JP2003154230A - Biological deodorizing apparatus - Google Patents

Biological deodorizing apparatus

Info

Publication number
JP2003154230A
JP2003154230A JP2001355835A JP2001355835A JP2003154230A JP 2003154230 A JP2003154230 A JP 2003154230A JP 2001355835 A JP2001355835 A JP 2001355835A JP 2001355835 A JP2001355835 A JP 2001355835A JP 2003154230 A JP2003154230 A JP 2003154230A
Authority
JP
Japan
Prior art keywords
malodorous
porous resin
biological deodorizing
packed beds
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.)
Pending
Application number
JP2001355835A
Other languages
Japanese (ja)
Inventor
Katsuyuki Kataoka
克之 片岡
Toshio Tsukamoto
敏男 塚本
Shigeki Yamashita
茂樹 山下
Toshihiro Tanaka
俊博 田中
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP2001355835A priority Critical patent/JP2003154230A/en
Publication of JP2003154230A publication Critical patent/JP2003154230A/en
Pending legal-status Critical Current

Links

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

  • Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a biological deodorizing apparatus using lightweight packed beds having a significant microorganism sticking and carrying effect and a significant malodorous component removing effect and free of increase of pressure drop due to sprinkling of washing water. SOLUTION: In the biological deodorizing apparatus 1 with a malodorous gas feed pipe 2 at the bottom, a treated gas discharge pipe 8 at the top and packed beds 3, 4 carrying microorganisms which degrade the malodorous components of malodorous gas within the apparatus, the packed beds are formed of a packing material obtained by coating the surfaces of porous resin moldings with an acetalized product of polyvinyl alcohol and the porous resin moldings are foamed moldings of polyurethane, polystyrene, polypropylene, polyethylene or polyacetal and preferably have an open cell structure in which the inlet and outlet of each cell are open at different portions of the surface of the resin.

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、生物脱臭装置に係り、
特に、し尿処理場、下水処理場、その他各種工場から発
生する悪臭ガスの悪臭成分を、活性汚泥等の微生物によ
り生物学的に分解して脱臭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,
In particular, the present invention relates to a biological deodorization device that deodorizes biologically degrading malodorous components of malodorous gas generated from human waste treatment plants, sewage treatment plants, and other factories by microorganisms such as activated sludge.

【0002】[0002]

【従来の技術】し尿処理場、下水処理場から発生する悪
臭ガスの悪臭成分は、硫化水素、メチルメルカプタン、
硫化メチル、二硫化メチル、アンモニア等である。この
中で比較的濃度が高いのは、硫化水素(5〜50pp
m)、アンモニア(1〜10ppm)である。生物脱臭
装置では、これらの成分は比較的分解し易いため、分解
効率が問題となることは少ない反面、これらの成分の分
解によって生成する微生物汚泥や単体硫黄等が、充填層
に蓄積して閉塞を生ずる問題がある。一方、メチルメル
カプタン(0.5〜5ppm)、硫化メチル、二硫化メ
チル(各々1ppm以下)の濃度は低いものの、これら
の成分は難分解性のため、分解効率が問題となる場合が
多い。
2. Description of the Related Art Malodorous components of malodorous gas generated from human waste treatment plants and sewage treatment plants are hydrogen sulfide, methyl mercaptan,
Examples include methyl sulfide, methyl disulfide, ammonia and the like. Among these, the relatively high concentration is hydrogen sulfide (5-50 pp
m) and ammonia (1 to 10 ppm). In a biological deodorizer, these components are relatively easy to decompose, so degradation efficiency is less of a problem, but microbial sludge and elemental sulfur produced by the decomposition of these components accumulate in the packed bed and block. There is a problem that causes. On the other hand, although the concentration of methyl mercaptan (0.5 to 5 ppm), methyl sulfide, and methyl disulfide (each 1 ppm or less) is low, the decomposition efficiency of these components often causes a problem because they are difficult to decompose.

【0003】このような悪臭ガスを脱臭するため、処理
塔の内部に、悪臭成分を分解する微生物を担持した疎水
性(水を吸収しないこと)ポリウレタンスポンジ立体網
目状粒状物等の多孔性樹脂成型体の充填層を設け、この
充填層に悪臭ガスを上向流で通気し、前記スポンジ粒状
物が担持する微生物で、悪臭成分を酸化分解することが
従来から行なわれている。充填層として多孔性樹脂成型
体を使用するのは、単位容積当たりの表面積が大で、軽
量であること、任意の形状に簡単に成型できるため、空
隙率等を調整することによって、過剰な微生物汚泥や単
体硫黄等の蓄積を抑えられると共に、充填層の上から散
水する洗浄水をスムースに流下させることができ、しか
も、洗浄水を上から散水しても変形・圧密しないだけの
強度があること、等の優れた特徴を備えた充填材である
からである。従来の発泡性樹脂成型体は、前記の如く優
れた特徴を備えているものの、運転初期の微生物の付着
が悪いという問題がある。そのため、初期の脱臭性能が
発揮されるまでの立ち上げ期間が長くなる問題があっ
た。
In order to deodorize such a malodorous gas, a porous resin molding such as a hydrophobic (not absorbing water) polyurethane sponge three-dimensional network granules carrying microorganisms for decomposing malodorous components inside the treatment tower. It has been conventionally practiced to provide a packing layer for the body, to ventilate a malodorous gas in an upward flow through this packing layer, and to oxidize and decompose the malodorous components by the microorganisms carried by the sponge particles. The use of a porous resin molded body as the filling layer has a large surface area per unit volume, is lightweight, and can be easily molded into an arbitrary shape. It is possible to suppress the accumulation of sludge and elemental sulfur, etc., and it is possible to smoothly flow down the washing water sprinkled from the top of the packed bed. Moreover, even if the washing water is sprinkled from above, it does not deform or consolidate. This is because the filler has excellent features such as that. Although the conventional foamable resin molded body has the excellent characteristics as described above, it has a problem that the adhesion of microorganisms at the initial stage of operation is poor. Therefore, there is a problem that the startup period until the initial deodorizing performance is exhibited becomes long.

【0004】[0004]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点に鑑み、悪臭成分を分解する微生物の担持効
果及び悪臭成分の除去効果が大きく、軽量で、洗浄水に
よって圧密化しない充填層を用いた生物脱臭装置を提供
することを課題とする。
SUMMARY OF THE INVENTION In view of the above problems of the prior art, the present invention has a large effect of supporting microorganisms for decomposing malodorous components and an effect of removing malodorous components, is lightweight, and is not compacted by washing water. An object is to provide a biological deodorizing device using a layer.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、底部に悪臭ガスの給気管と、上部に処
理ガスの排気管と、内部に悪臭ガスの悪臭成分を分解す
る微生物を担持した充填層と、該充填層に洗浄水を散布
する散水管とを備えた生物脱臭装置において、前記充填
層を、多孔性樹脂成型体の表面にポリビニルアルコール
のアセタール化物をコーティングした充填材で形成した
ものである。前記生物脱臭装置において、多孔性樹脂成
型体は、ポリウレタン、ポリスチレン、ポリプロピレ
ン、ポリエチレン又はポリアセタールの発泡成型物であ
り、また、前記多孔性樹脂成型体は、樹脂の表面の異な
る部位で入口と出口が開放した連続孔構造を有するのが
よい。
In order to solve the above problems, in the present invention, a microorganism for decomposing a malodorous component of a malodorous gas inside, an air supply pipe for a malodorous gas at the bottom, an exhaust pipe for a processing gas at the top. In a biological deodorizing device provided with a packed layer carrying a carrier, and a sprinkling pipe for spraying washing water to the packed layer, the packing layer is a packing material in which the surface of a porous resin molding is coated with an acetalized product of polyvinyl alcohol. It was formed in. In the biological deodorization device, the porous resin molded body is a foamed molded product of polyurethane, polystyrene, polypropylene, polyethylene or polyacetal, and the porous resin molded body has an inlet and an outlet at different sites on the surface of the resin. It should have an open pore structure.

【0006】[0006]

【発明の実施の形態】本発明は、発泡性樹脂成型体が、
充填材としては、微生物に分解されず、軽量で通気抵抗
が少なく、軽いこと、洗浄水によって圧密化せず、且つ
洗浄水をスムースに流下させることができるなどの優れ
た特徴を生かし、かつ微生物付着性を向上させる方法を
追及した結果、微生物が付着しにくい原因が、発泡性樹
脂成型体が極めて疎水性であることにあると判明し、発
泡性樹脂成型体の表面に、ポリビニルアルコール(PV
A)のアセタール化物をコーティングさせると、表面に
微生物が極めて効果的に増殖すると共に、発泡性樹脂成
型体に強度があり、かつ、水を吸収する量が適度である
ことから、充填材の自重によって充填層が圧密すること
がないため、ガスの通気抵抗が増加しないことを見出
し、本発明を完成した。これに対し、充填材自体を多孔
性・水膨潤性・親水性の樹脂にすると、充填材自体の圧
縮強度が小さく、しかも水を多量に吸収するため、この
ような充填材を高さ30cm以上に充填すると、下部が
上部の水を含んだ充填材の重みで圧縮されてしまい、ガ
スの通気抵抗が増加してしまうことが認められた。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention relates to a foamable resin molding,
The filler is not decomposed by microorganisms, is lightweight and has low ventilation resistance, is light, does not consolidate with washing water, and makes good use of the excellent characteristics such as allowing washing water to flow down smoothly, and microorganisms As a result of pursuing a method of improving the adhesiveness, it was found that the reason why the microorganisms are difficult to adhere is that the foamable resin molded body is extremely hydrophobic, and the polyvinyl alcohol (PV
When the acetalized product of A) is coated, microorganisms grow extremely effectively on the surface, the foamable resin molded body has strength, and the amount of absorbing water is moderate, so that the self-weight of the filler is The present invention has been completed by finding that the filling layer does not consolidate and the gas ventilation resistance does not increase. On the other hand, if the filler itself is made of a porous, water-swellable, and hydrophilic resin, the compressive strength of the filler itself is small and a large amount of water is absorbed. It was confirmed that the lower part is compressed by the weight of the filler containing water in the upper part, and the gas ventilation resistance is increased.

【0007】したがって、本発明の多孔性樹脂成型体
は、このように高さ30cm以上に充填しても、充填層
が圧縮することのない程度の圧縮強度を有するものであ
って、樹脂の材質自体に制限はないが、代表的なものと
しては、ポリウレタン、ポリスチレン、ポリプロピレ
ン、ポリエチレン、ポリアセタール等の発泡成型物があ
る。なお、これら多孔性樹脂成型物の代わりに、特開平
7−284630号公報に記載のように、耐水性合成繊
維を含有する繊維とバインダーよりなる板状繊維集合体
を用いる方法もあるが、繊維集合体は、繊維を嵩高く集
合させることによって、比表面積を極めて大きくするこ
とができる反面、三次元的に強度を持たせることが困難
である。一方、強度を持たせるために繊維の密度を上げ
ると、比表面積が小さくなるばかりでなく、余剰固形物
の排出や、スムースなガスの流れ及び散水された水の排
出を実現することが困難となる。したがって、最適な比
表面積と繊維の強度・空隙率とのバランスを考慮して、
最適な繊維密度に調整する必要があるが、加工が複雑に
なるといった問題がある。
Therefore, the porous resin molding of the present invention has such a compressive strength that the packed bed is not compressed even when it is packed to a height of 30 cm or more, and the material of the resin is Although it is not limited in itself, typical examples thereof include foamed molded products such as polyurethane, polystyrene, polypropylene, polyethylene, and polyacetal. There is also a method of using a plate-like fiber aggregate composed of a fiber containing a water-resistant synthetic fiber and a binder, as described in JP-A-7-284630, instead of these porous resin moldings. The aggregate can have an extremely large specific surface area by collecting the fibers in a bulky manner, but it is difficult to impart three-dimensional strength to the aggregate. On the other hand, if the density of the fibers is increased to have strength, not only the specific surface area becomes smaller, but also it is difficult to discharge excess solid matter, smooth gas flow and discharge of sprinkled water. Become. Therefore, considering the balance between the optimum specific surface area and the strength / porosity of the fiber,
It is necessary to adjust to the optimum fiber density, but there is a problem that processing becomes complicated.

【0008】これに対して、多孔性樹脂の場合は、形状
・サイズのみでなく、成型時の条件、例えば発泡成型の
場合の発泡率などを制御することで、比表面積等も調整
することができるため、最適な比表面積と強度・空隙率
とのバランスを考慮して、最適な充填材を容易に製作す
ることができる。多孔性樹脂の形状は、特に制限され
ず、例えば、粉体状・二次元的形状や三次元的形状のい
ずれであってもよい。多孔性樹脂は、無定形状(破砕
状)、粒状、ペレット状、球状、多面体(サイコロ
状)、ハニカム状、シート状、ブロック状、短冊状、中
空円筒状、サドル状などの形状を有していてもよい。多
孔性樹脂の構造は、多数の孔(又は細孔)を有する多孔
質(多孔構造)であればよく、三次元網目構造のネット
ワーク状の孔(又は細孔)を有していてもよい。
On the other hand, in the case of a porous resin, not only the shape and size, but also the specific surface area can be adjusted by controlling the conditions at the time of molding, for example, the foaming rate in the case of foam molding. Therefore, the optimum filler can be easily manufactured in consideration of the optimum balance between the specific surface area and the strength / porosity. The shape of the porous resin is not particularly limited, and may be, for example, a powder, a two-dimensional shape, or a three-dimensional shape. The porous resin has an amorphous shape (crushed shape), a granular shape, a pellet shape, a spherical shape, a polyhedron shape (dices shape), a honeycomb shape, a sheet shape, a block shape, a strip shape, a hollow cylinder shape, a saddle shape, or the like. May be. The structure of the porous resin may be porous (porous structure) having a large number of pores (or pores), and may have network-like pores (or pores) of a three-dimensional network structure.

【0009】多孔性樹脂のサイズは特に制限されず、通
常、平均径として、1〜50mm、好ましくは5〜40
mm程度の樹脂をランダムに充填してもよいし、一辺の
長さが500〜2000mm程度のブロックを一体型で
充填してもよい。多孔性樹脂の孔(又は細孔)の平均孔
径は、例えば、0.01〜3mm、好ましくは0.03
〜1mm程度である。孔(細孔)は、樹脂内に独立気泡
として一部が存在していてもよいが、少なくとも樹脂の
表面の異なる部位で入口と出口が開放した連続孔構造を
有するのが好ましい。特に、孔(細孔)は、樹脂の異な
る部位で開放(又は貫通)した連通孔を形成するのが好
ましく、樹脂の内部では、網目状などの形態で互いに連
通していてもよい。しかして、多孔性樹脂の一つである
三次元網目構造を有するポリウレタンスポンジのスポン
ジ骨格に、PVAをコーティングするには、例えば、次
のようにすればよい。
The size of the porous resin is not particularly limited, and usually has an average diameter of 1 to 50 mm, preferably 5 to 40.
A resin having a size of about mm may be randomly filled, or a block having a side length of about 500 to 2000 mm may be integrally filled. The average pore diameter of the pores (or pores) of the porous resin is, for example, 0.01 to 3 mm, preferably 0.03
It is about 1 mm. The pores (pores) may partially exist as closed cells in the resin, but preferably have a continuous pore structure in which the inlet and the outlet are open at least at different sites on the surface of the resin. In particular, it is preferable that the pores (pores) form communication holes that are open (or penetrate) at different portions of the resin, and may communicate with each other in the form of a mesh inside the resin. In order to coat the sponge skeleton of the polyurethane sponge having a three-dimensional network structure, which is one of the porous resins, with PVA, for example, the following may be performed.

【0010】すなわち、ポリウレタンスポンジ粒状物又
はブロックをPVA水溶液に浸漬したのち、引き上げ、
次に酸性ホルマリン水溶液に浸漬し、放置すると数時間
後にポリウレタンスポンジ骨格にPVAアセタール化物
がコーティングされたものができ上がる。なお、PVA
には界面活性能があるため、前記方法でもポリウレタン
に付着させることはできるが、さらに好適なコーティン
グ方法を検討した結果、まずポリウレタンスポンジを界
面活性剤水溶液に浸漬させ、界面活性剤の疎水基をポリ
ウレタン表面に吸着させ、親水基を外側に配向させた状
態で、PVA水溶液に浸漬させると、極めて効果的にP
VAがポリウレタンスポンジ骨格に付着することが認め
られた。この後、ホルマリン水溶液に浸漬させると、P
VAアセタール化物が十分付着したポリウレタンスポン
ジができ上がる。
That is, the polyurethane sponge granules or blocks are immersed in a PVA aqueous solution and then pulled up,
Next, after soaking in an acidic formalin aqueous solution and leaving it for a few hours, a polyurethane sponge skeleton coated with a PVA acetal compound is completed. In addition, PVA
Since it has a surface-active ability, it can be attached to polyurethane by the above method, but as a result of studying a more suitable coating method, first, the polyurethane sponge was dipped in an aqueous surfactant solution to remove the hydrophobic group of the surfactant. When it is adsorbed on the polyurethane surface and immersed in an aqueous PVA solution with the hydrophilic groups oriented outward, P is extremely effective.
It was observed that VA was attached to the polyurethane sponge skeleton. After that, when immersed in an aqueous formalin solution, P
A polyurethane sponge with a sufficient amount of VA acetal compound attached is completed.

【0011】次に、図1に示す本発明の生物脱臭装置の
断面構成図を用いて説明する。図1において、1は処理
塔で、底部に悪臭ガスの給気管2、内部には上下二段に
充填層3と4、各充填層3と4に洗浄水を上から散布す
る散水管5と6が設けられており、8は処理ガスの排気
管である。充填層3と4は、PVAアセタール化物がコ
ーティングされた多孔性樹脂成型体(粒径10mm程度
の粒状にカットしたものでも、1辺数m程度のブロック
状でもよい)で構成されている。充填層3と4を構成す
る充填材(多孔性樹脂成型体)6は、表面がPVAアセ
タール化処理によって極めて親水性に変わっているた
め、その内部と表面に悪臭成分を分解する微生物を速や
かにかつ多量に担持することができる。
Next, a description will be given with reference to the sectional configuration diagram of the biological deodorizing apparatus of the present invention shown in FIG. In FIG. 1, 1 is a treatment tower, an air supply pipe 2 for a malodorous gas at the bottom, a packing layer 3 and 4 in two upper and lower stages, and a sprinkling pipe 5 for spraying washing water from each packing layer 3 and 4 from above. 6 is provided, and 8 is an exhaust pipe for processing gas. The filling layers 3 and 4 are composed of a porous resin molded body coated with a PVA acetalized product (which may be cut into particles having a particle diameter of about 10 mm or a block shape having a side length of several meters). Since the surface of the filler (porous resin molded body) 6 that constitutes the filling layers 3 and 4 has become extremely hydrophilic due to the PVA acetalization treatment, microorganisms that decompose the malodorous components into the inside and the surface of the filling material quickly Moreover, a large amount can be supported.

【0012】充填層3と4を構成したら、散水管5と6
で充填層3と4に活性汚泥の希釈水、活性汚泥処理水、
河川水などを散布し、硝化菌、硫黄酸化菌等の微生物を
植菌して、給気管2から処理塔1内の底部に悪臭ガスを
給気し、下段の充填層3、次に上段の充填層4に上向流
で通気する。従って、硫化水素、アンモニアのみならず
メチルメルカプタン、硫化メチル、二硫化メチルといっ
た難分解性の成分も効率良く除去される。しかも、多孔
性樹脂成型体は優れた耐酸性を有するため、悪臭ガスに
よって生ずるSO4 2-等による強度低下がない。さら
に、悪臭物質の酸化分解により生成するSO4 2-、NH
+、NO 、NO 等を洗い流すための洗浄水
を、散水管5から多量に充填層3に散布しても、充填層
3を構成する充填材は連続気泡であり、圧縮強度が大き
いため、つぶれることが無く、洗浄水は、生成物を伴っ
て粒体内部及び流体同志の間隙中を、スムースに流下し
て処理塔の底に流れ落ち、排水管9から排水される。従
って、多量の洗浄水で洗浄を行なっても、充填層3は圧
密することがないと共に、該層を流下する洗浄水は、上
向流で通気する悪臭ガスの抵抗にならないので、圧力損
失は増大しない。
Once the packed beds 3 and 4 have been constructed, sprinkler tubes 5 and 6
In the packed beds 3 and 4, diluted water for activated sludge, treated water for activated sludge,
Disperse river water, etc., inoculate microorganisms such as nitrifying bacteria, sulfur-oxidizing bacteria, etc., and supply malodorous gas from the air supply pipe 2 to the bottom of the treatment tower 1, and then the lower packed bed 3, then the upper packed bed 3 The packed bed 4 is vented with an upward flow. Therefore, not only hydrogen sulfide and ammonia but also hard-to-decompose components such as methyl mercaptan, methyl sulfide and methyl disulfide can be efficiently removed. Moreover, since the porous resin molded body has excellent acid resistance, there is no reduction in strength due to SO 4 2- or the like generated by a malodorous gas. Furthermore, SO 4 2− , NH generated by oxidative decomposition of malodorous substances
Even if a large amount of cleaning water for washing away 4 + , NO 2 , NO 3 −, etc. is sprayed from the sprinkling pipe 5 to the packed bed 3, the packing material forming the packed bed 3 is an open cell and has a compressive strength. Since it is large, it does not collapse, and the wash water smoothly flows down along with the product inside the granules and in the gap between the fluids, flows down to the bottom of the treatment tower, and is discharged from the drain pipe 9. Therefore, even if washing is performed with a large amount of washing water, the packed bed 3 does not consolidate, and the washing water flowing down the bed does not become a resistance against the malodorous gas vented in the upward flow, so that the pressure loss is reduced. Does not increase.

【0013】[0013]

【実施例】以下、本発明を実施例により具体的に説明す
る。 実施例1 本発明の多孔性樹脂成型体の表面に、PVAのアセター
ル化物をコーティングした充填材を、次の方法で製作し
た。即ち、ポリウレタンスポンジをPVAの10重量%
水溶液に浸漬後、四ホウ酸ナトリウムの飽和溶液に浸漬
して、ポリウレタンスポンジの表面にPVAをコートし
た。次で、105℃で5分間熱処理した後、ホルマリン
に浸漬することによって、ポリウレタンスポンジの表面
にコートされたPVAを、アセタール化した。製作した
充填材の圧縮強度(25%変形)は、1200kPaで
あった。この充填材を図1に示す生物脱臭装置の充填層
に充填し、下水処理施設の水処理工程から発生する臭気
を原ガスとして脱臭処理した。
EXAMPLES The present invention will be specifically described below with reference to examples. Example 1 A filler having the surface of the porous resin molding of the present invention coated with an acetalized product of PVA was produced by the following method. That is, 10% by weight of PVA of polyurethane sponge
After being dipped in the aqueous solution, it was dipped in a saturated solution of sodium tetraborate to coat the surface of the polyurethane sponge with PVA. Next, after heat treatment at 105 ° C. for 5 minutes, the PVA coated on the surface of the polyurethane sponge was acetalized by being immersed in formalin. The compressive strength (25% deformation) of the manufactured filler was 1200 kPa. This packing material was filled in the packed bed of the biological deodorizing apparatus shown in FIG. 1, and the odor generated from the water treatment process of the sewage treatment facility was used as a raw gas for deodorization.

【0014】運転条件は次のとおりである。 硫化水素濃度 :2ppm メチルメルカプタン濃度 :0.04ppm 硫化メチル濃度 :0.013ppm 二硫化メチル濃度 :0.0025ppm 温 度 :24℃ 空塔速度 :400hr-1 空塔線速度 :0.22m/sec 散水頻度 :1時間に2分間 散水時の液ガス比 :3L/m3 脱臭処理開始から20日経過後、処理ガスの悪臭物質濃
度は、硫化水素0.001ppm以下、メチルメルカプ
タン0.001ppm以下、硫化メチル0.001pp
m以下、二硫化メチル0.001ppm以下となった。
以後、長期にわたって安定した悪臭物質除去性能を示
し、充填層の圧力損失も100Pa程度の低い値で安定
した。脱臭処理開始から1ヶ月経過後の脱臭成績を表1
に示す。
The operating conditions are as follows. Hydrogen sulfide concentration: 2ppm Methyl mercaptan concentration: 0.04ppm Methyl sulfide concentration: 0.013ppm Methyl disulfide concentration: 0.0025ppm Temperature: 24 ° C Superficial velocity: 400hr -1 Superficial linear velocity: 0.22m / sec Water sprinkling Frequency: Liquid gas ratio when sprinkling water for 1 minute for 2 minutes: 3 L / m 3 After 20 days from the start of deodorizing treatment, the malodorous substance concentration of the treated gas is 0.001 ppm or less of hydrogen sulfide, 0.001 ppm or less of methyl mercaptan, and methyl sulfide. 0.001pp
m or less and methyl disulfide 0.001 ppm or less.
Thereafter, stable malodorous substance removal performance was exhibited for a long period of time, and the pressure loss of the packed bed was stable at a low value of about 100 Pa. Table 1 shows the deodorization results one month after the start of deodorization treatment.
Shown in.

【0015】比較例1 図1に示す生物脱臭装置の充填層に、圧縮強度70kP
aのPVAスポンジを充填した他は、実施例1と同じ条
件で脱臭処理した。脱臭処理開始から20日経過後、処
理ガスの悪臭質濃度は、硫化水素0.001ppm以
下、メチルメルカプタン0001ppm以下、硫化メチ
ル0.001ppm以下、二硫化メチル0.001pp
m以下となり、実施例1と同等の悪臭物質除去性能を示
した。しかし、徐々に充填層の圧密化が進み、充填層の
圧力損失は運転開始当初150Pa程度であったもの
が、1ヶ月経過後に500Paまで上昇した。
Comparative Example 1 The packed bed of the biological deodorizer shown in FIG. 1 has a compressive strength of 70 kP.
The deodorizing treatment was performed under the same conditions as in Example 1 except that the PVA sponge of a. After 20 days from the start of the deodorizing treatment, the malodor concentration of the treated gas is 0.001 ppm or less of hydrogen sulfide, 0001 ppm or less of methyl mercaptan, 0.001 ppm or less of methyl sulfide, and 0.001 pp of methyl disulfide.
m was less than or equal to m, and the odorous substance removal performance equivalent to that of Example 1 was exhibited. However, the packed bed was gradually consolidated, and the pressure loss of the packed bed was about 150 Pa at the beginning of the operation, but increased to 500 Pa after one month.

【0016】比較例2 図1に示す生物脱臭装置の充填層に、圧縮強度1200
kPaのポリウレタンスポンジを充填した他は、実施例
1と同じ条件で脱臭処理した。脱臭処理開始から20日
経過後の処理ガスの悪臭質濃度は、硫化水素0.001
ppm以下、メチルメルカプタン0.004ppm、硫
化メチル0.007ppm、二硫化メチル0.0015
ppmであり、実施例1及び比較例1に比して高い値で
あった。充填層の圧力損失は100Pa程度の低い値で
安定していた。脱臭処理開始から1ヶ月経過後の脱臭成
績を表1に示す。
COMPARATIVE EXAMPLE 2 The packed bed of the biological deodorizer shown in FIG.
The deodorizing treatment was performed under the same conditions as in Example 1 except that the polyurethane sponge having kPa was filled. After 20 days from the start of the deodorizing process, the malodor concentration of the treated gas was 0.001 of hydrogen sulfide.
ppm or less, methyl mercaptan 0.004 ppm, methyl sulfide 0.007 ppm, methyl disulfide 0.0015
It was ppm, which was a higher value than those in Example 1 and Comparative Example 1. The pressure loss of the packed bed was stable at a low value of about 100 Pa. Table 1 shows the deodorizing results one month after the start of the deodorizing treatment.

【0017】[0017]

【表1】 [Table 1]

【0018】[0018]

【発明の効果】以上で明らかなように、本発明では、多
孔質樹脂成型体の表面にPVAアセタール化物をコーテ
ィングさせたもので構成した充填層3により、微生物が
極めて付着しやすく、充填物が圧縮されず圧力損失を増
大させず、しかも洗浄水をスムースに流下させ、該層3
を上向流する悪臭ガスの大部分の悪臭成分を分解し、脱
臭することができる。
As is apparent from the above, according to the present invention, the filling layer 3 formed by coating the surface of the porous resin molded body with the PVA acetalized product makes it extremely easy for microorganisms to adhere, and It is not compressed and pressure loss is not increased, and the washing water is allowed to flow smoothly, so that the layer 3
Most of the malodorous components of the malodorous gas flowing upwards can be decomposed and deodorized.

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

【図1】本発明の生物脱臭装置の一例を示す断面構成
図。
FIG. 1 is a cross-sectional configuration diagram showing an example of a biological deodorizing apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1:処理塔、2:給気管、3、4:充填層、5、6:充
填層への散水管、7:多孔性樹脂成型体の表面にPVA
のアセタール化物をコーティングした充填材、8:排気
管、9:排水管
1: Treatment tower, 2: Air supply pipe, 3, 4: Packed bed, 5, 6: Sprinkling pipe to packed bed, 7: PVA on surface of porous resin molding
Filler coated with acetalized product, 8: exhaust pipe, 9: drain pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山下 茂樹 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 田中 俊博 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 Fターム(参考) 4C080 AA07 BB02 CC03 CC04 CC05 CC08 CC13 HH05 HH09 JJ03 KK06 KK08 LL04 LL10 MM33 NN25 NN27 NN28 QQ03 QQ17 4D002 AA03 AA05 AA06 AA13 AB02 AC10 BA05 BA17 CA07 DA59 EA02 EA09 EA13 GA03 GB12 HA01    ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Shigeki Yamashita             11-1 Haneda Asahi-cho, Ota-ku, Tokyo Co., Ltd.             Inside the EBARA CORPORATION (72) Inventor Toshihiro Tanaka             11-1 Haneda Asahi-cho, Ota-ku, Tokyo Co., Ltd.             Inside the EBARA CORPORATION F-term (reference) 4C080 AA07 BB02 CC03 CC04 CC05                       CC08 CC13 HH05 HH09 JJ03                       KK06 KK08 LL04 LL10 MM33                       NN25 NN27 NN28 QQ03 QQ17                 4D002 AA03 AA05 AA06 AA13 AB02                       AC10 BA05 BA17 CA07 DA59                       EA02 EA09 EA13 GA03 GB12                       HA01

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 底部に悪臭ガスの給気管と、上部に処理
ガスの排気管と、内部に悪臭ガスの悪臭成分を分解する
微生物を担持した充填層と、該充填層に洗浄水を散布す
る散水管とを備えた生物脱臭装置において、前記充填層
を、多孔性樹脂成型体の表面にポリビニルアルコールの
アセタール化物をコーティングした充填材で形成したこ
とを特徴とする生物脱臭装置。
1. A malodorous gas supply pipe at the bottom, a processing gas exhaust pipe at the top, a packing layer carrying microorganisms that decompose the malodorous component of the malodorous gas inside, and washing water is sprayed on the packing layer. A biological deodorizing device comprising a water sprinkling pipe, wherein the filling layer is formed of a filling material in which a surface of a porous resin molded body is coated with an acetalized product of polyvinyl alcohol.
【請求項2】 前記多孔性樹脂成型体は、ポリウレタ
ン、ポリスチレン、ポリプロピレン、ポリエチレン又は
ポリアセタールの発泡成型物である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 device according to claim 1, wherein the porous resin molding is a foam molding of polyurethane, polystyrene, polypropylene, polyethylene or polyacetal.
【請求項3】 前記多孔性樹脂成型体は、樹脂の表面の
異なる部位で入口と出口が開放した連続孔構造を有する
ことを特徴とする請求項1又は2記載の生物脱臭装置。
3. The biological deodorizing device according to claim 1, wherein the porous resin molding has a continuous pore structure in which an inlet and an outlet are open at different portions of the surface of the resin.
JP2001355835A 2001-11-21 2001-11-21 Biological deodorizing apparatus Pending JP2003154230A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001355835A JP2003154230A (en) 2001-11-21 2001-11-21 Biological deodorizing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001355835A JP2003154230A (en) 2001-11-21 2001-11-21 Biological deodorizing apparatus

Publications (1)

Publication Number Publication Date
JP2003154230A true JP2003154230A (en) 2003-05-27

Family

ID=19167465

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001355835A Pending JP2003154230A (en) 2001-11-21 2001-11-21 Biological deodorizing apparatus

Country Status (1)

Country Link
JP (1) JP2003154230A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007268408A (en) * 2006-03-31 2007-10-18 Kurita Water Ind Ltd Gas pretreatment apparatus and washing method of gas pretreatment apparatus
KR100906997B1 (en) 2007-12-28 2009-07-08 엔텍이앤씨 주식회사 Fluidized bed scrubber using porous media for gas purification
WO2009090833A1 (en) * 2008-01-16 2009-07-23 Kabushiki Kaisha Toshiba Biological desulfurization apparatus
JP2009191166A (en) * 2008-02-14 2009-08-27 Toshiba Corp Biological desulfurization apparatus for biogas
CN101791618B (en) * 2010-02-09 2012-11-14 浙江大学 Refuse landfill obnoxious gas in-situ control method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007268408A (en) * 2006-03-31 2007-10-18 Kurita Water Ind Ltd Gas pretreatment apparatus and washing method of gas pretreatment apparatus
KR100906997B1 (en) 2007-12-28 2009-07-08 엔텍이앤씨 주식회사 Fluidized bed scrubber using porous media for gas purification
WO2009090833A1 (en) * 2008-01-16 2009-07-23 Kabushiki Kaisha Toshiba Biological desulfurization apparatus
JP2009167300A (en) * 2008-01-16 2009-07-30 Toshiba Corp Biological desulfurization apparatus and start-up method thereof
JP2009191166A (en) * 2008-02-14 2009-08-27 Toshiba Corp Biological desulfurization apparatus for biogas
CN101791618B (en) * 2010-02-09 2012-11-14 浙江大学 Refuse landfill obnoxious gas in-situ control method

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