JPS58112027A - Deodorizing apparatus - Google Patents
Deodorizing apparatusInfo
- Publication number
- JPS58112027A JPS58112027A JP56212986A JP21298681A JPS58112027A JP S58112027 A JPS58112027 A JP S58112027A JP 56212986 A JP56212986 A JP 56212986A JP 21298681 A JP21298681 A JP 21298681A JP S58112027 A JPS58112027 A JP S58112027A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- humidity
- treated
- air
- concn
- 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
- Incineration Of Waste (AREA)
- Treating Waste Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【発明の詳細な説明】
この発明はオゾンを用いた脱臭装置に関するものである
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a deodorizing device using ozone.
近年悪臭公害に対する関−心が高まり、脱臭装置の必要
性が説かれる中で様々な方・式を用いた脱臭装置が開発
されてきた。例えと、直燃式。In recent years, interest in odor pollution has increased and the necessity of deodorizing devices has been emphasized, and deodorizing devices using various methods have been developed. For example, direct combustion type.
吸着式、薬剤洗浄式などであり、それぞれの方式は一長
一短があるので、どの方式も主流とはならなかった。し
かし活性炭などを吸着及び酸化の触媒として、この上で
悪臭物質をオゾン酸化して無臭化、する触媒併用型オゾ
ン酸化脱臭装置が提案され、−躍′脚光を浴び始めた。There are adsorption methods, chemical cleaning methods, etc., and each method has its advantages and disadvantages, so none of them has become mainstream. However, a catalyst-combined ozone oxidation deodorization device has been proposed, which uses activated carbon as an adsorption and oxidation catalyst to oxidize malodorous substances with ozone to make them odorless, and has begun to attract attention.
従来の触媒併用型オゾン酸化脱臭装置として特公昭54
−221!5 に見られるようなものがあり、−例を
第1図に示す。Special Publication in 1977 as a conventional catalytic ozone oxidation deodorization device
221!5, an example of which is shown in Figure 1.
図において(1)は被処理空気、(2)はプロワ−0(
3)は悪臭濃度測定器、(4Iはオゾン濃度制御器。In the figure, (1) is the air to be treated, (2) is the blower 0 (
3) is a malodor concentration measuring device, (4I is an ozone concentration controller.
(5)はオゾナイザ−、(61d触媒の充填された反応
塔、<7)は処理空気である。(5) is an ozonizer, (61d reaction tower packed with catalyst, <7) is treated air.
次に動作について説明する。Next, the operation will be explained.
硫化水素、アンモニアなどの悪臭成分を含む被処理空気
(1)をブロワ−(2)で吸引する。被処理空気(1)
中の悪臭成分濃度は硫黄化合物モニターとアンモニアモ
ニターで構成される悪臭濃度測定器(3)で測定され、
オゾン濃度制御器(引へ入力される。オゾン濃度制御器
(4)は、この入力信号に基づいてオゾナイザ−(5)
の放電電力を制御するので、悪臭濃度に対応したオゾン
が被処理空気に添加される。オゾンを含んだ被処理空気
は触媒の充填された反応塔(6)内で酸化脱臭され処理
空気(7)として放出される。Air to be treated (1) containing malodorous components such as hydrogen sulfide and ammonia is sucked in by a blower (2). Air to be treated (1)
The concentration of malodorous components inside is measured with a malodor concentration measuring device (3) consisting of a sulfur compound monitor and an ammonia monitor.
The ozone concentration controller (4) controls the ozonizer (5) based on this input signal.
Since the discharge power is controlled, ozone corresponding to the odor concentration is added to the air to be treated. The air to be treated containing ozone is oxidized and deodorized in a reaction tower (6) filled with a catalyst and released as treated air (7).
従来の脱臭装置は以上のように構成されているので0例
えば触媒として活性炭を用いた場合被処理空気の相対湿
度が90チ以上になると脱臭性が急激に低下するという
欠点があった。これは湿度が高くなると触媒である活性
炭が疎水性であるにもかかわらずその表面が水分で僚わ
れるようになシ、酸化効率が低下するためである。Since the conventional deodorizing apparatus is constructed as described above, it has the disadvantage that, for example, when activated carbon is used as a catalyst, the deodorizing performance rapidly decreases when the relative humidity of the air to be treated becomes 90 degrees or higher. This is because when the humidity increases, the surface of activated carbon, which is a catalyst, becomes clogged with moisture, even though it is hydrophobic, and the oxidation efficiency decreases.
この発明は上記のような従来のものの欠点を除去するた
めになされたもので、悪臭成分濃度および湿度に基づい
てオゾンII゛度制御を制御することで、常に安定した
脱臭性能を得ることを目的としている。This invention was made in order to eliminate the drawbacks of the conventional methods as described above, and aims to always obtain stable deodorizing performance by controlling ozone II degree control based on the concentration of malodorous components and humidity. It is said that
以下この発明の一実施例を図について説明する。第2図
において、(8)は被処理空気(1)中の硫黄系悪臭成
分濃度を測定するための硫黄化合物モニター、(9)は
湿度を測定するための湿度センサー、a・はオゾン混合
後の被処理空気のオゾン濃度を測定するためのオゾンモ
ニターである。An embodiment of the present invention will be described below with reference to the drawings. In Figure 2, (8) is a sulfur compound monitor for measuring the concentration of sulfur-based malodorous components in the air to be treated (1), (9) is a humidity sensor for measuring humidity, and a is after ozone mixing. This is an ozone monitor for measuring the ozone concentration in the air being treated.
次に動作について説明する。ブロワ−(2)で吸引され
た被処理空気(11中の硫黄系悪臭成分およびアンモニ
ア濃度を硫黄化合物モニターおよびアンモニアモニター
で構成される悪臭濃度測定器(3)で、被処理空気01
の湿度を湿度センサー(9)で測定しオゾン濃度制御器
(4−6)へ入力する。Next, the operation will be explained. The concentration of sulfur-based malodorous components and ammonia in the air to be treated (11) sucked in by the blower (2) is measured using a malodor concentration meter (3) consisting of a sulfur compound monitor and an ammonia monitor.
The humidity is measured by a humidity sensor (9) and input to the ozone concentration controller (4-6).
オゾン濃度制御器(a−b)はオゾンモニター鱒で検知
するオゾン濃度が、悪臭成分濃度および湿度に対応した
鍛適オゾン濃度となるようにオゾナイザ−(5)の放1
11′tII力を制御する。オゾンを混合された被処理
空気は反応塔(61へ送られ、触媒上でオゾンによる接
触酸化反応により無臭化され、処理空気(7)として放
出される。The ozone concentration controller (a-b) controls the ozonizer (5) so that the ozone concentration detected by the ozone monitor trout becomes a suitable ozone concentration corresponding to the malodorous component concentration and humidity.
11'tII control the force. The air to be treated mixed with ozone is sent to a reaction tower (61), is deodorized by a catalytic oxidation reaction with ozone on a catalyst, and is discharged as treated air (7).
次に最適オゾン濃度の設定の仕方について説明する。例
えば触媒として、活性炭を用いる場合には最適オゾン濃
度は湿度が110%以下の場合には悪臭成分濃度の2〜
3倍程度でよいが、湿度が、これ以上の場合には3〜4
5倍程度にすればよい。ただし上記オゾン添加量は触媒
の種類。Next, a method of setting the optimum ozone concentration will be explained. For example, when activated carbon is used as a catalyst, the optimal ozone concentration is 2 to 20% of the odor component concentration when the humidity is 110% or less.
About 3 times the humidity is sufficient, but if the humidity is higher than this, increase the humidity by 3 to 4 times.
It can be increased to about 5 times. However, the amount of ozone added above depends on the type of catalyst.
反応条件忙よシ愛わるので適宜選定すれはよい。Since the reaction conditions vary, it is best to select them appropriately.
とζろでオゾナイ”ザーの能°力には限界があるので、
実際の運転に際して上記オゾン濃度を満たし得ない場合
には、最高オゾン濃度で運転することになるが、この様
な状態は長時間持続することはないので実用上問題はな
い。Since there is a limit to the ability of the ozonizer,
If the above-mentioned ozone concentration cannot be satisfied during actual operation, the operation will be performed at the maximum ozone concentration, but there is no practical problem because such a state will not last for a long time.
また、上記実施例では、オゾン発生量を制御するために
、オゾナイザ−の′j1iw電力を制御したが、オゾナ
イザ−に流入する9気ある。いは酸素の流量を制御して
も同様の効果な上けることができる。Further, in the above embodiment, in order to control the amount of ozone generated, the power of the ozonizer is controlled, but there is still 9 qi flowing into the ozonizer. Alternatively, the same effect can be achieved by controlling the flow rate of oxygen.
上述した如く、この発明によれは、悪臭成分濃度と湿度
に基づいてオゾン濃度を制御するようにしたため、湿度
が上がると脱臭性能が低下するという従来の脱臭装置の
欠点がなくなシ。As described above, according to the present invention, since the ozone concentration is controlled based on the concentration of malodorous components and humidity, the drawback of conventional deodorizing devices that deodorizing performance decreases when humidity increases is eliminated.
常に安定した脱臭性能が得られる効果がある。It has the effect of always providing stable deodorizing performance.
第1図は従来のオゾンを利用する脱臭装置を示す構成図
、第2図はこの発明の一実施例による脱臭装置を示す構
成図である。
図において、(1)は被処理空気、(2)はブロワ。
(3)は悪臭濃度測定器、(4)はオゾン濃度制御器。
(5)はオゾナイザ−0(6)は反応塔、(7)は処理
空気。
(81ハ湿度センサー、C9)はオゾンモニターである
。
なお図中、同一符号はそれぞれ同一部分を示す。
代理人 葛 野 信 −
特許庁長官殿
1.小作の表示 特願昭 56−21291NI
号2、発明の名称
属^装置
3、補正をするh
代表者片山仁へ部
5、補正の対象
明細書の発明の詳細な説明の欄
6、補正の内容
(リ IjIIa書の第3頁第12行の「性が急激k」
を「性能が急激に」と訂正する。
以上FIG. 1 is a block diagram showing a conventional deodorizing apparatus using ozone, and FIG. 2 is a block diagram showing a deodorizing apparatus according to an embodiment of the present invention. In the figure, (1) is the air to be treated, and (2) is the blower. (3) is a malodor concentration measuring device, and (4) is an ozone concentration controller. (5) is an ozonizer, (6) is a reaction tower, and (7) is treated air. (81C humidity sensor, C9) is an ozone monitor. Note that in the figures, the same reference numerals indicate the same parts. Agent Makoto Kuzuno - Commissioner of the Japan Patent Office 1. Display of small works Patent application Sho 56-21291NI
No. 2, Name of the invention ^ Device 3, Make the amendment h Representative Hitoshi Katayama Section 5, Column 6 for detailed explanation of the invention in the specification subject to the amendment, Contents of the amendment (Re) Page 3 of Book IjIIa Line 12: “Sex is suddenly k”
is corrected to "performance suddenly increased."that's all
Claims (1)
接触酸化反応を促進する触媒を充填せる反応塔において
無臭化するように構成された脱臭装置において、上記被
処理空気の湿度を検出する湿度センサ、当該被処理空気
中の悪臭成分濃度を検出する悪臭成分測定器、当該被処
理空気中のオゾン濃度を検出するオゾンモニタおよびこ
れらのセンサの検出値に応じて上記オゾナイザから供給
するオゾン量を制御する制御器を備え、当該被処理空気
中のオゾン濃度が被処理空気の湿度および悪臭成分濃度
に即して予め定めた値を維持するようにしたことを特徴
とする脱臭装置。Adding ozone generated by an ozonizer to the air to be treated,
In a deodorizing device configured to deodorize a reaction tower packed with a catalyst that promotes a catalytic oxidation reaction, a humidity sensor detects the humidity of the air to be treated, and a malodor sensor detects the concentration of malodorous components in the air to be treated. A component measuring device, an ozone monitor that detects the ozone concentration in the air to be treated, and a controller that controls the amount of ozone supplied from the ozonizer according to the detection values of these sensors, and the ozone concentration in the air to be treated is 1. A deodorizing device characterized in that the temperature is maintained at a predetermined value according to the humidity and the concentration of malodorous components in the air to be treated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56212986A JPS58112027A (en) | 1981-12-25 | 1981-12-25 | Deodorizing apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56212986A JPS58112027A (en) | 1981-12-25 | 1981-12-25 | Deodorizing apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58112027A true JPS58112027A (en) | 1983-07-04 |
Family
ID=16631571
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56212986A Pending JPS58112027A (en) | 1981-12-25 | 1981-12-25 | Deodorizing apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58112027A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63103728U (en) * | 1986-12-23 | 1988-07-05 | ||
JPH01128820U (en) * | 1988-02-22 | 1989-09-01 | ||
JP2007136415A (en) * | 2005-11-22 | 2007-06-07 | Takasago Thermal Eng Co Ltd | Ozone deodorizing apparatus and ozone deodorization method |
JP2008023478A (en) * | 2006-07-24 | 2008-02-07 | Sintokogio Ltd | Treatment method of exhaust gas, and treatment apparatus of exhaust gas |
JP2008100169A (en) * | 2006-10-19 | 2008-05-01 | Takasago Thermal Eng Co Ltd | Deodorization method |
-
1981
- 1981-12-25 JP JP56212986A patent/JPS58112027A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63103728U (en) * | 1986-12-23 | 1988-07-05 | ||
JPH01128820U (en) * | 1988-02-22 | 1989-09-01 | ||
JP2007136415A (en) * | 2005-11-22 | 2007-06-07 | Takasago Thermal Eng Co Ltd | Ozone deodorizing apparatus and ozone deodorization method |
JP2008023478A (en) * | 2006-07-24 | 2008-02-07 | Sintokogio Ltd | Treatment method of exhaust gas, and treatment apparatus of exhaust gas |
JP2008100169A (en) * | 2006-10-19 | 2008-05-01 | Takasago Thermal Eng Co Ltd | Deodorization method |
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