JPH03161019A - Biological deodorizing apparatus - Google Patents
Biological deodorizing apparatusInfo
- Publication number
- JPH03161019A JPH03161019A JP1298994A JP29899489A JPH03161019A JP H03161019 A JPH03161019 A JP H03161019A JP 1298994 A JP1298994 A JP 1298994A JP 29899489 A JP29899489 A JP 29899489A JP H03161019 A JPH03161019 A JP H03161019A
- Authority
- JP
- Japan
- Prior art keywords
- tower
- decomposing
- methyl
- decomposition tower
- packed bed
- 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
Links
- 230000001877 deodorizing effect Effects 0.000 title claims description 28
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 55
- 239000007789 gas Substances 0.000 claims abstract description 35
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims abstract description 30
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims abstract description 30
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 claims abstract description 24
- QMMFVYPAHWMCMS-UHFFFAOYSA-N Dimethyl sulfide Chemical compound CSC QMMFVYPAHWMCMS-UHFFFAOYSA-N 0.000 claims abstract description 11
- 244000005700 microbiome Species 0.000 claims description 16
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 241000894006 Bacteria Species 0.000 abstract description 24
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 25
- 239000010802 sludge Substances 0.000 description 17
- 239000000126 substance Substances 0.000 description 16
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 14
- 229910052717 sulfur Inorganic materials 0.000 description 14
- 239000011593 sulfur Substances 0.000 description 14
- WQOXQRCZOLPYPM-UHFFFAOYSA-N dimethyl disulfide Chemical compound CSSC WQOXQRCZOLPYPM-UHFFFAOYSA-N 0.000 description 11
- 235000016068 Berberis vulgaris Nutrition 0.000 description 10
- 241000335053 Beta vulgaris Species 0.000 description 10
- 238000004332 deodorization Methods 0.000 description 10
- VLXBWPOEOIIREY-UHFFFAOYSA-N dimethyl diselenide Natural products C[Se][Se]C VLXBWPOEOIIREY-UHFFFAOYSA-N 0.000 description 9
- 238000000034 method Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 3
- 239000010800 human waste Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000010979 pH adjustment Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 239000012670 alkaline solution Substances 0.000 description 2
- 239000007853 buffer solution Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 235000019645 odor Nutrition 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- -1 that is Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
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。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a biological deodorizing device, and particularly to a deodorizing device that biologically deodorizes bad odors generated from human waste treatment plants, sewage treatment plants, and various other factories. In particular, biological deodorization equipment that targets sulfur-based malodorous substances can perform stable and efficient deodorization by treating each sulfur-based malodorous substance in stages based on the properties of the deodorizing microorganisms. Regarding possible biological deodorization equipment.
[従来の技術及び先行技術コ
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rMMJと記す。)、硫化メチル(以下、rDM
SJ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.
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
て活性汚泥を使用している。[Prior Art and Prior Art] There are sulfur-based odorous substances as odorous components of odorous gases such as human waste and sewage. Sulfur-based odorous substances in the odorous gas include hydrogen sulfide (hereinafter referred to as "H2S"), methyl mercaptan (hereinafter referred to as rMMJ), and methyl sulfide (hereinafter referred to as rDM).
It is written as SJ. ), and attempts have been made to remove these sulfur-based odorous substances by biological deodorization. Conventionally, biological deodorizing devices for deodorizing odorous gases from human waste, sewage, and other wastewater use activated sludge as a source of microorganisms 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i
改生物構成となるまで、長期(40日以上)の1111
iを必要とするという欠点があった。For this reason, its microbial composition is not always optimal for biological deodorization, and it is difficult to achieve stable deodorization.
1111 for a long period of time (40 days or more) until it becomes a reformed composition.
It had the disadvantage of requiring i.
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&#Fとして、本発明者らはジメチルスルホオキシド
(以下、rDMsOJ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63−5
538。以下、「先願■」という。)。The present inventors have developed a technique for solving the above conventional problems, efficiently decomposing and removing sulfur-based odorous substances in odorous gas, and deodorizing with a short contact time using dimethyl sulfoxide (rDMsOJ A patent application was filed for the use of sulfur-based odor-degrading bacteria cultured in
538. Hereinafter, this will be referred to as "first application ■." ).
そして、先願■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貿分解菌
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63−7164
2。以下「先願II Jという。).
前記先11I及び先願1■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。Based on the technology of the previous application (2), it is a biological deodorizing device that removes bad odors by ventilating a packed bed of deodorizing material, and the packed bed of deodorizing material is made of sulfur-based odor-degrading bacteria cultured in DMSO. A patent application has been filed for a biological deodorizing device in which two or more stages of deodorizing material filled layers supporting the
2. (hereinafter referred to as "Prior Application II J"). According to the above-mentioned No. 11I and Prior Application 1■, the amount of deodorizing microorganisms in the device is increased by adding sulfur-based malodorous substance degrading bacteria and its growth substrate, that is, DMSO. This makes it possible to shorten the acclimatization period and stabilize deodorization.
[発明が解決しようとする課題コ
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 growth substrate used in Prior Applications I and II are expensive, it is possible to improve their use by further improving deodorizing efficiency and deodorizing stability. It is desirable to keep the amount to a minimum.
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 device that can stably and efficiently treat malodorous gas containing sulfur-based odorous substances 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、H2S分解微生物を担持した
充填層を有し、被処理ガスが導入される主に硫化水素を
分解する硫化水素分解塔と、メチルメルカプタン分解微
生物を担持した充填層を有し、前記硫化水素分解塔の排
出ガスが導入される主にメチルメルカプタンを分解する
メチルメルカプタン分解塔と、DMS分解微生物を担持
した充填層を有し、前記メチルメルカプタン分解塔の排
出ガスが導入される主に硫化メチルを分解する硫化メチ
ル分解塔とを備えたものである。[Means for Solving the Problems] The biological deodorizing device of the present invention has a packed bed supporting H2S decomposing microorganisms, a hydrogen sulfide decomposition tower mainly for decomposing hydrogen sulfide into which a gas to be treated is introduced, and a methyl A methyl mercaptan decomposition tower that mainly decomposes methyl mercaptan, into which exhaust gas from the hydrogen sulfide decomposition tower is introduced, a packed bed that supports mercaptan-degrading microorganisms, and a packed bed that supports DMS-degrading microorganisms; It is equipped with a methyl sulfide decomposition tower that mainly decomposes methyl sulfide into which the exhaust gas from the methyl mercaptan decomposition tower is introduced.
なお、本発明において、H2S分解塔、MM分解塔及び
DMS分解塔のうち、H2S分解塔の充填層には、活性
汚泥を支持するものを用いるのが好ましい。MM分M塔
の充填層は負荷量に応じて、活性汚泥及び/又はDMS
O培養菌を支持するものを用いるのが好ましい。また、
DMS分解塔の充填層は活性活泥を支持するものでもよ
いが、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調整の必要はないが、D
MSO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 H2S decomposition tower, MM decomposition tower, and DMS decomposition tower, it is preferable to use a bed that supports activated sludge in the packed bed of the H2S decomposition tower. The packed bed of the MM column is filled with activated sludge and/or DMS depending on the load amount.
It is preferable to use one that supports O culture bacteria. Also,
The packed bed of the DMS decomposition tower may support activated slurry, but preferably supports DMSO cultured bacteria. For the packed bed that supports activated sludge, it is sufficient to occasionally wash it with water, and there is no need to particularly adjust the pH.
The packed bed supporting the MSO culture preferably maintains its pH at neutrality.
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、ビ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、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 cultured bacteria in the packed bed in the treatment tower, it is preferable to fix the activated sludge or DMSO cultured bacteria in advance to a carrier such as beet and fill it into the tower. May be sprayed.
本発明の生物脱臭装置は、このようなビート等の担体を
用いる固定床式に限らず、流動床弐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 fixed bed type using a carrier such as beet, but also to a fluidized bed type.
C作用]
悪臭ガス中にH2 S,MM,DMSが混在する場合、
H2 S,MM%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、その他の臭気物貿の分解
を阻害する。C action] When H2S, MM, and DMS are mixed in the malodorous gas,
H2S and MM%DMS are easily decomposed in this order, and the presence of easily decomposable gases such as H2S 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!Il+ 養の長期化をもたらしていた.
これに対し、本発明の生物脱臭装置では、各々の悪臭成
分を分解する微生物を担持する充填層を設けた処理塔を
3塔以上の複数個直列に設け、給気される悪臭ガスの上
流側から順に、H2S分解塔、MM分解塔及びDMS分
解塔をそれぞれ独立に設定しているため、運転初期から
各塔において安定な処理を行なうことができる。Therefore, in order to stably treat such malodorous gases using biological deodorization equipment, it is necessary to form a system that decomposes each malodorous substance in stages, but with conventional methods, this system cannot be formed. This is why it takes a long time! This resulted in prolonged Il+ feeding. In contrast, in the biological deodorizing apparatus of the present invention, three or more treatment towers each equipped with a packed bed carrying microorganisms that decompose each malodorous component are installed in series, and the treatment towers are arranged in series on the upstream side of the malodorous gas to be supplied. Since the H2S decomposition tower, the MM decomposition tower, and the DMS decomposition tower are set independently from each other in this order, stable treatment can be performed in each tower from the initial stage of operation.
また、各処理塔において、各々個別に各悪臭成分に対し
て該悪臭成分を分解できるように、負荷の調整、菌量の
増袖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。なお、H2S分解塔、MM分解塔及びDMS分解塔
はそれぞれの硫黄系臭気物質を主として分解すればよく
、例えば、MM分解塔の下部で残留H2Sを分解したり
、DMS分解塔の下部で残留MMを分解したり、またH
2S分解塔の上部で一部のMMを分解したり、MM分解
塔の上部で一部のDMSを分解してもよい。In addition, in each treatment tower, each malodorous component can be decomposed individually, and optimal operational management can be performed for adjusting the load, increasing the amount of bacteria, etc., so it is possible to handle sudden load changes. Appropriate measures can also be taken against such cases. Note that the H2S decomposition tower, MM decomposition tower, and DMS decomposition tower only need to mainly decompose their respective sulfur-based odorous substances. For example, residual H2S may be decomposed at the bottom of the MM decomposition tower, or residual MM may be decomposed at the bottom of the DMS decomposition tower. or disassemble H
Some MM may be decomposed in the upper part of the 2S decomposition tower, and some DMS may be decomposed in the upper part of the MM decomposition tower.
更に、各々の処理塔において処理する悪臭成分に応じて
、塔内の充填層に用いる微生物として、活性汚泥又はD
MSO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, depending on the malodorous components to be treated in each treatment tower, activated sludge or D
By selecting MSO-cultured bacteria, it is possible to suppress the amount of DMSO-cultured bacteria used and reduce processing costs.
また、洗浄水やpH調整のための薬品等も必要最低限に
即えることができる。Additionally, cleaning water, chemicals for pH adjustment, etc. can be kept to the minimum necessary level.
[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] Hereinafter, an example of the present invention will be described with reference to the drawings.
第1図は本発明の生物脱臭装置の一実施例を示す概略的
な縦断面図である。FIG. 1 is a schematic vertical sectional view showing an embodiment of the biological deodorizing device of the present invention.
本実施例の生物脱臭装置は、直列に接続された4個のガ
ス処理塔5A,5B,5C,5Dを備えている。各処理
塔5A〜5Dは、それぞれ底部に被処理ガスの給気管I
A,IB,IC、IDを備え、上部に処理ガスの排出管
2A、2B、2C、2Dを備えている。また、各々の内
部には、通気される被処理ガス中の悪臭成分を分解する
微生物を担持した充填層3A,3B、3C,3Dが設け
られると共に、各充填層3A,3B,3C,3Dに洗浄
水を散布する敗水管4A、4B、4C、4Dが各充填層
3A〜3Dの上方に設けられている。11、12、13
は各排出管と給気管とを連通ずる接続配管である。14
、l5、16、17は散水管4A〜4Dへ給水する給水
管である。The biological deodorization apparatus of this embodiment includes four gas treatment towers 5A, 5B, 5C, and 5D connected in series. Each of the treatment towers 5A to 5D has an air supply pipe I for the gas to be treated at the bottom.
A, IB, IC, and ID, and processing gas discharge pipes 2A, 2B, 2C, and 2D are provided at the upper part. In addition, packed layers 3A, 3B, 3C, and 3D carrying microorganisms that decompose malodorous components in the gas to be treated to be vented are provided inside each, and each packed layer 3A, 3B, 3C, and 3D is provided with Water drain pipes 4A, 4B, 4C, and 4D for spraying washing water are provided above each of the packed beds 3A to 3D. 11, 12, 13
is a connecting pipe that communicates each exhaust pipe with the air supply pipe. 14
, 15, 16, and 17 are water supply pipes that supply water to the water sprinkler pipes 4A to 4D.
各処理塔5A〜5Dには、それぞれ充填層3A〜3D内
に湿度センサー6A,6B,6C,6Dが設けられると
共に、充填層3A〜3Dの下方にpHセンサー7A,7
B,7C,7Dが設けられている。これらの湿度センサ
ー6A〜6D及びpHセンサー7A〜7Dの検出値は給
水制御装置8の制御回路(図示略)に入力されており、
この検出値に基いて各処理塔5A〜5Dの敗水管4A〜
4Dに水、アルカリ7夜、緩衝液等が供給されるように
構成されている。Each of the treatment towers 5A to 5D is provided with humidity sensors 6A, 6B, 6C, and 6D in the packed beds 3A to 3D, and pH sensors 7A and 7 are provided below the packed beds 3A to 3D.
B, 7C, and 7D are provided. The detected values of these humidity sensors 6A to 6D and pH sensors 7A to 7D are input to a control circuit (not shown) of the water supply control device 8.
Based on this detected value, the wastewater pipes 4A to 5D of each treatment tower 5A to 5D are
The structure is such that water, alkali, buffer solution, etc. are supplied to 4D.
本実施例において、各処理塔5A〜5Dは上流側からそ
れぞれH2S分解塔、MM分解塔、DMDS (二硫化
メチル)分解塔、DMS分解塔とされている。In this embodiment, the treatment towers 5A to 5D are, from the upstream side, an H2S decomposition tower, a MM decomposition tower, a DMDS (methyl disulfide) decomposition tower, and a DMS decomposition tower, respectively.
即ち、各処理塔5A〜5Dの充填層3A〜3Dにはビー
トが充填されており、処理塔5Aの充填1l3Aには活
性汚泥が担持され、処理塔5Bの充填層3Bには負荷量
に応じて活性汚泥又はDMSO培養菌が担持されている
。また、処理塔5Cの充填層3Cには負荷量に応じて活
性汚泥又はDMSO培養菌が担持され、処理塔5Dの充
填Fl3DにはDMSO培養菌が担持されている。That is, the packed beds 3A to 3D of each treatment tower 5A to 5D are filled with beets, the packed bed 113A of the treatment tower 5A is loaded with activated sludge, and the packed bed 3B of the treatment tower 5B is loaded with beets. Activated sludge or DMSO culture bacteria are supported. Furthermore, activated sludge or DMSO cultured bacteria is supported on the packed bed 3C of the treatment tower 5C depending on the load amount, and DMSO cultured bacteria is supported on the packed Fl3D of the treatment tower 5D.
なお、図示はされていないが、各処理塔5A〜5Dの各
充填層3A〜3Dの上方部には、散水管14〜17とは
別に、DMSO培養菌又は活性汚泥を添加するための供
給管が設けられており、各処理塔5A〜5Dの処理効率
の低下や変動に応じて、DMSO培養菌又は活性汚泥を
添加できるように構成されている。Although not shown, in the upper part of each packed bed 3A to 3D of each treatment tower 5A to 5D, in addition to the water spray pipes 14 to 17, there is a supply pipe for adding DMSO cultured bacteria or activated sludge. is provided, and is configured such that DMSO cultured bacteria or activated sludge can be added in accordance with a decrease or fluctuation in the processing efficiency of each of the processing towers 5A to 5D.
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IAよりH2S+
醒塔5Aに導入する。悪臭ガ・スはH2S分解塔5Aの
充填層3Aを通過する過程で活性汚泥Cより処理されて
、含有されるH2Sが酸化分解される。H2S分解塔5
Aの処理ガスは排出管2Aより排出され、接続配管11
、給気管IBよりMM分解塔5Bに導入されて充填層3
Bを通過するA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。MM分
解塔5Bの処理ガスは、排出管2Bより排出され、接続
配管12、給気管1cよりDMDS分解塔5Cに導入さ
れて、充填層3Cを通過する過程で活性汚泥又はDMS
O培養菌により処理されて、含有されるDMDSが酸化
分解される。DMDS分解塔5Cの処理ガスは、排出管
2Cより排出され、接続配管13、給気管IDよりDM
S分解塔5Dに導入されて、充填層3Dを通過する過程
でDMSO培養菌により処理されて、なお含有されるD
MSが酸化分解される。In order to deodorize malodorous gas using such a biological deodorizing device, first, the malodorous gas is converted into H2S+ from the air supply pipe IA.
Introduce it to the awakening tower 5A. The foul-smelling gas and gas are processed by the activated sludge C in the process of passing through the packed bed 3A of the H2S decomposition tower 5A, and the H2S contained therein is oxidized and decomposed. H2S decomposition tower 5
Processing gas A is discharged from the exhaust pipe 2A, and connected to the connecting pipe 11.
, introduced into the MM decomposition tower 5B from the air supply pipe IB and packed into the packed bed 3.
In the step A where it passes through B, it is treated with activated sludge or DMSO cultured bacteria, and the contained MM is oxidized and decomposed. The treated gas from the MM decomposition tower 5B is discharged from the discharge pipe 2B, introduced into the DMDS decomposition tower 5C through the connection pipe 12 and the air supply pipe 1c, and is converted into activated sludge or DMS in the process of passing through the packed bed 3C.
The DMDS contained therein is oxidized and decomposed by the O-cultured bacteria. The processed gas from the DMDS decomposition tower 5C is discharged from the discharge pipe 2C, and is then discharged from the DMDS decomposition column 5C through the connection pipe 13 and the air supply pipe ID.
D is introduced into the S decomposition tower 5D and treated with DMSO cultured bacteria in the process of passing through the packed bed 3D.
MS is oxidized and decomposed.
このようにして、脱臭処理されたガスは、排出管2Dよ
り系外へ排出される。In this way, the deodorized gas is discharged to the outside of the system through the discharge pipe 2D.
なお、H2 S,MM,DMDS%DMS等の硫黄系悪
臭戒分は、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。Note that sulfur-based malodorous substances such as H2S, MM, and DMDS%DMS are oxidized and decomposed into sulfate ions by activated sludge or DMSO culture bacteria.
従って、各充填層3A〜3D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
オンが生威し、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4A〜4D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。Therefore, in each of the packed beds 3A to 3D, sulfuric acid ions are present in an amount approximately equal to the sulfur-based substances removed by oxidative decomposition of malodorous components, and gradually accumulate when left undisturbed. Since this sulfate ion inhibits the biological reaction of microorganisms, it is necessary to spray washing water onto each packed bed from the water sprinkler pipes 4A to 4D to wash the sulfate ion out of the tower.
また、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 replenish water to maintain the activity of microorganisms.
即ち、充填層3A〜3Dを長繊維状ビートを堆積して形
成する場合、長繊維状ビートとしては、泥炭地から採取
したビートを冬期屋外に放置して凍結乾燥したものを例
えば目開き8mm程度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1 m’あたり乾燥ビート換算で100〜1 50
kg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(ビ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敗布するの
が望ましい。That is, when forming the filled layers 3A to 3D by depositing long-fiber beets, the long-fiber beets are beets collected from peatland, left outdoors in the winter, and freeze-dried, with a mesh size of about 8 mm, for example. It can be used after sifting through a sieve to remove short pieces. The packing density of the packed bed is 100 to 150 in terms of dry beets per 1 m' of the packed bed.
kg is preferred. The filling height of the packed bed is preferably about 1 to 1.5 m, and the water content of the packed bed (the percentage of water weight in the total of beet weight and water weight) is preferably 50 to 80% in order to maintain the activity of microorganisms. is preferably 60 to 70%. Therefore, in order to obtain such a moisture content, water, water-containing sludge, DMSO aqueous solution,
It is desirable to pour out a culture solution containing DMSO as a substrate through a water sprinkler pipe.
また、各充填層の微生物に好適なpHを維持するために
水、アルカリ液、緩衝液等を敗布するのが望ましい。Further, in order to maintain a pH suitable for microorganisms in each packed bed, it is desirable to dispose of water, alkaline solution, buffer solution, etc.
本実施例の装置においては、各処理塔5A〜5Dにおい
て、湿度センサー6A〜6D,pHセンサー7A〜7D
により湿度及びpHを検出し、充填層3A〜3Dのビー
ト含水率が好適範囲を下回った場合又は所定のpH範囲
外となった場合には、シーケンサ−8の指令により散水
管4A〜4Dより湿度調整のための水等、或いはpH調
整のための水、アルカリ液又は11 (E液等を散布す
る。In the apparatus of this embodiment, in each treatment tower 5A to 5D, humidity sensors 6A to 6D and pH sensors 7A to 7D are provided.
When the beet moisture content of the packed beds 3A to 3D falls below the preferred range or is outside the predetermined pH range, the humidity and pH are detected by the water sprinkler pipes 4A to 4D according to a command from the sequencer 8. Spray water for adjustment, or water, alkaline solution, or 11 (E solution) for pH adjustment.
なお、各処理塔5A〜5Dにおける好適pHは下記の通
りである。In addition, the suitable pH in each treatment tower 5A-5D is as follows.
充填層3A〜3Dに散布された水等は、各処理塔5A〜
5Dに設けられた排水管(図示せず)より排出される。The water etc. sprinkled on the packed beds 3A to 3D are sent to the respective treatment towers 5A to 3D.
It is discharged from a drain pipe (not shown) provided in 5D.
なお、第1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、DMDSはMM分
解塔の下流部分又はDMS分解塔の上流部分で分解する
ことができるので、独立してDMDS分解塔を設けなく
てもよく、そのため処理塔はH2S分解塔、MM分解塔
、DMS分解塔の3塔だけであっても良い。また、5塔
以上設け、それぞれのガスについて複数の処理塔を設定
するようにしても良い。The biological deodorizing device shown in FIG. 1 is an embodiment of the present invention, and the present invention is not limited to the illustrated example unless it exceeds the gist thereof. For example, DMDS can be decomposed in the downstream part of the MM decomposition tower or in the upstream part of the DMS decomposition tower, so there is no need to provide a separate DMDS decomposition tower, and therefore the treatment tower is a H2S decomposition tower, a MM decomposition tower, There may be only three DMS decomposition towers. Alternatively, five or more towers may be provided, and a plurality of processing towers may be set for each gas.
[発明の効果]
以上詳述した通り、本発明の生物脱臭装置は、H2S分
解塔、MM分解塔、DMS分解塔が、順次直列に接続さ
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
分を分解する分解塔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 detailed above, in the biological deodorizing apparatus of the present invention, the H2S decomposition tower, the MM decomposition tower, and the DMS decomposition tower are sequentially connected in series. Since the decomposition towers are arranged in series to decompose each component in the appropriate order, there is almost no acclimatization period, and stable deodorization can be performed from an early stage, greatly shortening the time required to start up the equipment. can do.
■ 分解する悪臭ガスに応じて各処理塔の運転管理を行
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 treatment tower can be managed according to the malodorous gas to be decomposed, it is possible to take appropriate treatment and respond well to sudden load fluctuations.
■ 各処理塔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 treatment tower, it is possible to minimize the amount of DMSO cultured bacteria used, and the processing cost can be reduced.
■ 洗浄水やpH調整のための薬品等の使用量も必要最
低限に抑えることができる。■ The amount of cleaning water and chemicals used for pH adjustment can be kept to the minimum necessary.
等の効果が奏される。Effects such as these are produced.
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 device of the present invention, even malodorous gases containing many kinds of sulfur-based malodorous substances can be almost completely deodorized extremely stably, efficiently, and at low cost.
第1図は本発明の生物脱臭装置の一実施例を示す概略的
な縦断面図である。
IA,IB,IC,ID・・・給気管、2A,2B,2
C、2D・・・排出管、3A,3B,3C,3D・・・
充填層、4A,4B,4C、4D・・・散水管、5A・
・・処理塔(H2S分解塔)、
5B・・・処理塔(MM分解塔)、
5C・・・処理塔(DMDS分解塔)、5D・・・処理
塔(DMS分解塔)。FIG. 1 is a schematic vertical sectional view showing an embodiment of the biological deodorizing device of the present invention. IA, IB, IC, ID...Air supply pipe, 2A, 2B, 2
C, 2D...Discharge pipe, 3A, 3B, 3C, 3D...
Filled bed, 4A, 4B, 4C, 4D... Water pipe, 5A.
... treatment tower (H2S decomposition tower), 5B ... treatment tower (MM decomposition tower), 5C ... treatment tower (DMDS decomposition tower), 5D ... treatment tower (DMS decomposition tower).
Claims (1)
処理ガスが導入される主に硫化水素を分解する硫化水素
分解塔と、 メチルメルカプタン分解微生物を担持した充填層を有し
、前記硫化水素分解塔の排出ガスが導入される主にメチ
ルメルカプタンを分解するメチルメルカプタン分解塔と
、 硫化メチル分解微生物を担持した充填層を有し、前記メ
チルメルカプタン分解塔の排出ガスが導入される主に硫
化メチルを分解する硫化メチル分解塔と、 を備えてなる生物脱臭装置。(1) A hydrogen sulfide decomposition tower having a packed bed supporting hydrogen sulfide-degrading microorganisms and mainly decomposing hydrogen sulfide into which the gas to be treated is introduced, and a packed bed supporting methyl mercaptan-degrading microorganisms; It has a methyl mercaptan decomposition tower that mainly decomposes methyl mercaptan, into which the exhaust gas from the hydrogen sulfide decomposition tower is introduced, and a packed bed supporting methyl sulfide decomposing microorganisms, and a methyl mercaptan decomposition tower into which the exhaust gas from the methyl mercaptan decomposition tower is introduced. A biological deodorizing device comprising: a methyl sulfide decomposition tower that decomposes methyl sulfide; and a methyl sulfide decomposition tower.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1298994A JPH03161019A (en) | 1989-11-17 | 1989-11-17 | Biological deodorizing apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1298994A JPH03161019A (en) | 1989-11-17 | 1989-11-17 | Biological deodorizing apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03161019A true JPH03161019A (en) | 1991-07-11 |
Family
ID=17866855
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1298994A Pending JPH03161019A (en) | 1989-11-17 | 1989-11-17 | Biological deodorizing apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03161019A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05115742A (en) * | 1991-09-18 | 1993-05-14 | Nippon Gesuidou Jigyodan | Biological deodorizing apparatus |
US5236677A (en) * | 1992-03-13 | 1993-08-17 | Grupo Cydsa S.A. De C.V. | Biological process for the elimination of sulphur compounds present in gas mixtures |
JP2007216185A (en) * | 2006-02-20 | 2007-08-30 | Takasago Thermal Eng Co Ltd | Malodor component removal method for malodor gas |
-
1989
- 1989-11-17 JP JP1298994A patent/JPH03161019A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05115742A (en) * | 1991-09-18 | 1993-05-14 | Nippon Gesuidou Jigyodan | Biological deodorizing apparatus |
US5236677A (en) * | 1992-03-13 | 1993-08-17 | Grupo Cydsa S.A. De C.V. | Biological process for the elimination of sulphur compounds present in gas mixtures |
JP2007216185A (en) * | 2006-02-20 | 2007-08-30 | Takasago Thermal Eng Co Ltd | Malodor component removal method for malodor gas |
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