JP3255488B2 - Ozone decomposition method - Google Patents

Ozone decomposition method

Info

Publication number
JP3255488B2
JP3255488B2 JP11092993A JP11092993A JP3255488B2 JP 3255488 B2 JP3255488 B2 JP 3255488B2 JP 11092993 A JP11092993 A JP 11092993A JP 11092993 A JP11092993 A JP 11092993A JP 3255488 B2 JP3255488 B2 JP 3255488B2
Authority
JP
Japan
Prior art keywords
ozone
wavelength
oxygen
singlet oxygen
light
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
Application number
JP11092993A
Other languages
Japanese (ja)
Other versions
JPH06296823A (en
Inventor
正 持麾
Original Assignee
正 持麾
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 正 持麾 filed Critical 正 持麾
Priority to JP11092993A priority Critical patent/JP3255488B2/en
Priority to PCT/JP1994/000580 priority patent/WO1994024043A1/en
Priority to AU64369/94A priority patent/AU6436994A/en
Priority to CN94190201A priority patent/CN1037426C/en
Priority to TW83104470A priority patent/TW290526B/zh
Publication of JPH06296823A publication Critical patent/JPH06296823A/en
Application granted granted Critical
Publication of JP3255488B2 publication Critical patent/JP3255488B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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  • Treating Waste Gases (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は高濃度のオゾンを利用し
て、空気の殺菌、水の殺菌あるいは或る物質の表面活性
化を行う際、紫外線の照射によって発生する残留オゾン
を分解する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing residual ozone generated by irradiation with ultraviolet rays when disinfecting air, disinfecting water, or activating a certain substance using high-concentration ozone. About.

【0002】[0002]

【従来の技術】従来のオゾンの分解方法としては、オゾ
ンを活性炭に吸着させる活性炭吸着方法、熱によってオ
ゾンを分解する熱分解方法および触媒による分解方法が
知られている。
2. Description of the Related Art As conventional methods for decomposing ozone, there are known an activated carbon adsorption method for adsorbing ozone to activated carbon, a thermal decomposition method for decomposing ozone by heat, and a decomposition method using a catalyst.

【0003】[0003]

【発明が解決しようとする課題】しかし、高濃度のオゾ
ンを利用して、空気の殺菌、水の殺菌あるいは或る物質
の表面活性化を行う際に照射される紫外線によって発生
する残留オゾンの処理方法としては、前記した従来の活
性炭吸着方法、熱分解方法および触媒による分解方法を
用いるのは大容量のオゾンを分解するのには不適切であ
り、未だ適切な処理方法がないためにオゾンの高度利用
の大きな障壁となっていた。
However, treatment of residual ozone generated by ultraviolet rays irradiated when sterilizing air, disinfecting water, or activating a certain substance using high concentration ozone. As the method, the above-mentioned conventional activated carbon adsorption method, thermal decomposition method and decomposition method using a catalyst are not suitable for decomposing a large amount of ozone, and there is no appropriate treatment method. It was a major barrier to advanced use.

【0004】本発明は前記した問題点を解決せんとする
もので、その目的とするところは、オゾンが気相、液相
の如何を問わず分解して基底状態酸素に還元すると共に
殺菌を行うことによって空調のダクト内、ビル内の空気
の無菌化と、溶存酸素の高い無菌の水を供給することが
できるオゾンの分解方法を提供せんとするにある。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and has an object to ozone decompose irrespective of a gaseous phase or a liquid phase to reduce it to ground state oxygen and sterilize it. Accordingly, an object of the present invention is to provide a method of decomposing ozone, which can sterilize air in a duct for air conditioning and a building and supply sterile water having high dissolved oxygen.

【0005】[0005]

【課題を解決するための手段】本発明のオゾンの分解方
法は前記した目的を達成せんとするものであり、その手
段は、オゾンに波長240nm〜310nmの紫外線を
照射して一重項酸素を生成させた後、波長600nm〜
650nmの可視光線と波長1200nm〜1300n
mの近赤外線を照射して、オゾンが一重項酸素を経て電
磁波の誘導放出を行いながら、基底状態酸素に遷移させ
ることを特徴とする。
SUMMARY OF THE INVENTION The object of the present invention is to provide a method for decomposing ozone, which comprises irradiating ozone with ultraviolet light having a wavelength of 240 nm to 310 nm to produce singlet oxygen. After the
650nm visible light and wavelength 1200nm-1300n
m is irradiated with near-infrared rays, and the ozone undergoes a transition to ground state oxygen while stimulated emission of electromagnetic waves via singlet oxygen.

【0006】また本発明のオゾンの分解方法は、オゾン
に波長240nm〜310nmの紫外線レーザを照射し
て一重項酸素を生成させた後、波長600nm〜650
nmの可視光レーザ光および波長1200nm〜130
0nmの赤外線レーザ光を照射し、オゾンが一重項酸素
を経て電磁波の誘導放出を促進させながら、基底状態酸
素に遷移させることを特徴とするものである。
In the method for decomposing ozone according to the present invention, after irradiating ozone with an ultraviolet laser having a wavelength of 240 nm to 310 nm to generate singlet oxygen, a wavelength of 600 nm to 650 is obtained.
nm visible light laser light and a wavelength of 1200 nm to 130 nm
Irradiation with an infrared laser beam of 0 nm causes ozone to transition to ground state oxygen while promoting stimulated emission of electromagnetic waves via singlet oxygen.

【0007】[0007]

【作用】前記した如く方法による本発明のオゾンの分解
方法は、オゾン気相単体、空気とオゾンの混合気体、水
中に溶存するオゾン、あるいは水中に微細気泡となって
存在するオゾンに、240nm〜310nmの波長を持
つ紫外線を照射すると、 O3 +hυ(240nm〜310nm)→21 Δg+ 1
D すなわち、1重項酸素分子21 Δgと1重項酸素原子 1
Dとを生成する。
As described above, the method of decomposing ozone according to the present invention according to the present invention can be applied to the ozone gas phase alone, a mixed gas of air and ozone, ozone dissolved in water, or ozone present as fine bubbles in water, at a wavelength of 240 nm or less. When irradiating ultraviolet light having a wavelength of 310 nm, O 3 + hυ (240 nm to 310 nm) → 2 1 Δg + 1
D That is, a singlet oxygen molecule 2 1 Δg and a singlet oxygen atom 1
And D.

【0008】そして、紫外線の吸収によって励起された
1重項酸素分子は、波長600nm〜650nmの可視
光線が照射されると、1 D+hυ(600nm〜650nm)→2 3Σg すなわち、光子の誘導放出と共に基底酸素状態の分子2
3 Σgへと遷移する。
[0008] Then, singlet oxygen molecules excited by the absorption of ultraviolet light, the visible light wavelength 600Nm~650nm is irradiated, 1 D + hυ (600nm~650nm) → 2 3 Σg other words, the photon stimulated emission Molecule 2 in basal oxygen state
Transition to 3 Σg.

【0009】さらに、一重項酸素原子 1Dに波長120
0nm〜1300nmの近赤外線を照射すると、1 D+hυ(1200nm〜1300nm)→ 3Σg すなわち、基底酸素状態の原子 3Σgに遷移し、分解す
るものである。
Furthermore, wavelength singlet oxygen 1 D 120
When irradiated with near-infrared 0nm~1300nm, 1 D + hυ (1200nm~1300nm ) → 3 Σg i.e., a transition to the atoms 3 Shigumag basal oxygen conditions, it is intended to decomposition.

【0010】[0010]

【実施例】次に、本発明の実施の一例をオゾンと空気の
混合気体を分解するオゾン分解方法とその装置につい
て、以下に説明する。この方法および装置(図1)にお
いては、予めオゾンと空気の混合気体を人為的に生成し
ておいて、これに254nmの紫外線、633nmの可
視光線、さらには1270nmの近赤外線が照射されて
いる光帯を有する室内を通過させるものである。
Next, an embodiment of the present invention will be described below with reference to an ozone decomposing method for decomposing a mixed gas of ozone and air and an apparatus therefor. In this method and apparatus (FIG. 1), a gas mixture of ozone and air is artificially generated in advance, and irradiated with ultraviolet light of 254 nm, visible light of 633 nm, and near infrared light of 1270 nm. It passes through a room having a light band.

【0011】この装置は、エアーブロア1から送り込ま
れた空気はオゾン発生筒2の上部内に送り込まれるが、
このオゾン発生室2においては送り込まれた空気にオゾ
ン発生ランプ3の光線を照射し、送り込まれた空気がオ
ゾン発生室2の下部に到達した場合には、その一部がオ
ゾン4となる。
In this apparatus, the air sent from the air blower 1 is sent into the upper part of the ozone generating cylinder 2,
In the ozone generation chamber 2, the sent air is irradiated with a light beam from an ozone generation lamp 3. When the sent air reaches the lower part of the ozone generation chamber 2, a part of the air becomes ozone 4.

【0012】このオゾン4は、下部連通管5を通って1
重項酸素発生筒6に送り込まれ、紫外線照射管7により
波長253.7nmの紫外線が照射されて、オゾン4は
1重項酸素8を生成する。
The ozone 4 passes through the lower communication pipe 5 and
The ozone 4 is sent to the singlet oxygen generating cylinder 6 and irradiated with ultraviolet rays having a wavelength of 253.7 nm by the ultraviolet irradiation tube 7, so that the ozone 4 generates singlet oxygen 8.

【0013】この1重項酸素8は、さらに上部連通管9
を通って誘導放出分解筒10に送り込まれるが、この誘
導放出分解筒10は内面に鏡11が張られると共に波長
633nmの可視光He−Neレーザ12を光ファイバ
で導いて、プリズム13を通して照射することによって
生ずる光膜14が形成されている。
The singlet oxygen 8 is further supplied to the upper communication pipe 9
Through which the visible light He-Ne laser 12 having a wavelength of 633 nm is guided by an optical fiber and radiated through the prism 13. The resulting optical film 14 is formed.

【0014】さらに、この誘導放出分解筒10の下部に
は、波長1270nmの近赤外線を照射するレーザ光1
5からの近赤外線を光ファイバで導いて、プリズム16
を通して鏡11に照射することによって生じる光膜16
が形成されている。
Further, a laser beam 1 for irradiating near-infrared light having a wavelength of 1270 nm is provided below the stimulated emission decomposition tube 10.
The near-infrared rays from 5 are guided by an optical fiber,
Film 16 generated by irradiating mirror 11 through
Are formed.

【0015】従って、前記の誘導放出分解筒10に送り
込まれた1重項酸素8は、最初の光膜14を通過する際
に電磁波の誘導放出をを行って基底状態酸素に分解した
後、その下側に設けられた光膜16を通過する際に励起
酸素は完全に安定な基底状態の酸素17となって、下部
吐出口18から放出される。
Therefore, the singlet oxygen 8 sent to the stimulated emission decomposing cylinder 10 is subjected to stimulated emission of electromagnetic waves when passing through the first optical film 14 to be decomposed into ground state oxygen. When passing through the optical film 16 provided on the lower side, the excited oxygen becomes completely stable ground state oxygen 17 and is released from the lower discharge port 18.

【0016】このオゾンの基底状態の酸素17への遷移
を監視するために、各連通管5,9,18にオゾン濃度
計21,22,23を挿入し、モニタ20でオゾン濃度
の測定を行った。この時の室温18°C、各連通管5,
9,18における通過量は2リットル/分、オゾン濃度
計としてはオクトロニクス株式会社製のOZM−21−
2〜200型の気相用を用いた。
In order to monitor the transition of the ozone to the oxygen 17 in the ground state, ozone concentration meters 21, 22, and 23 are inserted into the communication tubes 5, 9, and 18, and the monitor 20 measures the ozone concentration. Was. At this time, the room temperature was 18 ° C.
The passing rate at 9 and 18 was 2 liters / minute, and as an ozone concentration meter, OZM-21 manufactured by Octronics Co., Ltd. was used.
A 2-200 type gas phase was used.

【0017】この時の各オゾン濃度計21,22,23
における濃度の測定値は下表の通りである。
At this time, each ozone concentration meter 21, 22, 23
The measured values of the concentration in are shown in the table below.

【表1】 [Table 1]

【0017】さらに、水中に溶存しているオゾン、もし
くは水中に微細気泡となって存在するオゾンを分解する
オゾンの分解方法と、その装置(図2)を第2実施例と
して次に説明する。予め溶存するオゾンの濃度が判って
いる溶存オゾン水31が下部入り口33から送り込まれ
る円筒形の筒32は、光ファイバー35によって導かれ
た波長254nmの紫外線を筒32の内側に張ってある
鏡34に、プリズム36によって拡張して照射して光膜
37を形成する。
Next, a method of decomposing ozone dissolved in water or ozone present as fine bubbles in water and an apparatus thereof (FIG. 2) will be described as a second embodiment. The cylindrical tube 32 into which the dissolved ozone water 31 whose concentration of dissolved ozone is known in advance is sent from the lower entrance 33 is directed to the mirror 34 extending the inside of the tube 32 with the ultraviolet light having a wavelength of 254 nm guided by the optical fiber 35. The optical film 37 is formed by expanding and irradiating with the prism 36.

【0018】筒32には、この光膜37の上側に、前記
と同様にして波長633nmの可視光線の光膜38を形
成し、さらに、この光膜38の上側に、近赤外線を放出
するレーザ光の波長1270nmの近赤外線により、前
記と同様にして光膜39を形成する。
On the tube 32, a light film 38 of visible light having a wavelength of 633 nm is formed above the light film 37 in the same manner as described above, and a laser emitting near-infrared light is formed above the light film 38. The optical film 39 is formed in the same manner as described above using near-infrared light having a wavelength of 1270 nm.

【0019】従って、筒32の下部の入り口33から筒
32内に送り込まれた溶存オゾン水31は光膜37,3
8,39を順次に通過して、筒32の上部からオーバー
フローさせるものであるが、これらの光膜37,38,
39を通過する際に、前実施例と同様な作用を受け、1
重項状態の酸素を経て安定した基底状態の酸素となるも
のである。
Therefore, the dissolved ozone water 31 sent into the cylinder 32 from the entrance 33 at the lower part of the cylinder 32 is applied to the optical films 37 and 3.
8 and 39 are sequentially passed and overflow from the upper part of the tube 32.
When passing through 39, the same action as in the previous embodiment is effected.
It is stable oxygen in the ground state via oxygen in the multiplet state.

【0020】この時の筒32の上部でオーバーフローす
る際の残留オゾンの量を測定するために、筒32の上部
40に溶存オゾンセンサ41を設置し、この溶存オゾン
センサ41が捕らえた溶存オゾンの量をモニタ42で測
定した。この時の通過水量は1リットル/分、水温は1
6°C、溶存オゾン計はバイオニクス機器株式会社製の
隔膜ポーロラグラフ方式/モデル0C−100である。
At this time, in order to measure the amount of residual ozone at the time of overflow at the upper part of the cylinder 32, a dissolved ozone sensor 41 is installed at the upper part 40 of the cylinder 32, and the dissolved ozone sensor 41 captures the dissolved ozone. The amount was measured on the monitor 42. At this time, the passing water volume is 1 liter / min, and the water temperature is 1
At 6 ° C., the dissolved ozone meter is a diaphragm polarographic system / model 0C-100 manufactured by Bionics Instruments.

【0021】この測定結果を次表に示す。The results of the measurement are shown in the following table.

【表2】 [Table 2]

【0022】前記第2実施例の発明は、前記各実施例の
波長253.6nmの紫外線を照射する紫外線照射管7
を、240nm〜310nmの紫外線レーザに、また、
波長633nmの可視光He−Neレーザ12を可視光
線レーザに、さらに、波長1270nmのレーザ光15
を近赤外線レーザに替えるもので、これにより前記各実
施例と同様な作用効果を生ずるものである。
The invention of the second embodiment is different from the ultraviolet irradiation tube 7 of the above-described embodiments for irradiating ultraviolet rays having a wavelength of 253.6 nm.
To an ultraviolet laser of 240 nm to 310 nm,
The visible light He-Ne laser 12 having a wavelength of 633 nm is used as a visible light laser, and the laser light 15 having a wavelength of 1270 nm is used.
Is replaced by a near-infrared laser, which produces the same operation and effect as the above-described embodiments.

【0023】なお、前記した2つの実施例にあっては、
可視光線照射と近赤外線照射の2つを順次行うものにつ
いて説明したが、いずれか一方のみの照射を行っても溶
存オゾンを分解することができる。もちろん、この場
合、可視光線照射と近赤外線照射の2つを行った方が、
分解効率は高いものである。
In the above two embodiments,
Although the description has been given of the case where the irradiation of visible light and the irradiation of near-infrared light are sequentially performed, the dissolved ozone can be decomposed even if irradiation of only one of them is performed. Of course, in this case, it is better to perform both visible light irradiation and near infrared irradiation.
The decomposition efficiency is high.

【0024】[0024]

【発明の効果】本発明は前記したように、光子の誘導放
出により励起された酸素が、基底状態への遷移で分解す
るオゾンの分解方法であり、オゾンが気相、液相の何れ
を問わず、分解することが可能である。
As described above, the present invention relates to a method for decomposing ozone in which oxygen excited by stimulated emission of photons is decomposed by transition to a ground state. Can be disassembled.

【0024】この分解方法においては、従来の熱分解方
法、触媒による分解方法および活性炭吸着方法等とは異
なり、分解過程において1重項酸素を経て基底状態酸素
に分解するために、酸素が蘇り、空気が無菌化されると
同時に殺菌され、従って、空調のダクト、もしくは空気
清浄器として組み込むことにより、現在問題となってい
る病院内感染はもとより、ビル内の空気の無菌化が達成
される。
In this decomposition method, unlike conventional thermal decomposition methods, catalytic decomposition methods and activated carbon adsorption methods, etc., oxygen is revived because it is decomposed into ground state oxygen via singlet oxygen in the decomposition process. The air is sterilized and sterilized at the same time, so by incorporating it as an air conditioning duct or air purifier, the sterilization of air in buildings as well as hospital infections, which are currently a problem, is achieved.

【0025】また、溶存オゾン水も同様に分解し、溶存
オゾンによる弊害がなくなり、養殖魚介はもとより、病
院の手洗い水、食品加工水、飲料水、井戸水等を安全な
水に変えて供給することが可能になる等の効果を有する
ものである。
In addition, dissolved ozone water is similarly decomposed, and the harm caused by dissolved ozone is eliminated, and it is necessary to supply not only cultured fish and shellfish but also hospital hand washing water, food processing water, drinking water, well water and the like to safe water. And the like.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の第1実施例の装置の断面図であるもの
である。
FIG. 1 is a sectional view of an apparatus according to a first embodiment of the present invention.

【図2】本発明の第2実施例の装置の断面図である。FIG. 2 is a sectional view of an apparatus according to a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

2 オゾン発生筒 3 オゾン発生ランプ 6 1重項酸素発生筒 7 紫外線照射管 10 誘導放出分解筒 12 可視光He−Neレーザ 14 可視光線の光膜 17 基底状態の酸素 31 溶存オゾン水 32 筒 37 紫外線の光膜 38 可視光線の光膜 39 近赤外線の光膜 2 Ozone generating tube 3 Ozone generating lamp 6 Singlet oxygen generating tube 7 UV irradiation tube 10 Stimulated emission decomposition tube 12 Visible light He-Ne laser 14 Visible light film 17 Oxygen in ground state 31 Dissolved ozone water 32 tube 37 UV Light film 38 Visible light film 39 Near infrared light film

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 オゾンに波長240nm〜310nmの
紫外線を照射して一重項酸素を生成させた後、波長60
0nm〜650nmの可視光線と波長1200nm〜1
300nmの近赤外線を照射して、オゾンが一重項酸素
を経て電磁波の誘導放出を行いながら、基底状態酸素に
遷移させることを特徴とするオゾンの分解方法。
After irradiating ozone with ultraviolet rays having a wavelength of 240 nm to 310 nm to generate singlet oxygen, a wavelength of 60 nm is obtained.
Visible light of 0 nm to 650 nm and wavelength of 1200 nm to 1
A method for decomposing ozone, which comprises irradiating near-infrared rays of 300 nm, and causing ozone to undergo a stimulated emission of electromagnetic waves via singlet oxygen, while transiting to ground state oxygen.
【請求項2】 オゾンに波長240nm〜310nmの
紫外線レーザを照射して一重項酸素を生成させた後、波
長600nm〜650nmの可視光レーザ光および波長
1200nm〜1300nmの赤外線レーザ光を照射
し、オゾンが一重項酸素を経て電磁波の誘導放出を促進
させながら、基底状態酸素に遷移させることを特徴とす
るオゾンの分解方法。
2. Ozone is irradiated with an ultraviolet laser having a wavelength of 240 nm to 310 nm to generate singlet oxygen, and then irradiated with a visible light laser light having a wavelength of 600 nm to 650 nm and an infrared laser light having a wavelength of 1200 nm to 1300 nm. Characterized in that a transition to ground state oxygen is made while promoting stimulated emission of electromagnetic waves via singlet oxygen.
JP11092993A 1993-04-14 1993-04-14 Ozone decomposition method Expired - Fee Related JP3255488B2 (en)

Priority Applications (5)

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JP11092993A JP3255488B2 (en) 1993-04-14 1993-04-14 Ozone decomposition method
PCT/JP1994/000580 WO1994024043A1 (en) 1993-04-14 1994-04-07 Method and apparatus for ozone decomposition by stimulated emission of electromagnetic wave
AU64369/94A AU6436994A (en) 1993-04-14 1994-04-07 Method and apparatus for ozone decomposition by stimulated emission of electromagnetic wave
CN94190201A CN1037426C (en) 1993-04-14 1994-04-07 Method and apparatus for ozone decomposition by stimulated emission of electromagnetic wave
TW83104470A TW290526B (en) 1993-04-14 1994-05-17

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DE19746930A1 (en) 1997-10-23 1999-04-29 Eco Computer Zubehoer Gmbh Process for improving the biological properties of water, edible oils, and fuels especially by oxygen enrichment
KR100367371B1 (en) * 2000-06-08 2003-01-10 유병호 Device For Manufacturing The Ozone Water
JP2006002232A (en) * 2004-06-18 2006-01-05 Shimizu Densetsu Kogyo Kk Washing drying method and washing drying device
JP5100473B2 (en) * 2008-03-31 2012-12-19 古河電気工業株式会社 Singlet oxygen generator
CN114569779B (en) * 2022-03-17 2024-08-30 深圳市晶宏照明有限公司 Disinfection method, disinfection device and computer readable storage medium

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