JPH04118023A - Method and device for deodorization using excrement soil of earthwork - Google Patents
Method and device for deodorization using excrement soil of earthworkInfo
- Publication number
- JPH04118023A JPH04118023A JP2201310A JP20131090A JPH04118023A JP H04118023 A JPH04118023 A JP H04118023A JP 2201310 A JP2201310 A JP 2201310A JP 20131090 A JP20131090 A JP 20131090A JP H04118023 A JPH04118023 A JP H04118023A
- Authority
- JP
- Japan
- Prior art keywords
- water
- alkaline
- gas
- layers
- wetted
- 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
- 238000000034 method Methods 0.000 title claims description 15
- 239000002689 soil Substances 0.000 title abstract description 4
- 238000004332 deodorization Methods 0.000 title description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 57
- 230000001877 deodorizing effect Effects 0.000 claims abstract description 25
- 239000000945 filler Substances 0.000 claims description 6
- 238000005070 sampling Methods 0.000 claims description 5
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- 238000001139 pH measurement Methods 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 230000007935 neutral effect Effects 0.000 abstract description 6
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 abstract description 3
- 239000004615 ingredient Substances 0.000 abstract 4
- 241000361919 Metaphire sieboldi Species 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 43
- 235000019645 odor Nutrition 0.000 description 16
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 238000001179 sorption measurement Methods 0.000 description 12
- 210000003608 fece Anatomy 0.000 description 11
- 239000010871 livestock manure Substances 0.000 description 10
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 8
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 8
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 8
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 8
- 229910052717 sulfur Inorganic materials 0.000 description 8
- 239000011593 sulfur Substances 0.000 description 8
- 229910021529 ammonia Inorganic materials 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000029087 digestion Effects 0.000 description 3
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 239000010800 human waste Substances 0.000 description 3
- 238000009736 wetting Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 230000001079 digestive effect Effects 0.000 description 1
- 102000038379 digestive enzymes Human genes 0.000 description 1
- 108091007734 digestive enzymes Proteins 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000010792 warming Methods 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1
本発明は、ごみ、し尿、下水等の清掃施設や、へい獣処
理場、化製場、畜産湯、飼料工場などから発生する臭気
成分の、みみずの糞土を使った脱臭方法及びその装置に
関するものである。[Detailed Description of the Invention] [Industrial Application Field 1] The present invention is a method for controlling odor components generated from cleaning facilities for garbage, human waste, sewage, etc., animal processing plants, chemical plants, livestock baths, feed factories, etc. , relates to a deodorizing method using worm excrement and an apparatus therefor.
[従来の技術]
みみずの糞土を用いたガスの脱臭方法は、特公昭54−
10553号公報及び特開平2−56216号公報に開
示されているように、同じ生物酸化方法としての活性汚
泥脱臭法、あるいは土壌脱臭法、又は活性炭吸着法に比
較しても有効な方法である。[Prior art] A method for deodorizing gas using worm excrement is disclosed in
As disclosed in JP-A No. 10553 and JP-A-2-56216, this method is more effective than other biological oxidation methods such as activated sludge deodorization, soil deodorization, or activated carbon adsorption.
しかし、みみずの糞土を使用した脱臭方法においては、
窒素系臭気ガス特にアンモニアは抜群の吸着・分解を示
すが、硫黄系の臭気ガスである硫化水素やメチルメルカ
プタンにおいては吸着・分解による脱臭効果が不十分で
ある。However, in the deodorizing method using worm excrement,
Nitrogen-based odorous gases, particularly ammonia, exhibit excellent adsorption and decomposition, but the deodorizing effect of sulfur-based odorous gases such as hydrogen sulfide and methyl mercaptan is insufficient.
[発明が解決しようとする課顕1
本発明は、上記従来技術では不十分である問題、c!5
.を解決し、硫黄系の臭気ガスの脱臭効果が高い方法及
び装置を提供しようとするものである。[Subject to be solved by the invention 1 The present invention solves problems for which the above-mentioned prior art is insufficient, c! 5
.. The purpose of the present invention is to provide a method and apparatus that are highly effective in deodorizing sulfur-based odor gases.
本発明の装置は、窒素系臭気の吸着分解には、従来の水
湿潤方式を採用し硫黄系の吸着にアルカリ性水を湿潤さ
せてpHを管理できる方式の装置とする。そのことによ
り、窒素系、硫黄系ガス臭気成分の除去効率の管理を向
上させることを目的とする。The apparatus of the present invention adopts the conventional water-wetting method for adsorption and decomposition of nitrogen-based odors, and uses alkaline water for adsorption of sulfur-based odors to control pH. The purpose of this is to improve the management of the removal efficiency of nitrogen-based and sulfur-based gas odor components.
[課題を解決するための手段]
本発明は上記課題を解決するために、みみずの糞土に充
填した複数の充填層を臭気ガスを含有する被処理ガスを
通過させて臭気ガスを除去する脱臭方法において、前記
被処理ガスを、水で湿潤した1層以上の前記充填層を通
過させた後、アルカリ性の水で湿潤した1層以上の前記
充填層を通過させることを特徴とするみみずの糞土を使
用した脱臭方法である。[Means for Solving the Problems] In order to solve the above problems, the present invention provides a deodorizing method in which a gas to be treated containing an odorous gas is passed through a plurality of packed beds filled with worm excrement to remove an odorous gas. , wherein the gas to be treated is passed through one or more of the packed beds moistened with water, and then passed through one or more of the packed beds moistened with alkaline water. This is the deodorizing method used.
上記方法を好適に実施することのできる本発明の装置は
、みみず糞土を脱臭剤とする生物酸化脱臭装置において
、充填剤の一部をアルカリ性に保持する充填層を設け、
この充填層には、充填剤温潤用の循環系統を付設する。The device of the present invention that can suitably carry out the above method is a biological oxidation deodorizing device that uses worm excrement as a deodorizer, and includes a packed layer that keeps a part of the filler alkaline.
This packed bed is equipped with a circulation system for warming and moistening the filler.
この循環系統はpH測定用採水口をそれぞれ設けた供給
管、戻水管から構成されている。This circulation system is composed of a supply pipe and a return pipe each provided with a water sampling port for pH measurement.
[作用]
湿潤みみず糞土による臭気ガスの吸着試験結果を第1表
に示す。試験は、窒素ガスに混入した臭気ガスの種類を
、アンモニア、硫化水素、メチルメルカプタンと変化さ
せたほかは同様とした。[Effect] Table 1 shows the results of an adsorption test of odor gas using wet worm excrement. The test was the same except that the type of odor gas mixed into the nitrogen gas was changed to ammonia, hydrogen sulfide, and methyl mercaptan.
アンモニアは完全に吸着・脱臭されているが、硫化水素
及びメチルメルカプタンは吸着・脱臭が不十分であった
。Ammonia was completely adsorbed and deodorized, but hydrogen sulfide and methyl mercaptan were not sufficiently adsorbed and deodorized.
各臭気ガスの常温における溶解度を第2表に示す。Table 2 shows the solubility of each odor gas at room temperature.
第1表及び第2表から、臭気ガスの脱臭効果の差異は臭
気ガスの水に対する溶解度に起因するものと考えられる
。From Tables 1 and 2, it is considered that the difference in the deodorizing effect of the odorous gases is due to the solubility of the odorous gases in water.
みみずの糞土の脱臭作用は、個々の糞粒が多孔質であっ
て臭気ガスを吸蔵・吸着する性質を持つ上に、みみずの
糞土中には種々の臭気ガスを分解する消化酵素やバクテ
リア等が生、ρ、して脱臭効果を発揮しており、これら
の消化酸素やバクテリアを活動させるには適当量の水分
の存在が必要で、臭気ガスがまず水に洛解し、それを微
生物が吸収し、酸化分解して無臭または臭気の少ない物
質に変えることが基本である。The deodorizing effect of worm excrement is due to the fact that individual feces are porous and have the property of storing and adsorbing odor gases, and worm excrement also contains digestive enzymes and bacteria that decompose various odor gases. In order to activate these digestive oxygen and bacteria, the presence of an appropriate amount of moisture is necessary, and the odor gas first dissolves into water, which is then absorbed by microorganisms. The basic idea is to oxidize and decompose it into odorless or low-odor substances.
したがって、硫黄系臭気ガスは水に対する溶解度が低い
ので、みみず糞土に捕捉され難く脱臭効果が低い。Therefore, since the sulfur-based odor gas has low solubility in water, it is difficult to be captured by worm excrement, and the deodorizing effect is low.
みみず糞土の湿潤に使用する水にアルカリ性とした水を
用いると、硫化水素等を化学的に中和することにより水
中への瀉解量を増大させることができ、それを微生物の
作用により酸化・分解し脱臭効果を向上させることがで
きる。If alkaline water is used to moisten worm manure, it is possible to chemically neutralize hydrogen sulfide and increase the amount of dissolved water into the water, which is then oxidized and oxidized by the action of microorganisms. It can be decomposed and the deodorizing effect can be improved.
第2図は吸着試験装置の説明図で、1は希釈ガスとして
の窒素ガスのボンベ、2は希釈ガスに試験する臭気ガス
を所定濃度に混入する試験ガス発生装置、3はバルブ、
4,5は吸着塔で、4には水温潤みみず糞土6を、5に
はアルカリ水温潤みみず糞±7を充填した。FIG. 2 is an explanatory diagram of the adsorption test apparatus, in which 1 is a cylinder of nitrogen gas as dilution gas, 2 is a test gas generator that mixes the odor gas to be tested into the dilution gas to a predetermined concentration, 3 is a valve,
4 and 5 were adsorption towers, 4 was filled with water temperature moist worm manure 6 and 5 was filled with alkaline water temperature moist worm manure ±7.
試験に用いたみみず糞土は、粒度3〜7mm含水率12
%、p )(5,5のもので、これを水で湿潤して含水
率を57%としたものを吸着塔4に、アルカリ水で湿潤
して含水率57%、pH8としたものを吸@塔5に充填
した。The worm manure used in the test had a particle size of 3 to 7 mm and a moisture content of 12.
%, p) (5.5), moistened with water to a moisture content of 57%, and moistened with alkaline water to a moisture content of 57% and pH 8, was placed in the adsorption tower 4. @Tower 5 was filled.
試験ガス発生装置により窒素・硫化水素混合ガスを発生
させ、ガスの圧力、流量、濃度を一定に保っで吸@塔4
.5に送込み、吸着性能を比軸した。試験結果を第3表
に示す。A test gas generator generates a nitrogen/hydrogen sulfide mixed gas, and the pressure, flow rate, and concentration of the gas are kept constant and the gas is pumped into the suction tower 4.
.. 5, and the adsorption performance was compared. The test results are shown in Table 3.
水湿潤の場合は50%の吸着率であったが、アルカリ水
湿潤の場合は100%吸着されその効果は明らかで、ア
ルカリ水湿潤の場合は吸着前のpHは8.0であったが
吸着後のpHは6.0に低下しており、硫化水素が化学
的に捕捉されていることを裏付けている。When wet with water, the adsorption rate was 50%, but when wet with alkaline water, it was 100% adsorbed, and the effect was clear. The subsequent pH dropped to 6.0, confirming that the hydrogen sulfide was chemically captured.
含窒素臭気ガスは、アルカリで分解されアンモニアを放
出する恐れがあるので、みみずの糞土を充填した複数の
充填層に被処理ガスを通過させる脱臭方法において、臭
気ガスを先ず水湿潤充填層を通過させて窒素系臭気ガス
の全部と硫黄系臭気ガスの一部を捕捉し、次いでアルカ
リ水湿潤充填層を通過させて硫黄系臭気ガスの残部を捕
捉することにより、脱臭効率を大幅に向上することがで
きる。Nitrogen-containing odorous gas may be decomposed by alkali and release ammonia, so in a deodorizing method in which the gas to be treated is passed through multiple packed beds filled with worm excrement, the odorous gas is first passed through a water-moist packed bed. The deodorizing efficiency is greatly improved by trapping all of the nitrogen-based odorous gases and a part of the sulfur-based odorous gases, and then passing through an alkaline water wet packed bed to capture the remainder of the sulfur-based odorous gases. I can do it.
水湿潤充填層及びアルカリ水湿潤充填層のそれぞれの暦
数は、臭気ガス種類及び量等を勘案して適宜決定される
。The respective calendar numbers of the water wet packed bed and the alkaline water wet packed bed are appropriately determined in consideration of the type and amount of the odor gas.
充填層における含水率は30〜60%程度が好適で、湿
潤水をアルカリ性とするためには、炭酸ソーダ、苛性ソ
ーダ等が使用可能で、アルカリ水湿潤充填層のpHは、
硫黄系臭電ガスの含有量等を勘案して8.0〜10.0
程度とされる。The moisture content in the packed bed is preferably about 30 to 60%, and in order to make the wetting water alkaline, soda carbonate, caustic soda, etc. can be used, and the pH of the alkaline water wet packed bed is:
8.0 to 10.0, taking into account the content of sulfur-based odor gas, etc.
It is considered to be a degree.
f実施例]
実施例1
200人用し尿性化水槽の消化槽の上部に、概要図を第
1図に示した脱臭装置を設けた。図において8は消化槽
、9はバルブ、10は吸気ブロワ、11.12.13は
みみず糞土充填層、14は脱臭ガス排気口である。f Example] Example 1 A deodorizing device, a schematic diagram of which is shown in FIG. 1, was installed above the digestion tank of a human waste water tank for 200 people. In the figure, 8 is a digestion tank, 9 is a valve, 10 is an intake blower, 11, 12, 13 is a worm manure filling layer, and 14 is a deodorizing gas exhaust port.
充填層はそれぞれ縦50cmX横50cmX厚さ]Oc
m、容積はそれぞれ259で、吸気ブロワの能力は3r
n’/min、90mmAqである。Each filling layer is 50cm long x 50cm wide x thick]Oc
m, the volume is 259, and the capacity of the intake blower is 3r.
n'/min, 90 mmAq.
図示の矢印は被処理ガスの流れを示す。The illustrated arrows indicate the flow of the gas to be processed.
粒径3〜7mm、含水率12%、p H5,5のみみず
糞土を水で湿潤して含水率57%とし、充填層11.1
2.13に用いた場合と、充填層12.13は上記の水
湿潤充填層とし、充填層11は上記のみみず糞土を炭酸
ソーダを用いて、含水率57%、pH9,0のアルカリ
性にした場合について、吸気と排気のアンモニアと硫化
水素を検知管方法により1回/日で3回測定した。−り
定結果を第4表に示す。被処理ガスを、水湿潤充填層を
通過させ得た後アルカリ水湿潤を通過させることにより
、完全に脱臭することができた。Worm manure with a particle size of 3 to 7 mm, a water content of 12%, and a pH of 5.5 was moistened with water to a water content of 57%, and a packed bed of 11.1
2.13, the packed bed 12.13 was the above-mentioned water-moist packed bed, and the packed bed 11 was made of the above-mentioned worm manure using soda carbonate to make it alkaline with a water content of 57% and a pH of 9.0. In this case, ammonia and hydrogen sulfide in the intake and exhaust air were measured three times once per day by the detector tube method. Table 4 shows the determination results. The gas to be treated could be completely deodorized by passing it through a water moist packed bed and then passing it through an alkaline water moist layer.
実施例2
第3図は生物脱臭塔のアルカリ層の制御系統を詳細に示
した例である。中性層41.42は水湿潤部、アルカリ
層43はアルカリ水湿潤部である。下方より臭気31を
押し込み中性層41゜42を経たガス32はアルカリ層
43を通って上部より排気33として排風する。 中性
層41.42には水34を散水管35を介して散水する
。Example 2 FIG. 3 is an example showing in detail the control system for the alkaline layer of a biological deodorizing tower. The neutral layers 41 and 42 are water-wet parts, and the alkaline layer 43 is an alkaline water-wet part. The gas 32 that pushes in the odor 31 from below and passes through the neutral layers 41 and 42 passes through the alkaline layer 43 and is discharged from the upper part as exhaust gas 33. Water 34 is sprinkled onto the neutral layers 41 and 42 through a sprinkler pipe 35.
余剰から排水される水は排水管36から排水される。Water drained from the surplus is drained through drain pipe 36.
アルカリ水湿潤部43の機構を説明する。The mechanism of the alkaline water wetting section 43 will be explained.
アルカリ層43は上部に充填剤投入部21を備λ、下部
に充填剤取出部23を備えている。アルカリ水散水管2
2はアルカリ層の上部がら散水する。この散水はポンプ
24によって供給管25を介して供給される。戻水管2
4はアルカリ層43の余剰水をタンク28へ戻す。供給
管25及び戻水管24にはそれぞれpH測定用のサンプ
リング管26を設けである。また戻り管24がタンク2
8に入る部分にフィルタ27が設けられている。The alkaline layer 43 has a filler input section 21 at the top and a filler takeout section 23 at the bottom. Alkaline water sprinkler pipe 2
2. Sprinkle water from the top of the alkaline layer. This watering is supplied by a pump 24 via a supply pipe 25. Return pipe 2
4 returns surplus water in the alkaline layer 43 to the tank 28. The supply pipe 25 and the return pipe 24 are each provided with a sampling pipe 26 for pH measurement. Also, the return pipe 24 is connected to the tank 2.
A filter 27 is provided at the portion where the filter 8 enters.
アルカリ水供給ポンプ29を運転し、上部散水管22よ
り散水する。戻水管24に取付けたサンブリンク管26
より採水しpHを測定する。The alkaline water supply pump 29 is operated and water is sprinkled from the upper water sprinkling pipe 22. Sunblink pipe 26 attached to return pipe 24
Sample water and measure pH.
また、タンク内液のpHは運転時、供給管25のサンプ
リング部26より採水し、タンク内液のアルカリ度を測
定し、必要に応じpHを調整しておく。アルカリ剤は生
物に無毒なものであれば何でもよく、緩衝剤として、リ
ン酸−アンモニウム等を添加すれば栄養剤ともなってよ
い。Furthermore, during operation, water is sampled from the sampling section 26 of the supply pipe 25, the alkalinity of the tank liquid is measured, and the pH is adjusted as necessary. Any alkaline agent may be used as long as it is non-toxic to living things, and it may also serve as a nutrient by adding ammonium phosphate or the like as a buffer.
p+の範囲は強アルカリ性は微生物の生育に適当ではな
く、通常の8〜9が望ましい。この範囲であれば微生物
の活性に問題はない。pHが7以下になると効率が落ち
ることがある。Strong alkalinity is not suitable for the growth of microorganisms, and the normal p+ range of 8 to 9 is desirable. Within this range, there is no problem with the activity of microorganisms. When the pH is lower than 7, the efficiency may decrease.
pi−1測定器は定置型でもよく、またはポータプル型
の簡易pH計で必要時に測定することでもよい。The pi-1 measuring device may be a stationary type, or a portable pH meter may be used to measure when necessary.
[発明の効果]
本発明により、し尿処理装置等から発生するアンモニア
系はもちろん、硫化水素やメチルメルカプタンなどのガ
スの脱臭を大幅に向上させることができた。[Effects of the Invention] According to the present invention, it has been possible to significantly improve the deodorization of gases such as hydrogen sulfide and methyl mercaptan as well as ammonia gases generated from human waste treatment equipment and the like.
第1図は実施例に用いた脱臭装置の概要図、第2図は吸
着試験装置の説明図、第3図は実施例の断面側面図であ
る。
1・・・窒素ガスボンベ 2・・・試験ガス発生装置
3.9・・・バルブ 4.5・・・吸着塔6・・
・水温潤みみず糞土
7・・・アルカリ水温潤みみず糞土
8・・・消化槽 10・・・吸気ブロワ11
.12.13・・・みみず糞土充填層14・・・脱臭ガ
ス排気口
22・・・アルカリ水撒水管
24・・・戻水管 25・・・供給管26・・
・サンプリング管FIG. 1 is a schematic diagram of the deodorizing device used in the example, FIG. 2 is an explanatory diagram of the adsorption test device, and FIG. 3 is a cross-sectional side view of the example. 1...Nitrogen gas cylinder 2...Test gas generator 3.9...Valve 4.5...Adsorption tower 6...
・Water temperature moist worm manure 7...Alkaline water temperature moist worm manure 8...Digestion tank 10...Intake blower 11
.. 12.13... Worm manure packed bed 14... Deodorizing gas exhaust port 22... Alkaline water sprinkling pipe 24... Return pipe 25... Supply pipe 26...
・Sampling tube
Claims (1)
含有する被処理ガスを通過させて臭気ガスを除去する脱
臭方法において、前記被処理ガスを、水で湿潤した1層
以上の前記充填層を通過させた後、アルカリ性の水で湿
潤した1層以上の前記充填層を通過させることを特徴と
するみみずの糞土を使用した脱臭方法。 2 みみず糞土を脱臭剤とする生物酸化脱臭装置におい
て、充填剤の一部をアルカリ性に保持する充填層を設け
、該充填層には、pH測定用採水口をそれぞれ設けた供
給管、戻水管からなる充填剤湿潤用の循環系統を付設し
たことを特徴とするみみずの糞土を使用した脱臭装置。[Claims] 1. A deodorizing method in which a gas to be treated containing an odorous gas is passed through a plurality of packed beds filled with worm excrement to remove the odorous gas, wherein the gas to be treated is moistened with water. A deodorizing method using worm excrement, which comprises passing through one or more of the packed beds and then passing through one or more of the packed beds moistened with alkaline water. 2. In a biological oxidation deodorizing device that uses worm excrement as a deodorizing agent, a packed layer that keeps a part of the filler alkaline is provided, and the packed layer is connected to a supply pipe and a return pipe each having a water sampling port for pH measurement. A deodorizing device using worm excrement, characterized in that it is equipped with a circulation system for moistening the filler.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14735090 | 1990-06-07 | ||
JP2-147350 | 1990-06-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04118023A true JPH04118023A (en) | 1992-04-20 |
Family
ID=15428200
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2201310A Pending JPH04118023A (en) | 1990-06-07 | 1990-07-31 | Method and device for deodorization using excrement soil of earthwork |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04118023A (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2999359A (en) * | 1956-04-25 | 1961-09-12 | Rolls Royce | Combustion equipment of gas-turbine engines |
JPS49124415A (en) * | 1972-09-07 | 1974-11-28 | ||
JPH05196232A (en) * | 1991-08-01 | 1993-08-06 | General Electric Co <Ge> | Back fire-resistant fuel staging type premixed combustion apparatus |
JPH0828871A (en) * | 1994-07-20 | 1996-02-02 | Hitachi Ltd | Gas turbine combustion device |
JP2007508515A (en) * | 2003-10-13 | 2007-04-05 | シーメンス アクチエンゲゼルシヤフト | Fuel combustion method and apparatus |
JP2010516995A (en) * | 2007-01-29 | 2010-05-20 | シーメンス アクチエンゲゼルシヤフト | Combustor in gas turbine |
JP2012149868A (en) * | 2011-01-19 | 2012-08-09 | General Electric Co <Ge> | System for flow control in multi-tube fuel nozzle |
-
1990
- 1990-07-31 JP JP2201310A patent/JPH04118023A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2999359A (en) * | 1956-04-25 | 1961-09-12 | Rolls Royce | Combustion equipment of gas-turbine engines |
JPS49124415A (en) * | 1972-09-07 | 1974-11-28 | ||
JPH05196232A (en) * | 1991-08-01 | 1993-08-06 | General Electric Co <Ge> | Back fire-resistant fuel staging type premixed combustion apparatus |
JPH0828871A (en) * | 1994-07-20 | 1996-02-02 | Hitachi Ltd | Gas turbine combustion device |
JP2007508515A (en) * | 2003-10-13 | 2007-04-05 | シーメンス アクチエンゲゼルシヤフト | Fuel combustion method and apparatus |
JP2010516995A (en) * | 2007-01-29 | 2010-05-20 | シーメンス アクチエンゲゼルシヤフト | Combustor in gas turbine |
JP2012149868A (en) * | 2011-01-19 | 2012-08-09 | General Electric Co <Ge> | System for flow control in multi-tube fuel nozzle |
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