JPH0144340B2 - - Google Patents
Info
- Publication number
- JPH0144340B2 JPH0144340B2 JP60229655A JP22965585A JPH0144340B2 JP H0144340 B2 JPH0144340 B2 JP H0144340B2 JP 60229655 A JP60229655 A JP 60229655A JP 22965585 A JP22965585 A JP 22965585A JP H0144340 B2 JPH0144340 B2 JP H0144340B2
- Authority
- JP
- Japan
- Prior art keywords
- deodorizing
- gas
- cleaning
- malodorous
- tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Landscapes
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Description
「産業上の利用分野」
本発明は悪臭ガスの脱臭方法、詳しくは悪臭ガ
スの洗浄による脱臭法の改良法に関する。
「従来の技術」
し尿処理場や下水処理場などで発生する悪臭ガ
スの脱臭方法として、従来、主に次の三方式、即
ち
(1) 吸着法
(2) 洗浄法
(3) 洗浄法+吸着法
が用いられている。
上記方式においてはすべての悪臭ガスを次の3
種類、
即ち
酸性ガス……硫化水素、メチルメルカプタン等
のイオウ化合物、酢酸、プロピオ
ン酸等の低級脂肪酸類
塩基性ガス……アンモニア、トリメチルアミン
等
中性ガス……硫化メチル、二硫化メチル等
に分類し、例えば下記の様に分類別に各々脱臭塔
を設置している。
"Industrial Application Field" The present invention relates to a method for deodorizing malodorous gas, and more particularly to a method for improving the deodorizing method by cleaning malodorous gas. ``Conventional technology'' Traditionally, the following three methods have been used to deodorize malodorous gases generated in human waste treatment plants, sewage treatment plants, etc.: (1) Adsorption method (2) Cleaning method (3) Cleaning method + adsorption method law is used. In the above method, all malodorous gases are
Types: Acidic gases: hydrogen sulfide, sulfur compounds such as methyl mercaptan, lower fatty acids such as acetic acid and propionic acid Basic gases: ammonia, trimethylamine, etc. Neutral gases: methyl sulfide, methyl disulfide, etc. For example, deodorizing towers are installed for each category as shown below.
【表】
対象とする悪臭ガスの混合組成比や濃度によ
り、上記方式を適当に選定し、組合せれば、十分
満足のいく脱臭効果を得ることが可能である。
「発明が解決しようとする問題点」
しかしながら、従来の脱臭塔は最低の場合でも
2塔(酸性ガス用、アルカリ性ガス用など)以上
必要であり、多い場合には4〜5塔も必要であり
設備費に関する限り、決して満足出来るものでは
なかつた。
本発明はこの様な従来の問題点に着目してなさ
れたものであり、従来より脱臭塔の数を大巾に削
減し、しかも悪臭ガスの除去率を向上させる脱臭
法を提供することを目的としている。
「問題点を解決するための手段」
上記の技術的課題を解決するために、本発明は
洗浄方式における脱臭方法において、気液接触部
に紫外線を照射させることからなるものである。
本発明において気液接触部(充填剤層)に紫外
線を照射すると悪臭ガスと洗浄薬液の両者が励起
され、洗浄効果が大巾に向上する。
本発明の洗浄液としては従来使用されている酸
アルカリ又は酸化剤などを使用出来るが、特に次
亜塩素酸ソーダ又は過酸化水素などの酸化剤は悪
臭ガスの性質の如何にかかわらず使用出来て好都
合である。紫外線照射は洗浄液と悪臭ガスが接触
する部分(充填材層)で行い、紫外線照射ランプ
の位置は任意に設置することが出来る。即ち、そ
れはたとえば縦型の洗浄方式では充填材層を縦に
貫通して設置し、横型の洗浄方式では充填材層の
側面に設置することが出来る。
「作 用」
光が物質に照射されると吸収され、この吸収さ
れた光は分子の電子を励起させ、生じた励起エネ
ルギーは他分子に移動するか、あるいは自分自身
の振動エネルギーに変換する。
その結果、室温においても分子は高温度に加熱
されたと同じ状態になり、分子内の結合に開裂が
起こる。
本発明において気液接触部に紫外線を照射する
事は、悪臭ガスと洗浄薬液の両者に上述の効果を
もたらし、結果として洗浄効果が大巾に上がるも
のと思われる。
以下本発明を実施例に従つて説明する。
実施例 1
市販のプラスチツク製の充填剤1を層高100cm、
径20cmに充填した縦型充填塔に、上部より
500ppmの次亜塩素酸ソーダ又は過酸化水素2を
ノズル3より添加する様にし、液2の循環量は50
ml/minとする。これに塔の下部入口4より、下
記組成の悪臭ガスを風量40/minの速度(空気
線流速度0.02m/sec、洗浄薬液量/ガス比1.25
ml/)で流通し、第1図の様に充填塔内部に縦
に設置した100W紫外線ランプ5より紫外線を照
射した場合の充填塔上部出口6の悪臭ガスの組成
は表―1の様になつた。紫外線照射を行わない従
来法と比較して、除去率に格段の差が見られる。
尚、7は循環ポンプである。[Table] If the above methods are appropriately selected and combined depending on the mixture composition ratio and concentration of the target malodorous gas, it is possible to obtain a sufficiently satisfactory deodorizing effect. "Problems to be Solved by the Invention" However, conventional deodorizing towers require at least two towers (one for acidic gas, one for alkaline gas, etc.), and in many cases, as many as four to five towers are required. As far as equipment costs were concerned, they were by no means satisfactory. The present invention has been made by focusing on these conventional problems, and aims to provide a deodorizing method that greatly reduces the number of deodorizing towers compared to the conventional method and improves the removal rate of malodorous gases. It is said that "Means for Solving the Problems" In order to solve the above-mentioned technical problems, the present invention provides a deodorizing method using a cleaning method, which comprises irradiating a gas-liquid contact portion with ultraviolet rays. In the present invention, when the gas-liquid contact area (filler layer) is irradiated with ultraviolet rays, both the malodorous gas and the cleaning chemical are excited, and the cleaning effect is greatly improved. As the cleaning solution of the present invention, conventionally used acids and alkalis or oxidizing agents can be used, but oxidizing agents such as sodium hypochlorite or hydrogen peroxide are particularly convenient because they can be used regardless of the nature of the malodorous gas. It is. The ultraviolet rays are irradiated at the area where the cleaning liquid and the foul-smelling gas come into contact (the filler layer), and the ultraviolet irradiation lamp can be placed at any position. That is, it can be placed, for example, vertically through the filler layer in a vertical cleaning mode, or on the side of the filler layer in a horizontal cleaning mode. ``Operation'' When light is irradiated onto a substance, it is absorbed, and this absorbed light excites the electrons in the molecule, and the resulting excitation energy is transferred to other molecules or converted into its own vibrational energy. As a result, even at room temperature, the molecule is in the same state as if it had been heated to a high temperature, and bonds within the molecule are cleaved. In the present invention, irradiating the gas-liquid contact area with ultraviolet rays brings about the above-mentioned effects on both the malodorous gas and the cleaning chemical, and as a result, it is thought that the cleaning effect will be greatly improved. The present invention will be explained below based on examples. Example 1 A commercially available plastic filler 1 was prepared with a layer height of 100 cm.
A vertical packed tower packed to a diameter of 20cm is filled from the top.
Add 500ppm of sodium hypochlorite or hydrogen peroxide 2 from nozzle 3, and the circulation amount of liquid 2 is 50ppm.
ml/min. Then, from the lower inlet 4 of the tower, a malodorous gas having the following composition is introduced at a flow rate of 40/min (air linear flow velocity 0.02 m/sec, cleaning chemical amount/gas ratio 1.25).
ml/) and is irradiated with ultraviolet light from a 100W ultraviolet lamp 5 installed vertically inside the packed tower as shown in Figure 1, the composition of the foul-smelling gas at the outlet 6 at the top of the packed tower is as shown in Table 1. Ta. There is a significant difference in removal rate compared to the conventional method that does not involve UV irradiation.
In addition, 7 is a circulation pump.
【表】
実施例 2
実施例1と同じ充填塔を用い悪臭ガス風量、洗
浄液循環量、紫外線ランプ等、実施例1と同じ条
件で悪臭ガスの種類と洗浄液の種類を変えて脱臭
試験を行つた。洗浄液としては苛性ソーダ、塩酸
を用いて表―2に示した悪臭ガスの除去を行い、
紫外線照射を行わない従来法と比較し、その結果
を表―2にまとめた。[Table] Example 2 Using the same packed tower as in Example 1, a deodorization test was conducted under the same conditions as in Example 1, such as the flow rate of malodorous gas, the amount of cleaning fluid circulated, and the ultraviolet lamp, while changing the type of malodorous gas and cleaning fluid. . Caustic soda and hydrochloric acid are used as cleaning solutions to remove the foul-smelling gases shown in Table 2.
A comparison was made with a conventional method that does not involve ultraviolet irradiation, and the results are summarized in Table 2.
【表】
上表より明らかな様に脱臭効率において、紫外
線照射を行わない従来法に比べ格段の差が見られ
る。
「発明の効果」
従来の脱臭法に比較して、紫外線照射を行つた
本発明では、前記実施例から明らかな様に、悪臭
ガスの除去率に格段の差が見られ、悪臭除去効率
を予期出来ないほど顕著に向上させることが出来
た。
又従来の脱臭法では、入口ガス濃度が数拾ppm
以下の場合、酸性ガス用、塩基性ガス用の脱臭塔
は各々1基は必要であり、入口ガス濃度が数拾
ppm以上の場合は酸性ガス用脱臭塔のみでも2段
(2基)必要であつた。
しかし、本発明を利用すれば入口ガス濃度が数
拾ppm以下の比較的低濃度の場合は洗浄液に次亜
塩素酸ソーダ又は過酸化水素などの酸化剤を使用
し、1基の脱臭塔で十分である。
又入口ガス濃度が数拾ppm以上の比較的高濃度
の場合にも酸性ガス用脱臭塔は1段(1基)で十
分であり、表3の如くである。[Table] As is clear from the table above, there is a significant difference in deodorizing efficiency compared to the conventional method that does not use ultraviolet irradiation. "Effects of the Invention" Compared to conventional deodorizing methods, the present invention, which uses ultraviolet irradiation, shows a significant difference in the removal rate of malodorous gases, as is clear from the above examples, and the expected malodor removal efficiency. I was able to improve it significantly. In addition, in conventional deodorization methods, the inlet gas concentration is several tens of ppm.
In the following cases, one deodorizing tower each for acidic gas and basic gas is required, and the inlet gas concentration is several tens of thousands.
If the amount exceeds ppm, two stages (two units) are required for the deodorizing tower for acidic gases alone. However, if the present invention is used, if the inlet gas concentration is relatively low, such as several tens of ppm or less, an oxidizing agent such as sodium hypochlorite or hydrogen peroxide can be used as the cleaning solution, and one deodorizing tower is sufficient. It is. Further, even when the inlet gas concentration is relatively high, such as several tens of ppm or more, one stage (one unit) of the deodorizing tower for acidic gas is sufficient, as shown in Table 3.
【表】
これにより脱臭装置の建設費、維持費、設置ス
ペースを従来に比較し大巾に削減することも出
来、これらの効果は当分野に多大な貢献をもたら
すものである。[Table] As a result, the construction cost, maintenance cost, and installation space of the deodorizing device can be significantly reduced compared to conventional methods, and these effects will make a significant contribution to this field.
添付図面は本発明実施の一例を示す縦型脱臭塔
の機構側面図である。
1……充填剤、2……洗浄液、3……ノズル、
4……塔の下部入口、5……紫外線ランプ、6…
…塔の上部出口、7……循環ポンプ。
The accompanying drawing is a mechanical side view of a vertical deodorizing tower showing an example of carrying out the present invention. 1... Filler, 2... Cleaning liquid, 3... Nozzle,
4... Bottom entrance of the tower, 5... Ultraviolet lamp, 6...
... Upper outlet of the tower, 7... Circulation pump.
Claims (1)
洗浄方式における脱臭方法において、気液接触部
に紫外線を照射させることを特徴とするし尿処理
場や下水処理場などで発生する悪臭ガスの脱臭方
法。1. A method for deodorizing foul-smelling gases generated in human waste treatment plants, sewage treatment plants, etc., which is a method for deodorizing a cleaning method using an oxidizing agent, acid, or alkali as a cleaning liquid, and is characterized by irradiating the gas-liquid contact area with ultraviolet rays.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60229655A JPS6287161A (en) | 1985-10-14 | 1985-10-14 | Deodorizing method using ultraviolet light |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60229655A JPS6287161A (en) | 1985-10-14 | 1985-10-14 | Deodorizing method using ultraviolet light |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6287161A JPS6287161A (en) | 1987-04-21 |
| JPH0144340B2 true JPH0144340B2 (en) | 1989-09-27 |
Family
ID=16895604
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60229655A Granted JPS6287161A (en) | 1985-10-14 | 1985-10-14 | Deodorizing method using ultraviolet light |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6287161A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006204683A (en) * | 2005-01-31 | 2006-08-10 | River Seisakusho:Kk | Apparatus for decomposing and eliminating chemical pollutant, specific malodorous component and bacterium |
| JP4915958B2 (en) * | 2008-03-26 | 2012-04-11 | パナソニック株式会社 | Air purifier |
| JP7133161B2 (en) * | 2017-08-22 | 2022-09-08 | メタウォーター株式会社 | Deodorizing system |
| JP7076778B2 (en) * | 2018-04-27 | 2022-05-30 | 株式会社微酸研 | Air deodorizing sterilization method, air deodorizing sterilization device and air deodorizing sterilization system |
-
1985
- 1985-10-14 JP JP60229655A patent/JPS6287161A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6287161A (en) | 1987-04-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101455938B (en) | Plasma biology deodorization technique and system of vent gas from steel-drum spray-painting production line | |
| CN208066104U (en) | A kind of chemical industry waste water station foul smell is collected and processing system | |
| CN110711485A (en) | Waste gas purification device for sewage treatment station of sterile raw material medicine production line | |
| CN110639346A (en) | Gas treatment device | |
| CN203540330U (en) | Treatment device of odor pollutant waste gas | |
| CN106621749A (en) | Waste gas purification equipment with stink removal and VOCs (volatile organic compounds) degradation functions | |
| JPH045484B2 (en) | ||
| JPH0144340B2 (en) | ||
| WO1996006045A1 (en) | Method and apparatus for the purification of gases and liquids | |
| KR102372779B1 (en) | Stack type adsorption apparatus for odor removal and odor removal device using the same | |
| CN113134278B (en) | Environment management device for garbage transfer station | |
| CN110694467A (en) | A clarification plant for handling waste gas is produced to bio-pharmaceuticals fungus sediment | |
| JP3743545B2 (en) | Deodorizing agent for aldehyde-containing gas and deodorizing method | |
| CN211562472U (en) | A clarification plant for bio-pharmaceuticals sewage treatment station produces waste gas | |
| CN205700076U (en) | A kind of low concentration sulfuration waste gas combination type purifier | |
| KR20230139446A (en) | Gseous Pollutants Purifying System | |
| KR20210155791A (en) | an odor removing equipment using both natural essences oils and porous medias and the odor removing method | |
| CN116789296A (en) | Method for treating stink of acidized wastewater of oil and gas field based on stripping absorption | |
| WO1997032660A3 (en) | Process and device for scrubbing waste gases containing ethylene oxide | |
| CN208642317U (en) | A UV photocatalytic industrial odor purification device | |
| JP2750588B2 (en) | Deodorizing device | |
| KR100290066B1 (en) | How to fix titanium dioxide, used as an air freshener, on activated carbon | |
| JP2000246050A (en) | Deodorizing apparatus | |
| KR100291604B1 (en) | How to Fix Titanium Dioxide Used as Air Freshener in Glass Tubes | |
| CN211562507U (en) | A clarification plant that is used for bio-pharmaceuticals stoving liquid sediment to produce waste gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
| LAPS | Cancellation because of no payment of annual fees |