JPS58131121A - Deodorizing method - Google Patents
Deodorizing methodInfo
- Publication number
- JPS58131121A JPS58131121A JP57014057A JP1405782A JPS58131121A JP S58131121 A JPS58131121 A JP S58131121A JP 57014057 A JP57014057 A JP 57014057A JP 1405782 A JP1405782 A JP 1405782A JP S58131121 A JPS58131121 A JP S58131121A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- treated
- deodorizing
- compost
- activated carbon
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Treating Waste Gases (AREA)
Abstract
Description
【発明の詳細な説明】
不発明はアンモニア、硫化水素などの臭気成分金倉んだ
悪臭ガスの処理において、熟成コンポストによる脱臭と
1[11の脱臭法(lI−組合せ、それぞれの特徴をい
かして全体として十分な脱臭を行、なう脱臭法に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION In the treatment of malodorous gas containing odorous components such as ammonia and hydrogen sulfide, deodorization using aged compost and 1[11 deodorization methods (lI-combination), making use of the characteristics of each, can be carried out as a whole. This article relates to a deodorizing method that performs sufficient deodorization.
従来下水汚泥コンポスト−8を発酵せしめた熟成コンポ
ストは脱臭効果金もっことが認識され、コンポストを脱
臭剤として用いた脱臭装置が提案されている。しかしこ
れらはすべてコンポストを用いた単独の脱臭装置により
、脱臭を行なったものであるため、数多い臭気成分の中
にはコンポストでは十分に脱臭できない成分がある点が
無視され、十分な脱臭効果が得られない場合が多かった
。It has been recognized that aged compost obtained by fermenting conventional sewage sludge compost-8 is highly effective in deodorizing, and a deodorizing device using compost as a deodorizing agent has been proposed. However, all of these were deodorized using a single deodorizing device using compost, so the fact that some of the many odor components cannot be sufficiently deodorized with compost is ignored, and sufficient deodorizing effects are not achieved. In many cases, it was not possible.
本発明の目的は、熟成コンポスト全開いた脱臭方法と他
の脱臭方法と全合理的に組合わせることによシ、全体と
して完全な脱臭法全提供することにある。The purpose of the present invention is to provide a completely complete deodorizing method by rationally combining the fully open deodorizing method for aged compost with other deodorizing methods.
以下不発明ft実施例に基づい説明する。The following description will be given based on an uninvented ft example.
下水汚泥、畜産廃棄物等を発酵処理せしめた熟成コンポ
ストは脱臭効果があることftgmされ、この熟成コン
ホストラ用いて悪臭ガスを脱臭することが提案されてい
る。Aged compost made by fermenting sewage sludge, livestock waste, etc. is known to have a deodorizing effect, and it has been proposed to use this aged compost to deodorize foul-smelling gases.
不発明は熟成コンポスト利用による脱臭法の改良で、次
表は熟成コンボス)k用いた脱臭実験の結果を示したも
のでめる。The invention was an improvement in the deodorizing method using aged compost, and the following table shows the results of a deodorizing experiment using aged compost.
上表の実験は熟成コンポストを100α高さに充填した
カラムに、多成分、複合臭気を流速0.5cII/Se
Cで通気させた場合の20日後における分析結果を示し
た。すなわち、熟成コンポストは極性の大きいアンモニ
ア、硫化水素およびメチルメルカプタンに対しては、か
なりの脱臭効果金もつものの、極性の小さい硫化メチル
、二硫化メチルに対してはめまり脱臭効果をもたないこ
とが判明した。In the experiment shown in the table above, multi-component, complex odors were applied to a column filled with aged compost to a height of 100α at a flow rate of 0.5 cII/Se.
The analysis results after 20 days when aerated at C were shown. In other words, aged compost has a considerable deodorizing effect on the highly polar ammonia, hydrogen sulfide, and methyl mercaptan, but it has no deodorizing effect on the less polar methyl sulfide and methyl disulfide. found.
そこで、熟成コンポストを脱臭剤として使用する場合に
は、この点を考慮して熟成コンポストで脱臭できない成
分に対しては、他の脱臭法を組合わせることによ勺、全
体として十分な脱臭効果を得ることが必要である。Therefore, when using aged compost as a deodorizing agent, consider this point and combine other deodorizing methods for components that cannot be deodorized with aged compost to achieve a sufficient overall deodorizing effect. It is necessary to obtain it.
不発明の一実施例を第1図によシ説明する。An embodiment of the invention will be explained with reference to FIG.
被処理ガス1Fi、プロワ−2を介して加湿器(又は除
湿器)3に導かれ、被処理ガスの湿度調整を行なう。こ
れは次段の脱臭槽4の熟成コンポストの含水率を所定値
に保つためのもので、被処理ガスの湿度が常に適正範囲
内に保たれている時は省略することができる。被処理ガ
ス中のアンモニア、硫化水素、メチルメルカプタンの大
部分、及び硫化メチル、二硫化メチルなどの一部分を熟
成コンポストによ勺除去した後、さらに後段の活性炭槽
5に導く。被処理ガスは箔性炭との接触により、大部分
の臭気成分が除去され、嗅覚で検知できる限界以下まで
脱臭される。The gas to be processed 1Fi is guided to a humidifier (or dehumidifier) 3 via a blower 2, and the humidity of the gas to be processed is adjusted. This is to maintain the moisture content of the aged compost in the next stage deodorizing tank 4 at a predetermined value, and can be omitted when the humidity of the gas to be treated is always maintained within an appropriate range. Most of the ammonia, hydrogen sulfide, methyl mercaptan, and a portion of methyl sulfide, methyl disulfide, etc. in the gas to be treated are removed by the aging compost, and then led to the activated carbon tank 5 in the subsequent stage. By contacting the gas to be treated with the foil charcoal, most of the odor components are removed, and the odor is deodorized to below the limit that can be detected by the sense of smell.
後段で活性炭を使用したことによって活性炭が極性の大
きいアンモニアなどに対しては、めまシ除去効果をもた
ないものの、極性の小さい二硫化メチルなどに対しては
大きい吸層容tをもたせることができる。すなわち、第
1図に示した方法によると、熟成コンポスト及び活性炭
のそれぞれの特徴をいかすことができ、全体として十分
な脱臭が行えるだけでなく、活性炭を単独で使用した場
合に比べて、活性炭の寿命をも延ばすことが可能となる
。Due to the use of activated carbon in the latter stage, activated carbon does not have the effect of removing blister against highly polar substances such as ammonia, but has a large absorption capacity t for substances with low polarity such as methyl disulfide. I can do it. In other words, according to the method shown in Figure 1, it is possible to take advantage of the respective characteristics of aged compost and activated carbon, and not only can sufficient deodorization be performed as a whole, but also the activated carbon It is also possible to extend the lifespan.
第2図は不発明による二番目の実施例を示す構成図であ
る。被処理ガス11をブロワ−12を介して次亜塩素酸
ソーダを用いた酸化洗浄塔13に導く。次亜塩素酸ソー
ダ溶液はポンプ141Cより洗浄塔の上部から散布され
、循環使用される。この時洗浄塔は単なるスプレー塔で
もラシヒリングなどを充填させた充填塔であってもよい
。また次亜塩素酸ソーダの濃度は、有効塩素濃度換算で
100〜s o o ppmに保つことが望ましく、こ
れ11、t−バー70−管15と貯槽からの供給管16
によって調節される。溶液のPHは、酸性側では酸化力
は強いものの溶液から塩素ガスなどの酸化性塩素が多量
に発生するのに対し、アルカリ側では酸化性塩素の発生
は少ないものの、特に二硫化メチルの酸化力が弱いこと
からPHは6〜8の中性域に保つことが望ましい。この
時、発生する少量の酸化性塩素や酸化されずに残有した
臭気成分は後段の熟成コンポスト層18によ)除去され
る。FIG. 2 is a block diagram showing a second embodiment according to the invention. The gas to be treated 11 is guided through a blower 12 to an oxidation cleaning tower 13 using sodium hypochlorite. The sodium hypochlorite solution is sprayed from the upper part of the washing tower by the pump 141C and is used for circulation. At this time, the washing tower may be a simple spray tower or a packed tower filled with Raschig rings or the like. In addition, it is desirable to maintain the concentration of sodium hypochlorite at 100 to soo ppm in terms of effective chlorine concentration.
adjusted by. When the pH of the solution is on the acidic side, the oxidizing power is strong, but a large amount of oxidizing chlorine such as chlorine gas is generated from the solution, whereas on the alkaline side, the oxidizing power of methyl disulfide is small, but the oxidizing power of methyl disulfide is small. Since the pH is weak, it is desirable to keep the pH in the neutral range of 6 to 8. At this time, a small amount of oxidizing chlorine generated and odor components remaining without being oxidized are removed by the subsequent aging compost layer 18).
熟成コンポストは、第1図のような脱臭槽に充填しても
よいが、通気速度をめまシ大きくすると熟成コンポスト
のもつ脱臭効果が弱くなるため、被処理ガス量が多い場
合には、第2図のように熟成コンホストラ積み付けた層
へ散気管17によ)被処理ガスを導く方法が望ましい。Aged compost may be filled into a deodorizing tank as shown in Figure 1, but if the aeration rate is increased rapidly, the deodorizing effect of aged compost will be weakened, so if the amount of gas to be treated is large, It is preferable to introduce the gas to be treated (through the diffuser pipe 17) into the stacked layer of the ripening combustor as shown in FIG.
熟成コンポスト層は、あまシ乾燥しすぎると脱臭効果が
低下するため、状況に応じて散水するなどの対策が必要
である。If the matured compost layer is allowed to dry out too much, its deodorizing effect will decrease, so measures such as sprinkling with water are required depending on the situation.
而して不発明による時は被処理ガス中に含有されるアン
モニア、メチルメルカプタン、硫化メチル、二硫化メチ
ルの大部分、及び硫化水素、トリメチルアミンなどのか
なうの部分を次亜塩素酸ソーダによシ酸化洗浄した後、
硫化水素等の残留臭気成分及び発生した酸化性塩素上熟
成コンポストにより除去できるため、全体として十分な
脱臭効果を得ることができるものである。In the case of non-invention, most of the ammonia, methyl mercaptan, methyl sulfide, methyl disulfide, hydrogen sulfide, trimethylamine, etc. contained in the gas to be treated are oxidized with sodium hypochlorite. After oxidation cleaning,
Since residual odor components such as hydrogen sulfide and the generated oxidizing chlorine can be removed by aging compost, a sufficient deodorizing effect can be obtained as a whole.
第1図及び第2図は本発明の脱臭法を実施する際に用い
る構成図である。
1.11・・・被処理ガス
2.12・・・ブロワ−
3・・・加湿器または除湿器
4・・・熟成コンポスト充填槽
5・・・活性炭槽
13・・・酸化吸収塔(次亜塩累酸ソーダ溶液J14・
・・ポンプ
15・・・オーバーフロー管
16・・・供給管
17・・・散気管
18・・・熟成コンポスト層
外1名 ゛FIG. 1 and FIG. 2 are block diagrams used when carrying out the deodorizing method of the present invention. 1.11... Gas to be treated 2.12... Blower 3... Humidifier or dehumidifier 4... Aged compost filling tank 5... Activated carbon tank 13... Oxidation absorption tower Sodium salt solution J14・
... Pump 15 ... Overflow pipe 16 ... Supply pipe 17 ... Diffusion pipe 18 ... 1 person outside the aging compost layer ゛
Claims (2)
臭剤として使用する脱臭法において、熟成コンポスト層
全通過後の被処理ガスを、さらに活性炭吸着層に導びき
、熟成コンポスト、活性炭の二段階で脱臭するようにな
したことt%徴とする脱臭法。(1) In a deodorizing method that uses the entire aged compost as a deodorizer, the gas to be treated that contains all the odor components is further guided to the activated carbon adsorption layer after passing through the aged compost layer, and the aged compost and activated carbon are separated. A deodorizing method that uses t% to deodorize in stages.
臭剤として使用する脱臭法において、熟成コンポスト層
の前段に、次亜塩素酸ソーダによる吸収塔を設け、被処
理ガスを次亜塩素酸ソーダと熟成コンポストの二段階に
て脱臭するようになしたこと金%徴とする脱臭法。(2) In the deodorizing method where all the gas to be treated containing odor components is used as a total deodorizing agent, an absorption tower using sodium hypochlorite is installed before the aging compost layer, and the gas to be treated is converted into sodium hypochlorite. A deodorizing method that is characterized by deodorizing in two stages of aging and composting.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57014057A JPS58131121A (en) | 1982-01-30 | 1982-01-30 | Deodorizing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57014057A JPS58131121A (en) | 1982-01-30 | 1982-01-30 | Deodorizing method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58131121A true JPS58131121A (en) | 1983-08-04 |
Family
ID=11850454
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57014057A Pending JPS58131121A (en) | 1982-01-30 | 1982-01-30 | Deodorizing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58131121A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60156529A (en) * | 1983-08-31 | 1985-08-16 | クレア テツヘ ビー・ヴイ | Biological treating method for gas and device therefor |
JPS61174922A (en) * | 1985-01-29 | 1986-08-06 | Daiwa House Kogyo Kk | Deodorizing apparatus |
JPS61212315A (en) * | 1985-03-15 | 1986-09-20 | Enzaimu Kk | Removing system for offensive odor by humus |
JP2006102646A (en) * | 2004-10-06 | 2006-04-20 | Kubota Corp | Deodorization apparatus and method |
JP2010082594A (en) * | 2008-10-02 | 2010-04-15 | National Agriculture & Food Research Organization | Environmental control method and device for organism deodorizing |
-
1982
- 1982-01-30 JP JP57014057A patent/JPS58131121A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60156529A (en) * | 1983-08-31 | 1985-08-16 | クレア テツヘ ビー・ヴイ | Biological treating method for gas and device therefor |
JPH0545285B2 (en) * | 1983-08-31 | 1993-07-08 | Kurea Tetsuhe Bv | |
JPS61174922A (en) * | 1985-01-29 | 1986-08-06 | Daiwa House Kogyo Kk | Deodorizing apparatus |
JPS61212315A (en) * | 1985-03-15 | 1986-09-20 | Enzaimu Kk | Removing system for offensive odor by humus |
JPH0456650B2 (en) * | 1985-03-15 | 1992-09-09 | Enzyme Kk | |
JP2006102646A (en) * | 2004-10-06 | 2006-04-20 | Kubota Corp | Deodorization apparatus and method |
JP4688465B2 (en) * | 2004-10-06 | 2011-05-25 | クボタ環境サ−ビス株式会社 | Deodorizing apparatus and deodorizing method |
JP2010082594A (en) * | 2008-10-02 | 2010-04-15 | National Agriculture & Food Research Organization | Environmental control method and device for organism deodorizing |
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