[go: up one dir, main page]

JP2017013001A - Functional water generator - Google Patents

Functional water generator Download PDF

Info

Publication number
JP2017013001A
JP2017013001A JP2015132293A JP2015132293A JP2017013001A JP 2017013001 A JP2017013001 A JP 2017013001A JP 2015132293 A JP2015132293 A JP 2015132293A JP 2015132293 A JP2015132293 A JP 2015132293A JP 2017013001 A JP2017013001 A JP 2017013001A
Authority
JP
Japan
Prior art keywords
electrode
water
gas
hydrogen
electrolysis
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.)
Granted
Application number
JP2015132293A
Other languages
Japanese (ja)
Other versions
JP6539131B2 (en
Inventor
寺島 健太郎
Kentaro Terajima
健太郎 寺島
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.)
Sharp Corp
Original Assignee
Sharp Corp
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 Sharp Corp filed Critical Sharp Corp
Priority to JP2015132293A priority Critical patent/JP6539131B2/en
Publication of JP2017013001A publication Critical patent/JP2017013001A/en
Application granted granted Critical
Publication of JP6539131B2 publication Critical patent/JP6539131B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

【課題】
従来、水素ガスやオゾンガスを水中に溶存させた機能水を生成するために、大掛かりな装置が必要であった。また、簡易なものは酸素ガスと水素ガスが混合していたりして、目的とするガスを高濃度で溶解させることが難しかった。
【解決手段】
第1電極と、第2電極と、第1電極と第2電極との中間位置に設置した隔壁とを備え、前記隔壁には水中のイオンを透過させるとともに気体は透過させない材料を使用する。また、電解容器の底部に旋回流発生部を設けて電解容器内の水に旋回流を与える。これにより、第2電極から発生したガスを電解容器内の水に溶解しやすくする。
【選択図】 図1
【Task】
Conventionally, in order to generate functional water in which hydrogen gas or ozone gas is dissolved in water, a large-scale apparatus is required. In addition, it is difficult to dissolve the target gas at a high concentration because simple gas such as oxygen gas and hydrogen gas are mixed.
[Solution]
A first electrode, a second electrode, and a partition wall provided at an intermediate position between the first electrode and the second electrode are provided, and the partition wall is made of a material that transmits ions in water and does not transmit gas. In addition, a swirl flow generator is provided at the bottom of the electrolysis vessel to give swirl to the water in the electrolysis vessel. Thereby, the gas generated from the second electrode is easily dissolved in the water in the electrolytic vessel.
[Selection] Figure 1

Description

本発明は、水の電気分解によって発生した水素ガスを利用する機能水生成器に関する。   The present invention relates to a functional water generator that uses hydrogen gas generated by electrolysis of water.

水素水の効用はこれまで生体内の有害な活性酸素及びフリーラジカルを除去する効果があるとして様々な研究がなされている。例えば、WO2007−21034参照。こうした抗酸化成分を生体中で発現させる場合、水中に溶存させる水素ガス濃度は可能な限り高くする必要がある。   Various studies have been made that the utility of hydrogen water has been effective in removing harmful active oxygen and free radicals in the living body. For example, see WO2007-21034. When such an antioxidant component is expressed in a living body, the concentration of hydrogen gas dissolved in water needs to be as high as possible.

従来、水道水を用いて電気分解により水中の水素濃度を増加させる場合、陰極表面から発生する水素ガスを水中に溶かしこむことによって水中の水素濃度を増加させるのが通例であり、例えば通常の整水器などのようなプレート状電極の間で発生した水素を水中に溶かしこむ手法を用いた商品など、多くの商品が上市されている。   Conventionally, when increasing the hydrogen concentration in water by electrolysis using tap water, it is customary to increase the hydrogen concentration in water by dissolving the hydrogen gas generated from the cathode surface in the water. There are many products on the market, such as products that use a technique that dissolves hydrogen generated between plate-like electrodes such as water vessels into water.

しかし、水中の水素濃度は静的条件にて電解を行った場合の水素ガス溶存濃度は1気圧の下では1.6ppmが最大であり、電解時に同時発生する酸素ガスの濃度によっては、この濃度は更に低下する。   However, the hydrogen concentration in water when the electrolysis is performed under static conditions is 1.6 ppm at a maximum under 1 atm, and this concentration depends on the concentration of oxygen gas generated simultaneously during electrolysis. Is further reduced.

一方、水素ガスを水中に効率よく溶存させるための手法としては電解によって生じた酸素ガスを除去し、更に、水を撹拌させる等の搖動を与えることによって水素ガス溶存度を一時的に過飽和まで上げることができることが知られており、この方法により水素ガス濃度を3ppm以上にまで増加させることが可能である。   On the other hand, as a method for efficiently dissolving hydrogen gas in water, oxygen gas generated by electrolysis is removed, and further, the hydrogen gas solubility is temporarily increased to supersaturation by giving peristalsis such as stirring water. It is known that the hydrogen gas concentration can be increased to 3 ppm or more by this method.

上記手法の代表例として、任意形状の枠体に陽極と陰極から成る電極を取り付けると共にこの陽極と陰極間にセパレータを配置して成る電極部と、前記電極部の陽極と陰極に通電するための通電部とからなる水素水生成用撹拌具が知られている。(特許文献1、以降先行例1とする)   As a representative example of the above method, an electrode part composed of an anode and a cathode is attached to a frame of an arbitrary shape and a separator is disposed between the anode and the cathode, and the anode and cathode of the electrode part are energized. There is known a stirring device for generating hydrogen water comprising an energization section. (Patent Document 1, hereinafter referred to as Prior Example 1)

また、別の例としては、水素の微細気泡を効率的かつ安定的に発生させることができ、長時間にわたって水中に水素を存在させて酸化還元電位を低く維持することができる水素還元水を効率的に製造可能な水素還元水の製造方法が提案されている。(特許文献2、以降先行例2とする)   As another example, hydrogen-reduced water can efficiently and stably generate hydrogen bubbles, and hydrogen-reduced water that can maintain a low oxidation-reduction potential by allowing hydrogen to exist in water for a long time. A method for producing hydrogen-reduced water that can be produced in an economical manner has been proposed. (Patent Document 2, hereinafter referred to as Prior Example 2)

特開2005−95808号公報Japanese Patent Laid-Open No. 2005-95808 特開2009−195882号公報JP 2009-195882 A

しかしながら、先行例1に示されている通常の撹拌方法では陽極と陰極で発生したガスを共に水中に溶存させるため、所望のガスのみを高濃度で水中に溶解させることは出来なかった。また、先行例2に示されているような手法によりガスを細径化して溶存させる手法を採る場合、旋回流を作った後、ガスを溶存させる必要があるため、機器としては大型化し、一般家庭に容易に導入しづらい、という問題点があった。   However, since the gas generated at the anode and the cathode is dissolved in water by the ordinary stirring method shown in the first example, only the desired gas cannot be dissolved in water at a high concentration. In addition, when the method of dissolving the gas by reducing the diameter by the method as shown in the preceding example 2, it is necessary to dissolve the gas after creating the swirling flow. There was a problem that it was difficult to introduce into the home easily.

上記問題点を解決するために、本発明に係る撹拌式機能水生成器は、中央部に第1電極を配し、周囲に第2電極として円筒状の網目構造電極を配し、前記第1電極と第2電極の間に水の浸漬時において、気体のみ分離可能な隔膜を配置した。また、略円筒構造からなる水の電解容器において、前記電解容器の下部に旋回流発生部を更に設け、前記電解容器の上部に排気口を設け、且つ、第2電極部上部を密閉する着脱可能な蓋を設けたことを特徴とする。   In order to solve the above-mentioned problems, the agitation-type functional water generator according to the present invention has a first electrode disposed in the center, and a cylindrical mesh structure electrode disposed as a second electrode around the first electrode. A diaphragm capable of separating only gas was disposed between the electrode and the second electrode when water was immersed. In addition, in the water electrolysis vessel having a substantially cylindrical structure, a detachable flow generator is further provided at the lower portion of the electrolysis vessel, an exhaust port is provided at the upper portion of the electrolysis vessel, and the upper portion of the second electrode portion is sealed. A special lid is provided.

また、本発明では、生成する機能水を水素水とする。また、前記第1電極は炭素棒で陽極であることを特徴とする。   In the present invention, the functional water to be generated is hydrogen water. The first electrode may be a carbon rod and an anode.

また、本発明では、前記着脱可能な蓋は加圧可能な機構を有することを特徴とする。   In the present invention, the detachable lid has a mechanism capable of being pressurized.

また、本発明では、前記金属電極は電極材の一部を円筒形状の中心、又は、外方向に向かう突起部として設けることを特徴とする。   In the present invention, the metal electrode is characterized in that a part of the electrode material is provided as a cylindrical center or a protruding portion directed outward.

また、本発明では、前記電解容器は本体に対して着脱可能であることを特徴とする。   In the present invention, the electrolytic container is detachable from the main body.

以上のように、本発明によれば、隔膜を水の浸漬時において気体を分離する材質とするので、電解時に第1電極から発生するガスを電解槽外に放出し、第2電極から発生するガスのみを水中に溶かしこむことが可能であり、また、第2電極の電極材の一部を円筒形状の中心方向に向かう突起部として設けることで効果的にガスを溶存させるができる。   As described above, according to the present invention, since the diaphragm is made of a material that separates gas when immersed in water, the gas generated from the first electrode during electrolysis is discharged out of the electrolytic cell and generated from the second electrode. Only the gas can be dissolved in water, and the gas can be dissolved effectively by providing a part of the electrode material of the second electrode as a protruding portion toward the center of the cylindrical shape.

これにより、生成する機能水を水素水とするとき、比較的コンパクトな機構を有しながら、水素ガスのみを効果的に水中に溶かしこむことが可能な撹拌式水素水生成器を形成することができる。   Thereby, when the functional water to be generated is hydrogen water, it is possible to form a stirring type hydrogen water generator capable of effectively dissolving only hydrogen gas in water while having a relatively compact mechanism. it can.

本発明の実施の形態1に係る機能水生成器の構造を示す図である。1 is a diagram showing a structure of a functional water generator according to Embodiment 1 of the present invention. 本発明の実施の形態2に係る機能水生成器の構造を示す図である。It is a figure which shows the structure of the functional water generator which concerns on Embodiment 2 of this invention. 本発明の実施の形態2に係る機能水生成器の撹拌の状態を示す図である。It is a figure which shows the state of stirring of the functional water generator which concerns on Embodiment 2 of this invention. 本発明の実施の形態3に係る機能水生成器の構造を示す図である。It is a figure which shows the structure of the functional water generator which concerns on Embodiment 3 of this invention. 本発明の実施の形態4に係る機能水生成器の構造を示す図である。It is a figure which shows the structure of the functional water generator which concerns on Embodiment 4 of this invention. 本発明の実施の形態4に係る機能水生成器の断面構造を示す図である。It is a figure which shows the cross-section of the functional water generator which concerns on Embodiment 4 of this invention. 本発明の実施の形態5に係る機能水生成器の構造を示す図である。It is a figure which shows the structure of the functional water generator which concerns on Embodiment 5 of this invention. 本発明の実施の形態6に係る機能水生成器の構造を示す図である。It is a figure which shows the structure of the functional water generator which concerns on Embodiment 6 of this invention.

〔実施の形態1〕
以下、図面に基づいて本発明の実施の形態を説明する。図1は、本発明に係る撹拌式水素水生成器の構成を示す一例である。
[Embodiment 1]
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is an example showing the configuration of a stirred hydrogen water generator according to the present invention.

本発明の撹拌式機能水生成器101は、中央部に第1電極1を配し、周囲に第2電極2として円筒状の網目構造を有する金属電極を配し、前記第1電極1と第2電極2の間に、水の浸漬時において、水中の溶解イオンは透過可能であり、気体のみ分離可能な隔膜3を配置した。また、略円筒構造からなる水の電解容器4において、前記電解容器4の下部に旋回流発生部5を更に設け、前記電解容器4の上部に排気口6を設け、且つ、第2電極部上部を密閉する着脱可能な蓋7を設けたことを特徴とする。また、第1電極1と第2電極2との間に直流電圧を印可するための電源部9を備える。   The agitation-type functional water generator 101 according to the present invention has a first electrode 1 at the center and a metal electrode having a cylindrical network structure as the second electrode 2 around the first electrode 1. Between the two electrodes 2, a diaphragm 3 capable of transmitting dissolved ions in water and separating only gas when water was immersed was disposed. Further, in the water electrolysis vessel 4 having a substantially cylindrical structure, a swirl flow generating portion 5 is further provided at the lower portion of the electrolysis vessel 4, an exhaust port 6 is provided at the upper portion of the electrolysis vessel 4, and the upper portion of the second electrode portion A removable cover 7 is provided for hermetically sealing. In addition, a power supply unit 9 for applying a DC voltage is provided between the first electrode 1 and the second electrode 2.

上記構成の電気分解部の動作について説明する。先ず、電解容器4内に原水を供給する。使用する原水としては、普通の水道水を用いることができる。具体的には、例えば、大阪府八尾市の水道水(pH=7.6、硬度45mg/L)を用いることができる。   The operation of the electrolysis unit having the above configuration will be described. First, raw water is supplied into the electrolytic vessel 4. Ordinary tap water can be used as raw water to be used. Specifically, for example, tap water (pH = 7.6, hardness 45 mg / L) from Yao City, Osaka Prefecture can be used.

前記電解容器4において電気分解が行われる。電解用電極としては、例えば中央に第1電極1として直径5〜10mmの炭素棒電極を配置し、第2電極2としては網目構造を持つ円筒状の金属電極を配置する。中央の炭素棒電極と周囲の金属電極の表面距離が10〜20mm程度となるように設置し、電気分解を行う。   Electrolysis is performed in the electrolytic vessel 4. As the electrode for electrolysis, for example, a carbon rod electrode having a diameter of 5 to 10 mm is disposed as the first electrode 1 in the center, and a cylindrical metal electrode having a network structure is disposed as the second electrode 2. It is installed so that the surface distance between the central carbon rod electrode and the surrounding metal electrode is about 10 to 20 mm, and electrolysis is performed.

この時、第1電極1、では以下式(1)、及び、第2電極2では式(2)の反応により、酸素ガス、及び、水素ガスが発生する。
O→1/2O↑+2H+2e ・・・式(1)
2HO+2e→H↑+2OH ・・・式(2)
At this time, oxygen gas and hydrogen gas are generated in the first electrode 1 by the reaction of the following formula (1) and in the second electrode 2 by the formula (2).
H 2 O → 1 / 2O 2 ↑ + 2H + + 2e - ··· formula (1)
2H 2 O + 2e → H 2 ↑ + 2OH Formula (2)

この時、前記第1電極1と第2電極2の間に、水の浸漬時において、水中に溶存しているイオンは透過可能であり、気体は分離可能な隔膜3を配置し、第1電極1から上記式(1)により発生する酸素ガスを、開放された第1電極室上部の排気口6から外部に放出させ、第2電極2から上記式(2)により発生する水素ガスのみを内部に滞留させる。   At this time, a diaphragm 3 is disposed between the first electrode 1 and the second electrode 2 so that ions dissolved in water can be transmitted and gas can be separated when the water is immersed. 1 to release the oxygen gas generated by the above formula (1) from the exhaust port 6 at the upper part of the opened first electrode chamber, and only the hydrogen gas generated by the above formula (2) from the second electrode 2 To stay in.

上記中央に配置した第1電極1である炭素棒電極は、チタン棒表面に白金などをコートした金属電極としても電気分解は行うことが可能である。陽極を金属電極とすると酸素ガスが発生しやすいというメリットがある。一方、炭素棒電極で作った場合、コスト安の他に、金属電極に比べて仕事関数が大きいため、同一電圧値において電解による酸素ガス発生を少なくできるというメリットがある。   The carbon rod electrode, which is the first electrode 1 arranged in the center, can be electrolyzed even as a metal electrode having a titanium rod surface coated with platinum or the like. When the anode is a metal electrode, there is an advantage that oxygen gas is easily generated. On the other hand, when it is made of a carbon rod electrode, it has a merit that generation of oxygen gas due to electrolysis can be reduced at the same voltage value because the work function is larger than that of a metal electrode in addition to low cost.

また、前記第2電極2として用いる円筒状の金属電極は、電極の内と外で通水し易い構造であることが望ましく、例えば網目成形、ラス成形、パンチングメタル成形などによって成形しても良い。また、金属電極としては水の電気分解を効率的に行いやすい金属、例えば白金、金、パラジウム、ロジウム、イリジウムの内、いずれか1つの金属またはその合金の他、それらの酸化物が好適である。   Further, the cylindrical metal electrode used as the second electrode 2 preferably has a structure that allows water to pass easily inside and outside the electrode, and may be formed by, for example, mesh forming, lath forming, punching metal forming, or the like. . Further, as the metal electrode, a metal that can easily perform electrolysis of water efficiently, for example, any one of platinum, gold, palladium, rhodium, and iridium, or an alloy thereof, or an oxide thereof is preferable. .

また、前記気体分離可能な隔膜3は、上記中央の電極の周囲を取り囲み、第1電極1で発生する酸素ガスが上記気体分離可能な隔膜3から外に漏れ出ない構造とする。例えば試験官状の構造、縦長のすり鉢構造などが考えられる。また、プラスチックによる骨組みに対して当該隔膜3を貼り付けるなどして素材の形状補強を行っても良い。当該隔膜3の素材としては、綿、麻、毛、絹などの天然繊維や、レーヨン、キュプラなどに代表される親水性繊維の他に、デュポン社のナフィオン(R)(登録商標)といったイオン交換膜などで形成してもよい。   In addition, the gas-separable diaphragm 3 surrounds the center electrode, and oxygen gas generated at the first electrode 1 does not leak out from the gas-separable diaphragm 3. For example, a tester-like structure or a vertically long mortar structure can be considered. Further, the shape of the material may be reinforced by attaching the diaphragm 3 to a plastic framework. The material of the diaphragm 3 includes natural fibers such as cotton, hemp, hair and silk, and hydrophilic fibers such as rayon and cupra, as well as ion exchange such as Nafion (R) (registered trademark) by DuPont. You may form with a film | membrane etc.

生成する機能水を水素水とするとき、本発明では、前記電解容器4の下部に旋回流発生部5を更に設け、気体分離可能な隔膜3により選択的に水中に放出される水素ガスに対して旋回流を発生し、掛かる旋回流により発生したせん断流を用いて、水素ガスを水中に効果的に溶存させることができる。   When the functional water to be generated is hydrogen water, in the present invention, a swirl flow generating portion 5 is further provided in the lower part of the electrolytic vessel 4, and the hydrogen gas selectively discharged into water by the gas-separable diaphragm 3 is used. Thus, the swirl flow is generated, and the hydrogen gas can be effectively dissolved in the water using the shear flow generated by the swirl flow applied.

〔実施の形態2〕
本実施の形態は、実施の形態1の蓋7に圧力を掛けるためのロック機構8を追加して備えたものである。その他の部分は、実施の形態1と同じであり、同じ機能部には同じ符号を付して説明を省略する。
前記電解容器4の上部に設けた蓋7は着脱可能であり、更に、図2に示すように可動ヒンジ部を設けた2〜4箇所程度のロック式の機構を有していることが望ましい。これは、このような機構とすることで、第2電極2である金属電極で発生した水素ガスを加圧状態において旋回流で水中に溶解させることが可能となるためであり、掛かる機構を設けることで水素ガスの溶解度を更に増加させることが可能である。なお、加圧機構としてはスクリューねじ込み式などであっても良いが加圧可能な機構であればこれらに限定されるものではない。
[Embodiment 2]
In the present embodiment, a lock mechanism 8 for applying pressure to the lid 7 of the first embodiment is additionally provided. The other parts are the same as those of the first embodiment, and the same function parts are denoted by the same reference numerals and the description thereof is omitted.
It is desirable that the lid 7 provided on the top of the electrolytic vessel 4 is detachable, and further has about 2 to 4 locking mechanisms with movable hinges as shown in FIG. This is because hydrogen gas generated at the metal electrode as the second electrode 2 can be dissolved in water in a swirling flow in a pressurized state by using such a mechanism, and a hanging mechanism is provided. Thus, it is possible to further increase the solubility of hydrogen gas. The pressurizing mechanism may be a screw screw type, but is not limited thereto as long as it is a pressurizable mechanism.

本発明の撹拌式機能水生成器102は、前記電解容器4において電気分解および旋回流の発生が行われる。例えば、中心に直径5mm、高さ70mmの炭素棒を第1電極1として陽極とし、表面距離10mmにて高さ70mmラス形状の白金コートチタン電極を第2電極2として陰極として周囲に設ける。電圧値:35〜45Vの直流電気で電気分解を行った時、電解直後から各電極表面で酸素及び水素が発生する。実施の形態1と同様に酸素が選択的に除去され、加圧された水素ガスに対し回転数900〜1200rpm程度の旋回流を旋回流発生部5で発生させることにより、2〜3分程度で水素濃度3ppm以上の高濃度の水素水を生成することができる。   The stirred functional water generator 102 of the present invention performs electrolysis and swirl generation in the electrolytic vessel 4. For example, a carbon rod having a diameter of 5 mm and a height of 70 mm is used as the first electrode 1 as an anode, and a platinum coated titanium electrode having a surface distance of 10 mm and a height of 70 mm is provided as a second electrode 2 as a cathode. Voltage value: When electrolysis is performed with direct current of 35 to 45 V, oxygen and hydrogen are generated on each electrode surface immediately after electrolysis. In the same manner as in the first embodiment, oxygen is selectively removed, and a swirling flow having a rotational speed of 900 to 1200 rpm is generated in the swirling flow generating unit 5 with respect to the pressurized hydrogen gas in about 2 to 3 minutes. High concentration hydrogen water having a hydrogen concentration of 3 ppm or more can be produced.

なお、図3に示すように、電解容器4に旋回流を生じると遠心力によって、水面が中心部で低く周縁部で高くなるが、前記第1電極1、第2電極2の少なくとも一方は撹拌中も電極全体が水に浸漬されていることが望ましい。これは常に電極が水に浸かっていることにより電解効率を向上させ、ガスを発生させ易くする理由の他に、必ずどちらかの電極が水に浸かっていることで、両極間で電流がショートし火花放電が発生することを防止するため、安全面から必要と考えられるからである。なお、図中の白抜き矢印は旋回流を示す。   As shown in FIG. 3, when a swirling flow is generated in the electrolytic vessel 4, the water surface is low at the center and high at the periphery due to centrifugal force, but at least one of the first electrode 1 and the second electrode 2 is stirred. It is desirable that the entire electrode is immersed in water. This is because the electrode is always immersed in water, improving the electrolysis efficiency and facilitating gas generation. In addition, one of the electrodes is always immersed in water, so that the current is shorted between the two electrodes. This is because it is considered necessary from the viewpoint of safety to prevent the occurrence of spark discharge. In addition, the white arrow in a figure shows a swirl flow.

〔実施の形態3〕
本実施の形態は、実施の形態2の第2電極2に突起部を追加して備えたものである。その他の部分は、実施の形態2と同じであり、同じ機能部には同じ符号を付して説明を省略する。本発明の別の実施例に係る形態を以下、図面に基づいて説明する。図4は、本発明に係る撹拌式機能水生成器の構成を示す。
[Embodiment 3]
In the present embodiment, a protrusion is added to the second electrode 2 of the second embodiment. The other parts are the same as those of the second embodiment, and the same function parts are denoted by the same reference numerals and the description thereof is omitted. A mode according to another embodiment of the present invention will be described below with reference to the drawings. FIG. 4 shows the structure of the stirring type functional water generator according to the present invention.

本発明の撹拌式機能水生成器103は、中央部に第1電極1を配し、周囲に第2電極2として円筒状の網目構造を有する金属電極を配し、前記第1電極1と第2電極2の間に、水の浸漬時において、イオンが透過可能であり、気体のみ分離可能な隔膜3を配置した。略円筒構造からなる水の電解容器4において、前記電解容器4の下部に旋回流発生部5を更に設け、前記電解容器4の上部に排気口6を設け、且つ、第2電極部上部を密閉する着脱可能な蓋7を設け、更に、前記第2電極2である金属電極は電極材の一部を円筒形状の中心方向に向かう突起部10が設けられていることを特徴とする。   The agitation-type functional water generator 103 according to the present invention has a first electrode 1 at the center and a metal electrode having a cylindrical network structure as the second electrode 2 around the first electrode 1. Between the two electrodes 2, a diaphragm 3 that allows permeation of ions when water is immersed and that can separate only gas is disposed. In the electrolysis vessel 4 having a substantially cylindrical structure, a swirl flow generator 5 is further provided at the lower portion of the electrolysis vessel 4, an exhaust port 6 is provided at the upper portion of the electrolysis vessel 4, and the upper portion of the second electrode portion is hermetically sealed. A removable lid 7 is provided, and the metal electrode as the second electrode 2 is further provided with a protruding portion 10 in which a part of the electrode material is directed toward the center of the cylindrical shape.

上記電気分解部と隔膜部の作用は実施例1に述べた通りであるが、本実施の形態では第1電極1を陽極、第2電極2を陰極とし、第2電極2を形成する電極材の一部に突起部10を設ける。旋回流が及ぶところであれば、突起部10は、第2電極の径方向の外向きであっても、内向きであってもよい。   The operation of the electrolysis part and the diaphragm part is as described in Example 1. In this embodiment, the first electrode 1 is an anode, the second electrode 2 is a cathode, and the electrode material for forming the second electrode 2 is used. A protrusion 10 is provided on a part of the protrusion. As long as the swirl flow reaches, the protrusion 10 may be outward in the radial direction of the second electrode or inward.

これは、通常の場合、旋回流を発生させても電解容器4内の水は同心円状の流れを形成するため、表面が平滑な状態の場合、せん断流は主に旋回流発生部5の周囲でのみ発生する。しかし、第2電極2を形成する電極材の一部に突起部10を設けた場合、せん断流はこれら突起部10の表面でも生じる。旋回流の流路に対して高さ2〜5mm程度の突起部を設けることにより、せん断流を発生させ易くし、せん断流によって未溶存の水素ガスを数μm〜数10μm程度の微細粒径泡、いわゆるマイクロバブルとして溶解させ、水中の水素ガス濃度を更に増加させることができる。   This is because the water in the electrolysis vessel 4 forms a concentric flow even if a swirl flow is generated in a normal case, so that the shear flow is mainly around the swirl flow generator 5 when the surface is smooth. Only occurs in However, when the protrusions 10 are provided on a part of the electrode material forming the second electrode 2, the shear flow is also generated on the surfaces of these protrusions 10. Providing protrusions with a height of about 2 to 5 mm with respect to the flow path of the swirl flow makes it easy to generate a shear flow, and undissolved hydrogen gas bubbles with a fine particle diameter of about several μm to several tens of μm due to the shear flow. It can be dissolved as so-called microbubbles to further increase the hydrogen gas concentration in the water.

なお、前記第2電極2である金属電極上の突起部10は中心方向を向いていることが望ましい。これは、中心方向に向けることで突起部10の先端を中心に水素ガスが生じやすくなるためである。また、電極を取り外して洗浄する際に引っかかりが無いため、洗浄が容易になる。   In addition, it is desirable that the protrusion 10 on the metal electrode that is the second electrode 2 is oriented in the center direction. This is because hydrogen gas is likely to be generated around the tip of the protrusion 10 by being directed in the center direction. Further, since there is no catch when the electrode is removed and cleaned, cleaning becomes easy.

〔実施の形態4〕
本実施の形態は、実施の形態3の電解容器4の内壁に突起部を追加して備えたものである。その他の部分は、実施の形態3と同じであり、同じ機能部には同じ符号を付して説明を省略する。以下、図面に基づいて説明する。図5は、本発明に係る撹拌式機能水生成器の構成を示す。また、図6は図5の電解容器4を水平に切断した断面図である。
[Embodiment 4]
In the present embodiment, a protrusion is added to the inner wall of the electrolytic vessel 4 of the third embodiment. The other parts are the same as those of the third embodiment, and the same functional parts are denoted by the same reference numerals and the description thereof is omitted. Hereinafter, description will be given based on the drawings. FIG. 5 shows the structure of the stirring type functional water generator according to the present invention. Moreover, FIG. 6 is sectional drawing which cut | disconnected the electrolytic vessel 4 of FIG. 5 horizontally.

本発明の撹拌式機能水生成器104は、中央部に第1電極1を配し、周囲に第2電極2として円筒状の網目構造を有する金属電極を配し、前記第1電極1と第2電極2の間に、水の浸漬時において、イオンが透過可能であり気体のみ分離可能な隔膜3を配置した。略円筒構造からなる水の電解容器4において、前記電解容器4の下部に旋回流発生部5を更に設け、前記電解容器4の上部に排気口6を設け、且つ、第2電極部上部を密閉する着脱可能な蓋7を設け、更に、前記第2電極2である金属電極には電極材の一部を円筒形状の中心方向に向かう突起部10とし、さらに電解容器4の内壁に突起11が設けられていることを特徴とする。   The agitation-type functional water generator 104 of the present invention has a first electrode 1 at the center and a metal electrode having a cylindrical network structure as the second electrode 2 around the first electrode 1. Between the two electrodes 2, a diaphragm 3 capable of transmitting ions and separating only gas when water was immersed was disposed. In the electrolysis vessel 4 having a substantially cylindrical structure, a swirl flow generator 5 is further provided at the lower portion of the electrolysis vessel 4, an exhaust port 6 is provided at the upper portion of the electrolysis vessel 4, and the upper portion of the second electrode portion is hermetically sealed. The metal electrode as the second electrode 2 has a part of the electrode material as a projecting portion 10 directed toward the center of the cylindrical shape, and a projection 11 is formed on the inner wall of the electrolytic vessel 4. It is provided.

本実施の形態では実施の形態3で説明した突起と同様の突起を突起11として電解容器4の内壁に設けた。第1電極1を陽極、第2電極2を陰極として電解を行うと、第1電極から酸素ガス、第2電極から水素ガスが発生する。本実施の形態では、第2電極2の突起によって発生させられる微細粒径の水素ガスが、電解容器4の突起11からも発生するせん断流で微細化される。旋回流の流路に対して高さ2〜5mm程度の突起部を設けることにより、せん断流を発生させ易くし、せん断流によって未溶存の水素ガスを数μm〜数10μm程度の微細粒径泡、いわゆるマイクロバブルとして溶解させ、水中の水素ガス濃度を更に増加させることができる。   In the present embodiment, a protrusion similar to the protrusion described in the third embodiment is provided as a protrusion 11 on the inner wall of the electrolytic vessel 4. When electrolysis is performed using the first electrode 1 as an anode and the second electrode 2 as a cathode, oxygen gas is generated from the first electrode and hydrogen gas is generated from the second electrode. In the present embodiment, the hydrogen gas having a fine particle size generated by the protrusions of the second electrode 2 is refined by a shear flow generated also from the protrusions 11 of the electrolytic vessel 4. Providing protrusions with a height of about 2 to 5 mm with respect to the flow path of the swirl flow makes it easy to generate a shear flow, and undissolved hydrogen gas bubbles with a fine particle diameter of about several μm to several tens of μm due to the shear flow. It can be dissolved as so-called microbubbles to further increase the hydrogen gas concentration in the water.

〔実施の形態5〕
本発明の別の実施例に係る形態を以下、図面に基づいて説明する。図7は、本発明に係る撹拌式機能水生成器105の構成を示す。
[Embodiment 5]
A mode according to another embodiment of the present invention will be described below with reference to the drawings. FIG. 7 shows a configuration of the agitation type functional water generator 105 according to the present invention.

本発明の撹拌式機能水生成器105は、実施の形態3の機能水生成器103の発展形である。中央部に第1電極1を配し、周囲に第2電極2として円筒状の網目構造を有する金属電極を配し、前記第1電極1と第2電極2の間に、水の浸漬時においてイオン透過可能であり気体のみ分離可能な隔膜3を配置した。略円筒構造からなる水の電解容器4において、前記電解容器4の下部に旋回流発生部5を更に設け、前記電解容器4の上部に排気口6を設け、且つ、第2電極部上部を密閉する着脱可能な蓋7を設けた。第1電極1を陽極、第2電極2を陰極として電解を行う。前記第2電極2の金属電極には、電極材の一部を円筒形状の中心方向に向かう突起部10が設けられている。本実施の形態では、更に、水素水の生成が完了した後、前記電解容器4は本体12に対して着脱可能であることを特徴とする。   The stirring type functional water generator 105 of the present invention is a development of the functional water generator 103 of the third embodiment. The first electrode 1 is arranged in the center, the metal electrode having a cylindrical network structure is arranged as the second electrode 2 in the periphery, and when the water is immersed between the first electrode 1 and the second electrode 2 A diaphragm 3 capable of ion permeation and separating only gas was disposed. In the electrolysis vessel 4 having a substantially cylindrical structure, a swirl flow generator 5 is further provided at the lower portion of the electrolysis vessel 4, an exhaust port 6 is provided at the upper portion of the electrolysis vessel 4, and the upper portion of the second electrode portion is hermetically sealed. A removable lid 7 is provided. Electrolysis is performed using the first electrode 1 as an anode and the second electrode 2 as a cathode. The metal electrode of the second electrode 2 is provided with a protruding portion 10 in which a part of the electrode material is directed toward the center of the cylindrical shape. In the present embodiment, the electrolytic vessel 4 is further detachable from the main body 12 after the generation of hydrogen water is completed.

上記本体12と電解容器4部分の接続は、ジュースミキサーなどで汎用されている接続形態などでよく、取り外しの際は、先ず上部の蓋7部分を取り外し、次いで第1電極1、第2電極2、隔壁3を備える電極容器を本体から取り外す。以上により、電解容器4に蓄えられた電解撹拌後の高濃度水素水をコップ13などに移し替えることが可能であり、また、一度コップ13に移し替え、放置されて水素が揮散してしまった水素水に再度電解撹拌をして水素を再溶存させるなど、需要者の利便性を向上させることができる。   The connection between the main body 12 and the electrolytic vessel 4 may be a connection form widely used in a juice mixer or the like. When removing, the upper lid 7 is first removed, and then the first electrode 1 and the second electrode 2 are connected. Then, the electrode container including the partition walls 3 is removed from the main body. As described above, it is possible to transfer the high-concentration hydrogen water after electrolytic stirring stored in the electrolytic vessel 4 to the cup 13 or the like, and once transferred to the cup 13 and left to stand, hydrogen has volatilized. It is possible to improve the convenience for consumers, such as re-dissolving hydrogen by electrolytically stirring again in hydrogen water.

〔実施の形態6〕   [Embodiment 6]

本実施の形態の撹拌式機能水生成器106は、実施の形態5の変形例である。構造は、図8に示す。実施の形態5と同じ機能を持つ機能部品には同じ符号を付し、説明を省略する。   The stirring type functional water generator 106 according to the present embodiment is a modification of the fifth embodiment. The structure is shown in FIG. Functional parts having the same functions as those in the fifth embodiment are denoted by the same reference numerals, and description thereof is omitted.

本発明の撹拌式機能水生成器106は、中央部に第1電極1を配し、周囲に第2電極2として円筒状の網目構造を有する金属電極を配し、前記第1電極1と第2電極2の間に、水の浸漬時においてイオン透過可能であり気体のみ分離可能な隔膜3を配置した。略円筒構造からなる水の電解容器4において、前記電解容器4の下部に旋回流発生部5を更に設け、前記電解容器4の上部に排気口6を設け、且つ、第2電極部上部を密閉する着脱可能な蓋7を設けた。実施の形態5とは、出力の極性が異なる電源部90が備えられる。   The agitation-type functional water generator 106 according to the present invention has a first electrode 1 at the center and a metal electrode having a cylindrical network structure as the second electrode 2 around the first electrode 1. Between the two electrodes 2, a diaphragm 3 that can transmit ions and separate only gas when water is immersed is disposed. In the electrolysis vessel 4 having a substantially cylindrical structure, a swirl flow generator 5 is further provided at the lower portion of the electrolysis vessel 4, an exhaust port 6 is provided at the upper portion of the electrolysis vessel 4, and the upper portion of the second electrode portion is hermetically sealed. A removable lid 7 is provided. A power supply unit 90 having a different output polarity from that of the fifth embodiment is provided.

本実施の形態では、実施の形態1〜5と異なって、第1電極1を陰極、第2電極2を陽極として電解を行う。第1電極に炭素棒、第2電極に白金コート電極を使用するのが好ましい。また、第2電極2の電極には、電極材の一部を円筒形状の中心方向に向かう突起部10が設けられている。本実施の形態では、更に、機能水の生成が完了した後、前記電解容器4は本体12に対して着脱可能であることを特徴とする。   In the present embodiment, unlike Embodiments 1 to 5, electrolysis is performed using the first electrode 1 as a cathode and the second electrode 2 as an anode. It is preferable to use a carbon rod for the first electrode and a platinum-coated electrode for the second electrode. Further, the electrode of the second electrode 2 is provided with a protruding portion 10 in which a part of the electrode material is directed toward the center of the cylindrical shape. In the present embodiment, the electrolytic vessel 4 is further detachable from the main body 12 after the generation of functional water is completed.

このような構成とすることで、本実施の形態の撹拌式機能水生成器106は、オゾン水生成器として機能する。陰極である第1電極からは水素ガスが発生し排気口6から室内に拡散する。陽極である第2電極からは酸素ガス及びオゾンガスが発生する。オゾンは酸素よりも水に溶けやすいので、結果的にオゾン水が生成される。   By setting it as such a structure, the stirring type functional water generator 106 of this Embodiment functions as an ozone water generator. Hydrogen gas is generated from the first electrode, which is the cathode, and diffuses into the room through the exhaust port 6. Oxygen gas and ozone gas are generated from the second electrode as the anode. Since ozone is more soluble in water than oxygen, ozone water is produced as a result.

略円筒構造からなる水の電解容器4の下部に旋回流発生部5を設けて、電解容器4の水を旋回させる。このようにすることで、第2電極に設けた突起部10による剪断力で酸素ガス、およびオゾンガスがさらに微細粒径泡にされる。第2電極部上部を密閉する着脱可能な蓋7は、これらのガスの溶解を促進する。   A swirl flow generator 5 is provided below the electrolytic vessel 4 having a substantially cylindrical structure, and the water in the electrolytic vessel 4 is swirled. By doing in this way, oxygen gas and ozone gas are made into a fine particle size bubble further by the shear force by the projection part 10 provided in the 2nd electrode. A detachable lid 7 that seals the upper part of the second electrode part promotes dissolution of these gases.

本実施の形態では、電解容器4に蓄えられた電解撹拌後の高濃度オゾン水をコップ13などに移し替えることが可能であり、また、一度コップ13に移し替え、放置されてしまったオゾン水に再度電解撹拌をしてオゾンを再溶存させるなど、需要者の利便性を向上させることができる。   In the present embodiment, it is possible to transfer high-concentration ozone water after electrolytic stirring stored in the electrolytic vessel 4 to a cup 13 or the like, and to ozone water that has been transferred to the cup 13 and left unattended. It is possible to improve the convenience of the consumer, for example, by re-electrolytic stirring to re-dissolve ozone.

以上、本発明の実施形態につき説明したが、本発明の範囲はこれに限定されるものではなく、発明の趣旨を逸脱しない範囲で種々の変更を加えて実施することができる。   Although the embodiments of the present invention have been described above, the scope of the present invention is not limited to these embodiments, and various modifications can be made without departing from the spirit of the invention.

〔まとめ〕
本発明の態様1において、電解槽の中心に炭素電極からなる第1電極と、金属電極からなる第2電極を設置する。第2電極は通水可能に金網構造や穴あき構造であることが好ましい。第1電極と第2電極の間に、水中のイオンは透過可能であるが空気は透過させない材質で隔壁を形成する。第1電極を陽極、第2電極を陰極として電解を行うとき、第1電極からは酸素、第2電極からは水素が発生する。
[Summary]
In the first aspect of the present invention, a first electrode made of a carbon electrode and a second electrode made of a metal electrode are installed at the center of the electrolytic cell. The second electrode preferably has a wire mesh structure or a perforated structure so that water can pass therethrough. A partition wall is formed between the first electrode and the second electrode using a material that can transmit ions in water but not air. When electrolysis is performed using the first electrode as an anode and the second electrode as a cathode, oxygen is generated from the first electrode and hydrogen is generated from the second electrode.

本発明では、気体を透過させない隔壁に妨げられて、第1電極から発生した酸素は、第2電極から発生した水素と混合されない構造となっている。第1電極から発生した酸素は、電極の上部に設置した排気口から室内へ拡散される。また、第2電極から発生した水素は、電解容器内の水に溶解される。これによって、いわゆる水素水が得られる。   In the present invention, oxygen generated from the first electrode is prevented from being mixed with hydrogen generated from the second electrode by being blocked by a partition wall that does not allow gas to pass therethrough. Oxygen generated from the first electrode is diffused into the room from an exhaust port provided at the top of the electrode. Further, hydrogen generated from the second electrode is dissolved in water in the electrolytic vessel. Thereby, so-called hydrogen water is obtained.

本発明では、水素の溶解を助けるために、電解容器の底部に撹拌装置(旋回流発生機)を設置した。また、隔壁と電解容器外郭との間は蓋によって覆われ、水中から室内への水素の拡散が防止される。   In the present invention, a stirrer (swirl flow generator) is installed at the bottom of the electrolytic vessel in order to help dissolve hydrogen. Further, the space between the partition wall and the outer shell of the electrolytic vessel is covered with a lid, so that diffusion of hydrogen from the water into the room is prevented.

本発明の態様2では、態様1で設けた蓋に圧力をかけるロック機構が追加される。これによって、電解容器中の水素濃度が高められる。   In aspect 2 of the present invention, a lock mechanism that applies pressure to the lid provided in aspect 1 is added. This increases the hydrogen concentration in the electrolytic vessel.

本発明の態様3では、第2電極に複数の突起が設けられる。突起は電解容器の径方向の内側、または外側に向いており、電解容器中の旋回流がこれらの突起に当たることでせん断力が発生する。水中の水素の泡がせん断力によって微細化され、いわゆるマイクロバブルとなって混合され、長時間安定して水中に留まることが出来る。これによって、水中の水素濃度が高くできる。   In the aspect 3 of the present invention, the second electrode is provided with a plurality of protrusions. The protrusions are directed inward or outward in the radial direction of the electrolytic container, and a shearing force is generated when the swirling flow in the electrolytic container hits these protrusions. Hydrogen bubbles in water are refined by shearing force and mixed as so-called microbubbles, and can remain in water stably for a long time. This can increase the hydrogen concentration in the water.

本発明の態様4では、態様3の構造に加えて電解容器の内壁にも突起が設けられる。突起は、第2電極に設けたものと同様の形状であって、電解容器の壁沿いの旋回流にせん断力が発生する。第2電極と電解容器壁との双方で、水中の水素の泡がせん断力によって微細化され、マイクロバブルとなって混合され、態様3よりも多くの泡が長時間安定して水中に留まることが出来る。これによって、水中の水素濃度がより高くできる。   In aspect 4 of the present invention, in addition to the structure of aspect 3, protrusions are also provided on the inner wall of the electrolytic vessel. The protrusion has the same shape as that provided on the second electrode, and a shearing force is generated in the swirling flow along the wall of the electrolytic vessel. In both the second electrode and the electrolytic vessel wall, hydrogen bubbles in water are refined by shearing force and mixed as microbubbles, and more bubbles than in mode 3 remain in water stably for a long time. I can do it. Thereby, the hydrogen concentration in water can be made higher.

本発明の態様5では、態様3で開示した電解容器部分を取り外し可能に構成した。このようにすることで、水素が溶け込んだ水素水を簡単に飲用などに使用することが出来る。   In aspect 5 of the present invention, the electrolytic container part disclosed in aspect 3 is configured to be removable. By doing in this way, hydrogen water in which hydrogen is dissolved can be easily used for drinking.

本発明の態様6では、態様5で開示した水素水発生器を第1電極と第2電極の極性を入れ替えて酸素水発生器、もしくはオゾン水発生器としたものである。第1電極を陰極、第2電極を陽極として、第1電極から水素、第2電極から酸素とオゾンを発生させる。第1電極から発生した水素は、排気口から室内へ拡散される。   In aspect 6 of the present invention, the hydrogen water generator disclosed in aspect 5 is an oxygen water generator or an ozone water generator in which the polarities of the first electrode and the second electrode are switched. Using the first electrode as a cathode and the second electrode as an anode, hydrogen is generated from the first electrode, and oxygen and ozone are generated from the second electrode. Hydrogen generated from the first electrode is diffused from the exhaust port into the room.

第2電極から発生した酸素またはオゾンは、電解容器内の水に溶解する。オゾンは酸素よりも水に溶けやすいため、いわゆるオゾン水が得られる。これによって、傷の消毒などに家庭でも簡単にオゾン水が有する殺菌力を利用することが可能になる。   Oxygen or ozone generated from the second electrode is dissolved in water in the electrolytic vessel. Since ozone is more soluble in water than oxygen, so-called ozone water is obtained. This makes it possible to easily use the bactericidal power of ozone water at home for disinfecting wounds.

1 第1電極
2 第2電極
3 隔壁
4 電解容器
5 旋回流発生部
6 排気口
7 蓋
8 ロック機構
9、90 電源部
10、11 突起部
12 本体
13 コップ
DESCRIPTION OF SYMBOLS 1 1st electrode 2 2nd electrode 3 Partition 4 Electrolysis container 5 Swirling flow generation part 6 Exhaust port 7 Lid 8 Lock mechanism 9, 90 Power supply part 10, 11 Protrusion part 12 Main body 13 Cup

Claims (5)

中央部に第1電極を配し、周囲に第2電極として円筒状の網目構造を有する金属電極を配し、前記第1電極と第2電極の間に水の浸漬時において、気体のみ分離可能な隔膜を配置した略円筒構造からなる水の電解容器において、
前記電解容器の下部に旋回流発生部を更に設け、
前記第1電極の上部に排気口を設け、且つ、第2電極部上部を密閉する着脱可能な蓋を設けたことを特徴とする、撹拌式機能水生成器。
A first electrode is arranged in the center, a metal electrode having a cylindrical network structure is arranged around the first electrode, and only gas can be separated when the water is immersed between the first electrode and the second electrode. In a water electrolysis container having a substantially cylindrical structure in which various diaphragms are arranged,
A swirl flow generator is further provided in the lower part of the electrolytic vessel,
An agitation type functional water generator, characterized in that an exhaust port is provided above the first electrode, and a detachable lid for sealing the upper part of the second electrode portion is provided.
請求項1において、前記第1電極は炭素棒であることを特徴とする、撹拌式機能水生成器。   The stirred functional water generator according to claim 1, wherein the first electrode is a carbon rod. 請求項1又は2において、前記着脱可能な蓋は加圧可能な機構を有することを特徴とする、撹拌式機能水生成器。   The stirring type functional water generator according to claim 1 or 2, wherein the detachable lid has a mechanism capable of being pressurized. 請求項1乃至3において、前記金属電極は電極材の一部を円筒形状の中心方向、又は、外方向に向かう突起部として設けることを特徴とする、撹拌式機能水生成器。   4. The agitation-type functional water generator according to claim 1, wherein the metal electrode is provided with a part of an electrode material as a projecting portion directed toward the center of the cylindrical shape or outward. 請求項1乃至4において、前記電解容器は本体に対して着脱可能であることを特徴とする、撹拌式機能水生成器。   5. The agitation type functional water generator according to claim 1, wherein the electrolytic vessel is detachable from the main body.
JP2015132293A 2015-07-01 2015-07-01 Functional water generator Expired - Fee Related JP6539131B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2015132293A JP6539131B2 (en) 2015-07-01 2015-07-01 Functional water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2015132293A JP6539131B2 (en) 2015-07-01 2015-07-01 Functional water generator

Publications (2)

Publication Number Publication Date
JP2017013001A true JP2017013001A (en) 2017-01-19
JP6539131B2 JP6539131B2 (en) 2019-07-03

Family

ID=57827971

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2015132293A Expired - Fee Related JP6539131B2 (en) 2015-07-01 2015-07-01 Functional water generator

Country Status (1)

Country Link
JP (1) JP6539131B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113278991A (en) * 2021-05-26 2021-08-20 华东理工大学 Method and device for enhancing electrolysis efficiency by using rotational flow field
JP2022158297A (en) * 2021-04-01 2022-10-17 泰章 田村 Method and apparatus for producing hydrogen water
CN115259298A (en) * 2022-09-26 2022-11-01 高唐县环境监控中心 Electrolytic catalytic oxidation sewage treatment device
JP2024054879A (en) * 2022-10-04 2024-04-18 株式会社ナノバブル研究所 Microproduct Generator

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59127793U (en) * 1983-10-17 1984-08-28 株式会社 宮川製作所 ion water water maker
WO1997046489A1 (en) * 1996-06-04 1997-12-11 Setoyama, Naomi Electrolyzed water generating apparatus, cleaning method using electrolyzed water, and cleaning agent used in same
JP2005052761A (en) * 2003-08-05 2005-03-03 Sawada Kinji Electrolyzed water forming device
JP2007136356A (en) * 2005-11-18 2007-06-07 Nikka Micron Kk Ozone water generator
JP2007196161A (en) * 2006-01-27 2007-08-09 Nikka Micron Kk Apparatus for producing hybrid ozonized water
US20100213050A1 (en) * 2009-02-17 2010-08-26 Mcalister Roy E Apparatus and method for controlling nucleation during electrolysis

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59127793U (en) * 1983-10-17 1984-08-28 株式会社 宮川製作所 ion water water maker
WO1997046489A1 (en) * 1996-06-04 1997-12-11 Setoyama, Naomi Electrolyzed water generating apparatus, cleaning method using electrolyzed water, and cleaning agent used in same
JP2005052761A (en) * 2003-08-05 2005-03-03 Sawada Kinji Electrolyzed water forming device
JP2007136356A (en) * 2005-11-18 2007-06-07 Nikka Micron Kk Ozone water generator
JP2007196161A (en) * 2006-01-27 2007-08-09 Nikka Micron Kk Apparatus for producing hybrid ozonized water
US20100213050A1 (en) * 2009-02-17 2010-08-26 Mcalister Roy E Apparatus and method for controlling nucleation during electrolysis

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022158297A (en) * 2021-04-01 2022-10-17 泰章 田村 Method and apparatus for producing hydrogen water
JP7699367B2 (en) 2021-04-01 2025-06-27 泰章 田村 Hydrogen water production method and production device
CN113278991A (en) * 2021-05-26 2021-08-20 华东理工大学 Method and device for enhancing electrolysis efficiency by using rotational flow field
CN113278991B (en) * 2021-05-26 2022-08-05 华东理工大学 Method and device for enhancing electrolysis efficiency by using rotational flow field
CN115259298A (en) * 2022-09-26 2022-11-01 高唐县环境监控中心 Electrolytic catalytic oxidation sewage treatment device
JP2024054879A (en) * 2022-10-04 2024-04-18 株式会社ナノバブル研究所 Microproduct Generator

Also Published As

Publication number Publication date
JP6539131B2 (en) 2019-07-03

Similar Documents

Publication Publication Date Title
AU2010201950B2 (en) Electrolysis device for preparation of hypochlorous water
CA2892547C (en) An electrolyzed water generating method and a generator
JP6539131B2 (en) Functional water generator
JP2016035099A (en) Hydrogen generation unit for hydrogen water production
JP2012217868A (en) Pot type generator of drinking hydrogen water
JP2018505037A (en) Functional water generator
JP6869188B2 (en) Reduction water production equipment and reduction water production method
KR20190128924A (en) A washing method using the electrolyted water of nano bubble and apparatus thereof
KR101027538B1 (en) Sterilizing electrolyzed water production apparatus, sterilized electrolyzed water production system and method comprising the same
JP6139809B1 (en) Electrolyzed water generating apparatus and electrolyzed water generating method
JP3228324U (en) Portable hydrogen water generator
JP2014113549A (en) Ozone water generator
WO2015141858A1 (en) Electrolyzed-water generation device
JP5244038B2 (en) Electrolyzed water mixing device
KR101054266B1 (en) Sterilizing electrolyzed water production apparatus, sterilized electrolyzed water production system and method comprising the same
JP3198341U (en) Simple electrolytic hydrogen water generator
JP2002069683A (en) Apparatus for manufacturing hypochlorite
JP2001191079A (en) Electrolyzed water generator
JP2008063648A (en) Apparatus for producing rinse water containing hydrogen peroxide, and method for producing rinse water containing hydrogen peroxide
JP2017148716A (en) Electrolytic hypochlorite water generator
JP4544793B2 (en) Electrolyzed water generator
JP7280854B2 (en) Electrolyzed water generator and hypochlorous acid water generation method
JP6675112B2 (en) Electrolysis raw water storage type electrolyzer
JP2016221451A (en) Electrolyzed water generation device and electrolysis unit
JP5948708B2 (en) Ozone water generator

Legal Events

Date Code Title Description
RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20161104

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20180323

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20190220

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20190305

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20190410

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20190514

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20190607

R150 Certificate of patent or registration of utility model

Ref document number: 6539131

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees