JPH07284629A - Biological deodorizing carrier - Google Patents

Biological deodorizing carrier

Info

Publication number
JPH07284629A
JPH07284629A JP6080594A JP8059494A JPH07284629A JP H07284629 A JPH07284629 A JP H07284629A JP 6080594 A JP6080594 A JP 6080594A JP 8059494 A JP8059494 A JP 8059494A JP H07284629 A JPH07284629 A JP H07284629A
Authority
JP
Japan
Prior art keywords
gel
carrier
adsorption
reaction zone
malodorous
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.)
Granted
Application number
JP6080594A
Other languages
Japanese (ja)
Other versions
JP2885060B2 (en
Inventor
Toshiyuki Nakajima
敏幸 中島
Masaichirou Nishie
雅一朗 西江
Morio Mimura
精男 三村
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel Ltd
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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP6080594A priority Critical patent/JP2885060B2/en
Publication of JPH07284629A publication Critical patent/JPH07284629A/en
Application granted granted Critical
Publication of JP2885060B2 publication Critical patent/JP2885060B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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)

Abstract

PURPOSE:To obtain a biological deodorizing carrier with the treating activity of a decomposing microorganism never lowered while keeping the entire device compact by providing a reaction zone carrying a malodorous material decomposing microorganism and a malodorous material adsorbing and desorbing zone to the carrier. CONSTITUTION:A polymer is dissolved in water to form a gel material soln., and the soln. is subjected to a chemical method with a cross-linking agent, etc., and a physical method of repeated freezing and melting and cross-linked to obtain a gel bead. The gelled bead is then introduced into a soln. of a gel material of the same or different kind to coat the surface with the gel soln. A specified malodorous material decomposing microorganism is mixed into the outer soln. before being gelled to form a gel entrapping the microorganism. Consequently, the biological deodorizing carrier 3 is provided with a reaction zone 2 carrying a malodorous material decomposing microorganism and a malodorous material adsorbing and desorbing zone 1.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、悪臭物質分解性微生物
を用いて悪臭物質の分解処理を行う生物脱臭担体に関す
るものであり、該担体は例えば下水処理場、屎尿処理
場、ゴミ処理場、畜産業施設などから発生する悪臭ガス
や液体(以下、合わせて被処理ガスと称することがあ
る)等の脱臭に利用できる。特に本発明の生物脱臭担体
は、処理すべき悪臭物質の濃度変動(存在・通過の有無
を含む)といった負荷変動にも対応して、有効に脱臭処
理を行うことが可能なものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biological deodorizing carrier for decomposing malodorous substances using a malodorous substance-degrading microorganism, which carrier is, for example, a sewage treatment plant, a human waste treatment plant, a waste treatment plant, It can be used for deodorizing offensive odor gas or liquid (hereinafter sometimes collectively referred to as gas to be treated) generated from livestock industry facilities. In particular, the biological deodorizing carrier of the present invention can effectively perform deodorizing treatment in response to load fluctuations such as concentration fluctuations (including presence / absence) of malodorous substances to be treated.

【0002】[0002]

【従来の技術】下水処理場、屎尿処理場などから排出さ
れる悪臭ガス等の処理法としては、従来より活性炭吸着
法、薬液洗浄法、生物脱臭法が知られており、なかでも
微生物の分解能力を活用した生物脱臭法は、経済的に有
利であることから、近年広く普及しつつある。
2. Description of the Related Art Activated carbon adsorption method, chemical cleaning method and biological deodorization method have been conventionally known as a method for treating odorous gas discharged from sewage treatment plants, human waste treatment plants, etc. The biological deodorization method utilizing the ability is becoming widespread in recent years because it is economically advantageous.

【0003】生物脱臭法としては主に充填塔方式が採用
されており、この方式はピート(泥炭)、セラミック多
孔体、プラスチック成形体、合成繊維、木炭、高分子ゲ
ル体、活性炭などを支持体として用い、これに微生物を
固定して充填塔に充填し、これに被処理ガスを通し、微
生物により分解させて脱臭を行うものである。
A packed tower system is mainly adopted as the biological deodorization method, and this system uses peat, ceramic porous body, plastic molded body, synthetic fiber, charcoal, polymer gel body, activated carbon as a support. The microorganism is fixed to the packed tower, and the packed tower is filled with the gas to be treated and decomposed by the microorganism to deodorize.

【0004】被処理ガスの悪臭原因物質のうち、分解脱
臭において特に問題となっているものとしては、硫化メ
チル(以下、MSと称することがある)、二硫化メチル
(以下、DMSと称することがある)、メチルメルカプ
タン(以下、MMPと称することがある)等がある。
Among the substances that cause the malodor of the gas to be treated, methyl sulfide (hereinafter sometimes referred to as MS) and methyl disulfide (hereinafter sometimes referred to as DMS) are particularly problematic in decomposition and deodorization. A) and methyl mercaptan (hereinafter sometimes referred to as MMP).

【0005】これら悪臭原因物質の被処理ガス中濃度は
それほど高いものでなく、しかも発生時刻と共に濃度変
動を示すものであり、場合によっては全く含まれないこ
とも時として生じる。この様に低濃度で且つ負荷変動が
あるために、この悪臭物質を分解して増殖する微生物に
とっては、基質としての悪臭物質が安定して供給されな
いことになり、該微生物の死滅あるいは分解酵素の生成
低下をもたらして悪臭物質分解活性が低下し、その結果
脱臭装置の効率が低下することは避け切れないこととさ
れていた。例えば、休日により下水処理場の操業が一時
休止したときには、分解微生物の存在する処理槽に新た
な悪臭物質が供給されなくなるが、この様な場合に脱臭
能力の低下が起こる。
The concentration of these malodorous substances in the gas to be treated is not so high, and moreover, the concentration changes with the generation time, and in some cases, it may not be contained at all. Due to such low concentration and load fluctuation, the malodorous substance as a substrate is not stably supplied to the microorganism that decomposes and proliferates the malodorous substance. It was inevitable that the production of odorous substances was reduced and the activity of decomposing malodorous substances was reduced, resulting in a reduction in the efficiency of the deodorizing device. For example, when the operation of the sewage treatment plant is suspended due to a holiday, a new malodorous substance is not supplied to the treatment tank containing the decomposing microorganisms, but in such a case, the deodorizing ability is lowered.

【0006】負荷変動を伴う物質は、上述の様に微生物
による分解処理が難しいことから、従来では活性炭によ
る物理吸着処理に依存することが多かった。そこで上述
の問題を解決する装置として、特開平3−181313
号公報に記載の生物脱臭装置(以下、先願公開発明と称
す)が示された。
[0006] Substances accompanied by load fluctuations are often difficult to decompose by microorganisms as described above, and thus, in the past, they have often relied on physical adsorption treatment by activated carbon. Therefore, as an apparatus for solving the above-mentioned problem, Japanese Patent Laid-Open No. 3-181313
The biological deodorizing device described in Japanese Patent Publication (hereinafter referred to as prior invention) is disclosed.

【0007】この生物脱臭装置は、悪臭物質を分解する
微生物を担持する充填層を、悪臭成分の各々に対して各
々の層、即ち硫化水素分解層、MMP分解層、MS分解
層という様に複数層設け、給気される悪臭ガス中の個々
の成分によって個別特異的に分解する様にしたものであ
って、特にMS分解層のガス流通上流側に、MSを破過
吸着した吸着材層を設けたものである。
This biological deodorizing apparatus has a plurality of packing layers carrying microorganisms for decomposing malodorous substances such as hydrogen sulfide decomposing layer, MMP decomposing layer and MS decomposing layer for each malodorous component. A layer is provided so as to be individually and specifically decomposed by each component in the malodorous gas to be supplied, and an adsorbent layer that has adsorbed MS through is adsorbed on the gas distribution upstream side of the MS decomposition layer. It is provided.

【0008】分解微生物のうち特にMS分解微生物は、
基質であるMSがなくなるとMS分解処理能力が低下す
る。そこで、給気される悪臭ガスにMSが存在しないと
きには、上記吸着材層からMSを脱着して、下流のMS
分解層にMSを供給するという様にしてMS分解微生物
にMSを常に供給し、MS分解能力を維持することによ
って高処理能力に保っている。
Among the degrading microorganisms, MS degrading microorganisms are
When MS that is a substrate disappears, the ability to decompose and decompose MS decreases. Therefore, when MS is not present in the malodorous gas to be supplied, MS is desorbed from the adsorbent layer to remove MS from the downstream side.
By supplying MS to the decomposition layer, MS is always supplied to MS-degrading microorganisms, and MS degrading ability is maintained to maintain high throughput.

【0009】[0009]

【発明が解決しようとする課題】しかしながら、上記公
報に開示された従来の生物脱臭装置は、別置きの吸着材
層を設備する必要がある為、装置が大型となり、また設
備費が過大になるという問題があった。本発明は以上の
様な問題を解決するためになされたものであって、別置
きの層を設けずに装置全体をコンパクトなものとしつ
つ、分解微生物が基質不足となって処理活性が落ちるこ
とのない生物脱臭担体を提供することを目的とする。
However, in the conventional biological deodorizing apparatus disclosed in the above publication, it is necessary to install a separate adsorbent layer, so the apparatus becomes large and the equipment cost becomes excessive. There was a problem. The present invention has been made in order to solve the above problems, in which the degrading microorganisms lack a substrate and the processing activity is reduced, while making the entire apparatus compact without providing a separate layer. It is an object to provide a biological deodorizing carrier that does not exist.

【0010】[0010]

【課題を解決するための手段】本発明に係る生物脱臭担
体は、悪臭物質分解性微生物を担持する反応ゾーン(以
下、反応ゾーンと称す)と、悪臭物質の吸脱着ゾーン
(以下、吸脱着ゾーンと称す)を併せ持つものである。
これら各ゾーンの配置形態は、吸脱着ゾーンを中央部と
し、それを囲む様に反応ゾーンが配置された構造とする
と良く、またその逆に反応ゾーンを中央にし、それを囲
む様に吸脱着ゾーンを配置しても良い。あるいは反応ゾ
ーンと吸脱着ゾーンとが向き合って結合配置されたもの
であっても良い。更に反応ゾーンの内部に吸脱着ゾーン
がパッチ状に散在する様な配置としても良く、種々の配
置形態が挙げられる。尚、反応ゾーンにはゲル状のもの
を用いるのが良い。
A biological deodorizing carrier according to the present invention comprises a reaction zone carrying a malodorous substance-degrading microorganism (hereinafter referred to as a reaction zone) and an adsorption / desorption zone for malodorous substances (hereinafter referred to as an adsorption / desorption zone). Is called).
The arrangement of each of these zones should be such that the adsorption / desorption zone is in the center and the reaction zone is arranged so as to surround it, and conversely, the reaction zone is in the center and the adsorption / desorption zone is surrounded so as to surround it. May be placed. Alternatively, the reaction zone and the adsorption / desorption zone may face each other and be connected and arranged. Further, the adsorption / desorption zones may be arranged in a patch form inside the reaction zone, and various arrangements may be mentioned. It is preferable to use a gel-like one for the reaction zone.

【0011】また本発明に係る生物脱臭担体は、上記反
応ゾーンと吸脱着ゾーンとをガス透過性隔壁を介して一
体化するのが好ましい。上記隔壁は骨格機能を発揮する
ものであり、この骨格機能を有する構造例としては、例
えば表面に細孔を有する筒状のもの、あるいは螺旋状の
もの等が挙げられる。
Further, in the biological deodorant carrier according to the present invention, it is preferable that the reaction zone and the adsorption / desorption zone are integrated via a gas permeable partition wall. The partition wall has a skeleton function, and examples of the structure having this skeleton function include a cylindrical one having pores on the surface, and a spiral one.

【0012】[0012]

【作用】本発明に係る生物脱臭担体の反応ゾーンとは、
悪臭物質を分解する微生物が担体に付着あるいは包括さ
れる等して担持されたゾーンであって、この反応ゾーン
において悪臭物質が分解脱臭処理される。該反応ゾーン
は微生物を包括固定することから、ゲル状のものが推奨
される。
The reaction zone of the biological deodorizing carrier according to the present invention is
This is a zone in which microorganisms decomposing malodorous substances are carried by being attached to or contained in a carrier, and the malodorous substances are decomposed and deodorized in this reaction zone. Since the reaction zone immobilizes microorganisms entrapped therein, a gel-like material is recommended.

【0013】生物脱臭担体の吸脱着ゾーンとは、上記悪
臭物質を一時的に吸収・貯蔵するゾーンであって、給気
される被処理ガス中に悪臭物質が存在しなくなるか、或
は非常に低濃度になったときに、該吸脱着ゾーンから悪
臭物質を脱着し拡散する。この拡散した悪臭物質を反応
ゾーンの悪臭物質分解微生物が基質として利用する。
The adsorption / desorption zone of the biological deodorant carrier is a zone for temporarily absorbing and storing the above-mentioned malodorous substance, and the malodorous substance does not exist in the gas to be supplied or is very high. When the concentration becomes low, the malodorous substance is desorbed and diffused from the adsorption / desorption zone. The malodorous substance decomposing microorganisms in the reaction zone utilize this diffused malodorous substance as a substrate.

【0014】この様に当該分解微生物には常にある程度
の濃度の悪臭物質が供給されるから、該微生物は死滅や
活性低下を起こさずに、常に一定水準の処理活性を保ち
得ることになる。つまり被処理ガス中の悪臭物質に濃度
変動(含有されない場合を含む)が起きても、反応ゾー
ンの微生物は安定した活性を維持することができる。
As described above, since the decomposing microorganisms are constantly supplied with a malodorous substance of a certain concentration, the microorganisms can always maintain a certain level of treatment activity without being killed or having a decrease in activity. That is, even if the concentration of the malodorous substance in the gas to be treated fluctuates (including the case where it is not contained), the microorganisms in the reaction zone can maintain a stable activity.

【0015】生物脱臭担体に用いるゲルとしては、ポリ
ビニルアルコール(以下、PVAと称す)、ポリエチレ
ングリコール、ポリアクリルアミド、ゼラチン、アルギ
ン酸ナトリウム等が挙げられる。また反応ゾーンにはゲ
ルが用いられるが、吸脱着ゾーンにはゲル以外のもの、
例えばゼオライト等を用いても良い。
Examples of the gel used as the biological deodorant carrier include polyvinyl alcohol (hereinafter referred to as PVA), polyethylene glycol, polyacrylamide, gelatin, sodium alginate and the like. Although a gel is used in the reaction zone, a material other than gel is used in the adsorption / desorption zone,
For example, zeolite or the like may be used.

【0016】既述の先願公開発明では、吸着材層の担体
の内部に微生物が侵入して層全体が微生物の生育層にな
ること、また微生物が侵入しない様な担体であっても該
担体表面に微生物が付着してMSの吸脱着能を低下させ
るのではないかと懸念しており、これを回避するという
観点から、吸着材層を別に設け、吸着材層を乾燥状態に
保って微生物が付着しない様にしていた。しかし本発明
の様な反応ゾーンで微生物を包括固定化し、吸脱着ゾー
ンでは微生物を包括固定化しない生物脱臭担体において
は、上記の様な問題を生じない。即ち反応ゾーンの微生
物はゲル内に閉じ込められているから、他の層に移って
いくことはなく、またたとえ微生物の増殖によりゲルに
亀裂が生じて微生物がゲルの外へ出たとしても、吸脱着
ゾーンはその内部に微生物が侵入し得ない担体で構成す
ることができるから、吸脱着ゾーンが反応ゾーン化して
しまうことはなく、吸脱着能を保つ。また先願公開発明
では下方の吸着材層に微生物がどんどん落下してくるた
め、乾燥により微生物の増殖を押える必要があったが、
本発明においては、生物脱臭担体の充填処理塔が常に散
水されていることから、ゲルの亀裂から出た微生物は洗
い流され、反応ゾーンのゲル外に多量の微生物が存在す
るということがない。
In the above-mentioned prior application published invention, microorganisms penetrate into the carrier of the adsorbent layer so that the entire layer becomes a growth layer for the microorganisms. I am concerned that microorganisms may adhere to the surface and reduce the adsorption and desorption ability of MS. From the viewpoint of avoiding this, a separate adsorbent layer is provided and the adsorbent layer is kept in a dry state to prevent the microorganisms from advancing. I tried not to attach it. However, the above-mentioned problems do not occur in the biological deodorizing carrier in which the microorganisms are entrapped and immobilized in the reaction zone and the microorganisms are not entrapped and immobilized in the adsorption / desorption zone as in the present invention. That is, since the microorganisms in the reaction zone are confined in the gel, they do not move to other layers, and even if the microorganisms crack due to the growth of microorganisms and the microorganisms go out of the gel, Since the desorption zone can be composed of a carrier into which microorganisms cannot invade, the adsorption / desorption zone does not become a reaction zone and retains the adsorption / desorption ability. Further, in the prior application published invention, since the microorganisms are gradually falling into the lower adsorbent layer, it was necessary to suppress the growth of the microorganisms by drying.
In the present invention, since the packing treatment tower of the biological deodorizing carrier is always sprinkled with water, the microorganisms that have come out from the cracks of the gel are washed away, and a large amount of microorganisms do not exist outside the gel in the reaction zone.

【0017】本発明の生物脱臭担体は、先願公開発明と
異なり反応ゾーンと吸脱着ゾーンを併せ持つ構成であ
り、別置の吸着材層を設ける必要がないことから、生物
脱臭装置をコンパクトなものにできる。
The biological deodorizing carrier of the present invention has a structure having both a reaction zone and an adsorption / desorption zone, unlike the invention disclosed in the prior application, and since it is not necessary to provide a separate adsorbent layer, the biological deodorizing device is compact. You can

【0018】次に本発明の生物脱臭担体のうち、ガス透
過性隔壁(以下、隔壁と称することがある)を介して反
応ゾーンと吸脱着ゾーンとが一体化した生物脱臭担体に
ついて説明する。ゲル担体等の様に荷重に対する強度が
弱い担体を用いる場合において、担体の内部に骨格とな
るガス透過性隔壁を備えることで、対荷重強度を高める
ことができる。
Next, of the biological deodorant carrier of the present invention, a biological deodorant carrier in which a reaction zone and an adsorption / desorption zone are integrated via a gas permeable partition wall (hereinafter sometimes referred to as partition wall) will be described. In the case of using a carrier such as a gel carrier which has a low strength against a load, by providing a gas permeable partition wall as a skeleton inside the carrier, the strength against a load can be increased.

【0019】このガス透過性隔壁を介して一方側には悪
臭物質の吸脱着を行う吸脱着ゾーンを備え、他方側には
悪臭物質分解微生物を担持した反応ゾーンを配置する。
そして前述の様に被処理ガス中の悪臭物質が不存在或は
極めて低濃度となった場合に、前記一方側の吸脱着ゾー
ンから悪臭物質が脱着・拡散し、隔壁を介して前記他方
側の反応ゾーンに担持された微生物に供給される。従っ
て前述と同様に、悪臭物質の負荷変動が生じているとき
であっても、微生物には常に必要量の悪臭物質が供給さ
れ、従って脱臭処理の活性が低下せず、安定に保たれ
る。
An adsorption / desorption zone for adsorbing and desorbing malodorous substances is provided on one side of the gas-permeable partition wall, and a reaction zone carrying malodorous substance-decomposing microorganisms is arranged on the other side.
Then, as described above, when the malodorous substance in the gas to be treated is absent or has an extremely low concentration, the malodorous substance is desorbed and diffused from the adsorption / desorption zone on the one side, and the malodorous substance on the other side is passed through the partition wall. It is supplied to the microorganisms carried in the reaction zone. Therefore, similarly to the above, even when the load of the malodorous substance changes, the required amount of malodorous substance is always supplied to the microorganisms, so that the activity of the deodorizing treatment is not lowered and is kept stable.

【0020】[0020]

【実施例】図1及び図2は本発明の実施例1,2に係る
生物脱臭担体を示す断面図である。図において、3は生
物脱臭担体で、長さは約1〜5cm、幅は約0.5〜
2.5cm程である。1は吸脱着ゾーンで、悪臭物質を
一時的に吸収して貯蔵し、悪臭物質を適宜脱着して拡散
するゾーンである。2は反応ゾーンで、ここには悪臭物
質分解微生物が付着或は包括により担持されており、該
微生物により悪臭物質の分解反応が行われるゾーンであ
る。次に図1に示す生物脱臭担体(実施例1)におい
て、反応ゾーンと吸脱着ゾーンを共にゲルとした場合の
製造方法について述べる。
1 and 2 are cross-sectional views showing a biological deodorizing carrier according to Examples 1 and 2 of the present invention. In the figure, 3 is a biological deodorizing carrier, which has a length of about 1 to 5 cm and a width of about 0.5 to
It is about 2.5 cm. An adsorption / desorption zone 1 is a zone in which a malodorous substance is temporarily absorbed and stored, and the malodorous substance is appropriately desorbed and diffused. Reference numeral 2 is a reaction zone, in which malodorous substance-degrading microorganisms are attached or supported by entrapment, and the microorganisms decompose the malodorous substance. Next, in the biological deodorizing carrier (Example 1) shown in FIG. 1, a production method in which the reaction zone and the adsorption / desorption zone are both gels will be described.

【0021】まず、ゲルとなる高分子を水に溶解してゲ
ル材の溶液とし、化学的或は物理化学的方法、例えばゲ
ル材溶液に架橋剤(PVAの場合ではホウ酸)を添加し
たり、或は凍結−融解を繰り返すといった方法で分子間
を架橋して高分子の鎖を部分的につなぎ止め、ゲル化さ
せる(第1段階)。例えばPVAゲルの場合では、PV
A溶液に少量のアルギン酸ナトリウムを混ぜ(尚、内側
のゾーンを反応ゾーンとする場合は、このとき悪臭物質
分解微生物を混ぜる)、これを塩化カルシウム溶液に滴
下して仮固めをし、更に凍結−融解を繰り返してPVA
を架橋し、ゲルビーズを作る。
First, a gel polymer is dissolved in water to form a gel material solution, and a chemical or physicochemical method, for example, a crosslinking agent (boric acid in the case of PVA) is added to the gel material solution. Or, by repeating freeze-thawing, the molecules are cross-linked to partially block the chains of the polymer to form a gel (step 1). For example, in the case of PVA gel, PV
Solution A is mixed with a small amount of sodium alginate (when the inner zone is used as the reaction zone, the malodorous substance-degrading microorganism is mixed at this time), which is added dropwise to the calcium chloride solution to temporarily solidify it, and then frozen- Repeat melting to PVA
Cross-link to make gel beads.

【0022】次に、このゲル化したものを、同種或は異
種のゲル材の入った溶液に入れ、表面にゲル溶液をコー
ティングする。このときゲル溶液の温度を変えて粘性を
加減することにより、コーティングの量を多くしたり、
或は少なくすることができる。これを上記と同様に化学
的或は物理化学的方法で架橋してゲル化させ(第2段
階)、図1に示すような二重構造のゲル担体をつくる。
この外側のゲル化前の溶液中に、特定の悪臭物質分解微
生物を混ぜておけば、その微生物を包括固定したゲル
(反応ゾーン2)とすることができる。尚、担体の強度
を上げるため、吸脱着ゾーンをゼオライト等の強度の高
いもので構成してこれを心材とし、該心材を包み込む様
に反応ゾーンのゲルを配置する様にしても良い。
Next, the gelled product is put into a solution containing a gel material of the same kind or different kinds, and the surface is coated with the gel solution. At this time, by changing the temperature of the gel solution to adjust the viscosity, the amount of coating can be increased,
Or it can be reduced. This is crosslinked by the chemical or physicochemical method in the same manner as described above and gelled (second step) to prepare a gel carrier having a double structure as shown in FIG.
By mixing a specific malodorous substance-decomposing microorganism into the solution on the outside before gelling, a gel (reaction zone 2) in which the microorganism is entrapped and immobilized can be obtained. In order to increase the strength of the carrier, the adsorption / desorption zone may be made of a material having high strength such as zeolite and used as a core material, and the gel in the reaction zone may be arranged so as to wrap the core material.

【0023】次に図2に示す生物脱臭担体(実施例2)
において、反応ゾーンと吸脱着ゾーンを共にゲルとした
場合の製造方法について述べる。上述と同様に第1段階
でできたゲルを、ゲル材の入った溶液に、実施例1の如
く完全に漬け込むのではなく、部分的に接触させて接着
し、上記と同様にゲル化し、図2に示す様な反応ゾーン
2と吸脱着ゾーン1が隣り合ったゲル担体をつくる。
Next, the biological deodorizing carrier shown in FIG. 2 (Example 2)
In the above, a production method in which both the reaction zone and the adsorption / desorption zone are made of gel will be described. Similarly to the above, the gel formed in the first step was not completely immersed in the solution containing the gel material as in Example 1, but was partially contacted and adhered, and gelated in the same manner as described above. The reaction zone 2 and the adsorption / desorption zone 1 as shown in 2 form a gel carrier in which they are adjacent to each other.

【0024】<実験>次に生物脱臭担体が悪臭物質を吸
脱着する能力を調べる実験モデルについて説明する。図
3はこの実験モデルを説明するための図である。図中、
4はPVAゲルのブロックで、悪臭物質の吸脱着を行
う。5はデシケータ、6はデシケータ5内に充満された
MSガスである。11はガラス容器で、その内部は悪臭
物質分解微生物を懸濁した無機培地7で満たされてい
る。尚、培地7には当初MSは存在しない。8は溶存酸
素電極で、培地7中の溶存酸素量を測定する。10はマ
グネティックスターラー、9はその回転子で、溶存酸素
電極8による測定の際に、電極8と溶液との接触を一定
に行なわせるために用いる。12は微生物の環境を適温
に保つための恒温槽である。尚、本実験ではPVAゲル
ブロック4が吸脱着ゾーンに、また培地7が反応ゾーン
に相当する。
<Experiment> Next, an experimental model for examining the ability of the biological deodorant carrier to adsorb and desorb malodorous substances will be described. FIG. 3 is a diagram for explaining this experimental model. In the figure,
Reference numeral 4 is a PVA gel block for absorbing and desorbing malodorous substances. Reference numeral 5 is a desiccator, and 6 is the MS gas filled in the desiccator 5. A glass container 11 is filled with an inorganic medium 7 in which the malodorous substance-degrading microorganisms are suspended. Initially, MS does not exist in the medium 7. A dissolved oxygen electrode 8 measures the amount of dissolved oxygen in the medium 7. Reference numeral 10 is a magnetic stirrer, and 9 is a rotor thereof, which is used to make the contact between the electrode 8 and the solution constant during measurement by the dissolved oxygen electrode 8. Reference numeral 12 is a constant temperature bath for keeping the environment of microorganisms at an appropriate temperature. In this experiment, the PVA gel block 4 corresponds to the adsorption / desorption zone, and the medium 7 corresponds to the reaction zone.

【0025】次に実験方法について説明する。まず図3
(a)に示す様に、100ppm のMSガス6(MSは悪
臭物質の代表として用いた)で満たされたデシケータ5
内にPVAゲルブロック4を入れ、12時間放置した。
その後図3(b)に示す様に、PVAゲルブロック4を
微生物懸濁無機培地7に浸漬し、該培地7の溶存酸素濃
度の経時変化を調べた。培地7にMSが存在した場合
は、微生物によりMSが酸化分解されて、容器11内の
酸素濃度が減少することとなる。従って培地7の溶存酸
素の減少を調べることにより、PVAゲルブロックがM
Sを吸収し(図3(a)での工程)、放出する(図3
(b)での工程)か否かが分かる。培地7の溶存酸素濃
度の測定結果を図4に示す。
Next, the experimental method will be described. First, Fig. 3
As shown in (a), the desiccator 5 filled with 100 ppm of MS gas 6 (MS was used as a representative of malodorous substances).
The PVA gel block 4 was put therein and left for 12 hours.
After that, as shown in FIG. 3 (b), the PVA gel block 4 was immersed in the microorganism-suspended inorganic medium 7, and the change in the dissolved oxygen concentration of the medium 7 with time was examined. When MS is present in the medium 7, the microorganisms oxidize and decompose the MS, and the oxygen concentration in the container 11 is reduced. Therefore, by examining the decrease in dissolved oxygen in medium 7, the PVA gel block
S is absorbed (step in FIG. 3A) and released (FIG. 3)
Whether or not it is the step in (b). The measurement result of the dissolved oxygen concentration of the medium 7 is shown in FIG.

【0026】図4に見られる様に、酸素濃度が減少して
おり、この結果からPVAゲルは悪臭物質(MS)を吸
収して貯蔵する能力を持ち、且つ拡散により外部に放出
することができるということが分かる。
As shown in FIG. 4, the oxygen concentration is decreased, and as a result, the PVA gel has the ability to absorb and store malodorous substances (MS) and can be released to the outside by diffusion. I understand that.

【0027】<実施例1>次に図1に示す生物脱臭担体
(実施例1)を用いて悪臭ガスを処理する場合について
説明する。予め生物脱臭担体3の吸脱着ゾーン1に悪臭
物質を吸着させておき、生物脱臭装置の処理塔に充填す
る。被処理ガスの処理に際し、悪臭物質が被処理ガス中
に存在する場合には、反応ゾーン2に担持された微生物
はその被処理ガス中の悪臭物質を分解処理し、脱臭され
たガスとして処理塔外へ排出する。このとき吸脱着ゾー
ン1の悪臭物質は該吸脱着ゾーン1に貯蔵された状態を
保つ。
<Embodiment 1> Next, the case where a malodorous gas is treated using the biological deodorizing carrier (Embodiment 1) shown in FIG. 1 will be described. A malodorous substance is adsorbed in advance in the adsorption / desorption zone 1 of the biological deodorizing carrier 3, and is filled in the treatment tower of the biological deodorizing device. When a malodorous substance is present in the gas to be treated during the treatment of the gas to be treated, the microorganisms carried in the reaction zone 2 decompose the malodorous substance in the gas to be treated and treat it as a deodorized gas in the treatment tower. Discharge to the outside. At this time, the malodorous substance in the adsorption / desorption zone 1 is kept stored in the adsorption / desorption zone 1.

【0028】次に被処理ガス中の悪臭物質の濃度が極め
て低濃度或は存在しない場合には、吸脱着ゾーン1の悪
臭物質が脱着して拡散し、反応ゾーン2の微生物がその
悪臭物質を取り込んで分解処理する。この様に上記微生
物には常に基質である悪臭物質が供給され、微生物は活
性を高く保ち続けることができる。尚、分解しきれなか
った過剰の悪臭を吸脱着ゾーンに蓄えることもできる。
Next, when the concentration of the malodorous substance in the gas to be treated is extremely low or absent, the malodorous substance in the adsorption / desorption zone 1 desorbs and diffuses, and the microorganisms in the reaction zone 2 remove the malodorous substance. Capture and disassemble. Thus, the above-mentioned microorganisms are constantly supplied with the malodorous substance as a substrate, and the microorganisms can keep their activity high. In addition, it is also possible to store excess malodor that has not been completely decomposed in the adsorption / desorption zone.

【0029】生物脱臭担体の構造として、図1(実施例
1)に示す様に、吸脱着ゾーン1を中央部とし、それを
囲む様に反応ゾーン2を配置するというように構造とす
れば、反応ゾーン2の微生物が被処理ガスに直接触れる
為、悪臭物質と微生物の接触効率が上がり脱臭効率が高
くなる。
As the structure of the biological deodorizing carrier, as shown in FIG. 1 (Example 1), if the structure is such that the adsorption / desorption zone 1 is at the center and the reaction zone 2 is arranged so as to surround it. Since the microorganisms in the reaction zone 2 come into direct contact with the gas to be treated, the contact efficiency between the malodorous substance and the microorganisms is increased and the deodorization efficiency is increased.

【0030】逆に反応ゾーンを中央にしそれを囲む様に
吸脱着ゾーンを配置する様にすれば、反応ゾーンに伝わ
る外部からの物理的、化学的環境変化が緩和される為、
微生物の生理的環境を安定に維持し易い。
On the contrary, if the adsorption / desorption zone is arranged so as to surround the reaction zone in the center, the physical and chemical environmental changes from the outside transmitted to the reaction zone are alleviated.
It is easy to stably maintain the physiological environment of microorganisms.

【0031】<実施例2>図2は本発明の実施例2に係
る生物脱臭担体を示す図である。図2に示す様に、本実
施例2の生物脱臭担体の構造は、反応ゾーン2と吸脱着
ゾーン1とが隣り合って配置されたものであるが、この
場合は、反応ゾーンにとっては反応効率が高くなる利点
があり、吸脱着ゾーンにとっては吸脱着効率が良くなる
という利点がある。
<Embodiment 2> FIG. 2 is a view showing a biological deodorizing carrier according to Embodiment 2 of the present invention. As shown in FIG. 2, the structure of the biological deodorizing carrier of Example 2 is such that the reaction zone 2 and the adsorption / desorption zone 1 are arranged adjacent to each other, but in this case, the reaction efficiency is high for the reaction zone. Has an advantage that the adsorption and desorption efficiency is improved for the adsorption and desorption zone.

【0032】上記実施例1,2の様に、反応ゾーンと吸
脱着ゾーンとを併せ持つ担体としては、両ゾーンを同種
の材料で構成しても良いし、異種の材料で構成しても良
い。反応ゾーンにはゲルが用いられるが、吸脱着ゾーン
にはゲル以外のものを用いても良く、例えば吸脱着ゾー
ンにゼオライトを用い、これを心材として反応ゾーンの
ゲルで包み込む構成としたものでも良い。尚担体として
PVAゲル担体を用いた場合は、耐久性が高く、比較的
低コストであるという利点を有する。
As in Examples 1 and 2, as a carrier having both a reaction zone and an adsorption / desorption zone, both zones may be made of the same material or different materials. Although a gel is used in the reaction zone, a material other than gel may be used in the adsorption / desorption zone. For example, zeolite may be used in the adsorption / desorption zone, and the gel may be wrapped in the reaction zone as a core material. . When a PVA gel carrier is used as the carrier, it has the advantages of high durability and relatively low cost.

【0033】<実施例3>次に隔壁を有する生物脱臭担
体について説明する。図5は本発明に係る生物脱臭担体
の実施例3を示す斜視図であり、図中、17は生物脱臭
担体、13は隔壁で、その表面には細孔16が多数設け
られている。14は吸脱着ゾーンのゲルで隔壁13内に
存在する。15は反応ゾーンのゲルで、隔壁13を包む
様に存在する。図6は生物脱臭装置における処理塔18
を示す概略断面図で、処理塔18には上記生物脱臭担体
17が充填してある。図中、19は被処理ガスの導入
管、20は処理済ガスの排出管である。
Example 3 Next, a biological deodorizing carrier having a partition will be described. FIG. 5 is a perspective view showing a third embodiment of the biological deodorant carrier according to the present invention. In the figure, 17 is a biological deodorant carrier, 13 is a partition wall, and a large number of pores 16 are provided on the surface thereof. 14 is a gel of the adsorption / desorption zone, which exists in the partition wall 13. 15 is a gel of the reaction zone, which exists so as to wrap the partition wall 13. FIG. 6 shows the treatment tower 18 in the biological deodorizer.
In the schematic cross-sectional view showing the above, the treatment tower 18 is filled with the biological deodorizing carrier 17. In the figure, 19 is an inlet pipe for the gas to be treated, and 20 is an exhaust pipe for the treated gas.

【0034】脱臭処理の操業においては、図6に示す様
に導入管19から被処理ガスが処理塔18に導入され、
生物脱臭担体17を経て塔外へ排出される。前述と同様
に、導入管19から導入される被処理ガス中に悪臭物質
が含まれる(微生物の活性が落ちない程度の濃度)場合
は、反応ゾーンゲル15(図5参照)の微生物によって
悪臭物質が分解処理されて、脱臭されたガスとなって排
出管20から排出される。導入される被処理ガス中の悪
臭物質が極めて低濃度或は含まれない場合は、吸脱着ゾ
ーンゲル14に貯蔵されていた悪臭物質が脱着して拡散
し、細孔16を通して反応ゾーンゲル15の微生物に供
給される。この様にして、常に微生物に悪臭物質が供給
されることとなるから、該微生物は基質不足による死滅
や活性低下を起こすことなく、高い分解処理活性を維持
し続ける。
In the deodorization operation, the gas to be treated is introduced into the treatment tower 18 through the introduction pipe 19 as shown in FIG.
It is discharged to the outside of the tower through the biological deodorizing carrier 17. Similarly to the above, when the odorous substance is contained in the gas to be treated introduced from the introduction pipe 19 (concentration that does not reduce the activity of the microorganism), the odorous substance is removed by the microorganism of the reaction zone gel 15 (see FIG. 5). The decomposed gas becomes a deodorized gas and is discharged from the discharge pipe 20. If the malodorous substance in the introduced gas to be introduced is extremely low in concentration or does not exist, the malodorous substance stored in the adsorption / desorption zone gel 14 is desorbed and diffused, and passes through the pores 16 to the microorganisms of the reaction zone gel 15. Supplied. In this way, the malodorous substance is constantly supplied to the microorganisms, and thus the microorganisms continue to maintain a high decomposition treatment activity without being killed or reduced in activity due to lack of substrate.

【0035】悪臭物質を脱着した吸脱着ゾーンゲル14
は、悪臭物質を含む被処理ガスが流入した際に、その悪
臭物質の一部を吸着し(他の一部は微生物により処理さ
れる)、次に被処理ガス中の悪臭物質が低濃度或は不含
有となるときに備える。
Adsorption / desorption zone gel 14 deodorizing malodorous substances
When a gas to be treated containing a malodorous substance flows in, it absorbs a part of the malodorous substance (the other part is treated by microorganisms), and then the malodorous substance in the gas to be treated has a low concentration or Is prepared when it is not contained.

【0036】本実施例3では、生物脱臭担体17は隔壁
13を有しているから、担体の強度が向上し、ゲルが圧
力によりつぶれてしまうということがない。特にゲルの
担体が水分含量比の高い低濃度ゲルの場合は加重に対す
る強度が弱いが、本実施例3の様に隔壁を用いることで
その強度が高まる。尚反応ゾーンゲル15、吸脱着ゾー
ンゲル14の材料としては上記実施例1,2と同様、同
種のものでも異種のものでも良く、また吸脱着ゾーンに
はゲルでないものを用いても良い。
In the third embodiment, since the biological deodorizing carrier 17 has the partition wall 13, the strength of the carrier is improved and the gel is not crushed by the pressure. In particular, when the gel carrier is a low-concentration gel having a high water content ratio, the strength against load is weak, but the strength is increased by using the partition wall as in the third embodiment. The materials for the reaction zone gel 15 and the adsorption / desorption zone gel 14 may be the same as or different from each other, as in Examples 1 and 2, and the adsorption / desorption zone may be a non-gel material.

【0037】本実施例3の様な筒状の隔壁13を有する
生物脱臭担体17は、例えば球状のものに比べ、担体同
士が密着せず適度な空隙を形成するから、被処理ガス通
風における圧力損失が低く抑えられ、送風ファンの電気
代等のコストを抑えることができる。また担体一つ当た
りの体積に対する比表面積が大きくなるから、悪臭物質
との接触効率が良くなる。尚、吸脱着ゾーンゲル14に
は、前もって悪臭物質を十分に吸着・貯蔵させておいて
もよいし、処理塔に充填してから被処理ガスに含まれる
悪臭物質を利用して吸着・貯蔵させても良い。
The biological deodorizing carrier 17 having the cylindrical partition wall 13 as in the third embodiment, for example, does not adhere to each other and forms an appropriate gap as compared with, for example, a spherical carrier. The loss can be kept low, and the cost of electricity for the blower fan can be reduced. Further, since the specific surface area with respect to the volume per carrier is large, the contact efficiency with the malodorous substance is improved. It should be noted that the adsorption / desorption zone gel 14 may be sufficiently adsorbed and stored with a malodorous substance in advance, or may be adsorbed and stored by using the malodorous substance contained in the gas to be treated after filling the treatment tower. Is also good.

【0038】上記隔壁の構造としては、図5に示す様な
表面に細孔を有する筒状の骨格構造に限るものではな
く、その形状,長さ,隔壁の厚さ等を種々変更しても良
い。この様な種々の形状の隔壁を用いることにより、担
体も種々の形状、例えば球状、ドーナツ状、棒状、らせ
ん状などの形状にすることができる。また隔壁表面に設
けられた細孔も上記図5に示す楕円形状に限るものでは
なく、内外への悪臭物質の拡散が可能であれば矩形,ス
リット状等、どのような形状であっても良い。
The structure of the partition wall is not limited to the cylindrical skeleton structure having pores on the surface as shown in FIG. 5, and the shape, length, partition wall thickness, etc. may be variously changed. good. By using partition walls having such various shapes, the carrier can also have various shapes, for example, a spherical shape, a donut shape, a rod shape, a spiral shape, or the like. Further, the pores provided on the partition wall surface are not limited to the elliptical shape shown in FIG. 5 and may have any shape such as a rectangular shape or a slit shape as long as the malodorous substance can diffuse in and out. .

【0039】尚上記実施例3では、反応ゾーンを外側
に、吸脱着ゾーンを内側としたが、これに限らず、逆に
反応ゾーンを内側にし、吸脱着ゾーンを外側にしても良
い。この場合は、外部の物理的、化学的環境変化が緩和
されてから反応ゾーンの微生物に到達するから、微生物
の生理学的環境を安定に維持し易くなる。
In the third embodiment, the reaction zone is on the outside and the adsorption / desorption zone is on the inside. However, not limited to this, the reaction zone may be on the inside and the adsorption / desorption zone may be on the outside. In this case, the external physical and chemical environment changes are mitigated before they reach the microorganisms in the reaction zone, which makes it easier to stably maintain the physiological environment of the microorganisms.

【0040】[0040]

【発明の効果】以上の様に本発明に係る生物脱臭担体に
おいては、反応ゾーンと吸脱着ゾーンを併せ持つ様にし
たから、悪臭物質の負荷変動が生じる様な場合があって
も、悪臭物質吸脱着用の別の層を設けずに生物脱臭装置
をコンパクトなものとしながら、悪臭分解微生物の活性
を高く保ち続けることができる。従って生物脱臭装置の
処理効率を高めるという効果がある。また本発明に係る
生物脱臭担体を生物脱臭装置に採用した場合には、装置
そのものの改変を要しないから、既存の装置への適用が
容易である。またガス透過性隔壁を介して反応ゾーンと
吸脱着ゾーンを一体化する様にしたから、担体の強度が
向上する。
As described above, since the biological deodorant carrier according to the present invention has both the reaction zone and the adsorption / desorption zone, even if there is a load fluctuation of the malodorous substance, the malodorous substance is absorbed. It is possible to keep the activity of the malodorous microorganisms high while keeping the biological deodorizing device compact without providing another layer for desorption. Therefore, there is an effect that the treatment efficiency of the biological deodorizing device is increased. Further, when the biological deodorizing carrier according to the present invention is adopted in the biological deodorizing device, since the device itself does not need to be modified, it can be easily applied to an existing device. Further, since the reaction zone and the adsorption / desorption zone are integrated through the gas permeable partition wall, the strength of the carrier is improved.

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

【図1】本発明の実施例1に係る生物脱臭担体を示す断
面図。
FIG. 1 is a sectional view showing a biological deodorizing carrier according to a first embodiment of the present invention.

【図2】本発明の実施例2に係る生物脱臭担体を示す断
面図。
FIG. 2 is a sectional view showing a biological deodorizing carrier according to Example 2 of the present invention.

【図3】担体の悪臭物質吸脱着能を調べる実験モデルの
説明図。
FIG. 3 is an explanatory diagram of an experimental model for investigating the malodorous substance adsorption / desorption ability of the carrier.

【図4】溶存酸素濃度の経時変化を示すグラフ。FIG. 4 is a graph showing changes in dissolved oxygen concentration with time.

【図5】本発明の実施例3に係る生物脱臭担体を示す斜
視図。
FIG. 5 is a perspective view showing a biological deodorizing carrier according to Example 3 of the present invention.

【図6】本発明の実施例3に係る生物脱臭担体を有する
処理塔を示す概略断面図。
FIG. 6 is a schematic sectional view showing a treatment tower having a biological deodorizing carrier according to a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 吸脱着ゾーン 2 反応ゾーン 3,17 生物脱臭担体 4 PVAゲルブロック 13 隔壁 14 吸脱着ゾーンゲル 15 反応ゾーンゲル 16 細孔 18 処理塔 DESCRIPTION OF SYMBOLS 1 Adsorption / desorption zone 2 Reaction zone 3,17 Biodeodorant carrier 4 PVA gel block 13 Partition wall 14 Adsorption / desorption zone gel 15 Reaction zone gel 16 Pore 18 Treatment tower

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 悪臭物質分解性微生物を担持する反応ゾ
ーンと、悪臭物質の吸脱着ゾーンを併せ持つことを特徴
とする生物脱臭担体。
1. A biological deodorant carrier having both a reaction zone for supporting a malodorous substance-degrading microorganism and an adsorption / desorption zone for a malodorous substance.
【請求項2】 悪臭物質分解性微生物を担持する反応ゾ
ーンと、悪臭物質の吸脱着ゾーンとが、ガス透過性隔壁
を介して一体化されたものであることを特徴とする生物
脱臭担体。
2. A biological deodorizing carrier, characterized in that a reaction zone carrying a malodorous substance-degrading microorganism and an adsorption / desorption zone for a malodorous substance are integrated through a gas-permeable partition wall.
JP6080594A 1994-04-19 1994-04-19 Biological deodorizing carrier Expired - Fee Related JP2885060B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6080594A JP2885060B2 (en) 1994-04-19 1994-04-19 Biological deodorizing carrier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6080594A JP2885060B2 (en) 1994-04-19 1994-04-19 Biological deodorizing carrier

Publications (2)

Publication Number Publication Date
JPH07284629A true JPH07284629A (en) 1995-10-31
JP2885060B2 JP2885060B2 (en) 1999-04-19

Family

ID=13722669

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6080594A Expired - Fee Related JP2885060B2 (en) 1994-04-19 1994-04-19 Biological deodorizing carrier

Country Status (1)

Country Link
JP (1) JP2885060B2 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52767A (en) * 1975-06-24 1977-01-06 Tetsuzo Iwai Deodorizing process
JPS6297628A (en) * 1985-10-23 1987-05-07 Fukuokashi Method for deodorizing soil containing porous inorganic substance
JPS6447424A (en) * 1987-08-12 1989-02-21 Three N Gijutsu Consultant Kk Mirobe utilizing filter used for deodorizing device, or the like
JPH03178316A (en) * 1989-12-06 1991-08-02 Ebara Infilco Co Ltd Deodorizing method for offensive odor gas

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52767A (en) * 1975-06-24 1977-01-06 Tetsuzo Iwai Deodorizing process
JPS6297628A (en) * 1985-10-23 1987-05-07 Fukuokashi Method for deodorizing soil containing porous inorganic substance
JPS6447424A (en) * 1987-08-12 1989-02-21 Three N Gijutsu Consultant Kk Mirobe utilizing filter used for deodorizing device, or the like
JPH03178316A (en) * 1989-12-06 1991-08-02 Ebara Infilco Co Ltd Deodorizing method for offensive odor gas

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