JP2901641B2 - Deodorizing device - Google Patents
Deodorizing deviceInfo
- Publication number
- JP2901641B2 JP2901641B2 JP1107783A JP10778389A JP2901641B2 JP 2901641 B2 JP2901641 B2 JP 2901641B2 JP 1107783 A JP1107783 A JP 1107783A JP 10778389 A JP10778389 A JP 10778389A JP 2901641 B2 JP2901641 B2 JP 2901641B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- humification
- tank
- organic matter
- liquid
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Treating Waste Gases (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ガス中の臭気成分を除去する脱臭装置に関
するものである。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deodorizing apparatus for removing an odor component in a gas.
従来、臭気ガスの脱臭装置として、水薬液等により臭
気成分の吸収除去が知られていたが、使用後の水,薬液
等に対しては後処理が必要になるという問題点があり、
このような問題点を排除するために、活性汚泥等の微生
物と接触させる生物脱臭装置が開発されている。Conventionally, as a deodorizing device for odor gas, absorption and removal of odor components by a liquid chemical or the like has been known. However, there is a problem that post-treatment is required for water, a chemical liquid, and the like after use.
In order to eliminate such a problem, a biological deodorizing device that comes into contact with microorganisms such as activated sludge has been developed.
しかしながら、活性汚泥等の微生物と接触させる生物
脱臭装置では、長期間酸性あるいはアルカリ性のいずれ
かに偏した臭気ガスと接触させると、pHが中性から極端
に外れて活性がなくなり、脱臭効果が低下するため、適
宜pH調整又は活性汚泥の交換を必要とするばかりか、処
理済のガス中に活性汚泥特有の臭気が残るため、脱臭の
あと又は同時に活性炭等の吸着剤を使用してさらに脱臭
を行うものが大部分であった。However, in biological deodorizers that come into contact with microorganisms such as activated sludge, when exposed to acidic or alkaline odorous gas for a long period of time, the pH deviates extremely from neutral and loses activity, and the deodorizing effect decreases. Therefore, not only is it necessary to adjust the pH or replace activated sludge as appropriate, but also because the odor peculiar to activated sludge remains in the treated gas, the deodorization can be further performed after or simultaneously with the use of an adsorbent such as activated carbon. Most did.
本発明は、液中の有機物を腐植化することによって脱
臭・酸化力を付与し、これらの液に臭気ガスを接触せし
めて極めて有利に脱臭を行うことができ、さらに、前記
有機物として活性汚泥を利用することにより、活性汚泥
自身のもつ脱臭効果を加え、より強力で効果的な脱臭を
行うことができる脱臭装置を提供することを目的とす
る。The present invention imparts deodorizing and oxidizing power by humifying organic substances in a liquid, makes it possible to very effectively deodorize the liquid by contacting an odor gas with these liquids, and furthermore, activates sludge as the organic substance. It is an object of the present invention to provide a deodorizing apparatus capable of adding a deodorizing effect of activated sludge by using the same, and performing more powerful and effective deodorizing.
上記目的を達成するため、請求項1に係る発明は、有
機物を含む液を腐植化するための腐植化促進剤を備えた
腐植化槽と、腐植化された有機物を含む液をスプレーす
るスプレー塔を備え、前記スプレー塔の下底部に溜まる
腐植化された有機物を含む液を循環ポンプでスプレー塔
の上部と前記腐植化槽の下部へ送出し、腐植化槽の上部
から排出される腐植化された有機物を含む液を気液分離
器を介して前記スプレー塔の上部に循環させるととも
に、臭気ガスを前記腐植化槽とスプレー塔の下部に通気
し、腐植化槽の上部から出てくる臭気ガスを気液分離器
で分離してスプレー塔の下部に供給し、臭気ガスをスプ
レー塔内において腐植化された有機物を含む液に接触さ
せることにより脱臭するようにしたものであるものであ
る。In order to achieve the above object, the invention according to claim 1 provides a humification tank provided with a humification accelerator for humifying a liquid containing organic matter, and a spray tower for spraying a liquid containing humified organic matter. The liquid containing humidified organic matter that accumulates at the lower bottom of the spray tower is sent to the upper part of the spray tower and the lower part of the humification tank by a circulation pump, and the humified substance discharged from the upper part of the humification tank is discharged. Circulating the liquid containing the organic matter to the upper part of the spray tower through a gas-liquid separator, and passing the odor gas to the humification tank and the lower part of the spray tower, and the odor gas coming out of the upper part of the humification tank. Is separated by a gas-liquid separator, supplied to the lower part of the spray tower, and deodorized by bringing the odor gas into contact with a liquid containing humified organic matter in the spray tower.
また、請求項2に係る発明は、請求項1に係る発明に
おいて、前記有機物を含む液が活性汚泥混合液であるこ
とを特徴とするものである。The invention according to a second aspect is the invention according to the first aspect, wherein the liquid containing the organic matter is an activated sludge mixed liquid.
本発明の場合、臭気ガスに含まれる空気によってエア
レーションすることにより、好気的条件下で有機物を含
む液を腐植化促進剤によって腐植化し、この腐植化され
た促進剤を含む液をスプレー塔で臭気ガスと接触させる
ことにより脱臭する。このように、本発明では、液中の
有機物を腐植化することによって脱臭、酸化力を付与し
ているので、液のpHが中性から極端に外れて活性がなく
なることがなく、大きな脱臭効果を発揮することができ
る。In the case of the present invention, by aeration with air contained in the odorous gas, the liquid containing organic matter is humidified by the humification accelerator under aerobic conditions, and the liquid containing the humidified accelerator is sprayed with a spray tower. Deodorizes by contact with odorous gas. As described above, in the present invention, the deodorizing and oxidizing power is imparted by humifying the organic matter in the liquid, so that the pH of the liquid does not extremely deviate from neutrality and the activity is not lost, and a large deodorizing effect is obtained. Can be demonstrated.
また、前記有機物を含む液として、下水処理,し尻処
理,一般排水処理などで利用される活性汚泥混合液(濃
縮された活性汚泥を含む)を利用した場合、腐植化した
活性汚泥は、腐植質のもつカルボキシル基や水酸基など
の官能基を有し、酸化・置換反応が強くなり、その作用
による脱臭が活性汚泥自身のもつ生物脱臭能力に補強さ
れることになり、酸化還元電位も高く保持されて脱臭が
一層効果的に行われる。さらに、腐植化活性汚泥自身も
活性汚泥特有の臭気が消えるので、この腐植化活性汚泥
で脱臭されたガスは一般の活性汚泥による脱臭ガスより
無臭化される。In addition, when an activated sludge mixture solution (including concentrated activated sludge) used in sewage treatment, butt sewage treatment, general wastewater treatment, or the like is used as the liquid containing the organic matter, the activated humus that has become humus becomes humus. It has functional groups such as carboxyl group and hydroxyl group, which have strong oxidation and substitution reactions, and the deodorization by its action is reinforced by the biological deodorization ability of the activated sludge itself, and the redox potential is also kept high The deodorization is performed more effectively. Furthermore, since the odor peculiar to activated sludge disappears in the activated humus itself, the gas deodorized by the activated humus is made more odorless than the deodorized gas generated by general activated sludge.
また、腐植化活性汚泥は、普通の活性汚泥よりもさら
に強いpH緩衝力をもつので、酸性側又はアルカリ性側に
偏した臭気ガスを処理してもpHの変動はほとんどなく、
pH調整が全く必要なくなり、そのままで長期間脱臭処理
を行うことができる。In addition, humus activated sludge has a stronger pH buffering power than ordinary activated sludge, so even if an odor gas biased toward the acidic side or alkaline side is treated, there is almost no change in pH,
There is no need for pH adjustment, and deodorization can be performed for a long period of time.
第1図に、本発明に係る脱臭装置の一実施例を示す。 FIG. 1 shows an embodiment of a deodorizing apparatus according to the present invention.
図において、3は処理対象とする臭気ガス、4は処理
対象とする臭気ガス3の一部を槽下部から導入し、槽内
に貯溜された有機物を含む液を前記導入される臭気ガス
によってエアレーションしながら腐植化促進剤7によっ
て腐植化する腐植化槽、5は腐植化槽4から排出される
腐植化有機物を含む液と臭気ガスとを気液分離し、分離
された腐植化有機物を含む液を前記スプレー塔6の天井
部から槽内に供給すると共に、分離された臭気ガスをス
プレー塔内6の下部から槽内に供給する気液分離器、6
は処理対象とする臭気ガス3を槽下部から導入し、該臭
気ガス3を腐植化有機物を含む液と接触させることによ
って脱臭し、脱臭後の処理ガスを槽上部から外部へ排出
するスプレー塔、7は腐植化槽4内に収納された腐植化
促進剤、8は前記スプレー塔6の下部に溜まった脱臭処
理後の腐植化有機物を含む液を前記腐植化槽7に貫流し
て戻すと共に、該脱臭処理後の腐植化有機物を含む液の
一部をスプレー塔6の天井部から槽内に再供給する循環
ポンプである。In the figure, reference numeral 3 denotes an odor gas to be treated, and 4 denotes a part of the odor gas 3 to be treated introduced from the lower portion of the tank, and a liquid containing organic matter stored in the tank is aerated by the introduced odor gas. While the humification tank 5 is humified by the humification accelerator 7, the humidification tank 5 gas-liquid separates the liquid containing humified organic matter and the odor gas discharged from the humification tank 4, and the liquid containing the separated humified organic matter. A gas-liquid separator, which supplies the separated odor gas into the tank from the lower part of the spray tower 6 while supplying the separated odor gas into the tank from the ceiling of the spray tower 6.
A spray tower for introducing odor gas 3 to be treated from the lower part of the tank, deodorizing the odor gas 3 by bringing the odor gas 3 into contact with a liquid containing humic organic matter, and discharging the deodorized processing gas from the upper part of the tank to the outside; 7 is a humification accelerator contained in the humification tank 4, 8 is a liquid containing humic organic matter after deodorization treatment accumulated in the lower part of the spray tower 6, flowing back to the humification tank 7, This is a circulating pump for re-supplying a part of the liquid containing humic organic matter after the deodorizing treatment from the ceiling of the spray tower 6 into the tank.
図示装置において、臭気ガスの脱臭処理は次のように
して行われる。In the illustrated apparatus, the odor gas is deodorized as follows.
腐植化糟4内において、腐植化促進剤7と有機物含有
液とを送給されてくる臭気ガス3によるエアレーション
による好気的条件下で接触させ、液中の有機物を腐植化
する。次いで、腐植化槽4の槽上部から排出される前記
腐植化有機物を含む液を気液分離器5でガスと液に分離
し、分離された腐植化有機物を含む液をスプレー塔6に
送り、天井部から槽内にスプレーする。In the humification chamber 4, the humification accelerator 7 and the organic substance-containing liquid are brought into contact under aerobic conditions by aeration by the odor gas 3 supplied thereto to humify the organic substances in the liquid. Next, the liquid containing the humified organic matter discharged from the upper part of the humification tank 4 is separated into gas and liquid by the gas-liquid separator 5, and the separated liquid containing the humified organic matter is sent to the spray tower 6, Spray into the tank from the ceiling.
スプレー塔6では、処理対象とする臭気ガス3と気液
分離器5で分離されたガスを槽下部から引き込むことに
より槽内を通過させるスクラバー方式で前記天井部から
スプレーされる腐植化有機物を含む液と接触させ、臭気
ガスの悪臭を脱臭した後、脱臭後の処理ガスを槽上部か
ら外部へ排出する。そして、槽内下部に至った処理後の
液の一部を循環ポンプ8によって再び天井部に循環して
スプレーすると共に、残りの液は再び腐食化糟4に返送
し、腐植化槽4において活性化して再使用する。このよ
うにして、有機物を含む液を取り替えることなしに長期
にわたって臭気ガスの脱臭を効果的に行うことができ
る。The spray tower 6 contains humic organic matter sprayed from the ceiling by a scrubber method in which the odor gas 3 to be treated and the gas separated by the gas-liquid separator 5 are drawn from the lower part of the tank and passed through the tank. After contact with the liquid to deodorize the odor of the odorous gas, the deodorized processing gas is discharged from the upper part of the tank to the outside. Then, a part of the treated liquid reaching the lower part in the tank is again circulated to the ceiling by the circulating pump 8 and sprayed, and the remaining liquid is returned to the corrosion tank 4 again and activated in the humification tank 4. And reuse. In this manner, the odor gas can be effectively deodorized for a long period of time without replacing the liquid containing an organic substance.
なお、腐槽化促進剤7としては、フミン酸,フルボ
酸,有機酸などを主成分とする腐植物質と、反応促進剤
としての鉄粉その他の鉄金属化合物を損糠してペレット
状に形成したものを使用する。この腐植化促進剤を有機
物を含む液中に0.01〜10重量%程度の割合で加えてエア
レーションすると、液中の有機物は腐植化され、カルボ
キシル基や水酸基などの官能基を有するようになり、酸
化・置換反応作用が強くなる。従って、この腐植化有機
物を含む液と臭気ガスとを接触させることによって効果
的な脱臭が行われる。As the humidification promoting agent 7, humic substances mainly containing humic acid, fulvic acid, organic acid and the like, and iron powder and other iron metal compounds as reaction accelerators are spoiled to form pellets. Use what you have done. When this humidification accelerator is added to a liquid containing an organic substance at a rate of about 0.01 to 10% by weight and aerated, the organic substance in the liquid is humidified and comes to have a functional group such as a carboxyl group or a hydroxyl group. -The substitution reaction becomes stronger. Therefore, effective deodorization is performed by bringing the liquid containing the humic organic matter into contact with the odorous gas.
また、前記腐植化槽4に貯溜する有機物を含む液とし
て、下水処理,し尻処理、一般排水処理などで利用され
る活性汚泥混合液を用いた場合、前述したように酸化・
置換反応がより強くなり、脱臭が一層効果的に行われ
る。When the activated sludge mixed liquid used in the sewage treatment, the butt sewage treatment, the general wastewater treatment and the like is used as the liquid containing the organic matter stored in the humification tank 4, as described above, the oxidation /
The substitution reaction becomes stronger, and deodorization is performed more effectively.
有機物含有液として活性汚泥混合液を使用した実験例
を以下に示す。An experimental example using an activated sludge mixed liquid as the organic substance-containing liquid is shown below.
活性汚泥混合液15l中に腐植化促進剤を7量%投入
し、エアレーションしながら約1ケ月間液中の有機物の
腐植化を続け、充分に腐植を進ませた腐植化活性汚泥を
得た。この腐植化活性汚泥のMLSSは3600〜4100mg/lで、
酸素呼吸速度は0.1〜1.1mg・O2/g・hであった。7% by weight of a humification accelerator was added to 15 liters of the activated sludge mixture, and humification of the organic matter in the liquid was continued for about one month while aeration was performed to obtain a humified activated sludge which had sufficiently advanced humus. MLSS of this humidification activated sludge is 3600-4100mg / l,
The oxygen respiration rate was 0.1-1.1 mg · O 2 / g · h.
まず、この腐植化活性汚泥中にH2Sの臭気ガスを吹き
込んで脱臭した結果は、第2図に示す通りであった。即
ち、H2Sの除去率をみると、実験開始後約1週間は不規
則な除去率を示したが、その後は漸次上昇し、約2週間
後には99%以上の除去率を示した。First, the result of deodorizing the humidified activated sludge by blowing odor gas of H 2 S into the activated humus was as shown in FIG. That is, the removal rate of H 2 S showed an irregular removal rate for about one week after the start of the experiment, but gradually increased thereafter, and showed a removal rate of 99% or more after about two weeks.
また、NH3の臭気ガスの場合は、第3図に示すよう
に、実験開始時から100%の除去率であった。In the case of the odor gas of NH 3 , as shown in FIG. 3, the removal rate was 100% from the start of the experiment.
さらに、前記H2S及びNH3の臭気ガス吹込みをそれぞれ
16時間中断した場合のpHの回復状況は、第4図に示すよ
うに、H2Sで0.2〜0.5、NH3で0.2〜0.3のpH回復能力を持
っていた。Further, the odor gas injection of the H 2 S and NH 3 was respectively performed.
As shown in FIG. 4, when the suspension was carried out for 16 hours, H 2 S had a pH recovery ability of 0.2 to 0.5 and NH 3 had a pH recovery ability of 0.2 to 0.3.
以上述べたように、請求項1に係る発明によれば、酸
性,アルカリ性のいずれの臭気ガスにも十分な脱臭力を
持ち、確実な脱臭を行うことができると共に、その強い
pH緩衝力によってpH調整等の必要を無くし、長期間にわ
たって効率のよい脱臭を持続することができる。As described above, according to the first aspect of the present invention, both the acidic and alkaline odor gases have a sufficient deodorizing power, and can reliably perform deodorization.
The need for pH adjustment or the like is eliminated by the pH buffering power, and efficient deodorization can be maintained for a long period of time.
また、請求項2に係る発明によれば、前記効果に加
え、酸化・置換反応がより強くなり、この酸化・還元作
用による脱臭が活性汚泥自身の持つ生物脱臭能力に補強
されるため、酸化・還元電位も高く保持され、脱臭をよ
り一層効果的に行うことができるものである。According to the second aspect of the present invention, in addition to the above effects, the oxidation / substitution reaction becomes stronger, and the deodorization due to this oxidation / reduction action is reinforced by the biological deodorization ability of the activated sludge itself. The reduction potential is also kept high, and deodorization can be performed more effectively.
第1図は本発明の一実施例を示す装置構成図、 第2図は本発明の実験例における経過日数に対するH2S
の入口濃度と除去率を示す線図、 第3図は本発明の実験例における経過日数に対するNH3
の入口濃度と除去率を示す線図、 第4図はH2SとNH3のそれぞれの脱臭時の経過時間に対す
るpHの回復状況を示す線図である。 3…臭気ガス 4…腐植化槽 5…気液分離器 6…スプレー塔 7…腐植化促進剤 8…循環ポンプFIG. 1 is an apparatus configuration diagram showing one embodiment of the present invention, and FIG. 2 is H 2 S with respect to elapsed days in an experimental example of the present invention.
FIG. 3 is a graph showing the inlet concentration and removal rate of NH 3, and FIG.
FIG. 4 is a graph showing the recovery status of pH with respect to the elapsed time at the time of deodorization of each of H 2 S and NH 3. 3 ... odor gas 4 ... humification tank 5 ... gas-liquid separator 6 ... spray tower 7 ... humification accelerator 8 ... circulation pump
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) B01D 53/38 B01D 53/77 ──────────────────────────────────────────────────続 き Continued on the front page (58) Fields surveyed (Int.Cl. 6 , DB name) B01D 53/38 B01D 53/77
Claims (2)
促進剤を備えた腐植化槽と、腐植化された有機物を含む
液をスプレーするスプレー塔を備え、 前記スプレー塔の下底部に溜まる腐植化された有機物を
含む液を循環ポンプでスプレー塔の上部と前記腐植化槽
の下部へ送出し、 腐植化槽の上部から排出される腐植化された有機物を含
む液を気液分離器を介して前記スプレー塔の上部に循環
させるとともに、臭気ガスを前記腐植化槽とスプレー塔
の下部に通気し、腐植化槽の上部から出てくる臭気ガス
を気液分離器で分離してスプレー塔の下部に供給し、 臭気ガスをスプレー塔内において腐植化された有機物を
含む液に接触させることにより脱臭することを特徴とす
る脱臭装置。1. A humification tank provided with a humification accelerator for humifying a liquid containing organic matter, a spray tower for spraying a liquid containing humified organic matter, and a lower bottom part of the spray tower. The liquid containing the accumulated humified organic matter is sent to the upper part of the spray tower and the lower part of the humification tank by a circulation pump, and the liquid containing the humified organic matter discharged from the upper part of the humification tank is separated into a gas-liquid separator. While circulating the odor gas through the upper part of the spray tower, passing the odor gas through the humification tank and the lower part of the spray tower, separating the odor gas coming out from the upper part of the humification tank with a gas-liquid separator, and spraying. A deodorizing device, which is supplied to a lower portion of a tower and deodorizes the odorous gas by bringing the odorous gas into contact with a liquid containing humified organic matter in a spray tower.
ることを特徴とする請求項1記載の脱臭装置。2. The deodorizing apparatus according to claim 1, wherein the liquid containing the organic substance is an activated sludge mixed liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1107783A JP2901641B2 (en) | 1989-04-28 | 1989-04-28 | Deodorizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1107783A JP2901641B2 (en) | 1989-04-28 | 1989-04-28 | Deodorizing device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02290224A JPH02290224A (en) | 1990-11-30 |
| JP2901641B2 true JP2901641B2 (en) | 1999-06-07 |
Family
ID=14467909
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1107783A Expired - Fee Related JP2901641B2 (en) | 1989-04-28 | 1989-04-28 | Deodorizing device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2901641B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117244392A (en) * | 2023-09-21 | 2023-12-19 | 华南理工大学 | A kind of biological filler and its preparation method and application |
-
1989
- 1989-04-28 JP JP1107783A patent/JP2901641B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117244392A (en) * | 2023-09-21 | 2023-12-19 | 华南理工大学 | A kind of biological filler and its preparation method and application |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02290224A (en) | 1990-11-30 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |