JPH06277667A - Water preparation device - Google Patents
Water preparation deviceInfo
- Publication number
- JPH06277667A JPH06277667A JP6849593A JP6849593A JPH06277667A JP H06277667 A JPH06277667 A JP H06277667A JP 6849593 A JP6849593 A JP 6849593A JP 6849593 A JP6849593 A JP 6849593A JP H06277667 A JPH06277667 A JP H06277667A
- Authority
- JP
- Japan
- Prior art keywords
- water
- diaphragm
- electrolytic cell
- electrolytic
- anode
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46152—Electrodes characterised by the shape or form
- C02F2001/46157—Perforated or foraminous electrodes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/4612—Controlling or monitoring
- C02F2201/46125—Electrical variables
- C02F2201/4613—Inversing polarity
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、整水機に関し、特には
整水機に内蔵される電解槽の構成に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water conditioner, and more particularly to the structure of an electrolytic cell incorporated in the water conditioner.
【0002】[0002]
【従来の技術】従来、整水機は、図3に示すようなプロ
セスでイオン水を生成していた。すなわち、整水機は水
道水等の原水に含まれるカルキや有機物等を取り除くた
めの活性炭フィルタ20と、雑菌や水中に含まれる錆等
を取り除く0.1μm程度の中空糸フィルタ21とを用
いて濾過して浄水とし、その浄水を数ミリ・メートル程
度の間隔をおいて設置された陽極22と陰極23と両電
極間にそれらと接触しないように設置された隔膜24と
を備える電解槽25中で電解して水の電気分解反応を起
こさせることにより、陽極22側で下式(1)に示すよ
うな酸素発生反応が生じさせて、酸素ガスと同時に生成
されるH+イオンにより酸性イオン水を生成し、同様
に、陰極23側で下式(2)に示すような水素発生反応
が生じさせて、水素ガスと同時に生成されるOHーイオ
ンによりアルカリイオン水を生成していた。2. Description of the Related Art Conventionally, water purifiers have produced ionic water by the process shown in FIG. That is, the water conditioner uses an activated carbon filter 20 for removing chlorine and organic substances contained in raw water such as tap water, and a hollow fiber filter 21 of about 0.1 μm for removing various bacteria and rust contained in water. In an electrolytic cell 25, which is filtered to obtain purified water, and which comprises the anode 22 and the cathode 23 installed at intervals of about several millimeters and a diaphragm 24 installed between both electrodes so as not to contact them. Electrolysis of water to cause an electrolysis reaction of water causes an oxygen generation reaction as shown in the following formula (1) on the anode 22 side, and H + ions generated at the same time as oxygen gas generate acidic ionized water. generates, similarly, a hydrogen generating reaction as shown in the following equation (2) gives rise at the cathode 23 side, was generated alkali ion water by OH chromatography ions generated simultaneously with the hydrogen gas.
【0003】[0003]
【化1】 [Chemical 1]
【0004】そして、これらのイオン水は隔膜24によ
って隔てられ、中和されることなく、それぞれ単独に取
り出すことができるようになっていた。These ionized waters are separated by the diaphragm 24 and can be independently taken out without being neutralized.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、上述し
たような従来の整水機では、電解に用いられる浄水の電
導度が小さいため、電極間隔が数ミリ・メートル程度で
あっても浄水の電気分解を起こすためには大きな電圧が
必要であった。また、電解電圧を小さくするために、電
極間隔を小さくする試みも行われているが、電極間隔を
小さくすると水の流路が狭くなり、電気分解ら必要な流
量が得られないという問題点があるため、根本的な解決
策にはなっていなかった。However, in the conventional water purifier as described above, since the electric conductivity of the purified water used for electrolysis is small, electrolysis of the purified water is performed even if the electrode interval is about several millimeters. A large voltage was required to cause In addition, in order to reduce the electrolysis voltage, attempts have been made to reduce the electrode spacing, but when the electrode spacing is reduced, the flow path of water becomes narrow, and there is a problem that the required flow rate cannot be obtained by electrolysis. As such, it was not a fundamental solution.
【0006】本発明は、上述した問題点を解決するため
になされたものであり、電解電圧が小さく、流路設計の
自由度の高い電解槽を備えた整水機を提供することを目
的としている。The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a water conditioner provided with an electrolytic cell having a small electrolysis voltage and a high degree of freedom in flow channel design. There is.
【0007】[0007]
【課題を解決するための手段】この目的を達成するため
に本発明の整水機は、内蔵される電解槽内に多孔質、あ
るいはメッシュ状の電極が隔膜に対して密着させた状態
で配設されている。In order to achieve this object, the water conditioner of the present invention is arranged in a built-in electrolytic cell with a porous or mesh-shaped electrode in close contact with a diaphragm. It is set up.
【0008】[0008]
【作用】上記の構成を有する本発明の整水機に内蔵され
る電解槽内には多孔質、あるいはメッシュ状の電極が隔
膜に対して密着させた状態で配設されており、内蔵され
る電解槽の電極間隔を隔膜の厚さにまで小さくすること
ができるため、電解電圧が小さくなる。また、電解され
る水の流路が電極の外側に設けられるため、電解電圧に
影響を与えることなく所定の流量が得られるよう自由に
設計することができる。The porous or mesh electrode is disposed in close contact with the diaphragm in the electrolytic cell incorporated in the water conditioner of the present invention having the above-mentioned structure and is incorporated therein. Since the electrode interval of the electrolytic cell can be reduced to the thickness of the diaphragm, the electrolysis voltage is reduced. Further, since the flow path of water to be electrolyzed is provided outside the electrode, it can be freely designed so as to obtain a predetermined flow rate without affecting the electrolysis voltage.
【0009】[0009]
【実施例】以下、本発明を具体化した一実施例を図面を
参照して説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.
【0010】まず始めに、図1を用いて本発明の整水機
に内蔵される電解槽1の構成を説明する。供給される水
の電気分解を行うための電極して設けられる陽極2、陰
極3は、ともに厚さ1mm(ミリ・メートル)のチタン板をエ
キスパンド加工してメッシュ状にした後、表面に白金メ
ッキを0.5μm(マイクロ・メートル)施したものである。そ
して、それら陽極2と陰極3の間には隔膜4が挟持され
ており、この隔膜4は、酸化チタンにより親水性を持た
せた厚さ0.2mmのフッ化ポリビニリデン樹脂の多孔
質シートにより構成されている。また、前記両電極の外
側には、ABS樹脂成型により作製された電解ケース5
が配設されており、この電解ケース5は陽極2、隔膜
4、陰極3の順で重ねた電極および隔膜を保持するとと
もに電解される水の流路を確保するシリコンスペーサ6
を電極との間に挟んだ状態で、ボルト7・ナット8で固
定されており、これらにより電解槽1が構成されてい
る。ここにおいて、前記電解槽1の見かけの電極面積は
100cm2(平方センチメートル)であり、図2は、上記のよ
うに構成される電解槽の断面図である。First, the structure of the electrolytic cell 1 incorporated in the water conditioner of the present invention will be described with reference to FIG. The anode 2 and the cathode 3, which are provided as electrodes for electrolyzing the supplied water, are made by expanding a titanium plate having a thickness of 1 mm (millimeters) into a mesh, and then plating the surface with platinum. 0.5 μm (micrometer). A diaphragm 4 is sandwiched between the anode 2 and the cathode 3, and the diaphragm 4 is made of a polyvinylidene fluoride porous sheet having a thickness of 0.2 mm and made hydrophilic by titanium oxide. It is configured. In addition, an electrolytic case 5 made by ABS resin molding is provided on the outside of both electrodes.
This electrolytic case 5 holds an electrode, a diaphragm, and an electrode in which an anode 2, a diaphragm 4, and a cathode 3 are stacked in this order, and a silicon spacer 6 that secures a flow path of water to be electrolyzed.
Is fixed with bolts 7 and nuts 8 in a state of being sandwiched between the electrodes and the electrodes, and these constitute the electrolytic cell 1. Here, the apparent electrode area of the electrolytic cell 1 is 100 cm 2 (square centimeter), and FIG. 2 is a sectional view of the electrolytic cell configured as described above.
【0011】次に図2を用いて本発明の整水機によるイ
オン水の生成プロセスを順に説明する。まず始めに、給
送されてくる水道水を活性炭フィルタ、中空糸フィルタ
により濾過して浄水とし、その浄水を入水口9から電解
槽1中に導入する。導入された浄水は、電解槽下部で陽
極室10と陰極室11に分けられ、それぞれの電極室を
電解槽上部に向かって流れる。次に、陽極2、陰極3間
には電位差が与えられ、陽極2側では酸素発生反応によ
りH+イオンが生じ、陽極室10内の水は酸性になる。
一方、陰極3側では水素発生反応によりOH-イオンが
生じ、陰極室11内の水はアルカリ性となる。そして、
酸性となった陽極室10内の水、アルカリ性となった陰
極室11内の水は、電解槽上部の酸性水出口12、アル
カリ水出口13よりそれぞれ排出される。Next, the production process of ionized water by the water purifier of the present invention will be described in order with reference to FIG. First, the supplied tap water is filtered by an activated carbon filter and a hollow fiber filter to obtain purified water, and the purified water is introduced into the electrolytic cell 1 through the water inlet 9. The purified water introduced is divided into an anode chamber 10 and a cathode chamber 11 at the lower part of the electrolytic cell, and flows through the respective electrode chambers toward the upper part of the electrolytic cell. Next, a potential difference is applied between the anode 2 and the cathode 3, H + ions are generated by the oxygen generation reaction on the anode 2 side, and the water in the anode chamber 10 becomes acidic.
On the other hand, on the cathode 3 side, OH − ions are generated by the hydrogen generation reaction, and the water in the cathode chamber 11 becomes alkaline. And
Water in the anode chamber 10 that has become acidic and water in the cathode chamber 11 that has become alkaline are respectively discharged from the acidic water outlet 12 and the alkaline water outlet 13 at the upper part of the electrolytic cell.
【0012】次に、上述した本発明の整水機を用いて、
実際に酸性水、アルカリ水の生成実験を行った結果につ
いて詳述する。まず始めに、実験の条件としては、電解
は定電圧方式を用い、電圧はDC10V(ホ゛ルト)とし
た。電解水は活性炭フィルタ、0.1μmの中空糸フィ
ルタを通した浄水を用い、流量はアルカリ水流量2.0
l/min(リットル毎分)、酸性水流量2.0l/min
とした。実験の結果、アルカリ水pH10.2、酸性水
pH4.0が得られた、電解電流は2.0A(アンヘ゜ア)
であった。比較のため、従来タイプの電解槽を備えた整
水機でも同様な実験を行った。実験に用いた整水機の電
解槽は、電極面積300cm2、電極間距離3.0mm
である。電解は定電圧方式を用い電圧はDC25Vとし
た。電解水は、前記実験と同様、活性炭フィルタ、中空
糸フィルタを通した浄水を用い、アルカリ水流量2.0
L/min、酸性水流量2.0L/minとした。実験
の結果、アルカリ水pH9.9、酸性水pH4.7、電
解電流1.5Aであった。Next, using the above-described water conditioner of the present invention,
The results of actual experiments of generating acidic water and alkaline water will be described in detail. First, as the conditions of the experiment, a constant voltage system was used for electrolysis and the voltage was DC 10V (volt). The electrolyzed water used is an activated carbon filter, purified water that has passed through a 0.1 μm hollow fiber filter, and the flow rate is an alkaline water flow rate of 2.0.
l / min (liter / min), acidic water flow 2.0 l / min
And As a result of the experiment, alkaline water pH 10.2 and acidic water pH 4.0 were obtained, and the electrolysis current was 2.0 A (ampere).
Met. For comparison, a similar experiment was conducted using a water conditioner equipped with a conventional type electrolytic cell. The electrolytic cell of the water conditioner used in the experiment had an electrode area of 300 cm 2 and an electrode distance of 3.0 mm.
Is. A constant voltage system was used for electrolysis, and the voltage was DC 25V. As the electrolyzed water, as in the above experiment, purified water that had been passed through an activated carbon filter and a hollow fiber filter was used, and an alkaline water flow rate was 2.0.
L / min, and acidic water flow rate was 2.0 L / min. As a result of the experiment, the pH of the alkaline water was 9.9, the pH of the acidic water was 4.7, and the electrolytic current was 1.5A.
【0013】以上の実験結果からわかるように、本発明
の整水機は、電極面積が従来のものの1/3にもかかわ
らず、2/5の電圧で1.3倍の電解電流を流すことが
でき、その結果より、高濃度のアルカリ水、酸性水を得
ることができた。また、本発明の整水機に内蔵された電
解槽1は、電極2,3、隔膜4等を変更することなくシ
リコンスペーサ6の厚みを変更し、流路を変えることに
より、所定の圧力で所定の流量を得ることができた。さ
らに、隔膜4の保持を電極2,3が行ってくれるため、
隔膜4を保持するための部品が必要ないというメリット
も得られた。As can be seen from the above experimental results, the water purifier according to the present invention can flow an electrolytic current of 1.3 times at a voltage of 2/5, though the electrode area is 1/3 that of the conventional one. As a result, highly concentrated alkaline water and acidic water could be obtained. In addition, the electrolytic cell 1 built in the water conditioner of the present invention has a predetermined pressure by changing the thickness of the silicon spacer 6 without changing the electrodes 2, 3, the diaphragm 4, etc., and changing the flow path. A predetermined flow rate could be obtained. Furthermore, since the electrodes 2 and 3 hold the diaphragm 4,
The merit that no part for holding the diaphragm 4 is required is also obtained.
【0014】[0014]
【発明の効果】以上詳述したことから明かなように、本
発明の整水機は、内蔵される電解槽内に多孔質、あるい
はメッシュ状の電極を隔膜に対して密着させた状態で配
設したことにより、電解槽の電極間隔を隔膜の厚さにま
で小さくすることができるため、電解電圧を小さくする
ことができ、また、電解される水の流路を電極の外側に
設けることにより、電解電圧に影響を与えず、所定の流
量が得られるよう自由に設計することができる。EFFECTS OF THE INVENTION As is clear from the above description, the water conditioner of the present invention is provided with a porous or mesh-shaped electrode placed in close contact with the diaphragm in the built-in electrolytic cell. By providing the electrolysis tank, the electrode interval can be reduced to the thickness of the diaphragm, so that the electrolysis voltage can be reduced, and the passage of water for electrolysis can be provided outside the electrodes. It can be freely designed so that a predetermined flow rate can be obtained without affecting the electrolysis voltage.
【図1】図1は本発明の整水機に内蔵される電解槽の構
成を示す図である。FIG. 1 is a diagram showing a configuration of an electrolytic cell incorporated in a water conditioning machine of the present invention.
【図2】図2は図1に示す電解槽の断面図である。2 is a cross-sectional view of the electrolytic cell shown in FIG.
【図3】図3は従来の整水機の構成を示す図である。FIG. 3 is a diagram showing a configuration of a conventional water conditioning machine.
1 電解槽 2 陽極 3 陰極 4 隔膜 1 Electrolyzer 2 Anode 3 Cathode 4 Diaphragm
Claims (1)
メッシュ状の電極を隔膜に対して密着させた状態で配設
したことを特徴とする整水機。1. A water conditioner characterized in that a porous or mesh-shaped electrode is provided in a built-in electrolytic bath in a state of being in close contact with a diaphragm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6849593A JPH06277667A (en) | 1993-03-26 | 1993-03-26 | Water preparation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6849593A JPH06277667A (en) | 1993-03-26 | 1993-03-26 | Water preparation device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06277667A true JPH06277667A (en) | 1994-10-04 |
Family
ID=13375339
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6849593A Pending JPH06277667A (en) | 1993-03-26 | 1993-03-26 | Water preparation device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06277667A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001027037A1 (en) * | 1999-10-14 | 2001-04-19 | Ecoaid Corp. | Apparatus for producing high-concentration electrolytic water |
KR20010035910A (en) * | 1999-10-04 | 2001-05-07 | 문재덕 | High Efficiency Electrolytic Water Production Equipment |
EP1592644A1 (en) * | 2003-01-17 | 2005-11-09 | Anderson H. Kim | In-water discharging core and sterilizing water supplying system using said core |
-
1993
- 1993-03-26 JP JP6849593A patent/JPH06277667A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010035910A (en) * | 1999-10-04 | 2001-05-07 | 문재덕 | High Efficiency Electrolytic Water Production Equipment |
WO2001027037A1 (en) * | 1999-10-14 | 2001-04-19 | Ecoaid Corp. | Apparatus for producing high-concentration electrolytic water |
EP1592644A1 (en) * | 2003-01-17 | 2005-11-09 | Anderson H. Kim | In-water discharging core and sterilizing water supplying system using said core |
EP1592644A4 (en) * | 2003-01-17 | 2006-10-04 | Anderson H Kim | In-water discharging core and sterilizing water supplying system using said core |
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