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JPS602058B2 - Sterilization, deodorization, anti-mold equipment - Google Patents
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JPS602058B2 - Sterilization, deodorization, anti-mold equipment - Google Patents

Sterilization, deodorization, anti-mold equipment

Info

Publication number
JPS602058B2
JPS602058B2 JP55066672A JP6667280A JPS602058B2 JP S602058 B2 JPS602058 B2 JP S602058B2 JP 55066672 A JP55066672 A JP 55066672A JP 6667280 A JP6667280 A JP 6667280A JP S602058 B2 JPS602058 B2 JP S602058B2
Authority
JP
Japan
Prior art keywords
ozone
electrode
sterilization
deodorization
water supply
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
Application number
JP55066672A
Other languages
Japanese (ja)
Other versions
JPS56163657A (en
Inventor
常義 大橋
賢二 大森
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP55066672A priority Critical patent/JPS602058B2/en
Publication of JPS56163657A publication Critical patent/JPS56163657A/en
Publication of JPS602058B2 publication Critical patent/JPS602058B2/en
Expired legal-status Critical Current

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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【発明の詳細な説明】 オゾンによる殺菌、殺藻、防轍効果や脱臭効果は古くか
ら知られている。
[Detailed Description of the Invention] The sterilizing, algaecide, rut-preventing, and deodorizing effects of ozone have been known for a long time.

従ってオゾンを使用している範囲も広く、例えば病院、
公共施設、劇場、食堂、銭湯等では便所、待合室、診察
室、教室、集会室、旅館、理容室、調理給食室「プール
、浴室、脱衣室等の殺菌、脱臭に、食品、酪農、肥料工
場や農業関係等ではカピ防止、防虫と酸素補給に、また
畜産、漁業関係では畜舎から終末処理場に至る全処理室
、冷凍および冷蔵設備、冷蔵庫、貯蔵庫等の殺菌、殺藻
、脱臭、防虫および肉類、魚類、野菜、果物等生鮮食品
の鮮度保持に、さらには解凍機等の浄水殺菌、高架水槽
内の飲料水の殺菌、殺藻等極めて多岐にわたっている。
しかるに従釆の電極板は本発明のようなくわ状または長
方形打抜きの形状ではなく、単なる一枚の平板状をして
いたから、相対する極板間で無声放電を起す個所は平板
の周縁に片寄り勝ちになるため、放電量すなわちオゾン
の発生量が少なく、前記の各分野に使用してもその効果
は余り期待できなかった。本発明は従来品とほぼ同一の
規模でオゾン濃度が10倍のオゾンおよびその溶解水を
得ることを目的としたもので、社会に益するところ極め
て大である。
Therefore, ozone is used in a wide range of areas, such as hospitals,
For sterilization and deodorization of public facilities, theaters, cafeterias, public baths, etc., toilets, waiting rooms, examination rooms, classrooms, meeting rooms, inns, barber shops, cooking and lunch rooms, swimming pools, bathrooms, changing rooms, etc., food, dairy, fertilizer factories, etc. In the agricultural industry, it is used to prevent mosquitoes, to prevent insects, and to supply oxygen. In the livestock and fisheries industry, it is used to sterilize, algaecide, deodorize, insect repel, and treat all processing rooms from livestock barns to final treatment plants, freezing and refrigeration equipment, refrigerators, storage rooms, etc. It is used in a wide range of applications, including maintaining the freshness of fresh foods such as meat, fish, vegetables, and fruits, purifying and sterilizing water in defrosters, sterilizing drinking water in elevated water tanks, and killing algae.
However, since the sub-electrode plate was not in the shape of a hoe or rectangular punch as in the present invention, but in the form of a single flat plate, the locations where silent discharge occurs between the opposing electrode plates were biased towards the periphery of the flat plate. Because of this, the discharge amount, that is, the amount of ozone generated, is small, and even when used in the above-mentioned fields, little effect could be expected. The purpose of the present invention is to obtain ozone and its dissolved water with an ozone concentration 10 times higher than that of conventional products on a scale similar to that of conventional products, and it is extremely beneficial to society.

以下、本発明の一実施例を図面について説明する。本発
明の構造は、つぎの通りである。
An embodiment of the present invention will be described below with reference to the drawings. The structure of the present invention is as follows.

すなわち、上下に蓋1,2を有しかつ上側方に給水用栓
3、下側方にオゾン熔解水供給用栓4を設けた外筒5内
にドーナツ形のメッシュの細かい気泡細分化網33を若
千枚挿着し、下部側方に複数個の小孔6をうがった有底
内筒7を挿直しかつ該内筒7の上端部8を細くして上蓋
1から突出させるととももこ該1にリリーフする弁27
を設けてなる気液混合装置9、電極板10を窓ぐわまた
は江戸時代の備中ぐわ等のように三乃至四ッ股形状にす
るか「若干個艮方形打抜きにしてその全表面をシリコン
ゴム張りにした放電素子11を、該表面に複数本接着さ
せたスベーサー12を介して股の向きを交互に逆向封こ
し、かつ分れた電極脚13の部分だけが相対するように
二の倍数枚重ね合わせて一体とした放電体11′の同一
の側に突出している電極端子14,15とそれぞれ接続
してその何れか一方を十、他方を−とし、一個のイグナ
ィター(パルストランス)16に配線した無声放電ユニ
ット17を、隣り同士の電極端子が互いに逆極性になる
ようにし、かつ隣り同士の電極板10の間隔が前記のよ
うに重ね合した電極板10の間隔に等しくなるように各
ユニット17を複数個配列してなるオゾナイザ−18と
、以下公知のミクロンフイルター19、レギュレーター
20、プレフィルター21、空気冷却器22およびコン
ブレッサー23を上記の順に直列に配管してある。つぎ
に作動方法について述べる。まず、この実施例ではリリ
ーフ弁27を1.1kg′のにセットし、上端部8に設
けてある開閉用栓24およびオゾン溶解水供給用栓4を
閉にした後、給水用栓3を開いて給水する。外筒5内の
圧力が1.1k9/地に達すると、リリーフ弁27は自
動的に閉じる。そこでオゾナィザー18の電源スイッチ
26を閉にし、内筒上端部8の開閉用栓24を関にした
後、コンブレッサー23を作動させると、該23から通
常45℃で湿度90%、圧力4k9/塊の空気が送り出
される。これをパイプ25にて空気冷却器22に導き、
空気温度を20qC、湿度40%位まで下げた後、塵挨
除去するためのプレフイルター21、圧力を1.2k9
/めまで下げるためのレギュレーター20、水分を完全
に除去するためのミクロンフィルター19を経て空気は
オゾナィザー18に送られる。清浄にして乾燥した空気
は第5図のA矢印方向からB矢印方向へ各放電体11′
の放電素子11,11間をオゾン化されつつ流れ、パイ
プ25によって気液混合装置9に送られる。かくして内
筒7に流入したオゾン化した空気は、該7の膨張により
温度降下を来たすとともに、外筒5内に満された水に触
れる面積が広くなるため、さらに水の温度に近かず〈。
内筒7が前記の空気で満されると下部側方に設けた複数
個の小孔6から気泡となって上述の水中に放出され、か
つ若干個の気泡細分化網33によって気泡は極微状とな
る。これは気液混合の条件が、同温同圧が理想的である
からである。そして20〜40分間経過すると、上記の
空気と水が20qoの場合で、水1そ中に溶解するオゾ
ン化した空気は0.5のこ達し、オゾン濃度も35〜4
肥PMになり、従釆品の4〜蛇PMに比してその1針音
の能力を有するオゾン溶解水が供給用栓4から得られる
。なお、パイプ25の途中から点線で分岐した28は酸
素ボンベで、該28を使用する場合には、ミクロンフィ
ルタ−19からコンブレッサー23までの装置が不要と
なる。使用の一実施例として解凍機等の水処理につき述
べると、第6図に示すように曝気槽29に解凍すべき食
品30を入れて栓4に継がるホース(図示せず)から蟻
気槽29の注水口31を経てオゾン溶解水32を導くと
、該水32は該糟29がラビリンス状になっているため
、該糟内を上下しつつオゾン気泡を放出し、食品30の
完全な殺菌と鮮度保持をすることができる。
That is, inside an outer cylinder 5 which has lids 1 and 2 on the upper and lower sides, and has a water supply tap 3 on the upper side and an ozone dissolution water supply tap 4 on the lower side, there is a donut-shaped mesh fine cell division network 33. The bottomed inner cylinder 7 with a plurality of small holes 6 bored on the sides of the lower part is re-inserted, and the upper end 8 of the inner cylinder 7 is made thinner to protrude from the upper cover 1. Valve 27 that provides relief to said 1
The gas-liquid mixing device 9 and the electrode plate 10 may be made into a three- to four-pronged shape like a window wafer or a Bicchu wafer from the Edo period, or may be punched out into slightly individual rectangular shapes and the entire surface covered with silicone rubber. A plurality of discharge elements 11 are sealed in opposite directions through a plurality of spacers 12 bonded to the surface thereof, and twice as many sheets are stacked so that only the separated electrode legs 13 face each other. They were connected to electrode terminals 14 and 15 protruding from the same side of the integrated discharge body 11', one of which was set to 10 and the other to -, and wired to one igniter (pulse transformer) 16. The silent discharge units 17 are arranged such that adjacent electrode terminals have opposite polarities, and the interval between adjacent electrode plates 10 is equal to the interval between the stacked electrode plates 10 as described above. An ozonizer 18 formed by arranging a plurality of ozonizers, a known micron filter 19, a regulator 20, a pre-filter 21, an air cooler 22, and a compressor 23 are connected in series in the above order.Next, the operating method will be explained. First, in this embodiment, the relief valve 27 is set to 1.1 kg', the opening/closing tap 24 provided at the upper end 8 and the ozone-dissolved water supply tap 4 are closed, and then the water supply tap 3 is closed. When the pressure inside the outer cylinder 5 reaches 1.1k9/ground, the relief valve 27 automatically closes.Then, close the power switch 26 of the ozonizer 18 and open/close the inner cylinder upper end 8. When the compressor 23 is operated after the plug 24 is connected, air is normally sent out from the compressor 23 at a temperature of 45° C., a humidity of 90%, and a pressure of 4k9/block.This is led to the air cooler 22 through a pipe 25.
After lowering the air temperature to 20qC and humidity to about 40%, use a pre-filter 21 to remove dust and reduce the pressure to 1.2k9.
The air is sent to the ozonizer 18 through a regulator 20 to lower the water content to 100%, and a micron filter 19 to completely remove moisture. The clean and dry air flows from the direction of arrow A to the direction of arrow B in each discharge body 11' in Fig. 5.
The gas flows between the discharge elements 11 and 11 while being ozonated, and is sent to the gas-liquid mixing device 9 via the pipe 25. The temperature of the ozonized air that has flowed into the inner cylinder 7 decreases due to the expansion of the inner cylinder 7, and the surface area that comes into contact with the water filled in the outer cylinder 5 increases, so that the temperature of the ozonized air does not approach that of the water.
When the inner cylinder 7 is filled with the air, air bubbles are released into the water from the plurality of small holes 6 provided on the lower side, and the air bubbles are made into extremely fine particles by the air bubble segmentation network 33. becomes. This is because the ideal gas-liquid mixing conditions are the same temperature and pressure. After 20 to 40 minutes have elapsed, in the above case where the air and water are 20 qo, the ozonized air dissolved in 1 water reaches 0.5 qo, and the ozone concentration also reaches 35 to 4 qo.
Ozone-dissolved water is obtained from the supply stopper 4, which becomes fertilizer PM and has the ability of one needle sound compared to the subordinate product 4 to snake PM. Note that 28 branched from the middle of the pipe 25 by a dotted line is an oxygen cylinder, and when this 28 is used, devices from the micron filter 19 to the compressor 23 are not required. Regarding water treatment using a defrosting machine as an example of its use, as shown in FIG. When ozone-dissolved water 32 is led through the water inlet 31 of 29, the water 32 releases ozone bubbles while moving up and down inside the pot, as the pot 29 has a labyrinth shape, completely sterilizing the food 30. and can maintain freshness.

なお、ちなみに本実施例のオゾナィザー18の容量は5
5そ′min、気液混合装置9の容量は66夕にしてあ
り、貯水後使用中は常時1.1k9/地の内圧を保つよ
うに給水用栓3を通して流水を補給する。本考案が何故
このように高濃度のオゾン化ができるのかというと、第
1は前述のように放電体11′の構造を変えて能率向上
を計ったことである。
Incidentally, the capacity of the ozonizer 18 in this example is 5
The capacity of the gas-liquid mixing device 9 is 66 minutes, and after storing water, during use, running water is supplied through the water tap 3 so as to maintain an internal pressure of 1.1 k9/ground at all times. The reason why the present invention is able to generate ozone at such a high concentration is that the first reason is that the structure of the discharge body 11' was changed to improve efficiency as described above.

それは第4図からもわかるように、たとえ電極板の大き
さは同一でも、くわ状に切り込みまたは打抜きをつけた
ため、電子の集まる電極の周縁の長さが二倍以上になり
、かつ、電極胸13の蚤子密度が高まるとともに、それ
を二の倍数枚重ね合せることによってオゾン化効率はさ
らに高まった。また隣り同士の電極板10の間隔を上述
の重ね合せた電極板10の間隔に等しくなるように複数
個配列して隣り同士の間でも放電させるようにしたこと
により、オゾン化は一層向上した。第2はこのオゾン化
空気を気液混合装置9に導き、同温同圧のもとで下方の
小孔6から小気泡として放出させ、かつ若干個の気泡細
分化網33によって気泡を極微状とし、水によく溶解す
るような気液混合機構にしたことである。以上に詳述し
たごとく本発明の装置を使用すれば、上述の諸効果を無
公害のもとで行なうことができるもので、社会に貢献す
ること極めて大である。
As can be seen from Figure 4, even if the size of the electrode plate is the same, the length of the periphery of the electrode, where electrons gather, is more than doubled due to the hoe-shaped cuts or punches, and the length of the electrode plate is more than doubled. As the density of 13 fleas increased, the ozonation efficiency was further increased by stacking double the number of layers. Moreover, ozonation was further improved by arranging a plurality of electrode plates 10 so that the spacing between adjacent electrode plates 10 was equal to the spacing between the stacked electrode plates 10 described above, and discharging even between adjacent electrode plates 10. Second, this ozonized air is introduced into the gas-liquid mixing device 9, where it is released as small bubbles from the small hole 6 at the bottom under the same temperature and pressure, and the bubbles are made into extremely fine particles by a few bubble segmentation networks 33. This is achieved by using a gas-liquid mixing mechanism that dissolves well in water. As described in detail above, by using the apparatus of the present invention, the above-mentioned effects can be achieved without causing any pollution, and it will greatly contribute to society.

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

第1図は本発明の一実施例の系統略図、第2図aはくわ
形電極板、同bは長方形打抜き電極板、第3図は放電体
の側面図、第4図は同平面図、第5図は放電体の配列を
示す平面略図、第6図は魚類解凍の場合の一実施例、第
T図aは窓ぐわ、同bは江戸時代の備中ぐわを示す。 なお、5:外筒、7:内筒、9:気液混合装置、10:
〈わ形電極板、10′:長方形打抜き電極板、11′:
放電体、16:ィグナィター、17:無声放電ユニット
、18:オゾナィザー、19:ミクロンフイルター、2
0:レギュレーター、21:プレフイルタ−、22:空
気冷却器、23:コンブレッサー、28:酸素ボンベ、
27:リリーフ弁、29:曝気槽、33:気泡細分化網
。 汐了図 汐Z鰯 グ3図 傘4図 メタ図 が3図 矛7図
Fig. 1 is a schematic system diagram of an embodiment of the present invention, Fig. 2a is a hoe-shaped electrode plate, Fig. 2b is a rectangular punched electrode plate, Fig. 3 is a side view of the discharge body, Fig. 4 is a plan view thereof, FIG. 5 is a schematic plan view showing the arrangement of the discharge bodies, FIG. 6 is an example of defrosting fish, FIG. In addition, 5: outer cylinder, 7: inner cylinder, 9: gas-liquid mixing device, 10:
<Raw-shaped electrode plate, 10': Rectangular punched electrode plate, 11':
Discharge body, 16: Igniter, 17: Silent discharge unit, 18: Ozonizer, 19: Micron filter, 2
0: Regulator, 21: Prefilter, 22: Air cooler, 23: Compressor, 28: Oxygen cylinder,
27: relief valve, 29: aeration tank, 33: bubble segmentation network. 3 figures, 3 figures, 4 figures, meta diagrams, 7 figures, 7 figures.

Claims (1)

【特許請求の範囲】[Claims] 1 上下に蓋1,2を有しかつ上側方に給水用栓3下側
方にオゾン溶解水供給用栓4を設けた外筒5内にドーナ
ツ形のメツシユの細かい気泡細分化網33を若干枚挿着
し、下部側方に複数個の小孔6をうがった有底内筒7を
挿置しかつ該内筒7の上端部8を細くして上蓋1から突
出させるとともに、該1にリリーフする弁27を設けて
なる気液混合装置9と、電極板10を窓ぐわまたは江戸
時代の備中ぐわ等のように三乃至四ツ股形状にするか若
干個長方形打抜きにしてその全表面をシリコンゴム張り
にした放電素子11を、該表面に複数本接着させたスペ
ーサー12を介して股の向きを交互に逆向きにし、かつ
分れた電極脚13の部分だけが対するように二の倍数枚
重ね合わせて一体とした放電体11の同一の側に突出し
ている電極端子14,15をそれぞれ接続してその何れ
か一方を+、他方を−とし、一個のイグナイター16に
配線した無声放電ユニツト17を、隣り同士の電極端子
が互いに逆極性になるようにし、かつ隣り同士の電極板
10の間隔が前記のように重ね合せた電極板10の間隔
に等しくなるように各ユニツト17を複数個配列してな
るオゾナイザー18と、以下公知のミクロンフイルター
19、レギユレーター20、プレフイルター21、空気
冷却器22、およびコンプレツサー23を上記の順に直
列に配管してなる空気送入装置との一連操作により、オ
ゾン濃度の高いオゾン溶解水を得て、これを上記気液混
合装置9の下部溶解水供給用栓4から配管を通して所要
の殺菌、脱臭、防黴域に供給し、各オゾン気泡を放出せ
しめて所期の殺菌、脱臭、防黴を果すようにした殺菌、
脱臭、防黴装置。
1. Inside the outer cylinder 5, which has lids 1 and 2 on the top and bottom and has a water supply tap 3 on the upper side and an ozone-dissolved water supply tap 4 on the lower side, a donut-shaped mesh fine bubble segmentation network 33 is installed. A bottomed inner cylinder 7 with a plurality of small holes 6 bored on the lower side is inserted, and the upper end 8 of the inner cylinder 7 is made thin to protrude from the upper lid 1. The gas-liquid mixing device 9 is equipped with a relief valve 27, and the electrode plate 10 is formed into a three- or four-pronged shape like a window wafer or a Bicchu wafer from the Edo period, or is punched out into rectangular pieces and its entire surface is Discharge elements 11 covered with silicone rubber are alternately turned in opposite directions via a plurality of spacers 12 bonded to the surface thereof, and the electrode legs 13 are arranged in multiples of two so that only the separated electrode legs 13 face each other. A silent discharge unit in which the electrode terminals 14 and 15 protruding from the same side of the discharge body 11 stacked one on top of the other are connected, one of them is set as + and the other as -, and wired to one igniter 16. A plurality of each unit 17 are arranged so that adjacent electrode terminals have opposite polarities and the interval between adjacent electrode plates 10 is equal to the interval between the electrode plates 10 stacked as described above. Through a series of operations of the ozonizer 18 arranged in the array and an air supply device formed by piping a known micron filter 19, regulator 20, prefilter 21, air cooler 22, and compressor 23 in series in the above order, Ozone dissolved water with a high ozone concentration is obtained, and this is supplied from the lower dissolved water supply tap 4 of the gas-liquid mixing device 9 to the required sterilization, deodorization, and anti-mold areas through piping, and each ozone bubble is released. Sterilization that achieves the desired sterilization, deodorization, and anti-mold effects,
Deodorizing and anti-mold equipment.
JP55066672A 1980-05-20 1980-05-20 Sterilization, deodorization, anti-mold equipment Expired JPS602058B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55066672A JPS602058B2 (en) 1980-05-20 1980-05-20 Sterilization, deodorization, anti-mold equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55066672A JPS602058B2 (en) 1980-05-20 1980-05-20 Sterilization, deodorization, anti-mold equipment

Publications (2)

Publication Number Publication Date
JPS56163657A JPS56163657A (en) 1981-12-16
JPS602058B2 true JPS602058B2 (en) 1985-01-18

Family

ID=13322629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55066672A Expired JPS602058B2 (en) 1980-05-20 1980-05-20 Sterilization, deodorization, anti-mold equipment

Country Status (1)

Country Link
JP (1) JPS602058B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58159898A (en) * 1982-03-18 1983-09-22 Mitsubishi Electric Corp Air diffuser
JPS62151999U (en) * 1986-03-20 1987-09-26

Also Published As

Publication number Publication date
JPS56163657A (en) 1981-12-16

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