a sectional view of a polluted air purifying apparatus according to an embodiment of the present invention.

【図2】 図2は図1のII−II線から見た断面図であ
る。
FIG. 2 is a sectional view taken along line II-II of FIG.

【図3】 図3は上記汚染空気浄化装置を用いた実験に
おける線速度とCO除去率との関係を示す図である。
FIG. 3 is a diagram showing a relationship between a linear velocity and a CO removal rate in an experiment using the above polluted air purifying apparatus.

【図4】 図4は上記汚染空気浄化装置を用いた実験に
おける線速度とNO除去率との関係を示す図である。
FIG. 4 is a diagram showing a relationship between a linear velocity and an NO removal rate in an experiment using the above polluted air purifying apparatus.

【図5】 図5は上記汚染空気浄化装置を用いた実験に
おける線速度と粉塵除去率との関係を示す図である。
FIG. 5 is a diagram showing a relationship between a linear velocity and a dust removal rate in an experiment using the polluted air purifying apparatus.

【符号の説明】[Explanation of symbols]

1…容器、2…玉砂利層、 3…支持層、4…土壌層、 5…遮水通気層、6…活性炭層、 11…エアーポンプ、12…流量コントローラ、 13…送気管、14…貯留水、 15…排水管、16…開閉弁、 21…水槽、22…開閉弁、23…送水管。 1 ... container, 2 ... gravel layer, 3 ... Support layer, 4 ... Soil layer, 5 ... Water-permeable ventilation layer, 6 ... Activated carbon layer, 11 ... Air pump, 12 ... Flow controller, 13 ... air supply pipe, 14 ... reserved water, 15 ... drain pipe, 16 ... open / close valve, 21 ... Water tank, 22 ... On-off valve, 23 ... Water pipe.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI B01D 53/56 B01D 53/34 116A 53/81 (56)参考文献 特開 平8−299749(JP,A) 特開 平7−299325(JP,A) 特開 平5−4020(JP,A) 特開 昭62−97628(JP,A) 特開 平7−24242(JP,A) 特開 平5−4019(JP,A) 特開 平10−128043(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 53/34 - 53/85 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI B01D 53/56 B01D 53/34 116A 53/81 (56) Reference JP-A-8-299749 (JP, A) JP-A-7 -299325 (JP, A) JP 5-4020 (JP, A) JP 62-97628 (JP, A) JP 7-24242 (JP, A) JP 5-4019 (JP, A) ) JP-A-10-128043 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) B01D 53/34-53/85

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 容器と、 上記容器内に収容され、微生物が繁殖可能でかつ空気が
流動可能な土壌層と、 上記容器内に上記土壌層の上側に収容され、空気が流動
可能な活性炭層と、 上記土壌層の下方から上記土壌層と上記活性炭層とに汚
染空気を通過させる空気流動部と 上記容器内の上記土壌層の上側に設けられ、下方に向け
て流れるように水を供給する給水部と、 上記容器内の上記土壌層の下側に収容され、気体と水が
流動可能でかつ上記汚染空気中の粉塵が付着する透水層
と、 上記容器の底部または上記底部の近傍に設けられ、上記
給水部から上記土壌層と上記透水層とを介して流動して
きた水を排水する排水部とを備え、 上記土壌層と上記活性炭層との間に、水を通過させずに
気体のみを通過させる遮水通気層を設け たことを特徴と
する汚染空気浄化装置。
1. A container, a soil layer contained in the container, in which microorganisms can propagate, and air can flow, and an activated carbon layer contained in the container above the soil layer and in which air can flow. When an air flow section for passing contaminated air from below the soil layer and the soil layer and the active carbon layer is provided on the upper side of the soil layer of the vessel, downwardly
And a water supply unit that supplies water so that the gas and water are stored under the soil layer in the container.
Water-permeable layer that is flowable and to which dust in the contaminated air adheres
And provided near the bottom of the container or the bottom,
Flow from the water supply through the soil layer and the permeable layer
A drainage part for draining incoming water is provided, and water is not passed between the soil layer and the activated carbon layer.
A contaminated air purifying device, which is provided with an impermeable aeration layer that allows only gas to pass through .
【請求項2】 請求項に記載の汚染空気浄化装置にお
いて、 上記活性炭層は、活性炭に微生物が繁殖可能な土壌を混
合した土壌混合活性炭層であることを特徴とする汚染空
気浄化装置。
2. The polluted air purifying apparatus according to claim 1 , wherein the activated carbon layer is a soil-mixed activated carbon layer in which activated carbon is mixed with soil in which microorganisms can grow.
【請求項3】 請求項1または2に記載の汚染空気浄化
装置において、 上記給水部から上記土壌層と上記透水層とを介して流動
してきた水を上記透水層で貯留可能なように、上記排水
部に開閉弁を設けたことを特徴とする汚染空気浄化装
置。
3. The polluted air purifying apparatus according to claim 1 or 2 , wherein the water flowing from the water supply section through the soil layer and the permeable layer can be stored in the permeable layer. A polluted air purifier characterized by having an opening / closing valve in the drainage section.
JP00073198A 1998-01-06 1998-01-06 Contaminated air purification device Expired - Fee Related JP3497718B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP00073198A JP3497718B2 (en) 1998-01-06 1998-01-06 Contaminated air purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP00073198A JP3497718B2 (en) 1998-01-06 1998-01-06 Contaminated air purification device

Publications (2)

Publication Number Publication Date
JPH11192413A JPH11192413A (en) 1999-07-21
JP3497718B2 true JP3497718B2 (en) 2004-02-16

Family

ID=11481889

Family Applications (1)

Application Number Title Priority Date Filing Date
JP00073198A Expired - Fee Related JP3497718B2 (en) 1998-01-06 1998-01-06 Contaminated air purification device

Country Status (1)

Country Link
JP (1) JP3497718B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5752482B2 (en) * 2011-05-11 2015-07-22 川崎重工業株式会社 Carbon dioxide recovery device and carbon dioxide recovery system
CN103691226A (en) * 2013-12-09 2014-04-02 李刘睿 Water washing box of water washing type air purifier

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JPH11192413A (en) 1999-07-21

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