JP2002028403A - Gas-liquid separator in ozone water rpoducer - Google Patents
Gas-liquid separator in ozone water rpoducerInfo
- Publication number
- JP2002028403A JP2002028403A JP2000217888A JP2000217888A JP2002028403A JP 2002028403 A JP2002028403 A JP 2002028403A JP 2000217888 A JP2000217888 A JP 2000217888A JP 2000217888 A JP2000217888 A JP 2000217888A JP 2002028403 A JP2002028403 A JP 2002028403A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- ozone
- ozone water
- water
- water tank
- 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】本発明はオゾン水生成器におけるオゾンガ
スとオゾン水とを分離する気液分離装置に関する。The present invention relates to a gas-liquid separator for separating ozone gas and ozone water in an ozone water generator.
【０００２】[0002]
【従来技術】一般に、オゾン水生成器は水道水等にオゾ
ンガスを溶解させてオゾン水を生成するもので、オゾン
水生成器から排出されたオゾン水は、病院の医療器具や
野菜、果物等の生鮮食品や厨房の備品、食器などの洗
浄、消毒、消臭等の用途に使用される。オゾン水は消
毒、消臭等には有効であるが、オゾンガスは健康上好ま
しくないと言われているので、水道水等にオゾンガスを
溶解させた後、溶解せずに余った余剰オゾンガスとオゾ
ン水とは完全に分離してオゾン水のみを排出する必要が
ある。2. Description of the Related Art Generally, an ozone water generator dissolves ozone gas in tap water or the like to generate ozone water, and ozone water discharged from the ozone water generator is used for hospital medical equipment, vegetables, fruits and the like. It is used for washing, disinfecting, deodorizing fresh foods, kitchen equipment, tableware, etc. Although ozone water is effective for disinfection and deodorization, it is said that ozone gas is not desirable for health, so after dissolving ozone gas in tap water etc., excess ozone gas and ozone water And only ozone water needs to be discharged.
【０００３】そのため、オゾン水生成器には図１０に示
すようなオゾン水タンク２０が設けられ、このオゾン水
タンク２０にオゾンガスと水との気液混合水が貯留さ
れ、ここでオゾンガスとオゾン水とに分離した後、オゾ
ンガスを分解処理して大気に放出し、オゾン水のみが排
出されるように構成されている。そのため、オゾン水タ
ンクには水流案内筒２１が形成され、内部に流入したオ
ゾンガスとオゾン水の気液混合水が渦を巻いて下方に移
動して吐出口２２に移動するように構成されている。オ
ゾン水の渦巻の内側の圧力は低くなるので、軽いオゾン
ガスの気泡２３は渦の内側に入り込み、やがてその浮力
により上昇して分解装置側に移動する。For this purpose, the ozone water generator is provided with an ozone water tank 20 as shown in FIG. 10, and the ozone water tank 20 stores a gas-liquid mixture of ozone gas and water. Then, the ozone gas is decomposed and released into the atmosphere, and only ozone water is discharged. Therefore, a water flow guide tube 21 is formed in the ozone water tank, and the ozone gas and the ozone water gas-liquid mixed water flowing inside are swirled and moved downward to move to the discharge port 22. . Since the pressure inside the ozone water swirl decreases, the light ozone gas bubbles 23 enter the inside of the swirl, and eventually rise due to their buoyancy and move to the decomposition device side.
【０００４】[0004]
【発明が解決しようとする課題】しかしながら、このよ
うな自然分離方式の気液分離装置を採用する場合、オゾ
ン水タンクには高さが必要となる。その理由は、タンク
が低いと、気泡は水流に巻き込まれて吐出口２２に引き
込まれてしまいやすいからである。オゾン水タンクが大
型であれば、比較的効率的に気液の分離を行なうことが
できるが、オゾン水タンクをコンパクトにしようとする
場合、オゾンガスの泡は上昇する前にオゾン水の流れに
巻き込まれて吐出口２２から排出されてしまいやすい。
特に、水量が増えたときに気泡が混入する傾向が強い。However, when such a natural-separation type gas-liquid separator is used, the ozone water tank needs to be high. The reason for this is that if the tank is low, the air bubbles are likely to be caught in the water stream and drawn into the discharge port 22. If the ozone water tank is large, gas-liquid separation can be performed relatively efficiently, but when trying to make the ozone water tank compact, the ozone gas bubbles are caught in the flow of ozone water before rising. And is easily discharged from the discharge port 22.
In particular, there is a strong tendency for bubbles to be mixed in when the amount of water increases.
【０００５】本発明は上記問題点を解消し、オゾンガス
とオゾン水とを効率よく分離するとともに、オゾン水タ
ンクを小型化できることができるオゾン水生成器におけ
る気液分離装置を提供することをその課題とする。SUMMARY OF THE INVENTION It is an object of the present invention to provide a gas-liquid separator for an ozone water generator capable of solving the above problems and efficiently separating ozone gas and ozone water and reducing the size of an ozone water tank. And
【０００６】[0006]
【課題を解決するための手段】前記課題を解決するた
め、本発明に係るオゾン水生成器における気液分離装置
は、オゾン発生体で発生させたオゾンガスを水に溶かし
た気液混合水を貯留するオゾン水タンクを備えたオゾン
水生成器において、上記オゾン水タンクには有底筒状部
を設け、筒状部には上端にオゾンガスの排出孔を形成す
るとともに、気液混合水の流入部と排出部とを上下位置
に形成し、上記流入部から気液混合水が渦を巻いて流入
するようになし、かつ流入部と排出部との中間部には筒
状部の内径を小さくする絞り部を形成したことを特徴と
する。In order to solve the above-mentioned problems, a gas-liquid separation device in an ozone water generator according to the present invention stores gas-liquid mixed water obtained by dissolving ozone gas generated by an ozone generator in water. In the ozone water generator provided with an ozone water tank, a bottomed cylindrical portion is provided in the ozone water tank, an ozone gas discharge hole is formed at the upper end of the cylindrical portion, and an inflow portion of the gas-liquid mixed water is formed. And the discharge portion are formed at the upper and lower positions so that the gas-liquid mixed water flows in a spiral form from the inflow portion, and the inner diameter of the cylindrical portion is reduced in the middle portion between the inflow portion and the discharge portion. A throttle portion is formed.
【０００７】なお、前記絞り部を多段に設けるのが好ま
しい。[0007] It is preferable to provide the throttle section in multiple stages.
【０００８】また、前記絞り部に代え、前記筒状部の排
出部近傍の中心には、気液混合水の渦中にあるオゾンガ
スの気泡が下方に移動するのを防止する突起部材を配置
するようにしてもよい。In addition, instead of the constriction, a projecting member for preventing the ozone gas bubbles in the vortex of the gas-liquid mixed water from moving downward is provided at the center of the cylindrical portion near the discharge portion. It may be.
【０００９】さらに、前記オゾン水タンクと有底筒状部
とを一体としてもよい。Further, the ozone water tank and the bottomed cylindrical portion may be integrated.
【００１０】[0010]
【発明の実施の形態】図１は本発明に係るオゾン水生成
器の概要図である。このオゾン水生成器本体１は公知の
オゾン水生成器と同じ構造を有するもので、オゾン発生
体（オゾナイザー）１と、水道蛇口２からの給水管３の
途中に配置したエジェクタ４と、エジェクタ４に水道水
を通す際にオゾンを吸引させて水道水とオゾンガスとを
混合、溶解させるためのオゾン水タンク５と、水道水に
溶解しきれなかったオゾンガスを処理する処理装置６
と、排出ホース７とから構成されている。オゾン発生体
１で発生したオゾンガスはエジェクタ４に吸引されて水
道水と混じり合い、オゾン水タンク５に貯留された後、
このタンク５内に設けられた気液分離装置によりオゾン
ガスは処理装置６で分解処理されて大気に排出され、オ
ゾン水は排出ホース７により排出されて使用に供され
る。FIG. 1 is a schematic diagram of an ozone water generator according to the present invention. The ozone water generator main body 1 has the same structure as a known ozone water generator, and includes an ozone generator (ozonizer) 1, an ejector 4 arranged in the middle of a water supply pipe 3 from a water tap 2, and an ejector 4. Ozone water tank 5 for mixing and dissolving tap water and ozone gas by sucking ozone when passing tap water through, and processing device 6 for treating ozone gas that could not be completely dissolved in tap water
And a discharge hose 7. Ozone gas generated by the ozone generator 1 is sucked into the ejector 4 and mixed with tap water, and stored in the ozone water tank 5.
Ozone gas is decomposed by a processing device 6 by a gas-liquid separation device provided in the tank 5 and discharged to the atmosphere, and ozone water is discharged by a discharge hose 7 for use.
【００１１】上記気液分離装置は、図２に示されるよう
に、オゾン水タンク５の内側（中央でなくてもよい）
に、上端を上蓋１１で閉じた有底筒状部１０を配置し、
筒状部１０の上部の流入部８に給水管３を開口させ、筒
状部１０の上蓋１１にはオゾンガスの排出孔１３を形成
し、筒状部１０の下端にはオゾン水の排出部１４を形成
するとともに、オゾン水タンク５の下部には吐出口７´
を形成したものである。筒状部１０の下端はオゾン水タ
ンク５の底部に当接している。給水管３は図３に示され
るように筒状部１０の中心から偏心した位置に配置され
ている。このため、流入部８から流入した気液混合水の
水流は、筒状部１０の内部で渦を巻くように流れる。As shown in FIG. 2, the gas-liquid separator is located inside the ozone water tank 5 (not necessarily at the center).
, A bottomed cylindrical part 10 whose upper end is closed by an upper lid 11 is arranged,
The water supply pipe 3 is opened at the inflow portion 8 at the upper part of the cylindrical portion 10, an ozone gas discharge hole 13 is formed at the upper lid 11 of the cylindrical portion 10, and the ozone water discharge portion 14 is formed at the lower end of the cylindrical portion 10. And an outlet 7 ′ is formed in the lower part of the ozone water tank 5.
Is formed. The lower end of the cylindrical portion 10 is in contact with the bottom of the ozone water tank 5. The water supply pipe 3 is disposed at a position eccentric from the center of the tubular portion 10 as shown in FIG. For this reason, the gas flow of the gas-liquid mixed water flowing from the inflow portion 8 flows in a swirl inside the cylindrical portion 10.
【００１２】また、流入部８と排出部１４との中間部に
は筒状部１０の内径を小さくする環状の絞り部１５が形
成されている。これにより、気液混合水の渦の長さが絞
り部１５によって短縮される。An annular throttle portion 15 for reducing the inner diameter of the cylindrical portion 10 is formed at an intermediate portion between the inflow portion 8 and the discharge portion 14. Thus, the length of the vortex of the gas-liquid mixed water is reduced by the throttle unit 15.
【００１３】処理装置６内には通常は触媒が充填され、
オゾンガスは触媒内を移動するうちに分解され、大気に
排出される。The processing unit 6 is usually filled with a catalyst,
Ozone gas is decomposed while moving through the catalyst and is discharged to the atmosphere.
【００１４】上記構成によれば、オゾン発生体１で発生
したオゾンガスはエジェクタ４に吸引されて水道水と混
じり合い、流入部８から給水管３を経てオゾン水タンク
５の筒状部１０に流入する。流入した気液混合水は筒状
部１０の内面の接線方向に流れ込んだ後、遠心力によっ
てその外周面に沿って渦巻き状に回り込みながら下方に
延び、さらに下端の排出部１４から筒状部１０の外側に
排出され、さらに吐出口７´から排出ホース７によって
排出される。According to the above configuration, the ozone gas generated by the ozone generator 1 is sucked by the ejector 4 and mixed with the tap water, and flows into the cylindrical portion 10 of the ozone water tank 5 from the inflow section 8 through the water supply pipe 3. I do. The gas-liquid mixed water that has flowed in flows tangentially to the inner surface of the cylindrical portion 10, and then extends downward while spirally wrapping around the outer peripheral surface thereof due to centrifugal force. And is further discharged from the discharge port 7 ′ by the discharge hose 7.
【００１５】ところで、気液混合水が渦巻くことで遠心
力による分離作用が働いて質量の小さいオゾンガスの気
泡１７は渦の中央側に集まる。しかも、図４に示すよう
に、流入部８と排出部１４との中間部には絞り部１５が
形成されているから、気液混合水の渦の長さが短くなる
（点線は絞り部１５がなかったときの渦の状態を示
す）。このため、渦の内側に保持された気泡１７も、高
い位置に保たれ、絞り部１５を通過しにくくなる。した
がって、気泡１７は浮力によりオゾン水の上方に浮上し
て排出孔から排出されて処理装置６に運ばれる。オゾン
ガスは処理装置６で分解処理されて大気に排出される。By the way, the gas-liquid mixed water swirls to cause a separation action by centrifugal force, so that the ozone gas bubbles 17 having a small mass gather at the center of the swirl. Further, as shown in FIG. 4, since the throttle portion 15 is formed in the middle portion between the inflow portion 8 and the discharge portion 14, the length of the vortex of the gas-liquid mixed water is shortened (the dotted line indicates the throttle portion 15). This shows the state of the vortex when there was no). Therefore, the bubble 17 held inside the vortex is also kept at a high position, and it is difficult for the bubble 17 to pass through the throttle unit 15. Therefore, the bubbles 17 float above the ozone water by buoyancy, are discharged from the discharge holes, and are carried to the processing apparatus 6. The ozone gas is decomposed by the processing device 6 and discharged to the atmosphere.
【００１６】上述のように、オゾン水とそれに含まれる
オゾンガスの気泡１７は筒状部１０の中で確実に分離さ
れるので、流量が増えても気液は良好に分離される。し
たがって、オゾン水タンク５の高さをあまり高くする必
要がなく、コンパクトにすることができる。As described above, since the ozone water and the bubbles 17 of the ozone gas contained in the ozone water are reliably separated in the cylindrical portion 10, even if the flow rate increases, the gas and liquid are well separated. Therefore, the height of the ozone water tank 5 does not need to be too high, and the ozone water tank 5 can be made compact.
【００１７】なお、絞り部１５は必ずしも環状に形成す
る必要はない。図５のように、筒状部１０の下部を絞る
構造にしてもよい。It is not always necessary to form the constricted portion 15 in an annular shape. As shown in FIG. 5, a structure in which the lower part of the cylindrical portion 10 is narrowed may be adopted.
【００１８】なお、上述の気液分離装置は必ずしもオゾ
ン水タンク５の内側に筒状体を設けた二重構造の例に限
定されない。例えば、図６のように、オゾン水タンク５
と有底筒状部１０とを一体として形成した構造であって
もよい。なお、符号１２は渦を発生させるための流入オ
ゾン水の案内筒である。The above-described gas-liquid separation device is not necessarily limited to the double structure in which the tubular body is provided inside the ozone water tank 5. For example, as shown in FIG.
And the bottomed cylindrical part 10 may be integrally formed. Reference numeral 12 denotes a guide tube for inflowing ozone water for generating a vortex.
【００１９】ところで、上図２のように、特に気液分離
装置が二重構造の場合は、図７に示すように、筒状部１
０の流入部８と排出部１４との中間部には筒状部１０の
内径を小さくする絞り部１５を２段（２段以上でもよ
い）に設けるのが好ましい。By the way, as shown in FIG. 2 above, especially when the gas-liquid separator has a double structure, as shown in FIG.
It is preferable to provide two stages (or two or more stages) of narrowing portions 15 for reducing the inner diameter of the cylindrical portion 10 at an intermediate portion between the zero inflow portion 8 and the discharge portion 14.
【００２０】その理由は、二重構造の場合には、気液混
合水の渦が上下に長くなりやすいので、混合水の流量が
急に増えたときなどの場合は、一段の絞り部１５では気
液分離が必ずしも十分でないが、このようなときでも、
絞り部１５が２段に形成されていれば、たとえ気泡１７
が上段の絞り部１５を通過しても、下段の絞り部１５は
通過できないので、排出部１４に気泡が混入することが
ない。The reason is that, in the case of the double structure, the vortex of the gas-liquid mixed water tends to be longer vertically, so that when the flow rate of the mixed water suddenly increases, the one-stage throttle unit 15 is not used. Although gas-liquid separation is not always sufficient,
If the squeezed portion 15 is formed in two steps, even if the bubble 17
Although the gas passes through the upper throttle section 15, it cannot pass through the lower throttle section 15, so that air bubbles do not enter the discharge section 14.
【００２１】なお、絞り部１５は３段以上あってもよ
く、また上段よりも下段の絞り部１５の方の内径を小さ
くするようにしてもよい。It should be noted that there may be three or more stops 15 and the inner diameter of the lower stop 15 may be smaller than that of the upper stop.
【００２２】次に、図８は、上記のような絞り部１５に
代え、筒状部１０の排出部１４近傍の中心に、気液混合
水の渦中にあるオゾンガスの気泡１７が下方に移動する
のを防止する突起部材１８を配置するようにしてもよ
い。Next, FIG. 8 shows that the ozone gas bubble 17 in the vortex of the gas-liquid mixed water moves downward at the center of the cylindrical portion 10 in the vicinity of the discharge portion 14 instead of the throttle portion 15 as described above. Alternatively, a projection member 18 for preventing the occurrence of the noise may be provided.
【００２３】このように構成することにより、突起部材
１８の周囲の部分は突起部材１８よりも上の部分に比べ
て体積が小さいから、気液混合水の密度は高くなる。密
度が高い部分には気泡１７は入り込みにくい。また、気
液混合水の渦は突起部材１８が邪魔するので、水の流れ
が阻害される。このため、気泡は渦の流れに引き込まれ
ないから、その浮力によって上方に移動する。したがっ
て、気液はよく分離される。With this configuration, the volume of the gas-liquid mixed water is increased because the volume around the projection 18 is smaller than the volume above the projection 18. Bubbles 17 are less likely to enter high density portions. Further, since the vortex of the gas-liquid mixed water is hindered by the projection member 18, the flow of water is hindered. Therefore, the bubbles are not drawn into the flow of the vortex, and move upward due to the buoyancy. Therefore, gas-liquid is well separated.
【００２４】なお、突起部材１８の上端の径は気液混合
水の渦の径よりも大きくするのが好ましい。It is preferable that the diameter of the upper end of the projecting member 18 be larger than the diameter of the vortex of the gas-liquid mixed water.
【００２５】ところで、上記突起部材１８も、二重構造
の気液分離装置の例に限定されない。例えば、図９のよ
うに、オゾン水タンク５と有底筒状部１０とを一体とし
て形成した構造にも適用することができる。Incidentally, the projection member 18 is not limited to the example of the gas-liquid separation device having the double structure. For example, as shown in FIG. 9, the present invention can also be applied to a structure in which the ozone water tank 5 and the bottomed cylindrical portion 10 are integrally formed.
【図１】オゾン水生成器の概略図FIG. 1 is a schematic diagram of an ozone water generator.
【図２】本発明に係るオゾン水生成器における気液分離
装置の一例の縦断面図FIG. 2 is a longitudinal sectional view of an example of a gas-liquid separation device in the ozone water generator according to the present invention.
【図３】上記気液分離装置の平面図FIG. 3 is a plan view of the gas-liquid separation device.
【図４】上記気液分離装置の要部の縦断面図FIG. 4 is a longitudinal sectional view of a main part of the gas-liquid separation device.
【図５】上記気液分離装置の他の例の縦断面図FIG. 5 is a longitudinal sectional view of another example of the gas-liquid separation device.
【図６】上記気液分離装置の筒状部とオゾン水タンクと
を一体にした例の縦断面図FIG. 6 is a longitudinal sectional view of an example in which a cylindrical portion of the gas-liquid separation device and an ozone water tank are integrated.
【図７】上記気液分離装置の別の例の縦断面図FIG. 7 is a longitudinal sectional view of another example of the gas-liquid separation device.
【図８】二重構造における上記気液分離装置のさらに別
の例の斜視図FIG. 8 is a perspective view of still another example of the gas-liquid separation device having a double structure.
【図９】上記気液分離装置のさらに別の例の縦断面図FIG. 9 is a longitudinal sectional view of still another example of the gas-liquid separation device.
【図１０】従来の気液分離装置の要部の模式図FIG. 10 is a schematic view of a main part of a conventional gas-liquid separation device.
１ オゾン水生成器 ５ オゾン水タンク ８ 流入部 ９ 吐出口 １０ 筒状部 １１ 上蓋 １３ 排出孔 １４ 排出部 １５ 絞り部 １８ 突起部材 DESCRIPTION OF SYMBOLS 1 Ozone water generator 5 Ozone water tank 8 Inflow part 9 Discharge port 10 Cylindrical part 11 Top lid 13 Drain hole 14 Drain part 15 Narrow part 18 Projection member
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 ＦＩ テーマコート゛(参考） Ｃ０２Ｆ 1/20 Ｃ０２Ｆ 1/20 Ａ ４Ｇ０４２ 1/50 ５３１ 1/50 ５３１Ｒ ５４０ ５４０Ｂ ５５０ ５５０Ｄ ５５０Ｈ 1/78 1/78 (72)発明者 藤井 清人 東京都中央区日本橋箱崎町６番６号 マッ クス株式会社内 (72)発明者 戸花 直樹 東京都中央区日本橋箱崎町６番６号 マッ クス株式会社内 (72)発明者 坂田 知昭 東京都中央区日本橋箱崎町６番６号 マッ クス株式会社内 Ｆターム(参考） 4D011 AA04 AA05 AC03 AD03 4D037 AA02 AB11 BA23 BB04 4D050 AA04 AB06 BB02 BD04 BD06 4G035 AA01 AB20 AE13 4G037 AA11 EA01 4G042 CE01 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/20 C02F 1/20 A 4G042 1/50 531 1/50 531R 540 540B 550 550D 550H 1/78 1 / 78 (72) Inventor Kiyoto Fujii 6-6 Nihonbashi-Hakozakicho, Chuo-ku, Tokyo Max. (72) Inventor Naoki Tohana 6-6 Nihonbashi-Hakozakicho, Chuo-ku, Tokyo Max Max (72) Inventor Tomoaki Sakata 6-6, Hakozakicho, Nihonbashi, Chuo-ku, Tokyo F-term in MAX Corporation (reference) 4D011 AA04 AA05 AC03 AD03 4D037 AA02 AB11 BA23 BB04 4D050 AA04 AB06 BB02 BD04 BD06 4G035 AA01 AB20 AE13 4G037A EA01 4G042 CE01
Claims (4)
水に溶かした気液混合水を貯留するオゾン水タンクを備
えたオゾン水生成器において、 上記オゾン水タンクには有底筒状部を設け、筒状部には
上端にオゾンガスの排出孔を形成するとともに、気液混
合水の流入部と排出部とを上下位置に形成し、上記流入
部から気液混合水が渦を巻いて流入するようになし、か
つ流入部と排出部との中間部には筒状部の内径を小さく
する絞り部を形成したことを特徴とするオゾン水生成器
における気液分離装置。1. An ozone water generator comprising an ozone water tank for storing gas-liquid mixed water obtained by dissolving ozone gas generated by an ozone generator in water, wherein the ozone water tank has a bottomed cylindrical portion. In addition, an ozone gas discharge hole is formed at an upper end of the cylindrical portion, and an inflow portion and a discharge portion of the gas-liquid mixed water are formed at upper and lower positions, and the gas-liquid mixed water flows in a spiral form from the inflow portion. A gas-liquid separator in an ozone water generator, wherein a throttle portion for reducing the inner diameter of the cylindrical portion is formed at an intermediate portion between the inflow portion and the discharge portion.
載のオゾン水生成器における気液分離装置。2. The gas-liquid separation device in the ozone water generator according to claim 1, wherein the throttle section is provided in multiple stages.
近傍の中心には、気液混合水の渦中にあるオゾンガスの
気泡が下方に移動するのを防止する突起部材を配置し
た、請求項１記載のオゾン水生成器における気液分離装
置。3. A projection member for preventing bubbles of ozone gas in a vortex of gas-liquid mixed water from being moved downward at the center of the cylindrical portion near the discharge portion, instead of the throttle portion. A gas-liquid separator in the ozone water generator according to claim 1.
体とした、請求項１、２又は３に記載のオゾン水生成器
における気液分離装置。4. The gas-liquid separator in the ozone water generator according to claim 1, wherein the ozone water tank and the bottomed cylindrical portion are integrated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000217888A JP2002028403A (en) | 2000-07-18 | 2000-07-18 | Gas-liquid separator in ozone water rpoducer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000217888A JP2002028403A (en) | 2000-07-18 | 2000-07-18 | Gas-liquid separator in ozone water rpoducer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002028403A true JP2002028403A (en) | 2002-01-29 |
Family
ID=18712933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000217888A Pending JP2002028403A (en) | 2000-07-18 | 2000-07-18 | Gas-liquid separator in ozone water rpoducer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2002028403A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004230294A (en) * | 2003-01-30 | 2004-08-19 | Komatsu Ltd | Air bubble removing device |
| KR100893069B1 (en) | 2007-12-28 | 2009-04-14 | 메가티엔에스 주식회사 | Distribution device |
| JP2018155485A (en) * | 2017-03-17 | 2018-10-04 | 日冷工業株式会社 | Gas-liquid separation device and refrigeration device including gas-liquid separation device |
| KR101963807B1 (en) * | 2018-09-17 | 2019-03-29 | 최예묵 | An ozone dissolution water treatment apparatus comprising two stage reactor |
-
2000
- 2000-07-18 JP JP2000217888A patent/JP2002028403A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004230294A (en) * | 2003-01-30 | 2004-08-19 | Komatsu Ltd | Air bubble removing device |
| KR100893069B1 (en) | 2007-12-28 | 2009-04-14 | 메가티엔에스 주식회사 | Distribution device |
| JP2018155485A (en) * | 2017-03-17 | 2018-10-04 | 日冷工業株式会社 | Gas-liquid separation device and refrigeration device including gas-liquid separation device |
| JP7146207B2 (en) | 2017-03-17 | 2022-10-04 | 日冷工業株式会社 | Refrigeration equipment with gas-liquid separator and gas-liquid separator |
| KR101963807B1 (en) * | 2018-09-17 | 2019-03-29 | 최예묵 | An ozone dissolution water treatment apparatus comprising two stage reactor |
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