Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP2697066B2 - Biological deodorizer - Google Patents
[go: Go Back, main page]

JP2697066B2 - Biological deodorizer - Google Patents

Biological deodorizer

Info

Publication number
JP2697066B2
JP2697066B2 JP1010376A JP1037689A JP2697066B2 JP 2697066 B2 JP2697066 B2 JP 2697066B2 JP 1010376 A JP1010376 A JP 1010376A JP 1037689 A JP1037689 A JP 1037689A JP 2697066 B2 JP2697066 B2 JP 2697066B2
Authority
JP
Japan
Prior art keywords
layer
packed bed
gas
decomposition layer
tower
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 - Lifetime
Application number
JP1010376A
Other languages
Japanese (ja)
Other versions
JPH02191522A (en
Inventor
尚 永見
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP1010376A priority Critical patent/JP2697066B2/en
Publication of JPH02191522A publication Critical patent/JPH02191522A/en
Application granted granted Critical
Publication of JP2697066B2 publication Critical patent/JP2697066B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

  • Treating Waste Gases (AREA)

Description

【発明の詳細な説明】 [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、その他各種工場等から発生する悪臭を生物学的
に脱臭する脱臭装置であって、とりわけ硫黄系悪臭物質
を対象とした生物脱臭装置において、脱臭を行なう微生
物の性質に基き、各硫黄系悪臭物質を段階的に処理する
ことにより、安定かつ効率的な脱臭を行なうことが可能
な生物脱臭装置に関する。
Description: TECHNICAL FIELD The present invention relates to a biological deodorizing device, and more particularly to a biological deodorizing device for biologically deodorizing a bad odor generated from a human waste treatment plant, a sewage treatment plant, and various factories. In particular, in a biological deodorizing apparatus for sulfur-based malodorous substances, it is possible to perform stable and efficient deodorization by treating each sulfur-type malodorous substance stepwise based on the properties of the microorganisms that perform the deodorization. A possible biological deodorizing device.

[従来の技術及び先行技術] し尿、下水等の臭気ガスの臭気成分として硫黄系臭気
物質がある。臭気ガス中の硫黄系臭気物質としては硫化
水素(以下、「H2S」と記す。)、メチルメルカプタン
(以下「MM」と記す。)、硫化メチル(以下、「DMS」
と記す。)等が知られており、従来より、これらの硫黄
系臭気物質を生物脱臭により除去する試みがなされてい
る。
[Prior Art and Prior Art] As an odor component of odor gas such as night soil and sewage, there is a sulfur odorant. Hydrogen sulfide (hereinafter referred to as “H 2 S”), methyl mercaptan (hereinafter referred to as “MM”), and methyl sulfide (hereinafter “DMS”)
It is written. ) And the like, and attempts have been made to remove these sulfur odorants by biological deodorization.

従来、し尿、下水、その他の廃水の臭気ガスの脱臭を
行なうための生物脱臭装置は、脱臭を行なう微生物源と
して返送汚泥を使用している。
2. Description of the Related Art Conventionally, a biological deodorizing apparatus for deodorizing odorous gas from human waste, sewage, and other wastewater uses returned sludge as a microorganism source for deodorizing.

このため、その微生物構成は、常に生物脱臭に最適な
構成であるとはいえず、安定な脱臭を行うことができる
微生物構成となるまで、長期(40日以上)の馴養を必要
とするという欠点があった。
For this reason, its microbial composition is not always the optimal composition for biological deodorization, and it requires long-term (40 days or more) acclimation until it becomes a microbial composition capable of performing stable deodorization. was there.

上記従来の問題点を解決し、臭気ガス中の硫黄系臭気
物質を効率的に分解除去し、短い接触時間で脱臭処理す
る技術として、本発明者らはジメチルスルホトキシド
(以下、[DMSO」と記す。)で培養された硫黄系臭気分
解菌を用いることを特許出願した(特願昭63−5538。以
下、「先願I」という。)。
As a technique for solving the conventional problems described above, efficiently decomposing and removing sulfur-based odorous substances in odorous gas, and deodorizing treatment in a short contact time, the present inventors have proposed dimethyl sulfoxide (hereinafter referred to as [DMSO] (Japanese Patent Application No. 63-5538, hereinafter referred to as "prior application I").

そして、先願Iの技術をもとに、脱臭材充填層に通気
して悪臭を除去する生物脱臭装置であって、該脱臭材充
填層として、DMSOで培養された硫黄系臭気物質分解菌を
支持してなる脱臭材充填層を直列に2段以上設けてなる
生物脱臭装置を特許出願した(特願昭63−71642。以下
「先願II」という。)。
Further, based on the technology of the prior application I, a biological deodorizing apparatus for removing malodor by ventilating a deodorizing material-filled layer, wherein the deodorizing material-filled layer contains sulfur-based odorant-degrading bacteria cultured in DMSO. A patent application has been filed for a biological deodorizing apparatus having two or more layers of supporting deodorizing materials in series (Japanese Patent Application No. 63-71642, hereinafter referred to as "prior application II").

前記先願I及び先願IIによれば、硫黄系悪臭物質分解
菌の添加及びその増殖基質、即ちDMSOの添加により、装
置内の脱臭微生物量を増加させ、馴養期間の短縮化並び
に脱臭の安定化を図ることが可能とされる。
According to the above-mentioned prior applications I and II, the amount of deodorizing microorganisms in the apparatus is increased by the addition of a sulfur-based malodorous substance-decomposing bacterium and the growth substrate thereof, that is, DMSO, thereby shortening the acclimatization period and stabilizing the deodorization. Can be achieved.

[発明が解決しようとする課題] しかしながら、先願I及び先願IIで採用される脱臭菌
及び増殖基質は、高価であるため、脱臭効果率及び脱臭
安定性をより一層改善することにより、その使用量を最
低限に抑えることが望まれる。
[Problems to be Solved by the Invention] However, since the deodorizing bacteria and the growth substrate used in the prior application I and the prior application II are expensive, the deodorizing effect rate and the deodorizing stability are further improved by further improving the deodorizing effect rate and the deodorizing stability. It is desirable to minimize the amount used.

本発明は、硫黄系臭気物質を含む悪臭ガスを安定かつ
効率的に、低コストで処理することができる生物脱臭装
置を提供することを目的とする。
An object of the present invention is to provide a biological deodorizing apparatus capable of stably and efficiently treating malodorous gas containing a sulfur-based odorous substance at low cost.

[課題を解決するための手段] 本発明の生物脱臭装置は、底部に悪臭ガスの給気管を
備える処理塔と、該処理塔内に上下方向に離して3段以
上の複数段設けられた、悪臭成分を分解する微生物を担
持し、かつ処理すべき悪臭ガスが、上向流で通気する充
填層と、各充填槽の上に洗浄水を散布する散水管と、相
互に上段と下段の充填層の間で、且つ下段の充填層に対
する散水管よりも上に設けられた、悪臭ガスの流れは通
すが、上から下への水流は阻止する仕切板と、該仕切板
上に溜る水を塔外に排出する排水管とを備える生物脱臭
装置であって、前記充填層は処理塔内に給気される悪臭
ガスの上流側から順に、硫化水素(H2S)分解層、メチ
ルメルカプタン(MM)分解層及び硫化メチル(DMS)分
解層を形成することを特徴とする。
[Means for Solving the Problems] The biological deodorization apparatus of the present invention is provided with a processing tower provided with an odor gas supply pipe at the bottom, and a plurality of three or more stages separated vertically in the processing tower. A filling layer that carries microorganisms that decompose malodorous components and that is to be treated, and a malodorous gas to be treated flows in an upward flow, a sprinkler pipe that sprays washing water onto each filling tank, and a top and bottom filling A partition plate provided between the layers and above the sprinkling pipe for the lower packed bed, which allows the flow of the offensive odor gas but blocks the flow of water from above to below, and the water collected on the partition plate A biological deodorizing device comprising a drain pipe for discharging the outside of the tower, wherein the packed bed is a hydrogen sulfide (H 2 S) decomposition layer, a methyl mercaptan ( (MM) decomposition layer and methyl sulfide (DMS) decomposition layer are formed.

なお、本発明において、処理塔内に形成されるH2S分
解層、MM分解層及びDMS分解層のうち、H2S分解層には、
活性汚泥を支持するものを用いるのが好ましい。MM分解
層は負荷量に応じて、活性汚泥及び/又はDMSO培養菌を
支持するものを用いるのが好ましい。また、DMS分解層
はDMSO培養菌を支持するものとするのが好ましい。活性
汚泥を支持する充填層については、時折散水洗浄をする
程度で良く、特にpH調製の必要はないが、DMSO培養菌を
支持する充填層は、そのpHを中性に維持することが好ま
しい。
In the present invention, among the H 2 S decomposition layer, the MM decomposition layer, and the DMS decomposition layer formed in the treatment tower, the H 2 S decomposition layer includes:
It is preferable to use one that supports activated sludge. It is preferable to use an MM decomposition layer that supports the activated sludge and / or the DMSO culture according to the load. Further, it is preferable that the DMS decomposition layer supports DMSO culture bacteria. The packed bed supporting the activated sludge only needs to be sprinkled and washed occasionally, and there is no particular need to adjust the pH. However, the packed bed supporting the DMSO culture is preferably maintained at a neutral pH.

処理塔内の充填層に活性汚泥又はDMSO培養菌を支持さ
せる方法としては、ピート等の担体に予め固定して塔内
に充填するのが望ましいが、担体充填後、各層に活性汚
泥又はDMSO培養菌を散布しても良い。
As a method for supporting activated sludge or DMSO culture bacteria in the packed bed in the treatment tower, it is preferable to fix the carrier on a carrier such as peat in advance and fill the tower.However, after the carrier is filled, activated sludge or DMSO culture is applied to each layer. Bacteria may be sprayed.

本発明の生物脱臭装置は、このようなピート等の担体
を用いる固体床式に限らず、流動床式にも適用できるこ
とは言うまでもない。
It goes without saying that the biological deodorizing apparatus of the present invention can be applied not only to a solid bed type using such a carrier such as peat but also to a fluidized bed type.

[作用] 悪臭ガス中にH2S、MM、DMSが混在する場合、H2S、M
M、DMSの順で分解され易く、H2Sのような易分解性ガス
の存在は、その他の臭気物質の分解を阻害する。
[Action] When H 2 S, MM, and DMS are mixed in the odorous gas, H 2 S, M
It is easily decomposed in the order of M and DMS, and the presence of easily decomposable gas such as H 2 S inhibits the decomposition of other odorous substances.

従って、生物脱臭装置により、このような悪臭ガスを
安定に処理するためには、各々の悪臭物質を段階的に分
解するシステムを形成する必要があるが、従来の方法で
は、このシステムを形成するまでに、長時間を要し、こ
のため馴養の長期化をもたらしていた。
Therefore, in order to stably treat such malodorous gas by the biological deodorizing device, it is necessary to form a system for decomposing each malodorous substance in a stepwise manner. However, in the conventional method, this system is formed. By the time, it took a long time, and this led to prolonged habituation.

これに対し、本発明の生物脱臭装置では、悪臭成分を
分解する微生物を担持する充填層を3段以上の複数段設
け、給気される悪臭ガスの上流側から順に、H2S分解
層、MM分解層及びDMS分解層をそれぞれ独立に形成して
いるため、運転初期から各層において安定な処理を行な
うことができる。
On the other hand, in the biological deodorizing apparatus of the present invention, a packed layer carrying microorganisms that decompose malodorous components is provided in three or more stages, and an H 2 S decomposition layer is provided in order from the upstream of the supplied malodorous gas. Since the MM decomposition layer and the DMS decomposition layer are formed independently of each other, stable processing can be performed in each layer from the beginning of operation.

また、各充填層において、各々個別に各悪臭成分に対
して該悪臭成分を完全に分解できるように、負荷の調
整、菌量の増補等について最適な運転管理を行なえるた
め、急激な負荷変動に対しても適切な処置を講じること
が可能である。
In addition, in each packed bed, it is possible to perform optimal operation management for load adjustment, increase of the amount of bacteria, etc. so that the malodor components can be completely decomposed individually for each malodor component. It is possible to take appropriate measures for

更に、各々の充填層において処理する悪臭成分に応じ
て、充填層に用いる微生物として、活性汚泥又はDMSO培
養菌を選択することにより、DMSO培養菌の使用量を抑
え、処理コストを低廉化することもできる。
Furthermore, by selecting activated sludge or DMSO culture bacteria as the microorganisms used in the packed bed according to the malodorous component to be treated in each packed bed, it is possible to reduce the amount of DMSO culture used and reduce the processing cost. Can also.

ところで、一般に、充填層を多段に設けた場合、下段
側の充填層はそれ自身に散布される洗浄水のほか、上段
側の充填層に散布されて該層から流れ落ちる洗浄水をも
受けるので、上段側の充填層に比して圧密化が進み、圧
力損失が増大するという問題がある。
By the way, in general, when the packed layer is provided in multiple stages, the lower packed layer receives not only the washing water sprayed on itself, but also the washing water sprayed on the upper packed layer and flowing down from the layer, There is a problem that the consolidation progresses as compared with the upper packed bed and the pressure loss increases.

しかしながら、本発明の構成に従って、各充填層毎
に、悪臭ガスの流れは通すが、上から下への水流は阻止
する仕切板と、該仕切板上に溜る水を塔外に排出する排
水管とを所定箇所に配置することにより、このような下
段側の充填層の圧密化、圧力損失の増大が解消される。
However, according to the configuration of the present invention, for each packed bed, a partition plate that allows the flow of the odorous gas but blocks the water flow from top to bottom, and a drain pipe that discharges the water accumulated on the partition plate to the outside of the tower By arranging at a predetermined position, the above-described compaction of the packed bed on the lower side and an increase in pressure loss are eliminated.

[実施例] 以下、図面を参照して本発明の実施例について説明す
る。
Example An example of the present invention will be described below with reference to the drawings.

第1図及び第2図は各々本発明の生物脱臭装置の一実
施例を示す概略的な縦断面図、及びその詳細を示す縦断
面図、第3図は第2図の要部拡大図である。
1 and 2 are schematic longitudinal sectional views showing one embodiment of the biological deodorizing apparatus of the present invention, and longitudinal sectional views showing details thereof, and FIG. 3 is an enlarged view of a main part of FIG. is there.

本実施例の生物脱臭装置は、底部に悪臭ガスの給気管
1を備え、上部に処理ガスの排出管2を備える処理塔3
内に、充填層4、5、6が、上下方向に離して、3段に
設けられ、下から順に、H2S分解層4、MM分解層5及びD
MS5分解層6が設定されている。
The biological deodorizing apparatus according to the present embodiment includes a processing tower 3 having an air odor gas supply pipe 1 at the bottom and a processing gas discharge pipe 2 at the top.
In the inside, packing layers 4, 5, and 6 are provided in three stages separated in the up-down direction, and the H 2 S decomposition layer 4, the MM decomposition layer 5, and D
The MS5 decomposition layer 6 is set.

即ち、塔3内にはグリット(格子体)7a、7b、7cが棚
設され、その上に多孔板や網状シートなどの通気、通水
性の支持部材8a、8b、8cが載置され、その上にピートで
充填層4、5、6が支持されている。これらの充填層
4、5、6のうち充填層(H2S分解層)4には活性汚泥
が、充填層(MM分解層)5には活性汚泥又はDMSO培養菌
が、充填層(DMS分解層)6にはDMSO培養菌が担持され
ている。
That is, grids (lattices) 7a, 7b, 7c are shelved in the tower 3, on which ventilation and water-permeable supporting members 8a, 8b, 8c such as perforated plates and net-like sheets are placed. Filled layers 4, 5, 6 are supported by peat on top. Among these packed layers 4, 5, and 6, the packed bed (H 2 S decomposition layer) 4 contains activated sludge, the packed bed (MM decomposition layer) 5 contains activated sludge or DMSO culture, and the packed bed (DMS decomposition). The layer (6) carries DMSO culture bacteria.

充填層4、5、6には、各々網目状部材11a、11b、11
cが垂直方向に、それぞれの下端を支持部材の8a、8b、8
cに当節して挿設されている。この網目状部材11a、11
b、11cは、板状のものでも、円筒形、多角筒形などの筒
形のものでも良い。筒形のものとしては、例えば日本ネ
トロン株式会社製の「ネトロンチューブTSXー244」(商
品名)(菱形の網目を構成する合成樹脂の太さ;約2.5m
m、菱形の網目の目開きの一辺の長さ;約5mm、直径;330
mmの円筒形)を使用することができる。
The packed layers 4, 5, and 6 have mesh members 11a, 11b, 11 respectively.
c is the vertical direction, each lower end of the supporting member 8a, 8b, 8
It is inserted in c. The mesh members 11a, 11
Each of b and 11c may be a plate-like member or a cylindrical member such as a cylindrical or polygonal tube. Examples of the cylindrical shape include, for example, "Netron Tube TSX-244" (trade name) manufactured by Japan Netron Co., Ltd. (the thickness of the synthetic resin constituting the diamond-shaped mesh; about 2.5 m
m, length of one side of mesh opening of rhombus; about 5 mm, diameter; 330
mm cylindrical shape) can be used.

本実施例は、このチューブを四本、一辺が1000mmの正
方形断面形状で、高さないし層厚が1500mmの各充填層
4、5、6中に同じ高さで均一に挿設した例であり、各
チューブ内にも長繊維のピートが充填してある。
This embodiment is an example in which four tubes are uniformly inserted at the same height into each of the packed layers 4, 5, and 6 having a square cross-sectional shape of 1000 mm on a side and a height or layer thickness of 1500 mm. Each tube is also filled with peat of long fibers.

このような網目状の支持部材11a、11b、11cで隔てら
れた充填層4、5、6の各部分は、各支持部材11a、11
b、11cと接触し、その接触摩擦力により支持部材11a、1
1b、11cに対して保持されるため、洗浄水を吸水して自
重を増しても充填層の下部を加重することが防止され、
これにより圧密化の進行は更に遅くなり、圧力損失の増
加の度合いを低減させることができる。
Each portion of the packed layers 4, 5, 6 separated by such mesh-like support members 11a, 11b, 11c is a support member 11a, 11
b, 11c, and the contact members 11a, 1c
Since it is held against 1b, 11c, even if the washing water is absorbed and its own weight is increased, it is prevented that the lower part of the packed bed is weighted,
As a result, the progress of consolidation is further slowed down, and the degree of increase in pressure loss can be reduced.

なお、本発明において、上記効果を有効に発現させる
ためには、1つの充填層内の支持部材相互の隣接間隔は
500mm以下であることが好ましい。
Note that, in the present invention, in order to effectively exhibit the above-described effects, the adjacent distance between the support members in one filling layer is preferably
Preferably it is 500 mm or less.

10a、10b、10cは各充填層4、5、6に洗浄水を散布
するスプレーノズルを均一な配置で備える散水管であっ
て、各々、散水本管10よりポンプPにより給水される。
Reference numerals 10a, 10b, and 10c denote water spray pipes provided with spray nozzles for spraying wash water on each of the packed layers 4, 5, and 6 in a uniform arrangement, and water is supplied from the water spray main pipe 10 by a pump P.

本発明の装置においては、相互に上段と下段の充填層
の間で、下段の充填層に洗浄水を散布する散水管の上
に、ガス流は上向させるが、洗浄水は流下させない仕切
板12a、12bを設けると共に、この仕切板12a、12b上に溜
る水を塔外に排出する排出管13a、13bが設けられてい
る。
In the device of the present invention, the partition plate between which the gas flow is directed upward, but the cleaning water is not allowed to flow, between the upper and lower packed beds, and on the sprinkler pipe for spraying the washing water on the lower packed bed. In addition to the provision of 12a and 12b, drain pipes 13a and 13b for discharging water collected on the partition plates 12a and 12b to the outside of the tower are provided.

この仕切板12a、12b及び排出管13a、13bの構成につい
て、第3図を参照して説明する。
The configuration of the partition plates 12a and 12b and the discharge pipes 13a and 13b will be described with reference to FIG.

第3図に示す如く、仕切板12aは、悪臭ガスを上向さ
せるが、洗浄水は流下させないようにするため、仕切板
12aには均一な配置で孔14を開設し、その各孔の縁に上
端が閉じた盲筒15を立設し、該盲筒の上部側面に窓孔16
を形成して構成されている。排出管13aは、処理塔3の
壁面の仕切板12aの取付部に形成された開口3aに接続さ
れている。
As shown in FIG. 3, the partition plate 12a makes the odorous gas upward, but the partition plate 12a prevents the washing water from flowing down.
Holes 14 are opened in a uniform arrangement in 12a, a blind cylinder 15 having a closed upper end is erected on the edge of each hole, and a window hole 16 is formed on the upper side surface of the blind cylinder.
Is formed. The discharge pipe 13a is connected to an opening 3a formed in a mounting portion of the partition plate 12a on the wall surface of the processing tower 3.

第2図において、17はエリミネータ、18は排水管であ
る。なお、図示はされていないが、各充填層4、5、6
の上方部には、散水管とは別に、DMSO培養菌又は活性汚
泥を添加するための供給管が設けられている。
In FIG. 2, 17 is an eliminator and 18 is a drain pipe. Although not shown, each of the packed layers 4, 5, 6
A supply pipe for adding DMSO culture bacteria or activated sludge is provided separately from the sprinkler pipe in the upper part of.

このような生物脱臭装置により、悪臭ガスの脱臭処理
を行なうには、まず、悪臭ガスを給気管1より処理塔3
に導入する。悪臭ガスは充填層(H2S分解層)4を通過
する過程で活性汚泥により処理されて、含有されるH2S
が酸化分解される。次いで、充填層(MM分解層)5を通
過する過程で活性汚泥又はDMSO培養菌により処理され
て、含有されるMMが酸化分解される。更に、充填層(DM
S分解層)6を通過する過程でなお含有されるDMSがDMSO
培養菌により酸化分解される。また、悪臭ガス中に二硫
化メチルがあれば。それもDMS分解層で酸化分解され
る。
In order to perform the deodorizing treatment of the malodorous gas by such a biological deodorizing apparatus, first, the malodorous gas is supplied from the air supply pipe 1 to the treatment tower 3.
To be introduced. The odorous gas is treated by activated sludge in the process of passing through the packed bed (H 2 S decomposition layer) 4 and contains H 2 S
Is oxidatively decomposed. Next, in the process of passing through the packed bed (MM decomposition layer) 5, it is treated with activated sludge or DMSO culture bacteria, and the contained MM is oxidatively decomposed. In addition, the packed bed (DM
DMS still contained in the process of passing through the (S decomposition layer) 6 is DMSO
Degraded oxidatively by culture. Also, if there is methyl disulfide in the odorous gas. It is also oxidatively decomposed in the DMS decomposition layer.

このようにして、脱臭処理されたガスは、エリミネー
タ17で水分を除去した後、塔頂の排出管2より排出され
る。なお、H2S、MM、DMS等の硫黄形悪臭成分は、活性汚
泥又はDMSO培養菌により硫酸イオンにまで酸化分解され
る。
The gas thus deodorized is discharged from the discharge pipe 2 at the top of the tower after water is removed by the eliminator 17. Note that sulfur-type malodorous components such as H 2 S, MM, and DMS are oxidatively decomposed to sulfate ions by activated sludge or DMSO culture bacteria.

従って、各充填層4、5、6には悪臭成分を酸化分解
して脱臭処理し、除去した硫黄系物質とほぼ等量の硫酸
イオンが生成し、放置して置くと次第に蓄積する。この
硫酸イオンは微生物の生物反応を阻害するため、各充填
層に散水管10a、10b、10cより洗浄水を散布し、硫酸イ
オンを塔外に洗い流す必要がある。
Accordingly, in each of the packed layers 4, 5, and 6, a malodorous component is oxidized and decomposed to perform a deodorizing treatment, and a sulfate ion of substantially the same amount as that of the removed sulfur-based substance is generated, and gradually accumulates when left to stand. Since this sulfate ion inhibits the biological reaction of microorganisms, it is necessary to spray the washing water from each of the water pipes 10a, 10b, and 10c to each packed bed to wash the sulfate ion out of the tower.

微生物の活性を維持するために水分を補給する必要も
ある。
It is also necessary to rehydrate in order to maintain the activity of the microorganism.

即ち、充填層3、4、5を長繊維状ピートを堆積して
形成する場合、長繊維状ピートとしては、泥炭地から採
取したピートを冬期屋外に放置して凍結乾燥したものを
目開き8mmの篩でふるって短いものを除去したものを用
いることができる。充填層の充填密度は、充填層1m3
たり乾燥ピート換算で100〜150kgが好ましい。充填層の
充填高さは1〜1.5m程度がよく、充填層の含水率(ピー
ト重量と水分重量の合計に占める水分重量の百分率)
は、微生物の活性を維持するため50〜80%好ましくは60
〜70%とするのが好ましい。従って、このような含水率
を得るために、処理中に必要に応じて、水、含水汚泥、
DMSO水溶液、DMSOを基質とする培養液等を散水管より散
布するのが望ましい。
That is, when the filling layers 3, 4, and 5 are formed by depositing long fibrous peat, the long fibrous peat is obtained by leaving the peat collected from peatland outdoors in the winter and freeze-drying it to obtain an opening of 8 mm. Can be used to remove short ones by sieving with a sieve. Packing density of the packed bed, 100~150Kg preferably a packed layer 1 m 3 per dry peat basis. The filling height of the packed bed is preferably about 1 to 1.5 m, and the moisture content of the packed bed (percentage of water weight in total of peat weight and water weight)
Is 50 to 80%, preferably 60 to maintain the activity of the microorganism.
It is preferably set to 70%. Therefore, in order to obtain such a water content, water, hydrous sludge,
It is desirable to spray a DMSO aqueous solution or a culture solution using DMSO as a substrate from a watering tube.

このような洗浄水等の散水を行なう場合、本発明の装
置においては、前述の如く仕切板12a、12b及び排水管13
a、13bが設けられていることから、上段側の充填層に散
布した洗浄水等が下段側の充填層にも降り、その圧密
化、電力損失増大の進行が速まることが防止される。即
ち、充填層5に散布された洗浄水等は、仕切板12aに阻
止されて、充填層4に降りることなく、排水管13aより
排出させる。同様に、充填層6に散布された洗浄水等
は、仕切板12bに阻止されて、充填層5に降りることな
く、排水管13bより排出される。
When watering such washing water or the like is performed, in the apparatus of the present invention, the partition plates 12a, 12b and the drain pipe 13 are provided as described above.
Since the a and 13b are provided, it is possible to prevent the washing water or the like sprayed on the upper packed layer from flowing down to the lower packed layer, thereby preventing the consolidation and the increase of the power loss from being accelerated. That is, the washing water or the like sprayed on the packed bed 5 is blocked by the partition plate 12a and discharged from the drain pipe 13a without descending to the packed bed 4. Similarly, the washing water or the like sprayed on the packed bed 6 is blocked by the partition plate 12b and discharged from the drain pipe 13b without descending to the packed bed 5.

充填層4に散布された洗浄水等は、処理塔3の底面に
流下した後、排水管18より排出される。
The washing water or the like sprayed on the packed bed 4 flows down to the bottom of the treatment tower 3 and is then discharged from the drain pipe 18.

なお、第1図〜第3図に示す生物脱臭装置は、本発明
の一実施例であって、本発明はその要旨を超えない限
り、図示の例に限定されるものではない。例えば、充填
層は3段に形成するものに限られず、4段或いは5段以
上の複数段形成しても良い。また、仕切板や排水機構に
ついても、その他の構成を採用することができる。
The biological deodorizing device shown in FIGS. 1 to 3 is an embodiment of the present invention, and the present invention is not limited to the illustrated example unless it exceeds the gist. For example, the filling layer is not limited to being formed in three stages, but may be formed in four stages or in five or more stages. Other configurations can be adopted for the partition plate and the drainage mechanism.

[発明の効果] 以上詳述した通り、本発明の生物脱臭装置は、処理塔
内に、H2S分解層、MM分解層、DMS分解層の充填層が、そ
れぞれ独立して多段に形成されているため、 予め悪臭成分の易分解性に応じた順でそれぞれの成
分を分解する充填層が直列配置されている状態であるた
め、馴養期間が殆どなく、早期より安定な脱臭処理を行
なうことができ、装置の立ち上げ期間を大幅に短縮する
ことができる。
[Effects of the Invention] As described in detail above, in the biological deodorization apparatus of the present invention, the H 2 S decomposition layer, the MM decomposition layer, and the packed layer of the DMS decomposition layer are formed in multiple stages independently in the treatment tower. Because the packed bed that decomposes each component in advance in the order according to the easy decomposability of the offensive odor components is arranged in series, there is almost no acclimatization period, and it is necessary to perform more stable deodorization treatment at an early stage. The start-up period of the device can be greatly reduced.

分解する悪臭ガスに応じて各充填層の運転管理を行
なうことができるため、急激な負荷変動に対しても適切
な処理を講じて良好な対応をなすことができる。
Since the operation of each packed bed can be controlled according to the malodorous gas to be decomposed, it is possible to take an appropriate process even for a sudden change in load and take a good response.

各充填層毎に微生物を選定できるため、DMSO培養菌
の使用量を最小限に抑えることが可能とされ、処理コス
トを引き下げることができる。
Since microorganisms can be selected for each packed bed, it is possible to minimize the amount of DMSO culture used, thereby reducing processing costs.

等の効果が奏される。And the like.

しかも、上段側の充填層に散布された洗浄水は下段側
の充填層に降ることなく、塔外に排水されるため、下段
側の充填層の圧密化、圧力損失の増大が上段側より速ま
ることがなく、長期間にわたり装置を安定に定常運転で
きる。
In addition, the washing water sprayed on the upper packed bed is discharged to the outside of the tower without descending to the lower packed bed, so that the lower packed bed becomes more compact and the pressure loss increases faster than the upper packed bed. And the device can be stably operated for a long period of time.

従って、本発明の生物脱臭装置によれば、多種類の硫
黄系悪臭物質を含む悪臭ガスをも、極めて安定に効率的
に、低コストでほぼ完全に脱臭することができる。
Therefore, according to the biological deodorizing apparatus of the present invention, malodorous gas containing various kinds of sulfur-based malodorous substances can be very stably and efficiently deodorized almost at low cost.

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

第1図及び第2図は各々本発明の生物脱臭装置の一実施
例を示す概略的な縦断面図、及びその詳細を示す縦断面
図、第3図は第2図の要部拡大図である。 1……給気管、2……排出管、 3……処理塔、4……充填層(H2S分解層)、 5……充填層(MM分解層)、 6……充填層(DMS分解層)、 10……散水管。
1 and 2 are schematic longitudinal sectional views showing one embodiment of the biological deodorizing apparatus of the present invention, and longitudinal sectional views showing details thereof, and FIG. 3 is an enlarged view of a main part of FIG. is there. 1 ...... supply pipe, 2 ...... discharge pipe, 3 ...... treating tower, 4 ...... packed bed (H 2 S decomposition layer), 5 ...... filling layer (MM decomposition layer), 6 ...... packed layer (DMS decomposition Layer), 10 ... watering tube.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】底部に悪臭ガスの給気管を備える処理塔
と、 該処理塔内に上下方向に離して3段以上の複数段設けら
れた、悪臭成分を分解する微生物を担持し、かつ処理す
べき悪臭ガスが上向流で通気する充填層と、 各充填槽の上に洗浄水を散布する散水管と、 相互に上段と下段の充填層の間で、且つ下段の充填層に
対する散水管よりも上に設けられた、悪臭ガスの流れは
通すが、上から下への水流は阻止する仕切板と、 該仕切板上に溜る水を塔外に排出する排水管と、 を備える生物脱臭装置であって、 前記充填層は処理塔内に給気される悪臭ガスの上流側か
ら順に、硫化水素分解層、メチルメルカプタン分解層及
び硫化メチル分解層を形成することを特徴とする生物脱
臭装置。
1. A processing tower provided with a gas supply pipe for malodorous gas at the bottom, and a plurality of three or more stages vertically separated in the processing tower, which carry microorganisms for decomposing malodorous components and treat the same. A filling layer through which the odorous gas to be ventilated in an upward flow, a sprinkling pipe for spraying washing water on each filling tank, and a sprinkling pipe between the upper and lower packing layers and for the lower packing layer. A biological deodorization system comprising: a partition plate provided above the partition plate, through which the flow of the offensive odor gas passes, but blocks the flow of water from above to below, and a drain pipe for discharging the water accumulated on the partition plate to the outside of the tower. An apparatus, wherein the packed bed forms a hydrogen sulfide decomposition layer, a methyl mercaptan decomposition layer, and a methyl sulfide decomposition layer in order from the upstream side of the malodorous gas supplied into the processing tower. .
JP1010376A 1989-01-19 1989-01-19 Biological deodorizer Expired - Lifetime JP2697066B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1010376A JP2697066B2 (en) 1989-01-19 1989-01-19 Biological deodorizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1010376A JP2697066B2 (en) 1989-01-19 1989-01-19 Biological deodorizer

Publications (2)

Publication Number Publication Date
JPH02191522A JPH02191522A (en) 1990-07-27
JP2697066B2 true JP2697066B2 (en) 1998-01-14

Family

ID=11748414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1010376A Expired - Lifetime JP2697066B2 (en) 1989-01-19 1989-01-19 Biological deodorizer

Country Status (1)

Country Link
JP (1) JP2697066B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20230027370A (en) * 2021-08-18 2023-02-28 주식회사 에이치앤엠바이오 Organic Waste Treatment Odor Removal Device

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4751529B2 (en) * 2001-05-16 2011-08-17 荏原実業株式会社 Deodorizing equipment using organisms and humus
CN109806760B (en) * 2019-04-03 2024-04-09 生态环境部南京环境科学研究所 Temperature-adjusting and humidity-adjusting biological filter device and application method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20230027370A (en) * 2021-08-18 2023-02-28 주식회사 에이치앤엠바이오 Organic Waste Treatment Odor Removal Device
KR102547791B1 (en) 2021-08-18 2023-06-28 주식회사 에이치앤엠바이오 Organic Waste Treatment Odor Removal Device

Also Published As

Publication number Publication date
JPH02191522A (en) 1990-07-27

Similar Documents

Publication Publication Date Title
US6069004A (en) Circulatory microorganic deodorizing system
JP2691517B2 (en) Biological deodorizer
JP2697066B2 (en) Biological deodorizer
JP3063103B2 (en) Biological deodorization method
JPH09313874A (en) Biological deodorizing device
JP2976457B2 (en) Biological deodorizer
KR200229825Y1 (en) Deodorant device used for bioceramic media and microorganisms
JPH08131761A (en) Filling type biological deodorization apparatus
JP3094494B2 (en) Biological deodorizer
JP2591874B2 (en) Biological deodorization method
KR200285699Y1 (en) Under ground concrete Biofilter using two stage Air Distributor
JP3500694B2 (en) Biological deodorizer
JPH04363111A (en) Organism deodorizing method
JPH03161019A (en) Biological deodorizing apparatus
JP2605769Y2 (en) Biological deodorizer
JPH0929056A (en) Biological deodorizer
JP2560374B2 (en) Biological deodorizing method, biological deodorizing device, and agent for improving decomposition activity of sulfur-based odorous substances in biological deodorizing device
JPH0711783Y2 (en) Biological deodorizer
JPH02126916A (en) Deodorizing device
JP3466274B2 (en) Biological deodorizer
JPH02126917A (en) Deodorizing method
JPH09150030A (en) Deodorizing device
JPH047016A (en) Biological deodorization equipment
JPH07303815A (en) Biological deodorizer
JPH06226033A (en) Biological deodorizing method

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080919

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090919

Year of fee payment: 12

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090919

Year of fee payment: 12