JP3476572B2 - Biological deodorizer - Google Patents
Biological deodorizerInfo
- Publication number
- JP3476572B2 JP3476572B2 JP33049194A JP33049194A JP3476572B2 JP 3476572 B2 JP3476572 B2 JP 3476572B2 JP 33049194 A JP33049194 A JP 33049194A JP 33049194 A JP33049194 A JP 33049194A JP 3476572 B2 JP3476572 B2 JP 3476572B2
- Authority
- JP
- Japan
- Prior art keywords
- biological
- malodorous
- flow path
- tank
- gas
- 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
【0001】[0001]
【産業上の利用分野】本発明は水処理設備から発生する
悪臭ガスを生物学的に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 device for biologically deodorizing malodorous gas generated from a water treatment facility.
【0002】[0002]
【従来の技術】し尿処理場や下水処理場等における最初
沈殿池、曝気槽、及び汚泥濃縮槽等からは、有機物の生
物学的分解過程で生成する硫化水素やメルカプタンタン
等の硫黄化合物、及びアンモニア等の悪臭物質を含有す
る悪臭ガスが発生する。2. Description of the Related Art Sulfur compounds such as hydrogen sulfide and mercaptan tan, which are produced in the process of biological decomposition of organic matter, from the first settling tank, aeration tank, sludge thickening tank, etc. in human waste treatment plants and sewage treatment plants, and A malodorous gas containing a malodorous substance such as ammonia is generated.
【0003】従来、上記発生した悪臭ガス中の悪臭物質
は、活性炭等の吸着剤で吸着除去する吸着法、アルカリ
溶液や次亜塩素酸溶液等で吸収除去する化学吸収法及び
微生物を担持した担体層で生物学的に分解除去する生物
分解法等により処理されている。Conventionally, the malodorous substances in the malodorous gas generated above are adsorbed and removed by an adsorbent such as activated carbon, a chemical absorption method by which they are absorbed and removed by an alkaline solution or a hypochlorous acid solution, and a carrier carrying microorganisms. The layer is treated by a biodegradation method or the like that is biologically decomposed and removed.
【0004】[0004]
【発明が解決しようとする課題】上記吸着法や化学吸収
法においては、設備費や薬液の消費等に伴う運転経費が
嵩み、また煩雑な維持管理を必要とする欠点が有り、ま
た従来の生物分解法においては、微生物の生育管理や分
解生成物の除去等に高度な技術を要すると共に、微生物
の生育適温は30℃前後であるため冬季等の気温が低下
する時期等には、脱臭効率を維持するために加熱が必要
になる等、温度管理が煩雑となると共に、悪臭ガスの加
熱経費も嵩む欠点がある。The above-mentioned adsorption method and chemical absorption method have the drawbacks that the operating costs are high due to equipment costs and consumption of chemicals, and that complicated maintenance is required. The biodegradation method requires sophisticated techniques for controlling the growth of microorganisms and removing decomposition products, and since the optimum temperature for growing microorganisms is around 30 ° C, the deodorization efficiency is low when the temperature decreases, such as in winter. However, there is a drawback that the temperature control becomes complicated, such as heating is required to maintain the temperature, and the cost of heating the malodorous gas increases.
【0005】尚、生物分解法の簡易な方法として、曝気
槽の活性汚泥混合液中に悪臭ガスを吹き込んで処理する
方法もあるが、悪臭ガスと活性汚泥混合液との接触が極
めて不十分のため、悪臭成分が十分に吸収されず、脱臭
効率が低い欠点がある。As a simple method of the biodegradation method, there is a method in which a malodorous gas is blown into the activated sludge mixed liquid in the aeration tank for treatment, but the contact between the malodorous gas and the activated sludge mixed liquid is extremely insufficient. Therefore, the malodorous components are not sufficiently absorbed and the deodorization efficiency is low.
【0006】従って、本発明は設備費や運転経費が低廉
で、運転管理等も容易な脱臭装置を提供する目的で、上
記活性汚泥混合液中に悪臭ガスを吹き込んで処理する方
法の簡便性に着目し、その欠点を解消することにより成
されたものである。Therefore, the present invention provides a deodorizing device which is low in equipment costs and operating costs, and which can be easily operated and managed. Therefore, in order to provide a simple method for treating malodorous gas by blowing it into the activated sludge mixture, It was made by paying attention and eliminating its drawbacks.
【0007】[0007]
【課題を解決するための手段】上記目的を達成する本発
明の要旨は、悪臭ガスを活性汚泥混合液で脱臭処理する
生物脱臭装置において、生物脱臭槽内に活性汚泥混合液
が循環流通する上昇流路及び下降流路とを設け、上昇流
路に空気の吹き込み手段、下降流路に悪臭ガスの導入手
段とを配設し、上部に活性汚泥混合液の散水手段及び排
出路と、頂部に処理ガスの排出路を具備したことを特徴
とする生物脱臭装置である。Means for Solving the Problems The gist of the present invention to achieve the above object is to increase the circulation of an activated sludge mixed solution in a biological deodorization tank in a biological deodorizing apparatus for deodorizing malodorous gas with an activated sludge mixed solution. A flow path and a descending flow path are provided, an ascending air flow means is provided in the ascending flow path, a malodorous gas introducing means is provided in the descending flow path, a sprinkling means and a discharge path for the activated sludge mixed liquid are provided on the upper part, and the top part is provided. The biological deodorizing device is characterized in that it is provided with a discharge path for treated gas.
【0008】また、生物脱臭槽内の活性汚泥混合液中
に、悪臭物質分解能を有する微生物を担持した生物担体
を分散混合したことを特徴とする上記生物脱臭装置であ
る。Further, the above-mentioned biological deodorizing apparatus is characterized in that a biological carrier carrying a microorganism having a degrading odor substance is dispersed and mixed in the activated sludge mixed solution in the biological deodorizing tank.
【0009】[0009]
【作用】曝気槽から供給された活性汚泥混合液(以下単
に混合液という。)を充填した生物脱臭槽の上昇流路に
空気吹き込み手段から空気を供給すると、エアリフト効
果により混合液の循環流が生起される。[Function] When air is supplied from the air blowing means to the ascending flow path of the biological deodorizing tank filled with the activated sludge mixed liquid (hereinafter simply referred to as mixed liquid) supplied from the aeration tank, the circulating flow of the mixed liquid is generated by the air lift effect. It is caused.
【0010】混合液の循環流が安定した段階で、水処理
設備から発生した悪臭ガスを悪臭ガス導入手段から生物
脱臭槽の下降流路に導入すると、循環流に伴われて下降
し、下端の連通部から上昇流路に流入して上昇し、本経
路を流通する間に悪臭物質が吸収され、更に混合液中の
微生物により生物学的に分解除去される。When the malodorous gas generated from the water treatment equipment is introduced from the malodorous gas introduction means into the descending flow path of the biological deodorizing tank at the stage where the circulation flow of the mixed liquid is stable, the malodorous gas descends along with the circulation flow, The malodorous substance is absorbed while flowing into the ascending flow path from the communicating portion and flowing up through this path, and further biologically decomposed and removed by the microorganisms in the mixed liquid.
【0011】尚、混合液中に悪臭物質分解能を有する硫
黄酸化菌や硝化菌等を担持した生物担体を分散混合する
ことにより、単位容積当たりの微生物濃度を高くでき、
悪臭物質の分解能を高くすることができる。By mixing and mixing a biological carrier carrying sulfur-oxidizing bacteria and nitrifying bacteria capable of degrading malodorous substances in the mixed solution, the concentration of microorganisms per unit volume can be increased,
The resolution of malodorous substances can be increased.
【0012】また通常は、悪臭物質の殆どは上記工程で
除去されるが、悪臭物質の含有量等によっては、混合液
中から槽内の空隙部に放散される処理ガス中に悪臭物質
が残留する場合もあるが、散水手段から散水される新規
な混合液により吸収され、槽内液中に循環混合されるこ
とにより処理される。Usually, most of the malodorous substances are removed in the above process, but depending on the content of the malodorous substances, the malodorous substances remain in the process gas emitted from the mixed solution into the voids in the tank. In some cases, it is absorbed by the novel mixed liquid sprinkled from the sprinkling means and is circulated and mixed in the liquid in the tank for treatment.
【0013】尚、悪臭物質が除去された処理ガスは、循
環流発生用の空気と共に処理ガスの排出路から大気中に
放散され、また槽内の混合液の一部は混合液の排出路か
ら曝気槽に返送される。The processing gas from which the malodorous substance has been removed is diffused into the atmosphere from the discharge path of the processing gas together with the air for generating the circulation flow, and a part of the mixed liquid in the tank is discharged from the discharge path of the mixed liquid. Returned to the aeration tank.
【0014】[0014]
【実施例】本発明を図面に基づいて説明する。図1は本
発明の一実施例の系統図であり、1は内筒と外筒との2
重筒構造の生物脱臭槽で、曝気槽10の側部に一体的に
付設され、内筒内を混合液の上昇流路2、内筒と外筒と
の間を混合液の下降流路3とし、上端及び下端に連通部
を有し、充填される混合液の循環流路を形成している。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described with reference to the drawings. FIG. 1 is a system diagram of an embodiment of the present invention, in which 1 is an inner cylinder and an outer cylinder.
This is a biological deodorization tank having a heavy-cylinder structure, which is integrally attached to a side portion of the aeration tank 10, and has a mixed liquid ascending passage 2 inside the inner cylinder and a mixed liquid descending passage 3 between the inner cylinder and the outer cylinder. And has a communicating portion at the upper end and the lower end to form a circulation flow path for the mixed liquid to be filled.
【0015】尚上記生物脱臭槽1は、設置面積の節約等
の関係から曝気槽10の側部に一体的に付設されるのが
好ましいが、曝気槽10と離して配置してもよい。The biological deodorization tank 1 is preferably attached integrally to the side of the aeration tank 10 in order to save the installation area, but it may be arranged separately from the aeration tank 10.
【0016】上記上昇流路2には空気供給ブロワ12か
ら供給される空気の吹き込み手段5、下降流路3には悪
臭ガス供給ブロワ11から供給される悪臭ガスの導入手
段4とが配設されており、生物脱臭槽1の上部には混合
液の散水手段6及び混合液の排出路7と、頂部には処理
ガスの排出路8が具備されている。The ascending flow path 2 is provided with a blowing means 5 for blowing air supplied from an air supply blower 12, and the descending flow path 3 is provided with a bad smell gas introduction means 4 supplied from a malodorous gas supply blower 11. The biological deodorizing tank 1 is provided with a sprinkling means 6 for the mixed liquid and a discharge passage 7 for the mixed liquid, and a discharge passage 8 for the treated gas at the top.
【0017】 尚、上記空気の吹き込み手段5及び悪臭
ガスの導入手段4は複数のノズルを設けた管でも、また
水処理設備で通常用いられている散気管等でもよく、空
気の吹き込み手段5に供給される空気は、供給ブロワ1
2で供給されるが、曝気空気供給ブロワ13から曝気槽
10に送られている生物処理用の空気を分岐して供給す
ることも可能であり、その場合には特に供給ブロワ12
を設ける必要はない。The air blowing means 5 and the malodorous gas introducing means 4 may be a tube provided with a plurality of nozzles, or an air diffusing tube or the like normally used in water treatment equipment. The air supplied is the supply blower 1
2 is supplied, but it is also possible to branch and supply the air for biological treatment sent from the aerated air supply blower 13 to the aeration tank 10. In that case, especially the supply blower 12
Need not be provided.
【0018】更に、上記混合液の散水手段6は、混合液
供給路9及び混合液供給ポンプ14を介して曝気槽10
に接続されており、上昇流路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
に配置されているのが好ましいが、これには限定され
ず、また混合液の排出路7はオ−バ−フロ−部材を介
し、曝気槽10と連通して接続されるのが好ましい。Further, the means for sprinkling the mixed solution 6 has the aeration tank 10 via the mixed solution supply passage 9 and the mixed solution supply pump 14.
It is preferable that a large number of spray nozzles are arranged on the plane at substantially equal intervals so that uniform water sprinkling is performed on the upper part of the ascending flow path 2, but it is not limited to this. The discharge passage 7 for the mixed liquid is preferably connected to the aeration tank 10 via an overflow member.
【0019】尚、生物脱臭槽1の混合液中に悪臭物質分
解能を有する硫黄酸化菌や硝化菌等を担持した微生物担
体を分散混合し、単位容積当たりの微生物濃度を高くす
ることにより、悪臭物質の分解効率を向上させるように
することも好ましく、微生物担体としては、活性炭、腐
植土、合成樹脂粒等の表面に微生物を着生繁殖させた担
体やポリビニルアルコ−ル、ポリエチレングリコ−ル等
に包括固定化した担体でもよい。A malodorous substance is obtained by dispersing and mixing a microbial carrier carrying sulfur-oxidizing bacteria and nitrifying bacteria capable of decomposing malodorous substances in the mixed liquid of the biological deodorization tank 1 to increase the concentration of microorganisms per unit volume. It is also preferable to improve the decomposition efficiency of the microbial carrier, and examples of the microbial carrier include activated carbon, humus, a carrier in which microorganisms are vegetatively propagated on the surface of synthetic resin particles, polyvinyl alcohol, polyethylene glycol and the like. The carrier may be entrapped and immobilized.
【0020】また、被処理ガス中に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、後段に活性
炭吸着塔を設け、更に吸着清浄化処理した後大気中に放
散するのが好ましい。When the gas to be treated contains a large amount of organic sulfur compounds which are difficult to be decomposed by microorganisms, they may remain in the treated gas. Therefore, an activated carbon adsorption tower is provided in the subsequent stage to further adsorb and clean the adsorption gas. It is preferable to diffuse into the atmosphere after chemical conversion treatment.
【0021】次に、上記構成の生物脱臭装置における作
用について以下記述すると、曝気槽10から混合液供給
路9を経て混合液供給ポンプ14で供給された混合液を
生物脱臭槽1に充填し、上昇流路2に、空気吹き込み手
段5から空気を供給すると、エアリフト効果により混合
液の循環流が生起される。Next, the operation of the biological deodorizing apparatus having the above structure will be described below. The biological deodorizing tank 1 is filled with the mixed liquid supplied from the aeration tank 10 via the mixed liquid supply passage 9 by the mixed liquid supply pump 14. When air is supplied to the ascending flow path 2 from the air blowing means 5, a circulating flow of the mixed liquid is generated due to the air lift effect.
【0022】混合液の循環流が安定した段階で、水処理
設備で発生した悪臭ガスを、悪臭ガス導入手段4から生
物脱臭槽1の下降流路3に導入すると、循環流に伴われ
て下降し、下端の連通部から上昇流路2に流入して上昇
し、本経路を流通する間に悪臭物質が吸収され、更に混
合液中の微生物により生物学的に分解除去される。When the malodorous gas generated in the water treatment facility is introduced from the malodorous gas introducing means 4 into the descending flow path 3 of the biological deodorizing tank 1 at the stage where the circulation flow of the mixed liquid is stable, the malodorous gas descends along with the circulation flow. Then, the malodorous substance is absorbed while flowing into the ascending flow path 2 from the communicating portion at the lower end and flowing up through the main passage, and further biologically decomposed and removed by the microorganisms in the mixed liquid.
【0023】尚、混合液中に悪臭物質分解能を有する硫
黄酸化菌や硝化菌等を担持した生物担体を分散混合する
場合には、単位容積当たりの微生物濃度が高まり、悪臭
物質の分解能を高くすることができる。When a biological carrier carrying sulfur-oxidizing bacteria or nitrifying bacteria capable of degrading malodorous substances is dispersed and mixed in a mixed solution, the concentration of microorganisms per unit volume is increased and the resolution of malodorous substances is increased. be able to.
【0024】また通常は、悪臭物質の殆どが上記工程で
除去されるが、悪臭物質の含有量等によっては、混合液
中から生物脱臭槽1内の空隙部に放散される処理ガス中
に残留する場合もあるが、曝気槽10に接続した混合液
供給路9から混合液供給ポンプ14で供給され、散水手
段6から散水される新規な混合液により吸収され、槽内
液中に循環混合されて処理される。Further, most of the malodorous substances are usually removed in the above process, but depending on the content of the malodorous substances, etc., they remain in the treated gas emitted from the mixed solution into the voids in the biological deodorization tank 1. In some cases, it is supplied by the mixed solution supply pump 14 from the mixed solution supply passage 9 connected to the aeration tank 10, absorbed by the new mixed solution sprayed from the sprinkling means 6, and circulated and mixed in the solution in the tank. Will be processed.
【0025】尚、悪臭物質が除去された処理ガスは、循
環流発生用の空気と共に処理ガスの排出路8から大気中
に放散され、また槽内の混合液の一部は混合液の排出路
7から曝気槽10に返送される。The processing gas from which the malodorous substances have been removed is diffused into the atmosphere from the processing gas discharge passage 8 together with the air for generating the circulating flow, and a part of the mixed liquid in the tank is discharged from the mixed liquid. It is returned from 7 to the aeration tank 10.
【0026】[0026]
【発明の効果】本発明の生物脱臭装置によれば下記の効
果が得られる。従来の吸着法や化学吸収法では、設備費
や薬液の消費等に伴う運転経費が嵩み、また煩雑な維持
管理を必要とし、また従来の生物分解法においては、微
生物の生育管理や分解生成物の除去等に高度な技術を要
すると共に、冬季等の気温が低下する時期等には、脱臭
効率を維持するために加熱が必要になる等、温度管理が
煩雑となると共に、悪臭ガスの加熱経費も嵩むが、適宜
な温度を持つ活性汚泥混合液中に悪臭ガスを吹き込んで
処理するため、気温の変化にも影響されにくく、また薬
液等も使用せず、設備費や運転経費も低廉である。According to the biological deodorizing apparatus of the present invention, the following effects can be obtained. The conventional adsorption method or chemical absorption method requires high operating costs due to equipment costs, consumption of chemicals, etc., and requires complicated maintenance.In the conventional biodegradation method, microbial growth control and decomposition production are required. In addition to requiring sophisticated technology to remove things, heating is required to maintain deodorization efficiency during periods such as winter when the temperature drops, and temperature control is complicated and heating of malodorous gas is required. Although the cost is high, the odorous gas is blown into the activated sludge mixture that has an appropriate temperature for treatment, so it is not easily affected by changes in temperature, and chemicals are not used, so equipment costs and operating costs are low. is there.
【図1】本発明の一実施例の系統図FIG. 1 is a system diagram of an embodiment of the present invention.
1:生物脱臭槽 2:上昇流路 3:下降流路 4:悪臭ガス導入手段 5:空気吹き込み手段 6:活性汚泥混合液散水手段 7:活性汚泥混合液排出路 8:処理ガス排出路 9:活性汚泥混合液供給路 10:曝気槽 11:悪臭ガス供給ブロワ 12:空気供給ブロワ 13:曝気空気供給ブロワ 14:活性汚泥混合液供給ポンプ 1: Biological deodorization tank 2: Ascending channel 3: Downward flow path 4: Odorous gas introduction means 5: Air blowing means 6: means for sprinkling activated sludge mixture 7: Activated sludge mixed liquid discharge channel 8: Process gas discharge path 9: Activated sludge mixed liquid supply path 10: Aeration tank 11: Bad smell gas supply blower 12: Air supply blower 13: Aerated air supply blower 14: Activated sludge mixed liquid supply pump
Claims (2)
生物脱臭装置において、生物脱臭槽内に活性汚泥混合液
が循環流通する上昇流路及び下降流路とを設け、上昇流
路に空気の吹き込み手段、下降流路に悪臭ガスの導入手
段とを配設し、上部に活性汚泥混合液の散水手段及び排
出路と、頂部に処理ガスの排出路を具備したことを特徴
とする生物脱臭装置。1. A biological deodorizing device for deodorizing malodorous gas with an activated sludge mixture, wherein an ascending flow path and a descending flow path for circulating the activated sludge mixed solution are provided in the biological deodorization tank, and air is provided in the ascending flow path. A biological deodorizing device characterized in that it is provided with a blowing means for the above, a means for introducing a malodorous gas in the descending flow path, and a sprinkling means and a discharge path for the activated sludge mixed liquid in the upper part and a discharge path for the treated gas in the top part. apparatus.
物質分解能を有する微生物を担持した生物担体を分散混
合したことを特徴とする請求項1記載の生物脱臭装置。2. The biological deodorizing apparatus according to claim 1, wherein a biological carrier carrying a microorganism having a capability of degrading malodorous substances is dispersed and mixed in the activated sludge mixed solution in the biological deodorizing tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33049194A JP3476572B2 (en) | 1994-12-08 | 1994-12-08 | Biological deodorizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33049194A JP3476572B2 (en) | 1994-12-08 | 1994-12-08 | Biological deodorizer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08155251A JPH08155251A (en) | 1996-06-18 |
JP3476572B2 true JP3476572B2 (en) | 2003-12-10 |
Family
ID=18233225
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33049194A Expired - Fee Related JP3476572B2 (en) | 1994-12-08 | 1994-12-08 | Biological deodorizer |
Country Status (1)
Country | Link |
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JP (1) | JP3476572B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5503834B2 (en) * | 2006-09-29 | 2014-05-28 | 大成建設株式会社 | Contaminated air purifier |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0687942B2 (en) * | 1988-05-19 | 1994-11-09 | 株式会社新潟鉄工所 | Biological deodorization method for odorous components |
JP3113668B2 (en) * | 1990-05-28 | 2000-12-04 | 日本化成株式会社 | Deodorization method |
-
1994
- 1994-12-08 JP JP33049194A patent/JP3476572B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH08155251A (en) | 1996-06-18 |
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