JPH0550074A - Decomposition apparatus of ozone dissolved in water - Google Patents
Decomposition apparatus of ozone dissolved in waterInfo
- Publication number
- JPH0550074A JPH0550074A JP19930691A JP19930691A JPH0550074A JP H0550074 A JPH0550074 A JP H0550074A JP 19930691 A JP19930691 A JP 19930691A JP 19930691 A JP19930691 A JP 19930691A JP H0550074 A JPH0550074 A JP H0550074A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- water
- wall
- dissolved
- decomposing
- 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
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は脱臭,殺菌,有機物の分
解などに用いたオゾンの余剰分を分解除去する溶存オゾ
ン分解装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dissolved ozone decomposing apparatus for decomposing and removing excess ozone used for deodorization, sterilization, decomposition of organic substances and the like.
【0002】[0002]
【従来の技術】オゾンは強力な酸化力を持っており、脱
臭をはじめ殺菌,有機物の分解などに効果を発揮する。
現在はプール水の浄化,半導体チップの洗浄,浄水場に
おける浄化処理、レトルト食品の殺菌などに利用されて
いるが、今後さらに多方面への応用が期待されている。
しかしその反面、過剰なオゾンは人体へ害を与える危険
性を持っており、オゾンを有効活用していくには、余剰
オゾンを分解する触媒あるいは装置の開発が必要不可欠
である。2. Description of the Related Art Ozone has a strong oxidizing power and is effective in deodorizing, sterilizing and decomposing organic substances.
Currently, it is used for purification of pool water, cleaning of semiconductor chips, purification treatment in water purification plants, sterilization of retort foods, etc., but it is expected to be applied to various fields in the future.
On the other hand, however, excess ozone poses a risk of harming the human body, and in order to effectively utilize ozone, it is essential to develop a catalyst or device that decomposes excess ozone.
【0003】現在、オゾンガスの除去については、熱分
解法や活性炭による吸着分解法の欠点を補なうオゾン分
解触媒の開発がかなり進んでおり、高濃度のオゾンガス
を長時間安定して分解除去することが可能となってき
た。At present, with respect to the removal of ozone gas, the development of ozone decomposition catalysts that make up for the drawbacks of the thermal decomposition method and the adsorption decomposition method using activated carbon has progressed considerably, and the ozone gas of high concentration can be decomposed and removed stably for a long time. It has become possible.
【0004】一方、水中の溶存オゾンについては、活性
炭による吸着除去が一般的な方法で、触媒の利用は今の
ところ行われていない。On the other hand, the dissolved ozone in water is generally adsorbed and removed by activated carbon, and no catalyst has been used so far.
【0005】[0005]
【発明が解決しようとする課題】このような従来のオゾ
ン除去方法で、水中の溶存オゾンを分解する場合、活性
炭による吸着除去を行うと、活性炭吸着剤が細菌繁殖の
温床となり、折角オゾンで殺菌された水が再び細菌で汚
染されるという問題があった。In the case of decomposing dissolved ozone in water by such a conventional ozone removal method, when it is adsorbed and removed by activated carbon, the activated carbon adsorbent becomes a hotbed for bacterial propagation and sterilized with ozone. There was a problem that the sewage water was contaminated with bacteria again.
【0006】本発明はこのような課題を解決するもの
で、水中溶存オゾンを高効率で分解除去し、細菌の繁殖
を抑制する簡単な構成の溶存オゾン除去装置を提供する
ことを目的とするものである。The present invention solves such problems, and an object of the present invention is to provide a dissolved ozone removing apparatus having a simple structure for decomposing and removing dissolved ozone in water with high efficiency and suppressing bacterial growth. Is.
【0007】[0007]
【課題を解決するための手段】このような課題を解決す
るために本発明は、電気絶縁性を有する容器の下部に設
けたオゾン水導入口と、前記容器の上部に設けた排出口
と、前記容器の内部に設けた撹拌羽および外壁と、前記
容器の外側に配設され、前記撹拌羽と外壁に電気的に接
続された電源とを備え、前記撹拌羽と外壁を電極として
電圧を印加しながら、前記導入口からオゾン水を導入
し、オゾンを電気分解して排出口より排出するようにし
たものである。In order to solve the above problems, the present invention provides an ozone water inlet provided in the lower part of an electrically insulating container, and an outlet provided in the upper part of the container. An agitation blade and an outer wall provided inside the container, and a power source disposed outside the container and electrically connected to the agitation blade and the outer wall, and a voltage is applied using the agitation blade and the outer wall as electrodes. However, ozone water is introduced from the inlet, and ozone is electrolyzed and discharged from the outlet.
【0008】また、撹拌羽と外壁をオゾン分解触媒で構
成するようにしたものである。Further, the stirring blade and the outer wall are constituted by an ozone decomposition catalyst.
【0009】[0009]
【作用】この構成によれば、溶存オゾンをオゾン分解触
媒による化学的分解と、撹拌羽と外壁を電極として電気
分解することにより、溶存オゾンをほぼ完全に分解する
ことができる。また、細菌が繁殖して脱オゾン水が汚染
されることもなくなり、衛生的で安全な水を供給するこ
とができる。According to this structure, the dissolved ozone can be almost completely decomposed by chemically decomposing the dissolved ozone by the ozone decomposing catalyst and electrolyzing it by using the stirring blade and the outer wall as electrodes. In addition, bacteria are not propagated to contaminate the deozoned water, and sanitary and safe water can be supplied.
【0010】さらに、本発明によれば、オゾン分解触媒
に電圧を印加することにより、触媒のオゾン分解活性を
向上させるとともに、水の電気分解により生成した水素
も溶存オゾンを分解させるので、溶存オゾンが高効率で
分解除去されることとなる。Further, according to the present invention, by applying a voltage to the ozone decomposing catalyst, the ozone decomposing activity of the catalyst is improved and the hydrogen produced by electrolysis of water also decomposes the dissolved ozone. Will be decomposed and removed with high efficiency.
【0011】[0011]
【実施例】以下に本発明の一実施例のオゾン分解装置を
図面を参照しながら説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An ozone decomposing apparatus according to an embodiment of the present invention will be described below with reference to the drawings.
【0012】図1に水中溶存オゾン分解装置の構成を示
す。図1に示すように容器7の下部にオゾン水導入口
1、上部に処理水の排出口6を備え、内部にプロペラ状
撹拌羽2、外壁3、電源4とで構成されている。撹拌羽
2と外壁3は電極を兼ねており、いずれもオゾン分解触
媒(Co系酸化物、Pt活性炭など)で構成されてい
て、電源4によって1.5〜10V望ましくは6〜8V
の電圧が印加されている。FIG. 1 shows the construction of an apparatus for decomposing dissolved ozone in water. As shown in FIG. 1, a container 7 is provided with an ozone water inlet 1 at the bottom, treated water outlet 6 at the top, and is composed of a propeller-shaped stirring blade 2, an outer wall 3, and a power source 4. The stirring blade 2 and the outer wall 3 also serve as electrodes, both of which are composed of an ozone decomposition catalyst (Co-based oxide, Pt activated carbon, etc.), and the power source 4 supplies 1.5 to 10 V, preferably 6 to 8 V.
Is being applied.
【0013】以下に本発明の具体的実施例を説明する。 (実施例1)上記のように構成された水中溶存オゾン分
解装置において、撹拌羽2と外壁3の電極材料としてL
a0.6Sr0.4Co0.9Fe0.1O3-8を主体とするCo系
酸化物を用い印加電圧8ボルトとし、濃度5mg/lの
オゾン水を流量1l/minで装置内に通水し、排出口
6における溶存オゾン濃度の経時変化を測定した。結果
を(表1)に示す。Specific examples of the present invention will be described below. (Example 1) In the water-dissolved ozone decomposing apparatus configured as described above, L was used as an electrode material for the stirring blade 2 and the outer wall 3.
a 0.6 Sr 0.4 Co 0.9 Fe 0.1 O 3-8 was used as the main component, and the applied voltage was 8 V. Ozone water with a concentration of 5 mg / l was passed through the device at a flow rate of 1 l / min and the discharge port was used. The time-dependent change of the dissolved ozone concentration in 6 was measured. The results are shown in (Table 1).
【0014】(実施例2)電極に電界を印加しない以外
は実施例1と同じ条件でオゾン水を通水し、排出口6で
の溶存オゾン濃度の経時変化を測定した。結果を(表
1)に示す。(Example 2) Ozone water was passed under the same conditions as in Example 1 except that no electric field was applied to the electrodes, and the change with time of the dissolved ozone concentration at the outlet 6 was measured. The results are shown in (Table 1).
【0015】(比較例1)撹拌羽2と外壁3を形成する
電極材料をオゾン分解触媒能を持たないステンレスに替
え、印加電圧を8ボルトとして実施例1と同様の条件で
通水し、排出口6での溶存オゾン濃度を測定した結果を
(表1)に示す。(Comparative Example 1) The electrode material forming the stirring blade 2 and the outer wall 3 was changed to stainless steel having no ozone decomposition catalytic ability, water was passed under the same conditions as in Example 1 with an applied voltage of 8 V, and then discharged. The results of measuring the dissolved ozone concentration at the outlet 6 are shown in (Table 1).
【0016】(比較例2)電界を印加しない状態で比較
例1と同様の条件で通水を行い、排出口6での溶存オゾ
ン濃度を測定した。結果を(表1)に示す。Comparative Example 2 Water was passed under the same conditions as in Comparative Example 1 without applying an electric field, and the concentration of dissolved ozone at the outlet 6 was measured. The results are shown in (Table 1).
【0017】[0017]
【表1】 [Table 1]
【0018】(表1)に示すように、実施例1の条件が
最も効果的にオゾンを分解し、以下実施例2,比較例
1,比較例2の順に残存オゾン量が増加する。As shown in (Table 1), the conditions of Example 1 decompose ozone most effectively, and the residual ozone amount increases in the order of Example 2, Comparative Example 1 and Comparative Example 2 below.
【0019】なお、本実施例ではオゾン分解触媒として
Co酸化物について説明したが、Ptや活性炭などのオ
ゾン分解触媒を用いても同様の効果が得られる。In the present embodiment, the Co oxide was explained as the ozone decomposition catalyst, but the same effect can be obtained by using an ozone decomposition catalyst such as Pt or activated carbon.
【0020】[0020]
【発明の効果】以上の実施例の説明からも明らかなよう
に、本発明によれば、オゾン分解触媒で構成された電極
に電界を印加しながら通水することによりオゾン分解触
媒の活性が向上し、通水直後から長時間にわたり安定し
て、溶存オゾンをほぼ安全に分解することが可能であ
る。As is apparent from the above description of the embodiments, according to the present invention, the activity of the ozone decomposition catalyst is improved by passing water while applying an electric field to the electrode composed of the ozone decomposition catalyst. However, it is possible to decompose dissolved ozone almost safely from immediately after passing water for a long time.
【図1】本発明の水中溶存オゾン分解装置の構成図FIG. 1 is a block diagram of an apparatus for decomposing dissolved ozone in water according to the present invention.
1 導入口 2 撹拌羽 3 外壁 4 電源 5 リード線 6 排出口 7 容器 1 inlet 2 stirring blade 3 outer wall 4 power supply 5 lead wire 6 outlet 7 container
Claims (2)
オゾン水導入口と、前記容器の上部に設けた排出口と、
前記容器の内部に設けた撹拌羽および外壁と、前記容器
の外側に配設され、前記撹拌羽と外壁に電気的に接続さ
れた電源とを備え、前記撹拌羽と外壁を電極として電圧
を印加しながら、前記導入口からオゾン水を導入し、オ
ゾン水を電気分解して排出口より排出する水中溶存オゾ
ン分解装置。1. An ozone water inlet provided in a lower portion of an electrically insulating container, and an outlet provided in an upper portion of the container,
An agitation blade and an outer wall provided inside the container, and a power source disposed outside the container and electrically connected to the agitation blade and the outer wall, and a voltage is applied using the agitation blade and the outer wall as electrodes. Meanwhile, an apparatus for decomposing dissolved ozone in water, which introduces ozone water from the inlet, electrolyzes the ozone water and discharges it from the outlet.
てなる請求項1記載の水中溶存オゾン分解装置。2. The water-dissolved ozone decomposing apparatus according to claim 1, wherein the stirring blade and the outer wall are constituted by an ozone decomposing catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19930691A JPH0550074A (en) | 1991-08-08 | 1991-08-08 | Decomposition apparatus of ozone dissolved in water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19930691A JPH0550074A (en) | 1991-08-08 | 1991-08-08 | Decomposition apparatus of ozone dissolved in water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0550074A true JPH0550074A (en) | 1993-03-02 |
Family
ID=16405610
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19930691A Pending JPH0550074A (en) | 1991-08-08 | 1991-08-08 | Decomposition apparatus of ozone dissolved in water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0550074A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6751174B1 (en) | 1999-08-31 | 2004-06-15 | Matsushita Electric Industrial Co., Ltd. | Disc reproducing system |
-
1991
- 1991-08-08 JP JP19930691A patent/JPH0550074A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6751174B1 (en) | 1999-08-31 | 2004-06-15 | Matsushita Electric Industrial Co., Ltd. | Disc reproducing system |
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