JP2605769Y2 - Biological deodorizer - Google Patents

Biological deodorizer

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Publication number
JP2605769Y2
JP2605769Y2 JP1993057351U JP5735193U JP2605769Y2 JP 2605769 Y2 JP2605769 Y2 JP 2605769Y2 JP 1993057351 U JP1993057351 U JP 1993057351U JP 5735193 U JP5735193 U JP 5735193U JP 2605769 Y2 JP2605769 Y2 JP 2605769Y2
Authority
JP
Japan
Prior art keywords
gas
water
treated
microorganisms
temperature
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
JP1993057351U
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Japanese (ja)
Other versions
JPH0724428U (en
Inventor
正樹 東條
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.)
Mitsubishi Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha Ltd
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Application filed by Mitsubishi Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP1993057351U priority Critical patent/JP2605769Y2/en
Publication of JPH0724428U publication Critical patent/JPH0724428U/en
Application granted granted Critical
Publication of JP2605769Y2 publication Critical patent/JP2605769Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案はし尿処理場、下水処理
場、その他各種工場から排出される悪臭を生物学的に分
解して脱臭処理する生物脱臭装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biological deodorizing apparatus for biologically decomposing and deodorizing odors discharged from human waste treatment plants, sewage treatment plants and other factories.

【0002】[0002]

【従来の技術】前記のし尿や下水処理場等で発生する悪
臭成分は、主に硫化水素、メチルメルカプタン等の硫黄
化合物及びアンモニア等であり、これらは微生物によっ
て分解することができるため、従来から微生物を着生担
持した充填層に悪臭ガスを流通させて処理する生物脱臭
装置が使用されている。
2. Description of the Related Art Offensive odor components generated in the above-mentioned human waste and sewage treatment plants are mainly hydrogen sulfide, sulfur compounds such as methyl mercaptan, and ammonia, which can be decomposed by microorganisms. BACKGROUND ART A biological deodorization apparatus is used in which a malodorous gas is passed through a packed bed on which microorganisms are formed and carried for treatment.

【0003】微生物を着生する担体としては、微生物の
着生、繁殖が良好に行われ、脱臭効率を長期間高く維持
することができるものとして、長繊維束、土壌、ビ−
ト、多孔質セラミックス及び活性炭等が主に用いられて
いる。
[0003] Carriers on which microorganisms can be formed include those capable of satisfactorily forming and reproducing microorganisms and maintaining a high deodorizing efficiency for a long period of time.
, Porous ceramics, activated carbon and the like are mainly used.

【0004】前記微生物を着生担持した充填層において
は、悪臭成分の生物学的酸化分解による生成物によりP
Hが低下し、微生物の生育を阻害させる恐れがあるた
め、生成物を洗浄除去する必要があり、また微生物の生
育に必要な水分を補給する等のため、適宜な散水器を備
えて充填層を定期的に散水洗浄している。
[0004] In the packed bed on which the above-mentioned microorganisms are formed and supported, P by the products of the biological oxidative decomposition of the malodorous components.
It is necessary to wash and remove the product because H may decrease and the growth of microorganisms may be inhibited. The water is washed regularly.

【0005】尚、散水される水としては、汚水の活性汚
泥による処理水、河川水又は地下水等が用いられ、また
散水は連続散水又は所定の時間間隔、例えば、1時間に
5分散水する等のように、間欠散水が行われているが、
連続散水の場合には、散水量が多くなり動力費が嵩むこ
とや、散水時に若干脱臭効果が低下する等の理由から、
一般的には間欠散水がおこなわれている。
As the water to be sprinkled, treated water by activated sludge of sewage, river water or groundwater is used. Sprinkling is carried out continuously or at predetermined time intervals, for example, water is dispersed 5 times an hour. As in the case of intermittent watering,
In the case of continuous sprinkling, the amount of sprinkling increases, the power cost increases, and the deodorizing effect decreases slightly during sprinkling.
Generally, intermittent watering is performed.

【0006】[0006]

【考案が解決しようとする課題】生物脱臭装置の脱臭効
果は、微生物の生物活性に依存するため、温度の影響を
大きく受ける。脱臭に関与する微生物は硫黄酸化菌や硝
化菌等であり、これらの菌体の生育適温はいずれも30
℃前後で、特に被処理ガスの温度が約10℃以下になる
と脱臭効果が顕著に悪化してくる。
The deodorizing effect of the biological deodorizing device depends on the biological activity of microorganisms, and is greatly affected by the temperature. Microorganisms involved in deodorization are sulfur oxidizing bacteria, nitrifying bacteria and the like.
When the temperature of the gas to be treated becomes about 10 ° C. or lower, the deodorizing effect is remarkably deteriorated.

【0007】従来の生物脱臭装置においては、処理対象
となる被処理ガスはある程度の温度を有している場合が
多く、また悪臭の発生も微生物に起因するため、気温の
低下時は悪臭の発生も少なくなる等として、温度の低下
に対して特段の対策も施されていなかった。
In a conventional biological deodorizing apparatus, the gas to be treated often has a certain temperature, and the generation of offensive odor is also caused by microorganisms. No particular countermeasures have been taken against a decrease in the temperature, for example, because the temperature has decreased.

【0008】しかし、冬季等の気温が極度に低くなる時
期、特に寒冷地においては、被処理ガスの温度も10℃
以下に低下し、また昼夜の気温差も極めて大きくなるた
め、微生物の生物活性に与える影響も甚大となり、脱臭
効果の悪化は無視できないため見直されてきている。
However, the temperature of the gas to be treated may be as low as 10 ° C. in winter or other seasons when the temperature becomes extremely low, especially in cold regions.
In addition, the temperature difference between daytime and nighttime becomes extremely large, the influence on the biological activity of microorganisms becomes significant, and the deterioration of the deodorizing effect cannot be ignored.

【0009】従って、本考案は維持管理が容易で、且つ
運転経費が安価であるという生物脱臭装置の利点を維持
すると共に、冬季等における気温の低下に対しても、容
易に対応でき、できるだけ脱臭効果が低下しない生物脱
臭装置の開発を目的としたものである。
Accordingly, the present invention maintains the advantages of the biological deodorizing apparatus, which is easy to maintain and inexpensive in operating costs, and can easily cope with a decrease in temperature in winter or the like, and deodorizes as much as possible. The purpose is to develop a biological deodorizer that does not reduce its effectiveness.

【0010】[0010]

【課題を解決するための手段】一般的に生物脱臭装置が
設置される場所は、汚水の生物処理装置に関係する設備
であり、生物処理装置から排出される処理水が常に10
℃以上の水温を保持していることに着目し、その処理水
がもつ熱量を被処理ガスの温度上昇に有効活用すること
によって、運転経費を安価に維持し、また設備も簡易に
することができることを知見し、本考案を成したもので
ある。
Generally, the place where the biological deodorizing device is installed is equipment related to the biological treatment device for wastewater, and the treated water discharged from the biological treatment device is always 10 units.
Focusing on maintaining a water temperature of ℃ or higher, by effectively utilizing the heat of the treated water to raise the temperature of the gas to be treated, it is possible to maintain low operating costs and simplify equipment. The inventor found out what can be done and made the present invention.

【0011】その本考案の要旨は、頂部に処理ガスの排
気管(26)、底部に被処理ガスの給気管(21)と排
水管(25)とを接続し、内部に微生物を担持した充填
層(2)と前記充填層(2)に散水する散水器(6)を
備え、被処理ガスを上向流で通気して悪臭成分を分解処
理する処理塔(1)の前記充填層(2)より下方に、汚
水を生物処理した処理水と被処理ガスとを接触させて被
処理ガスを昇温する昇温手段(3)を設け、前記散水器
(6)と前記昇温手段(3)とに供給される水の供給、
停止を所定の時間間隔で制御する制御手段(10)を備
えたことを特徴とする生物脱臭装置である。
The gist of the present invention is that a gas exhaust pipe (26) is connected to the top, and a gas supply pipe (21) and a drain pipe (25) for the gas to be treated are connected to the bottom. A water sprinkler (6) for spraying water to the bed (2) and the packed bed (2), and the packed bed (2) of the treatment tower (1) for decomposing the odorous component by passing the gas to be treated upwards. ), A temperature raising means (3) for bringing the treated gas obtained by biologically treating the sewage into contact with the gas to be treated to raise the temperature of the gas to be treated is provided, and the water sprayer (6) and the temperature increasing means (3) are provided. ) And the supply of water supplied to
A biological deodorizing device comprising a control means (10) for controlling the stop at predetermined time intervals.

【0012】[0012]

【作用】被処理ガスの給気管21から処理塔1に供給さ
れた悪臭成分を含有する被処理ガスは、昇温手段3を流
通する間に、汚水の生物処理水と接触して昇温され、更
に微生物が着生した充填層2を上向流で流通する間に、
悪臭成分が着生微生物により生物学的に酸化分解され、
清浄化した処理ガスとして排気管26から排出される。
The gas containing the malodorous component supplied to the processing tower 1 from the gas supply pipe 21 for the gas to be processed is contacted with the biologically treated water of the sewage while flowing through the temperature raising means 3 to be heated. While the packed bed 2 on which the microorganisms have set up is flowing in the upward flow,
Odorous components are biologically oxidatively decomposed by epiphytic microorganisms,
The exhaust gas is exhausted from the exhaust pipe 26 as a purified processing gas.

【0013】前記充填層2への微生物の担持は、運転初
期において、微生物及び栄養素等を含有するし尿や下水
等を生物処理した処理水を、散水器6から定期的に散水
することにより増殖着生させることができる。
The loading of the microorganisms on the packed bed 2 is carried out in the early stage of operation by periodically spraying treated water obtained by biologically treating human waste and sewage containing microorganisms and nutrients from the water sprayer 6 to multiply and accumulate. You can live.

【0014】また定常時における散水は、微生物の棲息
に必要な湿潤状態を保つとともに、悪臭成分の分解生成
物や過剰の増殖微生物等の洗浄除去のために行われ、通
常は間欠的に散水される。
[0014] Watering in a steady state is carried out in order to maintain a moist state necessary for the inhabitation of microorganisms, and to wash and remove decomposition products of malodorous components and excessively growing microorganisms. Usually, watering is carried out intermittently. You.

【0015】尚、被処理ガスが微生物により分解されに
くい有機硫黄化合物を多く含有する場合には、処理ガス
中にそれらが残留する恐れがあるため、通常は、後段に
設けられた活性炭吸着塔7により、更に吸着清浄化処理
された後大気中に放出される。
If the gas to be treated contains a large amount of organic sulfur compounds which are not easily decomposed by microorganisms, these may remain in the treated gas. Therefore, the activated carbon adsorption tower 7 provided at the subsequent stage is usually used. As a result, it is further released to the atmosphere after being subjected to adsorption cleaning treatment.

【0016】また充填層2の洗浄等に使用された水及び
昇温手段3で被処理ガス昇温用に供給された水は、処理
塔1の底部に滞留させた後、排水管25からドレンピッ
ト9を経て系外に排出される。
The water used for washing the packed bed 2 and the water supplied by the temperature raising means 3 for raising the temperature of the gas to be treated are retained at the bottom of the processing tower 1 and then drained from the drain pipe 25. It is discharged out of the system through the pit 9.

【0017】前記散水器6及び昇温手段3に供給される
水は、制御装置10により流量制御又は流路切替え制御
されて供給されるが、充填層2への散水が間欠的に行わ
れる場合には、昇温手段3での生物処理水の供給も間欠
的に行い、夫々の排水として排出してもよい。
The water supplied to the water sprinkler 6 and the temperature raising means 3 is supplied by controlling the flow rate or switching the flow path by the control device 10, but the water is supplied to the packed bed 2 intermittently. Alternatively, the supply of the biologically treated water in the temperature raising means 3 may be performed intermittently and discharged as respective wastewater.

【0018】しかし、冬季の夜間等気温が更に低下する
時間帯等には、昇温手段3への給水を連続的におこなう
のが好ましく、また昇温に使用された水の一部を散水器
6の散水用の水として循環使用してもよい。
However, it is preferable to continuously supply water to the temperature raising means 3 during a time period when the temperature further decreases, such as at night in winter, and a part of the water used for the temperature raising is sprayed. It may be circulated and used as water for sprinkling of No. 6.

【0019】[0019]

【実施例】本考案を図面に基づいて説明する。図1は本
考案の一実施例の系統図である。1は処理塔で、頂部に
処理ガスの排気管26、底部に被処理ガスの給気管21
と排水管25を接続し、内部に微生物を担持した充填層
2と充填層2に散水する散水器6を備え、また充填層2
よりも下方には散水管4と接触材層5から成る昇温手段
3が設けられている。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. FIG. 1 is a system diagram of one embodiment of the present invention. A processing tower 1 has a processing gas exhaust pipe 26 at the top and a gas supply pipe 21 at the bottom.
And a drain pipe 25, and a packed bed 2 carrying microorganisms therein and a water sprinkler 6 for spraying water on the packed bed 2 are provided.
Below this, a temperature raising means 3 comprising a water sprinkling pipe 4 and a contact material layer 5 is provided.

【0020】前記充填層2は長尺繊維束、多孔質セラミ
ックス及びプラスチック等微生物が着生する担体であれ
ば何れでもよいが、微生物の良好な着生、繁殖や、圧力
損失及び気液接触効率等の観点から長尺繊維束を多数集
束して充填層2を形成するのが好ましい。
The filler layer 2 may be any carrier such as long fiber bundles, porous ceramics, and plastics, on which microorganisms can be formed. However, good growth and propagation of microorganisms, pressure loss and gas-liquid contact efficiency can be achieved. From the viewpoint of the above, it is preferable to form the filling layer 2 by bundling a number of long fiber bundles.

【0021】前記散水器6は充填層2の上部に均一散水
が行われるよう、多数のスプレ−ノズルが平面上にほぼ
等間隔に配置されており、また充填層2を複数段設けて
もよい。
In the sprinkler 6, a large number of spray nozzles are arranged at substantially equal intervals on a plane so that water can be uniformly sprayed on the upper portion of the packed bed 2, and a plurality of packed beds 2 may be provided. .

【0022】前記昇温手段3として設けられた散水管4
は、前記散水器6と同様な構造が好ましく、また接触材
層5はセラミックスやプラスチック等、酸により腐食し
にくい材質の担体が用いられ、また昇温手段3として
は、前記散水管4と接触材層5とを組合せた構成に限定
されるものではなく、気液接触が良好に行われる手段で
あればよい。
A water pipe 4 provided as the temperature raising means 3
The contact member layer 5 is preferably made of a material that is hardly corroded by acid, such as ceramics or plastic, and the contact member layer 5 is made of a material that is in contact with the sprinkler tube 4 as the temperature raising means 3. The configuration is not limited to the configuration in which the material layer 5 is combined with the material layer 5 and may be any means that enables good gas-liquid contact.

【0023】7は活性炭吸着塔であり、内部に活性炭層
8が設けられ、下部に処理塔1で処理された処理ガスの
排気管26が接続され、上部には活性炭により吸着処理
された処理ガスを排出する排気管26bが接続されてい
る。
Reference numeral 7 denotes an activated carbon adsorption tower, in which an activated carbon layer 8 is provided, an exhaust pipe 26 for the treated gas treated in the treatment tower 1 is connected to the lower part, and a treated gas adsorbed by the activated carbon is attached to the upper part. Is connected to an exhaust pipe 26b that discharges air.

【0024】10は散水器6及び昇温手段3の散水管4
に供給される水の流量を制御する制御装置であり、制御
弁13a、13bの開閉を制御して水の供給流量の制御
及び供給管路の切替えを行うよう構成しているが、これ
に限定されるものではない。
Reference numeral 10 denotes a water sprinkler 6 and a water sprinkling pipe 4 of the temperature raising means 3.
Is a control device for controlling the flow rate of water supplied to the apparatus. The control apparatus controls opening and closing of the control valves 13a and 13b to control the supply flow rate of water and to switch the supply pipe. It is not something to be done.

【0025】11は散水器6及び散水管4に水を供給す
る給水ポンプであり、散水器6及び散水管4に供給され
る水が相違する場合には、それぞれの供給流路毎に配置
される。また、12は処理ガスを排出するため排気管2
6に設けられた排気ブロワであるが、排気ブロア12に
換えて、被処理ガスの給気管21に給気ブロアを設けて
もよい。
Numeral 11 denotes a water supply pump for supplying water to the sprinkler 6 and the sprinkler pipe 4. If the water supplied to the sprinkler 6 and the sprinkler pipe 4 is different, the water supply pump is arranged for each supply flow path. You. Reference numeral 12 denotes an exhaust pipe 2 for discharging the processing gas.
Although the exhaust blower is provided in 6, an air supply blower may be provided in the air supply pipe 21 of the gas to be processed instead of the exhaust blower 12.

【0026】次に、前記構成の生物脱臭装置で悪臭ガス
を脱臭処理する作用について以下記述する。し尿処理場
や下水処理場から発生した悪臭成分を含有する被処理ガ
スを給気管21から処理塔1に供給する。
Next, the operation of deodorizing odorous gas with the biological deodorizing device having the above-mentioned structure will be described. A gas to be treated containing a malodorous component generated from a night soil treatment plant or a sewage treatment plant is supplied to the treatment tower 1 from the air supply pipe 21.

【0027】供給された被処理ガスは、昇温手段3の接
触材層5を上向流で流通する間に、昇温給水管24を経
て散水管4から供給される生物処理水と接触されて、生
物処理水が持つ熱量との熱交換により昇温される。
The supplied gas to be treated is brought into contact with the biologically treated water supplied from the water sprinkling pipe 4 via the heating water supply pipe 24 while flowing through the contact material layer 5 of the temperature raising means 3 in an upward flow. Then, the temperature is raised by heat exchange with the calorific value of the biologically treated water.

【0028】昇温された被処理ガスは更に上向流し、微
生物が担持された充填層2を上向流で流通する間に、硫
化水素等の硫黄化合物やアンモニアを主体とする悪臭ガ
スが充填層2の着生微生物により生物学的に酸化分解さ
れ、アンモニアは硝酸イオン、硫黄化合物は硫酸イオン
として、充填層2に固定化される。
The heated gas to be treated further flows upward, and while flowing through the packed bed 2 carrying microorganisms in an upward flow, the odorous gas mainly composed of sulfur compounds such as hydrogen sulfide or ammonia is charged. Biologically oxidatively decomposed by the epiphytic microorganisms in the layer 2, ammonia is fixed to the packed layer 2 as nitrate ions and sulfur compounds as sulfate ions.

【0029】処理ガスは排気ブロワ12で吸引されて排
気管26から活性炭吸着塔7に供給され、活性炭層8を
上向流で流通する間に、微生物により分解されにくく残
留し易い有機硫黄化合物等が吸着除去され、排気管26
bを経て排気管26cから大気中に放出される。
The processing gas is sucked by the exhaust blower 12, supplied to the activated carbon adsorption tower 7 from the exhaust pipe 26, and flows through the activated carbon layer 8 in an upward flow. Is adsorbed and removed, and the exhaust pipe 26
The gas is discharged from the exhaust pipe 26c into the atmosphere via the line b.

【0030】尚、被処理ガスに含有された悪臭成分の組
成によっては、処理塔1のみで十分清浄化されるため、
処理ガスは活性炭吸着塔7に供給されることなく、排気
管26aを経て排気管26cから大気中に放出される。
Incidentally, depending on the composition of the malodorous component contained in the gas to be treated, the gas is sufficiently cleaned only in the treatment tower 1,
The processing gas is discharged to the atmosphere from the exhaust pipe 26c via the exhaust pipe 26a without being supplied to the activated carbon adsorption tower 7.

【0031】充填層2は硫酸イオン等の酸性成分が蓄積
し、PHを低下させて微生物の生育を阻害するため、連
続又は間欠的に散水して、それらを洗浄除去する必要が
あり、散水用の水は、給水ポンプ11で散水給水管23
を経て散水器6により、充填層2の上部に略均一に散水
される。
The packed layer 2 accumulates acidic components such as sulfate ions and lowers the pH to inhibit the growth of microorganisms. Therefore, it is necessary to spray water continuously or intermittently and wash and remove them. Water is supplied by the water supply pump 11 to the water supply pipe 23
And water is sprinkled almost uniformly on the upper part of the packed bed 2 by the sprinkler 6.

【0032】前記散水は、PHを低下させる酸性成分の
洗浄以外にも、微生物の生育に必要な栄養素の供給や好
適な湿潤状態の保持及び過剰に繁殖した微生物の除去等
に必要な操作である。
The watering is an operation necessary for supplying nutrients necessary for the growth of microorganisms, maintaining a suitable wet state, and removing excessively propagated microorganisms, in addition to washing the acidic components that lower the pH. .

【0033】また、散水に使用される水としては、河川
水、地下水等でもよいが、し尿や下水等を生物処理した
処理水を用いるのが、着生微生物や栄養素を適度に含有
し、PHの緩衝性も有しているため、微生物生育や好適
PHの維持のうえから好ましい。
The water used for sprinkling may be river water, groundwater, or the like. However, treated water obtained by biologically treating human waste or sewage is preferably used because it contains epiphytic microorganisms and nutrients appropriately, and It is also preferable from the viewpoint of microbial growth and maintenance of a suitable PH.

【0034】尚、散水時には若干脱臭効率が低下するた
め、間欠的に散水を行うのが好ましく、散水器6及び昇
温手段3への給水量は、制御弁13a、13bを制御装
置10で制御することにより行われるが、散水器6での
散水時には、昇温手段3での散水を停止し交互に散水す
るのが、動力費の低減や排水の後処理の関係から好まし
いが、気温が極度に低下する時期には、昇温手段3での
散水を連続的に行うのが好ましい。
Since the efficiency of deodorization is slightly reduced during water sprinkling, it is preferable to intermittently sprinkle water. The amount of water supplied to the sprinkler 6 and the temperature raising means 3 is controlled by the control device 10 by controlling the control valves 13a and 13b. In sprinkling with the sprinkler 6, it is preferable to stop the sprinkling with the temperature raising means 3 and alternately sprinkle water in view of reduction of power cost and post-treatment of drainage. It is preferable to continuously spray water by the temperature raising means 3 at the time when the temperature decreases.

【0035】処理塔1の底部に滞留した散水排水は、排
水管25からドレンピット9に供給され、一定量貯留さ
れた後排水管25aから系外に排出されるが、散水器6
と昇温手段3との散水を交互に行う場合には、排水の性
状が相違するため、別途に取り扱うのが好ましい。
The water sprinkled and drained at the bottom of the treatment tower 1 is supplied to the drain pit 9 from a drain pipe 25, and after being stored in a certain amount, discharged from the drain pipe 25a to the outside of the system.
When watering is performed alternately with the temperature raising means 3, the properties of the drainage are different, so it is preferable to handle the water separately.

【0036】[0036]

【考案の効果】本考案の生物脱臭装置によれば下記の効
果がえられる。冬季等の気温が極度に低くなる時期、特
に寒冷地等においては、被処理ガスの温度も10℃以下
に低下し、また昼夜の気温差も極めて大きくなり、微生
物の活性も低下して脱臭効果も悪くなるため、被処理ガ
スの温度を昇温するのが好ましいが、燃料を用い、加熱
装置を別置するのは運転経費や設備費の上昇から従来は
行われていなかった。本考案の生物脱臭装置では、汚水
を生物処理した処理水の持つ熱量を利用するため、運転
経費が安価で、また処理塔内に一体的に配置するため、
設置場所も大きくならず、更に散水装置程度の設備であ
るため、設備費も安価で、運転管理も容易である。
According to the biological deodorizing apparatus of the present invention, the following effects can be obtained. In winter, when the temperature becomes extremely low, especially in cold regions, the temperature of the gas to be treated also drops to 10 ° C or less, the temperature difference between day and night becomes extremely large, the activity of microorganisms decreases, and the deodorizing effect is obtained. Therefore, it is preferable to raise the temperature of the gas to be treated. However, it has not been conventionally performed to use a fuel and separately install a heating device due to an increase in operation costs and equipment costs. In the biological deodorization device of the present invention, since the heat amount of the treated water obtained by biologically treating the sewage is used, the operation cost is low, and since it is disposed integrally in the treatment tower,
Since the installation place is not large and the facility is almost the same as a sprinkler, the facility cost is low and the operation management is easy.

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

【図1】本考案の一実施例の系統図FIG. 1 is a system diagram of an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:処理塔 2:充填層 3:昇温手段 4:散水管 5:接触材層 6:散水器 7:活性炭吸着塔 8:活性炭層 9:ドレンピット 10:制御装置 11:給水ポンプ 12:排気ブロア 13a、13b:制御弁 21:給気管 22:給水管 23:散水給水管 24:昇温給水管 25、25a:排水管 26、26a、26b、26c:排気管 1: treatment tower 2: packed bed 3: heating means 4: water spray pipe 5: contact material layer 6: water sprayer 7: activated carbon adsorption tower 8: activated carbon bed 9: drain pit 10: control device 11: water supply pump 12: exhaust Blowers 13a, 13b: Control valve 21: Air supply pipe 22: Water supply pipe 23: Sprinkling water supply pipe 24: Heating water supply pipe 25, 25a: Drainage pipe 26, 26a, 26b, 26c: Exhaust pipe

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】頂部に処理ガスの排気管(26)、底部に
被処理ガスの給気管(21)と排水管(25)とを接続
し、内部に微生物を担持した充填層(2)と前記充填層
(2)に散水する散水器(6)を備え、被処理ガスを上
向流で通気して悪臭成分を分解処理する処理塔(1)の
前記充填層(2)より下方に、汚水を生物処理した処理
水と被処理ガスとを接触させて被処理ガスを昇温する昇
温手段(3)を設け、前記散水器(6)と前記昇温手段
(3)とに供給される水の供給、停止を所定の時間間隔
で制御する制御手段(10)を備えたことを特徴とする
生物脱臭装置。
An exhaust pipe (26) for a processing gas is connected to the top, and a gas supply pipe (21) and a drain pipe (25) for the gas to be processed are connected to the bottom, and a packed bed (2) carrying microorganisms therein. A sprinkler (6) for sprinkling water on the packed bed (2) is provided .
Of the treatment tower (1), which decomposes odorous components by ventilating in countercurrent
Biological treatment of sewage below the packed bed (2)
Raise the temperature of the gas to be treated by contacting the gas with the gas to be treated.
A heating means (3), wherein the water sprinkler (6) and the heating means
(3) supply and stop of the water supplied to the predetermined time interval
Control means (10) for controlling by means of
Biological deodorizer.
JP1993057351U 1993-09-30 1993-09-30 Biological deodorizer Expired - Fee Related JP2605769Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1993057351U JP2605769Y2 (en) 1993-09-30 1993-09-30 Biological deodorizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1993057351U JP2605769Y2 (en) 1993-09-30 1993-09-30 Biological deodorizer

Publications (2)

Publication Number Publication Date
JPH0724428U JPH0724428U (en) 1995-05-09
JP2605769Y2 true JP2605769Y2 (en) 2000-08-07

Family

ID=13053164

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1993057351U Expired - Fee Related JP2605769Y2 (en) 1993-09-30 1993-09-30 Biological deodorizer

Country Status (1)

Country Link
JP (1) JP2605769Y2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007136252A (en) * 2005-11-14 2007-06-07 Sumitomo Heavy Ind Ltd Deodorization method and apparatus for odor gas
JP2015208721A (en) * 2014-04-26 2015-11-24 喜弘 松村 Rapid and continuous separation deodorizing device

Also Published As

Publication number Publication date
JPH0724428U (en) 1995-05-09

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