JP3202564B2 - Deodorizing device - Google Patents
Deodorizing deviceInfo
- Publication number
- JP3202564B2 JP3202564B2 JP30502695A JP30502695A JP3202564B2 JP 3202564 B2 JP3202564 B2 JP 3202564B2 JP 30502695 A JP30502695 A JP 30502695A JP 30502695 A JP30502695 A JP 30502695A JP 3202564 B2 JP3202564 B2 JP 3202564B2
- Authority
- JP
- Japan
- Prior art keywords
- humus
- filler
- pumice
- silica component
- mainly composed
- 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 - Fee Related
Links
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/01—Deodorant compositions
- A61L9/014—Deodorant compositions containing sorbent material, e.g. activated carbon
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/52—Hydrogen sulfide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/58—Ammonia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/84—Biological processes
- B01D53/85—Biological processes with gas-solid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Materials Engineering (AREA)
- Epidemiology (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- Molecular Biology (AREA)
- Treating Waste Gases (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、脱臭装置に関する
もので、詳しくは塩基性臭気成分であるアンモニアのみ
ならず酸性臭気成分である硫化水素も効果的に除去する
脱臭装置に関するものである。The present invention relates to a deodorizing apparatus, and more particularly to a deodorizing apparatus for effectively removing not only ammonia as a basic odor component but also hydrogen sulfide as an acidic odor component.
【0002】[0002]
【従来の技術】従来、腐植物を用いた臭気ガスの脱臭方
法としては、例えば特開平2-290224号公報に記載の技術
が知られている。同公報には、フミン酸、フルボ酸等の
腐植化促進剤を使用して、有機物を含む液中の有機物を
腐植化させ、この液体に臭気ガスを接触させることによ
り脱臭する方法が開示されている。2. Description of the Related Art Conventionally, as a method for deodorizing odorous gas using humus, for example, a technique described in Japanese Patent Application Laid-Open No. 2-290224 is known. The publication discloses a method of dehumidifying an organic substance in a liquid containing the organic substance by using a humic acid accelerating agent such as humic acid or fulvic acid, and contacting the liquid with an odor gas to deodorize the liquid. I have.
【0003】しかし、この従来法では、塩基性臭気成分
であるアンモニアに対しては除去率100%の結果を示し
ているが、酸性臭気成分である硫化水素に対しては完全
に除去されないという問題点がある。硫化水素は少量で
も有毒で腐った卵のような臭気を持つので、完全に除去
されることが望まれている。However, this conventional method shows a result of 100% removal of ammonia as a basic odor component, but has a problem that hydrogen sulfide as an acidic odor component is not completely removed. There is a point. Since even small amounts of hydrogen sulfide have a toxic and rotten egg-like odor, it is desired that they be completely removed.
【0004】[0004]
【発明が解決しようとする課題】そこで、本発明の課題
は、従来法では完全に除去し得なかった酸性臭気成分で
ある硫化水素を効果的に除去する脱臭装置を提供するこ
とにある。Accordingly, an object of the present invention is to provide a deodorizing apparatus for effectively removing hydrogen sulfide, which is an acidic odor component, which cannot be completely removed by the conventional method.
【0005】[0005]
【0006】[0006]
【課題を解決するための手段】 上記課題を解決する本発
明にかかる脱臭装置 は脱臭塔本体内に多段に設けられた
充填材の上方に位置する少なくとも一段の充填材が腐植
物の溶出液を溶出性シリカ成分を有する軽石粉末に含浸
させた固形化濾過材であり、下方に位置する少なくとも
一段の充填材が腐植物を主体とする土壌成形体又は腐植
物の溶出液を溶出性シリカ成分を含有する軽石粉末に含
浸させた固形化濾過材から選ばれる少なくとも1種であ
ることを特徴とする。本発明に用いられる充填材には、
粉末又は粒状の活性炭を含有することも好ましい。 In order to achieve the object of the present onset to solve the above problems
The deodorizing apparatus according to the present invention is a solidification filtration system in which at least one filler positioned above a plurality of fillers provided in a deodorization tower main body is impregnated with a humus eluate into a pumice powder having a leachable silica component. At least one filler positioned below is selected from solidified filter media impregnated with a humus-based soil compact or a humus eluate in a pumice powder containing an eluting silica component. It is characterized by at least one kind. The filler used in the present invention includes:
It is also preferred to contain powdered or granular activated carbon.
【0007】本発明の好ましい態様としては、下方に位
置する少なくとも一段の充填材の周辺に充填材の液溜り
部を有することである。In a preferred aspect of the present invention, a liquid reservoir for the filler is provided around at least one lower stage of the filler.
【0008】他の好ましい態様としては、内部に、腐植
物を主体とする土壌粉体、粒体若しくは成形体又は溶出
性シリカ成分を含有する軽石の少なくとも1種を充填し
てなる反応槽を設け、前記循環槽内の液を導入して所定
時間反応後、前記循環槽に返送することである。In another preferred embodiment, a reaction tank is provided inside which is filled with at least one kind of soil powder, granules or compacts mainly composed of humus, or pumice containing an eluting silica component. After introducing the liquid in the circulation tank and reacting for a predetermined time, the liquid is returned to the circulation tank.
【0009】[0009]
【発明の実施の形態】本発明に用いられる腐植物を主体
とする土壌成形体は、腐植土壌、必要により他の無機材
(例えばマグネシウム)、バインダー又は溶出制限剤等
を混合して成形したペレットであり、ペレットの形状は
円柱、角柱、円盤等のいずれであってもよい。腐植物は
有用微生物の胞子あるいは有用微生物が多数生息してい
るものが好ましく用いられるが、溶出性シリカ成分を含
有していると、より好ましい。また、溶出性シリカ成分
を含有する軽石は、粘土鉱物や火山性の岩石で水に溶出
することができるシリカ成分を含有しているものが用い
られる。BEST MODE FOR CARRYING OUT THE INVENTION A soil compact mainly composed of humus used in the present invention is a pellet formed by mixing humus soil, if necessary, other inorganic materials (eg, magnesium), a binder or an elution-controlling agent, and the like. The shape of the pellet may be any of a cylinder, a prism, a disk, and the like. As the humus, spores of useful microorganisms or those in which a large number of useful microorganisms inhabit are preferably used, and it is more preferable that the humus contains an elutable silica component. As the pumice containing an eluting silica component, a clay mineral or a volcanic rock containing a silica component that can be eluted into water is used.
【0010】さらに固形化濾過材は、溶出性シリカ成分
を含有する軽石の微粉末を造粒し、腐植物を主体とする
土壌成形体から抽出した低分子のコロイド溶出液を含浸
させ、乾燥を数回繰り返すことにより造ることができ
る。[0010] Further, the solidified filter medium is formed by granulating pumice fine powder containing an eluting silica component, impregnating with a low-molecular colloid eluate extracted from a soil compact mainly composed of humus, and drying. It can be made by repeating several times.
【0011】本発明に用いられる充填材には、活性炭を
含有することができる。本発明では溶出性シリカ成分を
含有する軽石と粒状の活性炭を混合使用して充填材とし
たり、あるいは腐植物を主体とする土壌成形体中に粉末
又は粒状の活性炭を混合し、ペレット状にして用いた
り、また固形化濾過材中に粉末又は粒状の活性炭を混合
して造粒することができる。The filler used in the present invention can contain activated carbon. In the present invention, a filler is prepared by mixing pumice containing an eluting silica component and granular activated carbon, or a powder or granular activated carbon is mixed in a soil compact mainly composed of humus, and pelletized. It can be used or granulated by mixing powdered or granular activated carbon into a solidified filter medium.
【0012】本発明では充填材を脱臭塔本体内に多段に
設けるが、段数は製造コストや処理効率の面から二段が
好ましい。上段に軽石を用いる場合には、下段には腐植
物を主体とする土壌成形体や固形化濾過材を用いること
ができる。塔内で臭気ガスを軽石に接触させる前に腐植
物を主体とする土壌成形体に接触させることにより、ア
ンモニアの様な塩基性臭気成分以外に硫化水素の様な酸
性臭気成分の除去に効果を発揮するからである。In the present invention, the packing material is provided in multiple stages in the deodorization tower main body, but the number of stages is preferably two from the viewpoint of production cost and processing efficiency. When pumice is used in the upper stage, a soil compact mainly composed of humus or a solidified filter material can be used in the lower stage. By contacting the odorous gas with the soil compact mainly composed of humus before contacting the odorous gas with pumice in the tower, it is effective in removing acidic odorous components such as hydrogen sulfide in addition to basic odorous components such as ammonia. Because it demonstrates.
【0013】また上段に固形化濾過材を用いる場合に
は、下段には腐植物を主体とする土壌成形体を用いるこ
とができる。When a solidified filter material is used in the upper stage, a soil compact mainly composed of humus can be used in the lower stage.
【0014】本発明においては、上記の腐植物を主体と
する土壌成形体と固形化濾過材は混合して使用すること
ができる。In the present invention, the above-mentioned soil compact mainly composed of humus and a solidified filter material can be used as a mixture.
【0015】次に本発明の実施の形態を図面に基づき説
明する。図1は本発明の一実施形態を示す概略縦断面図
である。図1において、1は脱臭塔本体であり、円筒、
角筒等のいずれであってもよく、塔本体1の下方には、
臭気ガスの導入口2が設けられ、上方(側面上方を含
む)には処理済ガスの排出口3が設けられている。4
は、上段の充填材であり、支持板5上に軽石や固形化濾
過材の様な充填材4が充填されている。充填の高さは1
0〜50mm程度が好ましい。支持板5は網状体又はパ
ンチングメタルを用いることができる。Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a schematic longitudinal sectional view showing one embodiment of the present invention. In FIG. 1, reference numeral 1 denotes a deodorization tower main body,
Any of a square tube and the like may be used.
An odor gas inlet 2 is provided, and a treated gas outlet 3 is provided above (including the upper side). 4
Is a filler in the upper stage, and the filler 4 such as pumice or solidified filter material is filled on the support plate 5. Fill height is 1
It is preferably about 0 to 50 mm. The support plate 5 can be made of a mesh or punched metal.
【0016】6は下段の充填材であり、支持板7上に腐
植物を主体とする土壌形成体のような充填材6が充填さ
れている。支持板7は網状体やパンチングメタルを用い
ることができる。上段及び下段の充填材4、6として溶
出性の高い充填材を用いる場合には、図1の支持板5、
7に代えて図2のような構造を採用することも好まし
い。Reference numeral 6 denotes a lower filler, which is filled with a filler 6 such as a soil forming body mainly composed of humus on a support plate 7. The support plate 7 can use a net-like body or a punched metal. When a filler having a high elution property is used as the upper and lower fillers 4 and 6, the support plate 5 in FIG.
It is also preferable to adopt a structure as shown in FIG.
【0017】図2において、70は液溜り部であり、液
溜り部70内に充填材6が充填されている。71は臭気
ガスを通過させる複数の上昇管であり、該上昇管71に
は泡鐘72が設けられている。泡鐘72は上部が密封さ
れ、下方から進入した臭気ガスを側方の透孔73から排
出し、液溜り部70に入れる構造を有している。また7
2は上昇管71に間隙74を介して設けられる蓋体でも
あり、上昇管71に進入した臭気は該間隙74から液溜
り部70に入る構造を有している。75は下降管であ
り、液溜り部70から流出した液が下方に送られる。[0017] In FIG 2, 70 is a liquid reservoir, the filler 6 is filled in the liquid reservoir portion 70. Reference numeral 71 denotes a plurality of risers through which the odor gas passes, and the riser 71 is provided with a bubble bell 72. The bubble bell 72 has a structure in which the upper portion is sealed, and the odor gas that has entered from below is discharged from the side through-hole 73 and is introduced into the liquid reservoir 70. 7
2 is <br/> the riser 71 even lid provided with a gap 74, odors entering the riser 71 has a structure into the liquid reservoir portion 70 from the gap 74. Reference numeral 75 denotes a downcomer, through which the liquid flowing out of the liquid reservoir 70 is sent downward.
【0018】8は上段の充填材4の上方に設けられる散
水部であり、9は下段の充填材6の上方に設けられる散
水部であり、各々スプレーノズル81、91が複数設けられ
ている。10は脱臭塔本体1の下部に設けられた循環槽で
あり、該槽内の循環液はポンプ11を介して前記散水部
8、9に各々送液される。12は必要により設けられる反
応槽であり、内部には溶出性シリカ成分を含有する軽
石、腐植物を主体とする土壌形成体を充填した充填部13
が設けられ、その下方に散気管14が設けられ、前記循環
液はポンプ15を介して反応槽12に送られ、臭気成分の分
解・資化等が行われる。Reference numeral 8 denotes a water spraying section provided above the upper filler 4, and reference numeral 9 denotes a water spraying section provided above the lower filler 6, and a plurality of spray nozzles 81 and 91 are provided respectively. Reference numeral 10 denotes a circulation tank provided at a lower portion of the deodorization tower main body 1, and circulating liquid in the tank is sent to the water sprinkling units 8 and 9 via a pump 11. Reference numeral 12 denotes a reaction tank provided as needed, and a pumice containing an eluting silica component therein, a filling section 13 filled with a soil former mainly composed of humus.
The circulating liquid is sent to a reaction tank 12 via a pump 15 to decompose and assimilate odor components.
【0019】本発明では、臭気成分は気液接触により液
体側に移行した後、分解・資化等が循環系でかなり進行
するので、上記の反応槽12は必ずしも必要ではないが、
臭気ガスの負荷が高い場合には反応槽12を設けることに
より、効率的に長期にわたる運転が可能になる。In the present invention, the above-mentioned reaction tank 12 is not always necessary, since the odor component is transferred to the liquid side by gas-liquid contact, and then decomposition and assimilation proceed considerably in the circulation system.
When the load of the odor gas is high, the provision of the reaction tank 12 enables efficient long-term operation.
【0020】なお、臭気成分の分解・資化等を促進する
上では、循環槽10内に溶出性シリカ成分を有する軽石や
腐植物を主体とする土壌成形体を金網のカゴ等に充填
し、浸漬させておくことも好ましいことである。In order to promote the decomposition and assimilation of odorous components, a soil compact mainly composed of pumice or humus having an eluting silica component is filled in a circulation tank 10 in a basket of wire mesh. It is also preferable to keep it immersed.
【0021】[0021]
【実施例】以下、本発明の一実施例について説明する。An embodiment of the present invention will be described below.
【0022】実施例1 図1に示す脱臭装置を用いて、以下の条件下で実験を行
った。充填材としては、上段の充填材4に、溶出性シリ
カ成分を含有する軽石を用い、下段の充填材6に、腐植
物を主体とする土壌成形体(4mmφ×10mmLのペレッ
ト)を用いた。また支持板5、7としては網状体を用い
た。その他の実験条件は表1に示す通りである。Example 1 An experiment was conducted using the deodorizing apparatus shown in FIG. 1 under the following conditions. As the filler, a pumice containing an eluting silica component was used as the filler 4 in the upper stage, and a soil compact (4 mmφ × 10 mmL pellet) mainly composed of humus was used as the filler 6 in the lower stage. Further, nets were used as the support plates 5 and 7. Other experimental conditions are as shown in Table 1.
【0023】[0023]
【表1】 [Table 1]
【0024】表1に示す量の臭気ガスを導入口2より導
入し、塔本体1内を上向流で循環液と接触させ、処理済
ガスは排出口3より排出した。The amount of odorous gas shown in Table 1 was introduced from the inlet 2, and the inside of the tower body 1 was brought into contact with the circulating liquid in an upward flow, and the treated gas was discharged from the outlet 3.
【0025】臭気ガスは塩基性臭気成分であるアンモニ
アと酸性臭気成分である硫化水素について、臭気ガスの
導入口2と処理済ガスの排出口3における濃度をJIS
法により測定した。その結果を表2に示す。The odor gas is determined by measuring the concentrations of ammonia (basic odor component) and hydrogen sulfide (acid odor component) at the odor gas inlet 2 and the treated gas outlet 3 according to JIS.
It was measured by the method. Table 2 shows the results.
【0026】実施例2 実施例1において、上段の充填材4を固形化濾過材に代
え、下段の充填材6を固形化濾過材(粒径5mmφ)に代
えた以外は同様に実験を行った。その結果を表2に示
す。Example 2 An experiment was conducted in the same manner as in Example 1, except that the upper filler 4 was replaced with a solidified filter medium and the lower filler 6 was replaced with a solidified filter medium (particle diameter: 5 mmφ). . Table 2 shows the results.
【0027】比較例1 実施例1において、軽石を用いずに上段と下段の充填材
4と6の両方共に腐植物を主体とする土壌成形体に代え
た以外は同様にして実験を行った。その結果を表2に示
す。Comparative Example 1 An experiment was conducted in the same manner as in Example 1 except that pumice was not used and both the upper and lower fillers 4 and 6 were replaced with soil compacts mainly composed of humus. Table 2 shows the results.
【0028】[0028]
【表2】 [Table 2]
【0029】実施例3 実施例1、2及び比較例1において経過日数に対する硫
化水素の除去状況を調べ、その結果を図3に示す。図3
において、線Aは実施例1、線Bは実施例2、線Cは比
較例1を示している。Example 3 In Examples 1 and 2 and Comparative Example 1, the state of removal of hydrogen sulfide with respect to the elapsed days was examined, and the results are shown in FIG. FIG.
, Line A indicates Example 1, line B indicates Example 2, and line C indicates Comparative Example 1.
【0030】図3から明らかなように、実施例1及び2
では実験開始10日後には100%の除去率を示したが、比
較例1では15日経っても最高除去率は98%であった。15
日以降は、硫化水素の除去率は徐々に低下した。As is apparent from FIG.
Showed a 100% removal rate 10 days after the start of the experiment, but in Comparative Example 1, the maximum removal rate was 98% even after 15 days. Fifteen
After the day, the removal rate of hydrogen sulfide gradually decreased.
【0031】[0031]
【発明の効果】本発明によれば、従来法では完全に除去
し得なかった酸性臭気成分である硫化水素を効果的に除
去することができる。また本発明によれば、有機性臭気
成分も効果的に除去できる。According to the present invention, hydrogen sulfide which is an acidic odor component, which cannot be completely removed by the conventional method, can be effectively removed. Further, according to the present invention, an organic odor component can also be effectively removed.
【図1】本発明の一実施例を示す縦断面図FIG. 1 is a longitudinal sectional view showing one embodiment of the present invention.
【図2】本発明の他の実施例を示す要部断面図FIG. 2 is a sectional view of a main part showing another embodiment of the present invention.
【図3】本発明の実施例における経過日数に対する硫化
水素の除去率を示す線図FIG. 3 is a graph showing the removal rate of hydrogen sulfide with respect to the number of elapsed days in an example of the present invention.
1:脱臭塔 2:導入口 3:排出口 4、6:充填材 5、7:支持板 8、9:散水部 10:循環槽 11、15:ポンプ 12:反応槽 13:充填部 14:散気部 70:液溜り部 71:上昇管 72:泡鐘 73:透孔 74:間隙 75:下降管 81、91:スプレーノズル 1: Deodorization tower 2: Inlet 3: Outlet 4, 6: Filling material 5, 7: Support plate 8, 9: Water sprinkling unit 10: Circulation tank 11, 15: Pump 12: Reaction tank 13: Filling unit 14: Sprinkling Gas part 70: Liquid pool part 71: Up pipe 72: Bubble bell 73: Through hole 74: Gap 75: Down pipe 81, 91: Spray nozzle
フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 53/34 - 53/88 Continuation of front page (58) Field surveyed (Int. Cl. 7 , DB name) B01D 53/34-53/88
Claims (3)
処理済ガスの排出口を有する脱臭塔本体内に充填材を多
段に設け、該脱臭塔本体の下部に循環槽を設け、各段の
充填材の上方に循環槽から供給される循環液の散水部を
有する脱臭装置において、上方に位置する少なくとも一
段の充填材が腐植物の溶出液を溶出性シリカ成分を含有
する軽石粉末に含浸させた固形化濾過材であり、下方に
位置する少なくとも一段の充填材が下記(1)〜(2)から選
ばれる少なくとも1種であることを特徴とする脱臭装
置。 (1) 腐植物を主体とする土壌成形体 (2) 腐植物の溶出液を溶出性シリカ成分を含有する軽石
粉末に含浸させた固形化濾過材 1. A deodorization tower body having an odor gas introduction port below and a treated gas discharge port above is provided in multiple stages in a deodorization tower main body, and a circulation tank is provided at a lower portion of the deodorization tower main body. In a deodorizer having a sprinkling section of a circulating liquid supplied from a circulation tank above each of the fillers, at least one of the fillers located above has a pumice powder containing a silica component that elutes a humus eluate. A deodorizing device, characterized in that the solidified filter material impregnated with at least one of the below-mentioned fillers is at least one selected from the following (1) and (2). (1) Soil compacts mainly composed of humus (2) Solidified filter media in which the eluate of humus is impregnated with pumice powder containing an eluting silica component
周辺に、充填材の溶出液の液溜り部を有することを特徴
とする請求項1に記載の脱臭装置。 2. The deodorizing apparatus according to claim 1, further comprising a reservoir for an eluate of the filler around at least one stage of the filler located below.
体若しくは成形体又は溶出性シリカ成分を含有する軽石
の少なくとも1種を充填してなる反応槽を設け、前記循
環槽内の液を導入して所定時間反応後、前記循環槽に返
送することを特徴とする請求項1又は2に記載の脱臭装
置。 3. A reaction tank filled with at least one kind of soil powder, granules or compacts mainly composed of humus, or pumice containing an eluting silica component, is provided therein. 3. The deodorizing apparatus according to claim 1 , wherein the liquid is returned to the circulation tank after reacting for a predetermined time after introducing the liquid.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30502695A JP3202564B2 (en) | 1995-10-30 | 1995-10-30 | Deodorizing device |
TW085112347A TW359625B (en) | 1995-10-30 | 1996-10-09 | Deodorizer |
CN96122679A CN1072511C (en) | 1995-10-30 | 1996-10-29 | Deodorization device |
KR1019960049893A KR100196627B1 (en) | 1995-10-30 | 1996-10-30 | Deodorizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30502695A JP3202564B2 (en) | 1995-10-30 | 1995-10-30 | Deodorizing device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09122436A JPH09122436A (en) | 1997-05-13 |
JP3202564B2 true JP3202564B2 (en) | 2001-08-27 |
Family
ID=17940205
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30502695A Expired - Fee Related JP3202564B2 (en) | 1995-10-30 | 1995-10-30 | Deodorizing device |
Country Status (4)
Country | Link |
---|---|
JP (1) | JP3202564B2 (en) |
KR (1) | KR100196627B1 (en) |
CN (1) | CN1072511C (en) |
TW (1) | TW359625B (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100344060B1 (en) * | 2000-03-14 | 2002-07-24 | 한국생산기술연구원 | Scruber Type Dry Spray Apparatus For Deodorizing With Natural Deodorizing Neutralizer |
JP2005334843A (en) * | 2004-05-31 | 2005-12-08 | Matsushita Electric Ind Co Ltd | Porous natural stone deodorant and porous natural stone deodorizing apparatus using the same |
CN100408150C (en) * | 2006-02-06 | 2008-08-06 | 顾建 | Improved deodourization device of soil |
KR100833653B1 (en) * | 2007-04-11 | 2008-06-03 | 부경엔지니어링주식회사 | Deodorizing device |
CN101049512B (en) * | 2007-05-14 | 2012-09-05 | 西原环保工程(上海)有限公司 | Biological deodoration equipment of charcoal biology medium |
KR20120047295A (en) * | 2009-08-31 | 2012-05-11 | 도꾸리쯔 교세이호징 노우교 ? 쇼쿠힝 산교 기쥬쯔 소고 겡뀨 기꼬우 | Deodorizing material and deodorizing device |
CN101913711A (en) * | 2010-05-26 | 2010-12-15 | 优泥可环保技术有限公司 | Sludge modifying machine and water treatment facility provided with sludge modifying machines in parallel |
JP6345466B2 (en) * | 2014-03-31 | 2018-06-20 | クボタ環境サ−ビス株式会社 | Deodorization device |
JP6278796B2 (en) * | 2014-03-31 | 2018-02-14 | クボタ環境サ−ビス株式会社 | Deodorization device |
CN108057337B (en) * | 2017-12-15 | 2024-01-12 | 信开环境投资有限公司 | Two-section layered rear-mounted induced air ring energy type deodorizing system and deodorizing process |
CN112546773A (en) * | 2020-09-27 | 2021-03-26 | 湖南嘉顺华新材料有限公司 | Dust removal equipment for spray tower |
KR102535535B1 (en) | 2020-12-18 | 2023-05-24 | 대한민국 | Exhaust Gas Purification Facility Using Ozone And Ultraviolet Rays |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3775216D1 (en) * | 1987-07-20 | 1992-01-23 | Kajima Corp | DESODORING DEVICE. |
JPH05321321A (en) * | 1992-06-09 | 1993-12-07 | Mitsui Kinzoku Kyushu Kiko Kk | Deodorizing device in waste storage facility |
JPH07185258A (en) * | 1993-12-28 | 1995-07-25 | Matsushita Electric Works Ltd | Deodorizing apparatus |
JPH08245970A (en) * | 1995-03-09 | 1996-09-24 | Tokyo Gas Co Ltd | Removing device for odorizing component of town gas |
-
1995
- 1995-10-30 JP JP30502695A patent/JP3202564B2/en not_active Expired - Fee Related
-
1996
- 1996-10-09 TW TW085112347A patent/TW359625B/en active
- 1996-10-29 CN CN96122679A patent/CN1072511C/en not_active Expired - Fee Related
- 1996-10-30 KR KR1019960049893A patent/KR100196627B1/en not_active IP Right Cessation
Non-Patent Citations (1)
Title |
---|
G.Alexander著、井上勝也 訳「シリカと私」(1971年6月)東京化学同人p.79−84 |
Also Published As
Publication number | Publication date |
---|---|
TW359625B (en) | 1999-06-01 |
KR100196627B1 (en) | 1999-06-15 |
KR970020162A (en) | 1997-05-28 |
CN1072511C (en) | 2001-10-10 |
JPH09122436A (en) | 1997-05-13 |
CN1157174A (en) | 1997-08-20 |
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