JP2001070746A - Deodorization method and apparatus - Google Patents

Deodorization method and apparatus

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Publication number
JP2001070746A
JP2001070746A JP25174699A JP25174699A JP2001070746A JP 2001070746 A JP2001070746 A JP 2001070746A JP 25174699 A JP25174699 A JP 25174699A JP 25174699 A JP25174699 A JP 25174699A JP 2001070746 A JP2001070746 A JP 2001070746A
Authority
JP
Japan
Prior art keywords
sludge
tank
deodorizing
deodorization
pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP25174699A
Other languages
Japanese (ja)
Inventor
Seiichi Futaboshi
清一 二星
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP25174699A priority Critical patent/JP2001070746A/en
Publication of JP2001070746A publication Critical patent/JP2001070746A/en
Pending legal-status Critical Current

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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

Landscapes

  • Treating Waste Gases (AREA)
  • Degasification And Air Bubble Elimination (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a deodorization apparatus capable of deororizing a large quantity of malodorous gases at a low cost using sludge (wastewater) generated in a wastewater treatment site and humus (soil) and keeping highly efficient and durable deodorization effects. SOLUTION: A deodorization tank 2 is provided with a gas diffusing diffuser 7 installed in the lower part for diffusing a malodorous gas G in sludge X in a bubble state, a sludge layer X stored therein, a water-permeable container 12 hung in the sludge layer X for storing a granular material of humus, a defoaming mechanism 18 for supplying activated sludge X upward through a circulation pump 15 from a sludge discharge pipe 14 and spraying the sludge X to the upper face of the sludge layer X, and a gas discharge cylinder 5 connected with a gas discharge port 4 formed in the ceiling thereof and containing an activated carbon-packed layer 6.

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、例えば、生ゴミ
や同処理機や生ゴミ処理場、ゴミ焼却場、屎尿処理場な
どにおいて発生する臭気(悪臭)をはじめ、各種の有機
性臭気を脱臭する方法とその脱臭装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to deodorizing various organic odors such as garbage and odors generated in garbage disposal machines, garbage disposal plants, garbage incineration plants, human waste treatment plants, and the like. And a deodorizing device therefor.

【0002】[0002]

【従来の技術】近年、とくに生ゴミの処理が問題になっ
ており、各種生ゴミの処理機も開発されてきている。こ
の種の処理機の場合に、内部温度が生ゴミの醗酵・分解
処理により50〜70℃に上昇する。このため、処理機
から悪臭が発生するのに加えて、臭気を送給する配管等
に生ゴミから発生した水分が結露水として生じ、その結
露水が悪臭を発生するという不具合がある。
2. Description of the Related Art In recent years, the treatment of garbage has become a problem, and various garbage processors have been developed. In the case of this type of processor, the internal temperature rises to 50 to 70 ° C. due to the fermentation / decomposition treatment of garbage. For this reason, in addition to the generation of offensive odor from the processing machine, there is a problem that water generated from garbage is generated as dew condensation water in a pipe or the like for supplying odor, and the dew condensation water generates a malodor.

【0003】従来、上記のような悪臭に対しては、化学
薬剤を噴霧させて臭気成分と化学反応させ中和して脱臭
する方法が一般的である。
[0003] Conventionally, a method of spraying a chemical agent to chemically react with odor components to neutralize and deodorize such malodors is generally used.

【0004】その他の先行技術に、特開平8−1641
92号公報に記載のように、数種類の植物を原料として
それらの葉や茎などを真空乾留法または圧搾法と、真空
蒸留法と、精製と、脱色と、熟成との各工程を経て得ら
れた消臭エキスに、水で希釈した超酸化水を添加して混
合した植物性脱臭剤が提案されている。
[0004] Other prior arts include Japanese Patent Application Laid-Open No. 8-16441.
As described in JP-A-92-92, several kinds of plants are used as raw materials and their leaves and stems are obtained through the steps of vacuum distillation or squeezing, vacuum distillation, purification, decolorization, and aging. A vegetable deodorant has been proposed in which superoxidized water diluted with water is added to a deodorant extract and mixed.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記し
た従来の化学薬剤からなる脱臭剤により脱臭する方法で
は、次のような問題がある。
However, the above-mentioned conventional method for deodorizing with a deodorant comprising a chemical agent has the following problems.

【0006】 発生している臭気成分を化学的に中和
し、脱臭するものであるから、いいかえれば臭気成分の
発生源を根源から断つものでないから、持続性がなく、
頻繁に化学薬剤を散布する必要がある。
[0006] Since the generated odor component is chemically neutralized and deodorized, in other words, the source of the odor component is not cut off from the root, so there is no persistence.
Frequent application of chemicals is required.

【0007】 化学薬剤であるから、長期にわたり使
用すると周辺の環境に害を及ぼすおそれがあるうえに、
動植物に対しても悪影響を及ぼすおそれがある。
[0007] Since it is a chemical agent, if it is used for a long time, it may harm the surrounding environment.
It can also have a negative effect on animals and plants.

【0008】 上記公報に記載の植物性脱臭剤の場
合、製造工程が複雑で、大量生産に不向きであり、また
脱臭剤としての脱臭効果が遮光密閉容器に保存しても1
カ月程度と非常に短い。
[0008] In the case of the plant deodorant described in the above publication, the production process is complicated and is not suitable for mass production.
Very short, about a month.

【0009】 とくに上記した生ゴミや生ゴミ処理機
から発生する結露水の悪臭に対しては、薬剤を用いて化
学的に中和し脱臭する方法では、臭気を十分に消すこと
が困難なうえに、生ゴミの量は膨大で、薬剤で対応する
ことは、コスト面だけでなく、社会環境のうえからも問
題視されている。
[0009] In particular, it is difficult to sufficiently eliminate the odor by the method of chemically neutralizing and deodorizing the above-mentioned garbage and dew condensation water generated from the garbage disposal machine by using a chemical. In addition, the amount of garbage is enormous, and responding with chemicals is a problem not only in terms of cost but also in terms of the social environment.

【0010】この発明は上述の点に鑑みなされたもの
で、汚水処理場で発生する汚泥(汚水)と腐植(土)を
使用して安価で大量な臭気ガスの脱臭処理が可能で、し
かも脱臭効果が高く持続性を具備する脱臭方法とその脱
臭装置とを提供することを目的としている。
The present invention has been made in view of the above points, and it is possible to use a sludge (sewage) and a humus (soil) generated at a sewage treatment plant to deodorize a large amount of odorous gas at a low cost. It is an object of the present invention to provide a deodorizing method and a deodorizing device which have high effects and have a high sustainability.

【0011】[0011]

【課題を解決するための手段】上記の目的を達成するた
めに本発明に係る脱臭方法は、脱臭槽に汚泥を貯留し、
該汚泥に対し0.5〜1.0重量%の腐植(腐植土を含
む)を投入して活性化させた状態で、前記脱臭槽内の汚
泥中に空気を導入して空気撹拌による初期調整を行って
前記汚泥の活性化と安定化を図った後、生ゴミ等から発
生する臭気ガスを、前記脱臭槽内の汚泥中に微細な気泡
状態にして導入し、活性化させた汚泥に接触させて臭気
ガスを分解し脱臭することを特徴としている。
Means for Solving the Problems To achieve the above object, a deodorizing method according to the present invention comprises storing sludge in a deodorizing tank,
With the humus (including humus) of 0.5 to 1.0% by weight added to the sludge and activated, air is introduced into the sludge in the deodorization tank to perform initial adjustment by air stirring. After activating and stabilizing the sludge, odor gas generated from garbage and the like is introduced into the sludge in the deodorization tank in the form of fine bubbles, and comes into contact with the activated sludge. The odor gas is decomposed and deodorized.

【0012】上記の構成を有する本発明の脱臭方法によ
れば、脱臭槽内に貯留された汚泥中において投入された
腐植中の土壌菌群(通性嫌気バクテリアと、好気性バク
テリア、若しくは通性嫌気バクテリアと好気性バクテリ
アのバクテリア群)が汚泥中の諸成分を栄養源として培
養される。一方、汚泥は土壌菌群の繁殖により熟成し活
性化される。本来、土壌菌群中のバクテリアが代謝産物
(分泌物)を産出するが、その代謝産物が脱臭成分つま
り臭気除去成分を具有しているので、脱臭機能が発揮さ
せれるものである。また、好気性および通性嫌気バクテ
リアなどの土壌菌が産出する分泌物には、殺菌作用や抗
菌作用もあるため、脱臭効果だけでなく抗菌効果も同時
に生じる。さらに、腐植を使用するのはとくに好気性お
よび通性嫌気バクテリアの含有量が多く腐敗菌の増殖を
防止し、また品質の良い腐植が比較的容易にかつ安価に
得られるからである。
[0012] According to the deodorizing method of the present invention having the above-described structure, the soil bacteria group (humid anaerobic bacteria, aerobic bacteria, or facultative bacteria) in the humus introduced into the sludge stored in the deodorizing tank. An anaerobic bacterium and an aerobic bacterium group are cultivated using various components in the sludge as a nutrient source. On the other hand, sludge is matured and activated by propagation of soil fungi. Bacteria in the soil fungi naturally produce metabolites (secretions), but the metabolites have a deodorizing component, that is, an odor removing component, so that the deodorizing function can be exerted. In addition, since secretions produced by soil bacteria such as aerobic and facultative anaerobic bacteria have a bactericidal action and an antibacterial action, not only a deodorizing effect but also an antibacterial effect occur simultaneously. Furthermore, humus is used because it has a particularly high content of aerobic and facultative anaerobic bacteria to prevent the growth of spoilage bacteria, and it is possible to obtain high-quality humus relatively easily and inexpensively.

【0013】そして、本発明の脱臭方法によると、脱臭
槽内に貯留されている活性化された汚泥に導入された臭
気ガスが散気分散されて効率よく接触し、ガス中の悪臭
成分と土壌菌群のバクテリアが産出する代謝産物が具有
している脱臭成分とが反応して、悪臭成分である揮発性
物質を固定化したり、さらに分解して臭気成分の発散を
防止したりすることによって、脱臭作用を発揮する。な
お、汚泥に対する腐植の投入割合が、0.5%未満にな
ると、汚泥の活性化が遅くなるため、短期間で効率よく
活性化させるためには0.5%以上にする必要がある。
一方、1.0%を超えても問題はないが、経済性を考え
ると1.0%程度までにするのがよい。ところで、本明
細書で、腐植とは、土壌や石炭などに含まれる動植物が
分解してできた黒褐色の有機質をいい、詳しくは、腐植
は植物や動物が微生物によって分解され、炭酸ガス、
水、アンモニア等の無機ガスとともに、糖類、キノン
類、アミノ酸、タンパク質等の低分子有機物ができ、こ
れらの低分子有機物が脱水結合を繰り返して高分子の再
合成産物となるが、この再合成産物と分解途上および未
分解有機物の総称であり、当然に、腐植土も入る。
According to the deodorizing method of the present invention, the odor gas introduced into the activated sludge stored in the deodorizing tank is diffused and dispersed, and efficiently comes into contact with each other. By reacting with deodorizing components possessed by metabolites produced by bacteria of the bacteria group to fix volatile substances, which are malodorous components, and to further decompose to prevent emission of odor components, Deodorizes. In addition, when the input ratio of humus to sludge is less than 0.5%, the activation of sludge is delayed. Therefore, in order to efficiently activate sludge in a short period of time, it is necessary to be 0.5% or more.
On the other hand, although there is no problem if it exceeds 1.0%, it is preferable to set it to about 1.0% in consideration of economy. By the way, in this specification, humus refers to black-brown organic matter formed by the decomposition of animals and plants contained in soil, coal, and the like.Specifically, humus is the decomposition of plants and animals by microorganisms, carbon dioxide,
Water, inorganic gases such as ammonia, and low molecular organic substances such as sugars, quinones, amino acids, and proteins are formed, and these low molecular organic substances repeat the dehydration bond to become high molecular resynthesis products. And undecomposed organic matter, and naturally includes humus.

【0014】請求項2に記載のように、前記汚泥の濃度
を3,000〜12,000mg/lに保持するととも
に、前記臭気ガスの導入量を前記汚泥量1m3当たり3
0m3/h(時間)以下に設定することが望ましい。
According to a second aspect of the present invention, the concentration of the sludge is maintained at 3,000 to 12,000 mg / l, and the amount of the odor gas introduced is reduced to 3 per m 3 of the sludge amount.
It is desirable to set it to 0 m 3 / h (time) or less.

【0015】請求項2記載の脱臭方法によれば、汚泥の
濃度3,000mg/l未満に低下すると、脱臭能力に
欠け十分な脱臭作用が得られないから、汚水処理設備か
ら汚泥を供給するか、又は有機物を多量に含む汚水を供
給することにより汚泥濃度の安定化を図る。一方、汚泥
濃度が12,000mg/lを超えると、汚泥濃度が濃
くなり、汚泥の粘性が高くなり過ぎて臭気ガスとの接触
効率が低下するからである。また臭気ガスの導入量が3
0m3/hを超えると、活性化汚泥の本来有する脱臭能
力を超え、満足のいく脱臭作用が期待できなくなるから
である。
According to the deodorizing method of the present invention, if the concentration of the sludge is reduced to less than 3,000 mg / l, sufficient deodorizing action cannot be obtained due to lack of deodorizing ability. Alternatively, the sludge concentration is stabilized by supplying wastewater containing a large amount of organic matter. On the other hand, if the sludge concentration exceeds 12,000 mg / l, the sludge concentration becomes too high, the viscosity of the sludge becomes too high, and the efficiency of contact with the odorous gas decreases. The amount of odor gas introduced is 3
If it exceeds 0 m 3 / h, the activated sludge exceeds the inherent deodorizing ability, and a satisfactory deodorizing action cannot be expected.

【0016】上記の目的を達成するための本発明の請求
項3に係る脱臭装置は、汚泥を貯留し、導入する臭気ガ
スを該汚泥に接触させて脱臭する脱臭槽を備えた脱臭装
置において、前記脱臭槽が、該槽内の下部に配設され、
前記臭気ガスを気泡状にして前記汚泥中に散気させるた
めの散気ディフューザーと、該散気ディフューザーから
汚泥の上面までの高さが600mm以上になるように貯
留される汚泥層と、該汚泥層内に吊設され腐植(腐植土
を含む)の粒状化(ペレット状)物を収容する籠などの
通水性容器と、前記脱臭槽の底部付近に設けた汚泥排出
管から循環ポンプを介して活性汚泥を上方へ送給し、脱
臭槽内の汚泥層の上面の上方に配設した消泡ノズルから
汚泥を汚泥層上面に噴射する消泡機構と、前記脱臭槽の
天井に設けた排気口に連設され排気路の途中に活性炭充
填層を設けた排気筒とを備えている。
According to a third aspect of the present invention, there is provided a deodorizing apparatus having a deodorizing tank for storing sludge, bringing an odor gas to be introduced into contact with the sludge, and deodorizing the sludge. The deodorizing tank is disposed at a lower part in the tank,
An air diffuser for bubbling the odor gas into the sludge, and a sludge layer stored so that the height from the air diffuser to the upper surface of the sludge is at least 600 mm; and Through a circulation pump from a water-permeable container such as a basket that is suspended in the bed and contains granulated (pellet-like) humus (including humus soil) and a sludge discharge pipe provided near the bottom of the deodorization tank A defoaming mechanism for feeding the activated sludge upward and injecting the sludge onto the upper surface of the sludge layer from a defoaming nozzle disposed above the upper surface of the sludge layer in the deodorization tank, and an exhaust port provided on the ceiling of the deodorization tank And an exhaust pipe provided with an activated carbon packed bed in the middle of the exhaust path.

【0017】上記の構成を有する請求項3に係る脱臭装
置によれば、脱臭槽内に貯留された汚泥は通水性容器内
の腐植と適度に接触し、腐植中の土壌菌群によって熟成
され活性化される。このとき、散気ディフューザーから
導入される空気によって汚泥が十分に撹拌、活性化が促
進される。この状態で、臭気ガスが脱臭槽内の汚泥中に
散気ディフューザーから導入され、臭気ガスによって撹
拌され、汚泥と臭気ガスとの接触が十分に図られる。臭
気ガスが汚泥の上面から抜け出すときに、多量の泡が発
生するが、これらの泡は、消泡機構によって循環させる
汚泥(汚泥水)を消泡ノズルから噴射することにより消
される。とくに散気ディフューザーから汚泥の上面まで
の高さを600mm以上に設定して臭気ガスが汚泥と十
分にかつ少なくとも脱臭に必要な時間は接触が図られる
ようにしたから、臭気成分が確実に分解除去される。そ
して、臭気ガスは無臭に近いガスとなって排気筒から排
気されるが、汚泥を使用している関係から、微量の土壌
臭および汚泥臭が残ることがあっても、これらの臭いは
活性炭で吸着するので、外部へは無臭状態で排気するこ
とができる。
According to the deodorizing apparatus according to the third aspect of the present invention, the sludge stored in the deodorizing tank comes into appropriate contact with the humus in the water-permeable container, and is matured and activated by the soil fungus group in the humus. Be transformed into At this time, the sludge is sufficiently stirred and activated by the air introduced from the diffuser. In this state, the odor gas is introduced into the sludge in the deodorization tank from the diffuser, and is stirred by the odor gas, whereby the sludge and the odor gas are sufficiently contacted. When the odor gas escapes from the upper surface of the sludge, a large amount of bubbles are generated, and these bubbles are eliminated by injecting sludge (sludge water) circulated by the defoaming mechanism from the defoaming nozzle. In particular, the height from the diffuser to the top of the sludge is set to 600 mm or more so that the odor gas can contact the sludge sufficiently and at least for the time required for deodorization, so that the odor components are reliably decomposed and removed. Is done. Then, the odor gas becomes almost odorless gas and is exhausted from the exhaust stack.However, due to the use of sludge, even if a slight amount of soil odor and sludge odor may remain, these odors can be removed by activated carbon. Since it is adsorbed, it can be exhausted to the outside without odor.

【0018】請求項4に記載のように、前記脱臭槽内の
上端部に多数の小孔を有する多孔板を配設し、該多孔板
の中央部を貫通して上方に一部突出する水封管を取り付
け、前記脱臭槽の前記多孔板の上方に汚泥又は汚水の注
入部を設ける一方、多孔板の下方にオーバーフローする
汚泥の排水管の上端排水口を上向きに開口させて汚泥層
中から脱臭槽の外部に向けて配管し、前記消泡ノズルを
前記多孔板の上方と下方の汚泥上面の間とにそれぞれ下
向きに配設することが望ましい。
According to a fourth aspect of the present invention, a perforated plate having a large number of small holes is provided at an upper end portion in the deodorizing tank, and the water partially protrudes upward through a central portion of the perforated plate. Attach a sealed tube and provide a sludge or wastewater injection section above the perforated plate of the deodorization tank, while opening the upper end drain port of the drainage pipe of the sludge overflowing below the perforated plate upward from the sludge layer. It is preferable that piping is provided to the outside of the deodorization tank, and the defoaming nozzle is disposed downward between the upper part of the perforated plate and the lower part of the sludge upper surface.

【0019】請求項4記載の脱臭装置によれば、多孔板
上に汚泥(水)が水封管の上方突出長さ(実施例では2
0〜30mm)程度に常に溜って汚泥水膜を形成する。
多孔板上に落下注入された汚泥水は、水封管から下方の
汚泥層内に流入する。この状態で、多孔板の小孔を突き
抜ける臭気ガスが汚泥水膜をも突き抜けて排気筒より排
出されるので、多孔板上の汚泥とも積極的に接触し、脱
臭されることになる。また、泡は多孔板と汚泥層の上面
との間の空間部および多孔板上に溜った汚泥水膜の上方
の空間部にそれぞれ発生して溜るが、これらの泡は消泡
ノズルから噴射される汚泥水によって消される。また汚
泥排水管によって、脱臭槽内の汚泥の上面高さが所定高
さに自動的に維持され、管理が容易にである。
According to the deodorizing device of the fourth aspect, the sludge (water) is projected upward on the perforated plate by the length of the water seal tube (2 in the embodiment).
(0 to 30 mm) to form a sludge water film.
The sludge water dropped and injected on the perforated plate flows into the lower sludge layer from the water seal tube. In this state, the odor gas that penetrates through the small holes of the perforated plate also passes through the sludge water film and is discharged from the exhaust pipe, so that the odor gas comes into active contact with the sludge on the perforated plate and is deodorized. Bubbles are generated and accumulated in the space between the perforated plate and the upper surface of the sludge layer and in the space above the sludge water film accumulated on the perforated plate, respectively, and these bubbles are ejected from the defoaming nozzle. Is extinguished by sludge water. In addition, the sludge drain pipe automatically maintains the upper surface height of the sludge in the deodorization tank at a predetermined height, thereby facilitating management.

【0020】請求項5に記載のように、前記汚泥排水管
の他端を上端を開口した汚泥分離槽の上下方向の中間位
置付近に接続し、該汚泥分離槽の底部付近に接続した汚
泥戻し管の他端を前記脱臭槽の上端部に接続し、前記汚
泥分離槽内の上端部付近にオーバーフローする水を排出
する排水管の上端排水口を上向きに開口させて配管する
とともに、該排水管の上端排水口を、前記脱臭槽内に配
管した前記汚泥排水管の上端排水口よりも低い位置に設
定するとよい。
The sludge drainage pipe is connected at the other end thereof to an intermediate position in the vertical direction of a sludge separation tank having an open upper end, and the sludge return pipe is connected to a vicinity of a bottom of the sludge separation tank. The other end of the pipe is connected to the upper end of the deodorization tank, and the upper end of the drainage pipe for discharging water overflowing near the upper end in the sludge separation tank is opened upward and piped. The upper end drainage port may be set at a position lower than the upper end drainage port of the sludge drainage pipe provided in the deodorization tank.

【0021】請求項5記載の脱臭装置によれば、脱臭槽
へ汚水、汚泥水あるいは生ゴミ処理機や生ゴミ処理場で
発生する結露水を注入する場合に、オーバーフローして
水とともに汚泥が流出するが、流出する汚泥が汚泥分離
槽において水と分離されて回収され、脱臭槽へ戻される
ので、汚泥濃度が所定濃度に保たれやすく、管理が容易
になる。したがって、とくに生ゴミ処理機や生ゴミ処理
場で発生する生ゴミ臭の結露水も同時に脱臭処理するの
に、好適である。
According to the fifth aspect of the present invention, when injecting sewage, sludge water or dew water generated in a garbage disposal machine or a garbage disposal plant into the deodorization tank, the sludge overflows with the water. However, the outflowing sludge is separated from the water in the sludge separation tank, collected, and returned to the deodorization tank, so that the sludge concentration is easily maintained at a predetermined concentration and the management becomes easy. Therefore, it is particularly suitable for simultaneously deodorizing garbage dew water generated in a garbage disposal machine or a garbage disposal plant.

【0022】[0022]

【発明の実施の形態】以下、この発明に係る脱臭装置の
実施の形態について図面に基づいて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a deodorizing apparatus according to the present invention will be described below with reference to the drawings.

【0023】図1は脱臭装置の実施例を示す全体系統
図、図2は図1の脱臭槽を拡大して示す概要断面図、図
3は図2の多孔板付近を拡大して示す部分断面図であ
る。
FIG. 1 is an overall system diagram showing an embodiment of a deodorizing apparatus, FIG. 2 is a schematic sectional view showing an enlarged deodorizing tank of FIG. 1, and FIG. 3 is a partial sectional view showing an enlarged view of the vicinity of a perforated plate of FIG. FIG.

【0024】図1に示すように、脱臭装置1は脱臭槽2
と汚泥分離槽3とを備え、両槽2・3は一定の間隔をあ
けて並設されている。脱臭槽2は円筒形又は角筒形の上
面中央部に排気口4を有する筒体からなる。排気口4に
は排気筒(煙突)5が上向きに連設され、排気筒5内の
上下方向の中間部には活性炭充填層6が介設されてい
る。充填層6の活性炭は交換可能に、排気筒5の側面に
開閉扉(図示せず)が設けられている。
As shown in FIG. 1, a deodorizing device 1 includes a deodorizing tank 2.
And a sludge separation tank 3. Both tanks 2 and 3 are juxtaposed at a certain interval. The deodorizing tank 2 is formed of a cylindrical body having an exhaust port 4 at the center of the upper surface of a cylindrical or rectangular tube. An exhaust pipe (chimney) 5 is connected to the exhaust port 4 in an upward direction, and an activated carbon filled layer 6 is interposed in an intermediate portion of the exhaust pipe 5 in the vertical direction. An opening / closing door (not shown) is provided on the side surface of the exhaust pipe 5 so that the activated carbon of the packed bed 6 can be replaced.

【0025】図2に示すように脱臭槽2内において、底
部よりやや上方に散気ディフューザー7が配設され、臭
気ガス導入管8の一端が散気ディフューザー7の下部に
接続されている。散気ディフューザー7は円弧状球面7
aとその外周面7bに多数の小孔(図示せず)を有し、
臭気ガスを微細な気泡状にして汚泥中に散気する。この
散気ディフューザー7の頂面から600mm以上を上方
に離間させた位置(高さ)に、汚泥水排出管9の漏斗状
上端開口9aを上向きにして配設し、排出管9を下向き
に延ばした後に略直角に屈曲して脱臭槽2の側壁2aよ
り外部へ導き出している。散気ディフューザー7には、
既製品の例えば三鈴工業株式会社の超微細気泡散気管
(商品名(商標):エラストックス)を使用できる。
As shown in FIG. 2, an air diffuser 7 is disposed slightly above the bottom in the deodorizing tank 2, and one end of an odor gas introducing pipe 8 is connected to a lower portion of the air diffuser 7. The diffuser 7 is an arcuate spherical surface 7
a and a number of small holes (not shown) on its outer peripheral surface 7b,
Odor gas is diffused into sludge in the form of fine bubbles. At a position (height) 600 mm or more upward from the top surface of the diffuser 7, the sludge water discharge pipe 9 is disposed with the funnel-shaped upper end opening 9 a facing upward, and the discharge pipe 9 is extended downward. After that, it is bent at a substantially right angle and is led out from the side wall 2a of the deodorization tank 2. In the diffuser 7,
An off-the-shelf product, for example, an ultra-fine bubble diffuser (trade name (trademark): Erastocks) of Misuzu Industrial Co., Ltd. can be used.

【0026】排出管9の上端開口9aより上方に、直径
15mm程度の多数の孔10aを開けた多孔板(本例で
はパンチングプレート)10が装着されている。この多
孔板10の中央部に、図3に示すように水封管11を上
端部を上方に突出させかつ貫通して配設している。水封
管11の上方突出長さは、本例では20〜30mmにし
て、多孔板10上に汚泥による水膜が厚さt=20〜3
0mm程度に形成されるように構成する。また、水封管
11の下端は図2のように脱臭槽2の上下方向の中間位
置よりやや下方まで延設し、汚泥中に開口させている。
A perforated plate (a punching plate in this example) 10 having a large number of holes 10a having a diameter of about 15 mm is mounted above the upper end opening 9a of the discharge pipe 9. As shown in FIG. 3, a water sealing tube 11 is disposed at the center of the perforated plate 10 so that the upper end thereof projects upward and penetrates. In this example, the upwardly projecting length of the water sealing tube 11 is set to 20 to 30 mm, and the water film of the sludge on the perforated plate 10 has a thickness t = 20 to 3
It is configured to be formed to about 0 mm. The lower end of the water seal tube 11 extends slightly below the middle position in the vertical direction of the deodorization tank 2 as shown in FIG. 2, and is opened in the sludge.

【0027】図2のように、脱臭槽2の汚泥中に、腐植
をペレット状に成型した粒状体を収納する通気性容器1
2が吊設されている。この容器12は例えば籠状容器か
らなり、腐植粒状体を逐次補充できるように、脱臭槽2
の側壁2aに開閉扉(図示せず)を設けて容器12を出
し入れ可能にし、側壁2aの内側に容器12を吊るして
配置できるようになっている。なお、腐植Zの種類につ
いては特に限定するものではないが、落葉樹の落ち葉と
動物由来の分解物が温暖な気候の下で十分に分解され、
それから再合成物となったのちに、カルシウムで飽和さ
れてできた中性腐食を原料とし、バイオテクノロジーに
よって低分子化し、量を増やしてミセルコロイドとして
安定化させた腐植を使用するのが望ましい。中性腐食は
8000年間地中に密閉埋蔵されてできた腐食であり、
微生物に分解される栄養型腐食の量が多く、したがって
バイオテクノロジーによって産生されるフルボ酸および
その鉄錯体の含有量が数十%に及ぶからである。
As shown in FIG. 2, a gas-permeable container 1 for storing granular material obtained by molding humus into pellets in sludge in a deodorization tank 2.
2 are suspended. The container 12 is, for example, a basket-shaped container, and is provided with a deodorizing tank 2 so that humic particulates can be sequentially replenished.
An opening / closing door (not shown) is provided on the side wall 2a to allow the container 12 to be taken in and out, and the container 12 can be suspended and arranged inside the side wall 2a. The type of humus Z is not particularly limited, but the fallen leaves of deciduous trees and decomposed substances derived from animals are sufficiently decomposed in a warm climate,
It is then desirable to use humus, which is made from neutral corrosion formed by saturation with calcium after the resynthesis has been made, and which has been reduced in molecular weight by biotechnology and stabilized in the form of micelle colloid by increasing the amount. Neutral corrosion is corrosion that has been buried underground for 8,000 years.
This is because the amount of vegetative corrosion degraded by microorganisms is large, and thus the content of fulvic acid and its iron complex produced by biotechnology reaches several tens of percent.

【0028】また、脱臭槽2の底部に汚泥の排出口13
を設け、排出口13に循環ポンプ14を介設した汚泥循
環管15の一端を接続する。汚泥循環管15の他端側は
2本に分岐して脱臭槽2内に挿入し、各分岐管15a・
15bの端部に消泡ノズル16・17を連結して消泡機
構18を構成する。そして、一方の消泡ノズル16を多
孔板10の下方で中央部寄りに、また他方の消泡ノズル
17を多孔板10の上方で中央部に配置する。
The sludge discharge port 13 is provided at the bottom of the deodorization tank 2.
And one end of a sludge circulation pipe 15 provided with a circulation pump 14 is connected to the discharge port 13. The other end of the sludge circulation pipe 15 is branched into two and inserted into the deodorization tank 2, and each of the branch pipes 15a.
The defoaming nozzles 16 and 17 are connected to the end of 15b to form a defoaming mechanism 18. Then, one defoaming nozzle 16 is disposed below the perforated plate 10 toward the center, and the other defoaming nozzle 17 is disposed above the perforated plate 10 at the center.

【0029】さらに、汚泥水排出管9の他端を汚泥分離
槽3の上下方向の中間位置よりやや上に接続する。汚泥
分離槽3の底部に汚泥排出口20を設け、排出口20に
汚泥戻し管21の一端を接続し、他端を脱臭槽2の上面
(壁)2cあるいは側壁2aを貫通して設けた開口22
/23(図2)に接続している。汚泥分離槽3の上端は
開放したままにし、排水管24の漏斗状上端開口24a
を上向きにして上端開放位置よりやや低い位置に配設
し、排水管24を下向きに延ばした後に略直角に屈曲し
て汚泥分離槽3の側壁3aより外部へ導き出し、排水溝
(図示せず)や河川などに導いている。
Further, the other end of the sludge water discharge pipe 9 is connected to a position slightly above the vertical intermediate position of the sludge separation tank 3. An opening provided with a sludge discharge port 20 at the bottom of the sludge separation tank 3, one end of a sludge return pipe 21 connected to the discharge port 20, and the other end provided through the upper surface (wall) 2 c or the side wall 2 a of the deodorization tank 2. 22
/ 23 (FIG. 2). The upper end of the sludge separation tank 3 is left open, and the funnel-shaped upper end opening 24 a of the drain pipe 24 is opened.
Is disposed at a position slightly lower than the upper end open position with the upper side upward, the drain pipe 24 is extended downward, and then bent substantially at a right angle to be guided to the outside from the side wall 3a of the sludge separation tank 3 to be drained (not shown). And rivers.

【0030】汚泥戻し管21を流通させる汚泥の戻し
は、電動ポンプを用いずにエアリフトポンプ作用によっ
て行わせる。つまり、図1に示すように、散気ディフュ
ーザー7に臭気ガス導入管8を分岐し、分岐管8aの一
端を電磁開閉弁25を介して戻し管21の途中に接続す
る。本例の場合、臭気ガスは生ゴミ処理機41で発生す
るものを導入する関係上、ミストセパレータ26を介し
て配管28により捕集ブロワー27に接続し、結露水等
の水分をミストセパレータ26にて除去し、ガス(気
体)分のみ送給する。配管28のミストセパレータ26
の下流側で配管28に介設した開閉弁38の下流側に、
開閉弁30を介設した空気導入用の配管29の一端を接
続する。また、生ゴミ処理機41の結露水Wの排水口4
1aに一端を接続した結露水導入管31に送給ポンプ3
2を介設し、他端を脱臭槽2の上下方向の中間位置より
やや下方に接続する。そして導入管31の途中に、ミス
トセパレータ26の下端に接続した配管33を接続す
る。さらに、汚水・汚泥処理施設40から汚水・汚泥X
の送給管34を、脱臭槽2内の貯留汚泥層Xの上面と多
孔板10の空間部35に接続する。なお、送給管34に
は送給ポンプ36および開閉弁37を介設する。
The return of the sludge flowing through the sludge return pipe 21 is performed by an air lift pump function without using an electric pump. That is, as shown in FIG. 1, the odor gas introduction pipe 8 is branched to the diffuser 7, and one end of the branch pipe 8 a is connected to the middle of the return pipe 21 via the electromagnetic on-off valve 25. In the case of this example, since the odor gas introduces what is generated in the garbage disposal machine 41, the odor gas is connected to the collection blower 27 via a mist separator 26 via a pipe 28, and moisture such as dew water is supplied to the mist separator 26. To remove and send only gas (gas). Mist separator 26 of pipe 28
Downstream of the on-off valve 38 interposed in the pipe 28 on the downstream side of
One end of an air introducing pipe 29 provided with an on-off valve 30 is connected. Further, the drain 4 of the dew condensation water W of the garbage disposal machine 41 is provided.
The feed pump 3 is connected to the condensed water introduction pipe 31 having one end connected to 1a.
2 and the other end is connected slightly below the vertical middle position of the deodorization tank 2. Then, a pipe 33 connected to the lower end of the mist separator 26 is connected in the middle of the introduction pipe 31. Further, from the sewage / sludge treatment facility 40, the sewage / sludge X
Is connected to the upper surface of the stored sludge layer X in the deodorization tank 2 and the space 35 of the perforated plate 10. The feed pipe 34 is provided with a feed pump 36 and an on-off valve 37.

【0031】以上のようにして、本発明の実施例に係る
脱臭装置1が構成される。この脱臭装置の使用態様を以
下に説明する。
As described above, the deodorizing apparatus 1 according to the embodiment of the present invention is configured. The usage of this deodorizing device will be described below.

【0032】 脱臭槽2に汚泥送給管34により汚泥
Xを送給し、所定量の汚泥Xを貯留する。
The sludge X is fed to the deodorization tank 2 through a sludge feed pipe 34, and a predetermined amount of the sludge X is stored.

【0033】 脱臭槽2内の汚泥Xに対しては0.5
〜1.0重量%の腐植Zを投入して活性化させると同時
に、脱臭槽2内の汚泥層X中に、散気ディフューザー7
から空気Aを導入して空気撹拌による初期調整を2〜3
日間行い、汚泥Xの活性化と安定化を図る。このとき、
開閉弁30を開放し、開閉弁38を閉じる。
The sludge X in the deodorization tank 2 is 0.5
At the same time, the humus Z of about 1.0% by weight is charged and activated, and at the same time, the diffuser 7 is introduced into the sludge layer X in the deodorization tank 2.
The initial adjustment by air agitation by introducing air A from
It is carried out for a day to activate and stabilize sludge X. At this time,
The on-off valve 30 is opened, and the on-off valve 38 is closed.

【0034】 の状態でペレット状腐植Zを籠状容
器12に収納し、脱臭槽2内の汚泥層X中に吊設する。
In the state described above, the pellet-shaped humus Z is housed in the basket-shaped container 12 and suspended in the sludge layer X in the deodorization tank 2.

【0035】 生ゴミ処理機41から発生する臭気ガ
スGを、脱臭槽2内の汚泥X中に散気ディフューザー7
から微細な気泡状態にして散気させる。このとき、臭気
ガスGの1時間当たりの散気量は、脱臭槽2内に汚泥層
Xの貯留容量1m3当たりで30m3以内に調整する。な
お、開閉弁30を閉じ、開閉弁38を開放する。
The odor gas G generated from the garbage disposer 41 is diffused into the sludge X in the deodorization tank 2 by the diffuser 7.
From the air to form fine bubbles. At this time, aeration per hour of odorous gas G is adjusted within 30 m 3 in storage capacity 1 m 3 per sludge layer X in deodorizing tank 2. The on-off valve 30 is closed and the on-off valve 38 is opened.

【0036】 生ゴミ処理機41内では、通常40℃
〜70℃の温度で生ゴミの醗酵分解処理が行われるため
に、生ゴミ処理機41内に多量の結露水Wが生じる。ま
た、生ゴミ処理機41内の臭気ガスGの送風路において
も結露水Wが発生するが、この結露水Wはミストセパレ
ータ26内で分離され、生ゴミ処理機41内で発生した
結露水Wとともに結露水導入管31を通って脱臭槽2内
の汚泥層X中に導入される。生ゴミから生じる結露水W
は、悪臭があるうえにBODが150〜200mg/l
の汚濁成分を含んでいるため、臭気ガスGと同様に汚泥
Xに接触させて脱臭・汚水処理を行う。
In the garbage disposer 41, the temperature is usually 40 ° C.
Since the garbage is fermented and decomposed at a temperature of about 70 ° C., a large amount of dew water W is generated in the garbage processor 41. Condensation water W is also generated in the odor gas G ventilation path in the garbage disposal machine 41, and the dew condensation water W is separated in the mist separator 26 and condensed water W generated in the garbage disposal machine 41. At the same time, it is introduced into the sludge layer X in the deodorization tank 2 through the dew condensation water introduction pipe 31. Condensation water W generated from garbage
Has a bad odor and a BOD of 150 to 200 mg / l
Therefore, the deodorizing and sewage treatment is performed by contacting with the sludge X in the same manner as the odor gas G.

【0037】 脱臭効果を安定させて有効に維持する
ために、汚泥層Xの汚泥濃度は3000〜12000m
g/lに保持する必要があるため、汚泥濃度が3000
mg/l以下に低下したときには、脱臭槽2に汚泥送給
管34により汚水・汚泥処理施設40から汚泥Xを送給
する。本例の脱臭装置1では、オーバーフローする泥水
Yを一旦、汚泥分離槽3へ導き、上澄水Uと分離して汚
泥Xを脱臭槽2へ戻すので、汚泥濃度が一定に保たれや
すい。上澄水Uは排水溝等へ排水される。
In order to stabilize the deodorizing effect and keep it effective, the sludge concentration of the sludge layer X is 3000 to 12000 m
g / l, so that the sludge concentration is 3000
When the concentration is reduced to mg / l or less, the sludge X is fed from the sewage / sludge treatment facility 40 to the deodorization tank 2 through the sludge feed pipe 34. In the deodorizing apparatus 1 of this example, since the overflowing muddy water Y is once guided to the sludge separation tank 3 and separated from the supernatant water U, and the sludge X is returned to the deodorizing tank 2, the sludge concentration is easily kept constant. The supernatant water U is drained to a drain or the like.

【0038】また、図3に示すように、多孔板10上に
は所定厚みの汚泥水膜Mが常時形成されており、脱臭槽
2内に導入され散気された臭気ガスGが汚泥Xと十分に
接触したのち、多孔板10の孔10aから抜け出すが、
この際に汚泥水膜Mと接触して再び脱臭処理化される。
このような多孔板10を設けて一定厚みの汚泥水膜Mを
形成する構造は、臭気ガスGの脱臭が困難な場合、つま
り臭気成分が多量に含まれる場合に設ければよく、省く
ことも可能である。そして、脱臭済みの臭気ガスG’は
排気筒5から排気され、活性炭6を通過するときに、汚
泥臭等が除去され、排気される。
As shown in FIG. 3, a sludge water film M having a predetermined thickness is always formed on the perforated plate 10, and the odor gas G introduced into the deodorization tank 2 and diffused is mixed with the sludge X. After sufficient contact, it comes out of the hole 10a of the perforated plate 10,
At this time, it comes into contact with the sludge water film M and is deodorized again.
Such a structure in which the perforated plate 10 is provided to form the sludge water film M having a constant thickness may be provided when it is difficult to deodorize the odor gas G, that is, when a large amount of odor components is contained, and may be omitted. It is possible. Then, the deodorized odor gas G 'is exhausted from the exhaust pipe 5, and when passing through the activated carbon 6, sludge odor and the like are removed and exhausted.

【0039】さらに、散気ディフューザー7から散気さ
れる臭気ガスGが汚泥層Xおよび汚泥水膜Mから抜け出
した際に多量の泡が発生するが、これらの泡は消泡機構
18によって消される。すなわち、脱臭槽2の底部に沈
降している汚泥Xが循環管14を通って循環ポンプ15
により循環され、汚泥層Xの上面に貯留されている泡お
よび多孔板10上の汚泥水膜Mの上面に貯留されている
泡に消泡ノズル16・17から噴射・放出される。この
結果、泡が消えて内部の脱臭されたガスが排気筒5から
外部へ排出される。
Further, when the odor gas G diffused from the diffuser 7 escapes from the sludge layer X and the sludge water film M, a large amount of bubbles are generated. These bubbles are eliminated by the defoaming mechanism 18. . That is, the sludge X settling at the bottom of the deodorization tank 2 passes through the circulation pipe 14 and the circulation pump 15
The foam is stored in the upper surface of the sludge layer X and the foam stored in the upper surface of the sludge water film M on the perforated plate 10 is ejected and discharged from the defoaming nozzles 16 and 17. As a result, the bubbles disappear and the deodorized gas inside is discharged from the exhaust pipe 5 to the outside.

【0040】上記のようにして、本例の場合には生ゴミ
処理機41から発生する臭気ガスGとともに、結露水W
も同時に脱臭処理される。そして、臭気ガスGは無臭化
されて大気中に排出されるとともに、結露水Wは脱臭さ
れて汚泥X中の上澄水(上澄液)Uとともに排水され
る。一方、脱臭処理には化学物質は使用せず、自然に存
在する腐植と汚泥とを使用したことから、安価にしかも
大量の臭気ガスをしょりすることができる。また脱臭設
備に関しては、基本的には脱臭槽2を備えればよく、こ
の脱臭槽2が脱臭処理作業とともに、汚泥の活性化を図
るリアクターとしても機能するので、設備コストも安
く、設置スペースも小さくて済む。
As described above, in the case of the present embodiment, the dew water W
Is also deodorized at the same time. Then, the odor gas G is deodorized and discharged into the atmosphere, and the dew water W is deodorized and discharged together with the supernatant water (supernatant) U in the sludge X. On the other hand, no chemical substance is used for the deodorization treatment, and naturally occurring humus and sludge are used, so that a large amount of odorous gas can be dripped at low cost. In addition, as for the deodorizing equipment, it is basically sufficient to provide the deodorizing tank 2, and this deodorizing tank 2 functions as a reactor for activating the sludge together with the deodorizing treatment, so that the equipment cost is low and the installation space is small. Small enough.

【0041】[0041]

【発明の効果】以上説明したことから明らかなように、
この発明の脱臭方法とその装置には、次のような優れた
効果がある。
As is apparent from the above description,
The deodorizing method and apparatus according to the present invention have the following excellent effects.

【0042】(1) 汚水処理場で発生する汚泥(汚水)
と腐植(土)を使用して安価で大量な臭気ガスの脱臭処
理が可能で、しかも脱臭効果が高く持続性を具備する。
とくに本発明の脱臭方法では、脱臭槽内に貯留された汚
泥中において投入された腐植中の土壌菌群が汚泥・汚水
を栄養源として培養される一方、汚泥は土壌菌群の繁殖
により熟成し活性化され、汚泥に含有される土壌菌群中
のバクテリアが代謝産物を産出し、その代謝産物が脱臭
成分つまり臭気除去成分を具有しているので、脱臭機能
が発揮される。また、汚泥の活性化に、好気性および通
性嫌気バクテリアの含有量が多く、品質の良い腐植を使
用したので、比較的容易にかつ安価に得られる。さら
に、脱臭槽内に貯留されている活性化された汚泥に導入
された臭気ガスが散気分散されて効率よく接触し、ガス
中の悪臭成分と土壌菌群のバクテリアが産出する代謝産
物が具有している脱臭成分とが反応し、脱臭作用を発揮
する。
(1) Sludge (sewage) generated at a sewage treatment plant
And humus (soil) can be used to deodorize a large amount of odorous gas at a low cost, and has a high deodorizing effect and a long lasting effect.
In particular, in the deodorizing method of the present invention, while the soil bacteria group in the humus introduced in the sludge stored in the deodorization tank is cultured using sludge / sewage as a nutrient source, the sludge is aged by the propagation of the soil bacteria group. The bacteria in the soil fungus group that is activated and contained in the sludge produce metabolites, and the metabolites have a deodorizing component, that is, an odor removing component. In addition, a high content of aerobic and facultative anaerobic bacteria and high-quality humus are used for activating sludge, so that the sludge can be obtained relatively easily and inexpensively. Furthermore, the odorous gas introduced into the activated sludge stored in the deodorization tank is diffused and dispersed and efficiently comes into contact with it, and the odorous components in the gas and the metabolites produced by the bacteria of the soil bacteria group are present. It reacts with the deodorizing component and exerts a deodorizing effect.

【0043】(2) 請求項2記載の脱臭方法では、汚泥
の濃度3,000mg/l未満に低下すると、脱臭能力
に欠け十分な脱臭作用が得られないから、汚水処理設備
から汚泥を供給するか、又は有機物を多量に含む汚水を
供給することにより汚泥濃度の安定化を図っているの
で、優れた脱臭効果が継続して保たれる。
(2) In the deodorizing method according to the second aspect, if the concentration of the sludge is reduced to less than 3,000 mg / l, sufficient deodorizing action cannot be obtained due to lack of deodorizing ability. Alternatively, since the sludge concentration is stabilized by supplying wastewater containing a large amount of organic substances, an excellent deodorizing effect is continuously maintained.

【0044】(3) 本発明の請求項3に係る脱臭装置で
は、上記した脱臭方法が確実に実施でき、しかも脱臭槽
内に散気ディフューザーから導入される空気によって汚
泥が十分に撹拌、活性化が促進され、臭気ガスが脱臭槽
内の汚泥中に散気ディフューザーから導入され、臭気ガ
スによって撹拌され、汚泥と臭気ガスとの接触が十分に
図られるうえに、臭気ガスおよび空気が汚泥の上面から
抜け出すときにも汚泥と十分に接触されるとともに、散
気ディフューザーから汚泥の上面までの高さを600m
m以上に設定して臭気ガスが汚泥と十分にかつ少なくと
も脱臭に必要な時間は接触が図られるようにしたから、
臭気成分が確実に分解除去され、臭気ガスは無臭に近い
ガスとなって導入された排気筒から外部へは無臭状態で
排気することができる。
(3) In the deodorizing apparatus according to the third aspect of the present invention, the above-mentioned deodorizing method can be reliably carried out, and the sludge is sufficiently stirred and activated by the air introduced from the diffuser into the deodorizing tank. Is promoted, and odor gas is introduced into the sludge in the deodorization tank from the diffuser, stirred by the odor gas, and the sludge and the odor gas are sufficiently brought into contact with each other. The sludge is sufficiently in contact with the sludge when it comes out of the room, and the height from the diffuser to the top of the sludge is 600m.
m or more so that the odor gas is sufficiently in contact with the sludge and at least for the time required for deodorization,
Odor components are reliably decomposed and removed, and the odor gas can be exhausted to the outside from the exhaust pipe introduced as a nearly odorless gas in an odorless state.

【0045】(4) 請求項4記載の脱臭装置では、多孔
板上に汚泥(水)が20〜30mm程度に常に溜って汚
泥水膜を形成した状態で、多孔板の小孔を突き抜ける臭
気ガスが汚泥水膜をも突き抜けて排気筒より排出される
ので、多孔板上の汚泥とも積極的に接触し、脱臭される
ので、脱臭効果が非常に高い。また汚泥排水管によっ
て、脱臭槽内の汚泥の上面高さが所定高さに自動的に維
持されるので、管理が容易にである。
(4) In the deodorizing device according to the fourth aspect, the odorous gas penetrating through the small holes of the perforated plate in a state in which the sludge (water) constantly accumulates to about 20 to 30 mm on the perforated plate to form a sludge water film. Is also discharged from the exhaust pipe through the sludge water film, so that it positively contacts sludge on the perforated plate and is deodorized, so that the deodorizing effect is very high. In addition, the sludge drain pipe automatically maintains the upper surface height of the sludge in the deodorization tank at a predetermined height, thereby facilitating management.

【0046】(5) 請求項5記載の脱臭装置は、脱臭槽
へ汚水、汚泥水あるいは生ゴミ処理機や生ゴミ処理場で
発生する結露水を注入する場合に、オーバーフローして
水とともに汚泥が流出するが、流出する汚泥が汚泥分離
槽において水と分離されて回収され、脱臭槽へ戻される
ので、汚泥濃度が所定濃度以上に保たれやすく、管理が
容易で、とくに生ゴミ処理機や生ゴミ処理場で発生する
生ゴミ臭の結露水も同時に脱臭処理するのに、好適であ
る。
(5) In the deodorizing apparatus according to the fifth aspect, when injecting sewage, sludge water or dew water generated in a garbage disposal machine or a garbage disposal plant into the deodorization tank, the sludge overflows with water. Although the sludge flows out, it is separated from the water in the sludge separation tank, collected and returned to the deodorization tank, so that the sludge concentration is easily maintained at a predetermined concentration or more, and it is easy to manage. It is suitable for deodorizing water condensed water of garbage generated at the garbage disposal site at the same time.

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

【図1】本発明の脱臭装置の実施例を示す全体系統図で
ある。
FIG. 1 is an overall system diagram showing an embodiment of a deodorizing device of the present invention.

【図2】図1の脱臭槽を拡大して示す概要断面図であ
る。
FIG. 2 is a schematic sectional view showing the deodorizing tank of FIG. 1 in an enlarged manner.

【図3】図2の多孔板10付近を拡大して示す部分断面
図である。
FIG. 3 is an enlarged partial cross-sectional view showing the vicinity of a perforated plate 10 of FIG. 2;

【符号の説明】[Explanation of symbols]

1 脱臭装置 2 脱臭槽 3 汚泥分離槽 5 排気筒 7 散気ディフューザー 10 多孔板 11 水封管 12 通水性容器 16・17 消泡ノズル 18 消泡機構 DESCRIPTION OF SYMBOLS 1 Deodorizing device 2 Deodorizing tank 3 Sludge separation tank 5 Exhaust pipe 7 Diffusing diffuser 10 Perforated plate 11 Water seal tube 12 Water permeable container 16.17 Defoaming nozzle 18 Defoaming mechanism

───────────────────────────────────────────────────── 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) B01D 53/81 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) B01D 53/81

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 脱臭槽に汚泥を貯留し、該汚泥に対し
0.5〜1.0重量%の腐植を投入して活性化させた状
態で、前記脱臭槽内の汚泥中に空気を導入して空気撹拌
による初期調整を行って前記汚泥の活性化と安定化を図
った後、 生ゴミ処理機等から発生する臭気ガスを、前記脱臭槽内
の汚泥中に微細な気泡状態にして導入し、活性化させた
汚泥に接触させて臭気ガスを分解し脱臭することを特徴
とする脱臭方法。
1. Sludge is stored in a deodorization tank and air is introduced into the sludge in the deodorization tank in a state where humus of 0.5 to 1.0% by weight is added to the sludge to activate the sludge. After performing the initial adjustment by air stirring to activate and stabilize the sludge, the odor gas generated from the garbage disposer and the like is introduced into the sludge in the deodorization tank in the form of fine bubbles. And deodorizing by decomposing odorous gas by contacting with activated sludge.
【請求項2】 前記汚泥の濃度を3,000〜12,00
0mg/lに保持するとともに、前記臭気ガスの導入量
を前記汚泥量1m3当たり30m3/hの範囲内に設定す
る請求項1記載の脱臭方法。
2. The sludge concentration of 3,000 to 12,000.
2. The deodorizing method according to claim 1, wherein the amount of the odorous gas is set within a range of 30 m 3 / h per 1 m 3 of the sludge while maintaining the concentration at 0 mg / l.
【請求項3】 汚泥を貯留し、導入する臭気ガスを該汚
泥に接触させて脱臭する脱臭槽を備えた脱臭装置におい
て、 前記脱臭槽が、該槽内の下部に配設され、前記臭気ガス
を気泡状にして前記汚泥中に散気させるための散気ディ
フューザーと、該散気ディフューザーから汚泥の上面ま
での高さが600mm以上になるように貯留される汚泥
層と、該汚泥層内に吊設され腐植の粒状化物を収容する
籠などの通水性容器と、前記脱臭槽の底部付近に設けた
汚泥排出管から循環ポンプを介して活性汚泥を上方へ送
給し、脱臭槽内の汚泥層の上面の上方に配設した消泡ノ
ズルから汚泥を汚泥層上面に噴射する消泡機構と、前記
脱臭槽の天井に設けた排気口に連設され排気路の途中に
活性炭充填層を設けた排気筒とを備えていることを特徴
とする脱臭装置。
3. A deodorizing apparatus comprising a deodorizing tank for storing sludge and bringing odor gas to be introduced into contact with the sludge to deodorize the odor gas, wherein the deodorizing tank is disposed at a lower portion in the tank, and A diffuser for diffusing air into the sludge in the form of bubbles, a sludge layer stored so that the height from the diffuser to the upper surface of the sludge is at least 600 mm, and Activated sludge is fed upward through a circulating pump from a water-permeable container such as a basket that houses suspended granules of humus and a sludge discharge pipe provided near the bottom of the deodorization tank, and the sludge in the deodorization tank A defoaming mechanism for injecting sludge from the defoaming nozzle disposed above the upper surface of the bed to the sludge layer upper surface, and an activated carbon filling layer provided in the middle of the exhaust passage connected to the exhaust port provided on the ceiling of the deodorization tank Deodorizing equipment characterized by having an exhaust pipe .
【請求項4】 前記脱臭槽内の上端部に多数の小孔を有
する多孔板を配設し、該多孔板の中央部を貫通して上方
に一部突出する水封管を取り付け、前記脱臭槽の前記多
孔板の上方に汚泥又は汚水の注入部を設ける一方、多孔
板の下方にオーバーフローする汚泥の排水管の上端排水
口を上向きに開口させて汚泥層中から脱臭槽の外部に向
けて配管し、前記消泡ノズルを前記多孔板の上方と下方
の汚泥上面の間とにそれぞれ下向きに配設した請求項3
記載の脱臭装置。
4. A perforated plate having a large number of small holes is provided at an upper end portion in the deodorizing tank, and a water seal tube which penetrates a central portion of the perforated plate and partially protrudes upward is attached. While the sludge or wastewater injection section is provided above the perforated plate of the tank, the upper end drain port of the drainage pipe of the sludge overflowing below the perforated plate is opened upward so that the sludge layer is directed to the outside of the deodorization tank. 4. A pipe, wherein the defoaming nozzle is disposed downward between the upper part of the perforated plate and the lower part of the sludge upper surface.
The deodorizing device described.
【請求項5】 前記汚泥排水管の他端を上端を開口した
汚泥分離槽の上下方向の中間位置付近に接続し、該汚泥
分離槽の底部付近に接続した汚泥戻し管の他端を前記脱
臭槽の上端部に接続し、前記汚泥分離槽内の上端部付近
にオーバーフローする水を排出する排水管の上端排水口
を上向きに開口させて配管するとともに、該排水管の上
端排水口を、前記脱臭槽内に配管した前記汚泥排水管の
上端排水口よりも低い位置に設定した請求項4記載の脱
臭装置。
5. The other end of the sludge drainage pipe is connected to the vicinity of a vertical intermediate position of a sludge separation tank having an open upper end, and the other end of the sludge return pipe connected to the vicinity of the bottom of the sludge separation tank is deodorized. Connected to the upper end of the tank, the upper end drainage of the drainage pipe for discharging water overflowing near the upper end in the sludge separation tank is opened upward and piped, and the upper end drainage of the drainage pipe, 5. The deodorizing apparatus according to claim 4, wherein the apparatus is set at a position lower than an upper end drainage port of the sludge drainage pipe provided in the deodorization tank.
JP25174699A 1999-09-06 1999-09-06 Deodorization method and apparatus Pending JP2001070746A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25174699A JP2001070746A (en) 1999-09-06 1999-09-06 Deodorization method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25174699A JP2001070746A (en) 1999-09-06 1999-09-06 Deodorization method and apparatus

Publications (1)

Publication Number Publication Date
JP2001070746A true JP2001070746A (en) 2001-03-21

Family

ID=17227320

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25174699A Pending JP2001070746A (en) 1999-09-06 1999-09-06 Deodorization method and apparatus

Country Status (1)

Country Link
JP (1) JP2001070746A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002336639A (en) * 2001-05-16 2002-11-26 Ebara Jitsugyo Co Ltd Deodorizing equipment utilizing organism and humus
CN105080306A (en) * 2014-05-05 2015-11-25 沈阳白云机械有限公司 Intelligent sewage odor comprehensive treatment device
KR101841483B1 (en) * 2017-09-15 2018-05-04 김경호 Refrigerator for semiconductor process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002336639A (en) * 2001-05-16 2002-11-26 Ebara Jitsugyo Co Ltd Deodorizing equipment utilizing organism and humus
CN105080306A (en) * 2014-05-05 2015-11-25 沈阳白云机械有限公司 Intelligent sewage odor comprehensive treatment device
KR101841483B1 (en) * 2017-09-15 2018-05-04 김경호 Refrigerator for semiconductor process

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