JPH06285467A - Water conditioning machine - Google Patents

Water conditioning machine

Info

Publication number
JPH06285467A
JPH06285467A JP7937193A JP7937193A JPH06285467A JP H06285467 A JPH06285467 A JP H06285467A JP 7937193 A JP7937193 A JP 7937193A JP 7937193 A JP7937193 A JP 7937193A JP H06285467 A JPH06285467 A JP H06285467A
Authority
JP
Japan
Prior art keywords
water
reverse osmosis
filter
pure water
electrolytic cell
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
Application number
JP7937193A
Other languages
Japanese (ja)
Inventor
Kazuo Kobayashi
和夫 小林
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.)
Brother Industries Ltd
Original Assignee
Brother Industries Ltd
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 Brother Industries Ltd filed Critical Brother Industries Ltd
Priority to JP7937193A priority Critical patent/JPH06285467A/en
Publication of JPH06285467A publication Critical patent/JPH06285467A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/4618Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE:To provide a water conditioning machine which produces ionic water having constant properties from any kind of raw water by installing a reverse osmosis membrane which can give pure water, a feeder which makes desirable water by conditioning, and an electrolytic cell which electolyzes the conditioned water. CONSTITUTION:A water conditioning machine 1 comprises an active carbon filter 2 which removes chlorinated lime and organic substances contained in raw water such as city water, a hollow fiber filter 3 which removes bacteria and fine particles, a reverse osmosis filter 4 which removes ions and dissolved gas, a feeder 5 which feeds a desired material into the obtained pure water for conditioning, and an electrolytic cell 8 in which the conditioned water is converted by electrolysis into alkaline ionic water on the cathode 6 side and into acid ionic water on the anode side. In the water conditioning machine, pure water is obtained from raw water by the reverse osmosis filter 4, desired conditioned water is produced by incorporating an optional material fed from the feeder 5 into the obtained pure water, and the conditioned water is electrolyzed by the electrolytic cell 5.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、整水機に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water regulating machine.

【0002】[0002]

【従来の技術】従来、整水機は、図6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
道水等の原水を、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、その浄水を陽極22と陰極23と隔膜
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を生じさせて、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)に示ような水素発生反
応を生じさせて、水素ガスと同時に生成されるOH
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, a water purifier has produced ionized water by a process as shown in FIG. That is, the water purifier filters raw water such as tap water using an activated carbon filter 20 for removing chlorine and organic matter, and a hollow fiber filter 21 of about 0.1 μm for removing various bacteria and rust contained in water. To produce purified water, and the purified water is electrolyzed in an electrolytic bath 25 having an anode 22, a cathode 23, and a diaphragm 24 to cause an electrolysis reaction of water, so that the anode 22 has the following formula (1). H 2 + ions generated at the same time as oxygen gas to generate acidic ionized water,
Similarly, cause hydrogen generating reaction shown as the following formula (2) 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における活性炭フィルタでは、水
道水中に含まれるイオンや溶存気体を、ほとんど吸着す
ることができなかった。また、前記イオンや溶存気体の
分子は大きさが0.01μm以下であるため、0.1μ
m程度の中空糸フィルタではほとんど取り除くことがで
きなかった。さらには、水道水中に含まれるイオンや溶
存気体の成分や量は、地域や季節、時には時刻によって
変化するものであるため、電解に用いる浄水のイオンや
溶存気体の成分や量は千差万別であった。その結果、浄
水の電導度が一定せず電解条件に影響を与えていた。ま
た、さらには具体的な成分の影響を列挙すれば、浄水中
のカルシウムイオン、マグネシウムイオン量の変化は、
イオン水中のミネラル濃度の変化をもたらし、溶存二酸
化炭素、炭酸イオン、溶存アンモニア、硝酸イオンは、
+イオン、OH-イオンに対して緩衝作用を持つため、
イオン水のpHに影響を与えていた。一方、塩素イオン
濃度の変化は、イオン水中に含まれる残留塩素濃度に影
響を与えるとともに、イオン水の酸化還元電位にも影響
を及ぼしていた。このように、従来の整水機では、所望
のpHやミネラル濃度、酸化還元電位等の特性を持った
イオン水を安定して得るのは困難であった。
However, the activated carbon filter in the conventional water conditioner as described above could hardly adsorb ions and dissolved gas contained in tap water. In addition, since the size of the ions or dissolved gas molecules is 0.01 μm or less,
It could hardly be removed with a hollow fiber filter of about m. Furthermore, since the components and amounts of ions and dissolved gases contained in tap water vary depending on the region, season, and sometimes the time, the components and amounts of ions and dissolved gases used in electrolysis water vary widely. Met. As a result, the conductivity of the purified water was not constant and affected the electrolysis conditions. Moreover, if the effects of specific components are listed, changes in the amount of calcium ion and magnesium ion in purified water are as follows:
It causes a change in the mineral concentration in ionized water, and dissolved carbon dioxide, carbonate ions, dissolved ammonia, nitrate ions,
Since it has a buffering effect on H + and OH ions,
It affected the pH of ionized water. On the other hand, the change in the chlorine ion concentration affected not only the residual chlorine concentration contained in the ionized water but also the redox potential of the ionized water. As described above, it has been difficult to stably obtain ion water having desired characteristics such as pH, mineral concentration, and redox potential with the conventional water purifier.

【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、如何なる原水を用いても常に一
定の特性を持ったイオン水を得ることのできる整水機を
提供することを目的としている。
The present invention has been made in order to solve the above-mentioned problems, and it is an object of the present invention to provide a water conditioner capable of always obtaining ionized water having a certain characteristic even if any raw water is used. Has an aim.

【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、水道水等の原水を通過させて純水
を得ることが可能な逆浸透膜と、その逆浸透膜により得
られる純水に対して任意の物質を添加し、所望の水に調
整する添加装置と、その添加装置により調整された水を
電解する電解槽とを備えている。
In order to achieve this object, a water purifier according to the present invention comprises a reverse osmosis membrane capable of passing through raw water such as tap water to obtain pure water, and a reverse osmosis membrane thereof. It is provided with an adding device for adding an arbitrary substance to the pure water obtained by the above to adjust it to a desired water, and an electrolytic cell for electrolyzing the water adjusted by the adding device.

【0008】また、前記逆浸透膜が原水を純水と濃縮水
とに分ける機能を有し、更には前記電解層が前記添加装
置により調整された水を陰極側で電解し、且つ前記濃縮
水を陽極側で電解するものであってもよい。
Further, the reverse osmosis membrane has a function of dividing raw water into pure water and concentrated water, and further, the electrolytic layer electrolyzes water adjusted by the adding device on the cathode side, and May be electrolyzed on the anode side.

【0009】或いは、前記逆浸透膜が原水を純水と濃縮
水とに分ける機能を有し、更には前記電解層が前記添加
装置により調整された水を陽極側で電解し、且つ前記濃
縮水を陰極側で電解するものであってもよい。
Alternatively, the reverse osmosis membrane has a function of dividing raw water into pure water and concentrated water, and further, the electrolytic layer electrolyzes water adjusted by the adding device on the anode side, and May be electrolyzed on the cathode side.

【0010】[0010]

【作用】上記の構成を有する本発明の整水機は、原水か
ら逆浸透膜を用いて純水を得た後、その純水に添加装置
より任意の物質を添加することにより所望の水を調整
し、その調整した水を電解槽により電解するため、原水
に含まれるイオンや溶存気体に影響を受けることなく、
所望のアルカリイオン水、酸性イオン水を安定して得る
ことができる。
In the water purifier of the present invention having the above-mentioned structure, pure water is obtained from raw water by using a reverse osmosis membrane, and then a desired water is added to the pure water by adding an arbitrary substance to the pure water. It is adjusted and the adjusted water is electrolyzed by the electrolyzer, so it is not affected by the ions and dissolved gas contained in the raw water.
The desired alkaline ionized water and acidic ionized water can be stably obtained.

【0011】また、アルカリイオン水のみが一定の特性
を有しておれば良い場合においては、原水を、逆浸透膜
を通過した純水と残りの濃縮水に分け、純水に任意の物
質を添加した水を電解槽の陰極側で、濃縮水を陽極側で
電解することにより、上記構造に比較してより多量の所
望のアルカリイオン水を安定して得ることができる。
Further, when only the alkaline ionized water needs to have a certain characteristic, the raw water is divided into pure water which has passed through the reverse osmosis membrane and the remaining concentrated water, and the pure water is charged with an arbitrary substance. By electrolyzing the added water on the cathode side and the concentrated water on the anode side of the electrolytic cell, a larger amount of desired alkaline ionized water can be stably obtained as compared with the above structure.

【0012】また同様に、酸性イオン水のみが一定の特
性有しておれば良い場合においては、原水を、逆浸透膜
を通過した純水と残りの濃縮水に分け、純水に任意の物
質を添加した水を電解槽の陽極側で、濃縮水を陰極側で
電解することにより、より多量の所望の酸性イオン水を
安定して得ることができる。
Similarly, in the case where only acidic ionized water needs to have a certain characteristic, the raw water is divided into pure water that has passed through the reverse osmosis membrane and the remaining concentrated water, and the pure water is mixed with any substance. It is possible to stably obtain a larger amount of the desired acidic ionized water by electrolyzing the water added with the water on the anode side of the electrolytic cell and the concentrated water on the cathode side.

【0013】[0013]

【実施例】以下、本発明を具体化した実施例を図面を参
照して説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0014】まず始めに、図1を用いて本発明の第1の
実施例である整水機1の構成の概要を説明する。この整
水機1は、水道水等の原水中に含まれるカルキや有機物
を除去するための活性炭フィルタ2と、雑菌や微粒子を
取り除くための0.1μmの中空糸フィルタ3と、イオ
ンや溶存気体を取り除く逆浸透フィルタ4と、得られた
純水に所望の物質を添加し調整するための添加装置5
と、調整された水を電解して陰極6側でアルカリイオン
水、陽極7側で酸性イオン水を生成するための電解槽8
とから構成されている。尚、前記電解槽8はポリエステ
ル不織布の隔膜9を用いた2室式の電解槽であり、電極
は陰極6、陽極7ともにチタン基板に白金メッキを施し
たものを用いた。
First, an outline of the configuration of a water leveling machine 1 according to the first embodiment of the present invention will be described with reference to FIG. This water purifier 1 is composed of an activated carbon filter 2 for removing chlorine and organic substances contained in raw water such as tap water, a 0.1 μm hollow fiber filter 3 for removing bacteria and fine particles, and ions and dissolved gas. Reverse osmosis filter 4 for removing impurities, and addition device 5 for adding and adjusting a desired substance to the obtained pure water
And an electrolyzer 8 for electrolyzing the adjusted water to generate alkaline ionized water on the cathode 6 side and acidic ionized water on the anode 7 side.
It consists of and. The electrolytic cell 8 is a two-chamber type electrolytic cell using a diaphragm 9 of polyester non-woven fabric, and both the cathode 6 and the anode 7 are formed by plating a titanium substrate with platinum.

【0015】また、前記逆浸透フィルタ4は、図2に示
すように、ポリアミド樹脂で作成された逆浸透膜10
と、水路を確保するためのポリプロピレン不織布11を
重ねてスパイラル状に巻いた構造となっている。そし
て、前記不織布11の両端面は、図3に示すように1枚
おきに逆浸透膜10によりカバーされている。
As shown in FIG. 2, the reverse osmosis filter 4 has a reverse osmosis membrane 10 made of polyamide resin.
And a polypropylene non-woven fabric 11 for securing a water channel is overlapped and spirally wound. The opposite end surfaces of the nonwoven fabric 11 are covered with the reverse osmosis membrane 10 every other sheet, as shown in FIG.

【0016】次に、図2を用いて逆浸透フィルタ4によ
って水道水から純水を得る工程を説明する。まず始め
に、フィルタの片側端面から圧力を加えて水道水を送る
と、その水道水は端面のカバーされていない不織布11
中を通って逆浸透フィルタ4内に導入される。そして、
導入された水の一部は、圧力によって逆浸透膜10を通
過し、純水となって両端がカバーされた不織布中11に
導かれ、さらにスパイラルの中心部に集められて純水出
口12から取り出される。一方、残りの水は濃縮されて
反対側の端面で集められ、濃縮水出口13から排出され
る。ここにおいて、得られる純水と濃縮水の割合は1:
1程度である。この逆浸透フィルタ4の能力を確認する
ため、水道水と、水道水を活性炭フィルタ2、中空糸フ
ィルタ3、逆浸透膜フィルタ4で処理した水の特性比較
を行った結果を表1に示す。
Next, the process of obtaining pure water from tap water by the reverse osmosis filter 4 will be described with reference to FIG. First, when tap water is sent by applying pressure from one end face of the filter, the tap water is not covered by the non-woven fabric 11 on the end face.
It is introduced into the reverse osmosis filter 4 through the inside. And
A part of the introduced water passes through the reverse osmosis membrane 10 by pressure, becomes pure water, is guided to the inside of the nonwoven fabric 11 whose both ends are covered, and is further collected at the center of the spiral to be discharged from the pure water outlet 12. Taken out. On the other hand, the remaining water is concentrated and collected on the opposite end face and discharged from the concentrated water outlet 13. Here, the ratio of pure water and concentrated water obtained is 1:
It is about 1. In order to confirm the performance of the reverse osmosis filter 4, Table 1 shows the results of characteristics comparison between tap water and water obtained by treating tap water with the activated carbon filter 2, the hollow fiber filter 3 and the reverse osmosis membrane filter 4.

【0017】[0017]

【表1】 [Table 1]

【0018】上記表より、目的の純水が得られているこ
とが確認された。
From the above table, it was confirmed that the desired pure water was obtained.

【0019】次に、本実施例の整水機1を用い、3種類
の水道水を用いて実際にイオン水生成実験を行った。
尚、実験は炭酸量、硬度、残留塩素、pHに注目して行
った。以下、3種類の水道水の特性を表2に示す。
Next, using the water purifier 1 of this embodiment, an ion water production experiment was actually conducted using three types of tap water.
The experiment was conducted by paying attention to the amount of carbonic acid, hardness, residual chlorine and pH. The characteristics of the three types of tap water are shown in Table 2 below.

【0020】[0020]

【表2】 [Table 2]

【0021】実験条件として、電解電流は1A(アンヘ゜
ア)、総流量2.0L/min(リットル毎分)、陰極6
側、陽極7側ともに0.5L/min、捨て水(濃縮
水)1.0L/minとした。また、添加剤としては、
陰極6側は乳酸カルシウム、陽極7側は塩化カルシュウ
ムを用い、それぞれ純水で1mol/L(モル毎リットル)に
調整した後、定量ポンプを用いてそれぞれの極側へ10
-3mol/Lになるよう添加した。
As experimental conditions, the electrolysis current was 1 A (ampere), the total flow rate was 2.0 L / min (liter / min), and the cathode 6 was used.
Side and anode 7 side were 0.5 L / min, and the waste water (concentrated water) was 1.0 L / min. Moreover, as an additive,
Calcium lactate was used for the cathode 6 side, calcium chloride was used for the anode 7 side, and each was adjusted to 1 mol / L (mol per liter) with pure water, and then 10 electrodes were applied to each electrode side using a metering pump.
-3 mol / L was added.

【0022】実験によって陰極6側から得られたアルカ
リイオン水、陽極7側から得られた酸性イオン水の特性
を表3に示す。
Table 3 shows the characteristics of the alkaline ionized water obtained from the cathode 6 side and the acidic ionized water obtained from the anode 7 side by the experiment.

【0023】[0023]

【表3】 [Table 3]

【0024】表より明らかなように、本実施例の整水機
1は、原水の特性にかかわらず常に一定の特性のアルカ
リイオン水、酸性イオン水を得ることができる。
As is apparent from the table, the water purifier 1 of this embodiment can always obtain alkaline ionized water and acidic ionized water having a constant characteristic regardless of the characteristic of the raw water.

【0025】次に、図4を用いて、本発明の第2の実施
例の構成を説明する。整水機14は、水道水中に含まれ
るカルキや有機物を除去するための活性炭フィルタ2
と、雑菌や微粒子を取り除くための0.1μmの中空糸
フィルタ3と、イオンや溶存気体を取り除く逆浸透フィ
ルタ4と、得られた純水に所望の物質を添加して調整す
るための添加装置5と、調整された水を陰極6側で電解
してアルカリイオン水を生成し、純水と同時に生成する
濃縮水を陽極7側で電解して酸性イオン水を生成するた
めの電解槽8とから構成されている。尚、前記逆浸透フ
ィルタ4から電解槽8までの流路以外はすべて第1の実
施例と同じものをのを用いた。
Next, the configuration of the second embodiment of the present invention will be described with reference to FIG. The water conditioner 14 is an activated carbon filter 2 for removing chlorine and organic matter contained in tap water.
A hollow fiber filter 3 of 0.1 μm for removing bacteria and fine particles, a reverse osmosis filter 4 for removing ions and dissolved gas, and an addition device for adjusting a desired substance by adding a desired substance to the obtained pure water. 5 and an electrolytic cell 8 for electrolyzing the adjusted water on the cathode 6 side to generate alkaline ionized water, and for electrolyzing concentrated water produced simultaneously with pure water on the anode 7 side to generate acidic ionized water. It consists of In addition, except for the flow path from the reverse osmosis filter 4 to the electrolytic cell 8, the same one as in the first embodiment was used.

【0026】本実施例の整水機14を用い、3種類の水
道水を用いて実際にイオン水生成実験を行った。ここに
おいて、実験は炭酸量、硬度、残留塩素、pHに注目し
て行なった。また、前記3種類の水道水の特性は上述の
第1の実施例の実験に用いた表2に示したものと同様で
ある。
Using the water conditioner 14 of this embodiment, an ion water production experiment was actually conducted using three types of tap water. Here, the experiment was conducted paying attention to the amount of carbonic acid, hardness, residual chlorine, and pH. The characteristics of the three types of tap water are the same as those shown in Table 2 used in the experiment of the first embodiment described above.

【0027】実験条件として、電解電流は1A、総流量
2.0L/min、陰極6側、陽極7側ともに1.0L
/minとした。また、添加剤は乳酸カルシウムを用
い、純水で1mol/Lに調整した後、定量ポンプを用
いて陰6極側へ10-3mol/Lになるよう添加した。
この実験によって陰極6側から得られたアルカリイオン
水、陽極7側から得られた酸性イオン水の特性を表4に
示す。
As experimental conditions, the electrolysis current was 1 A, the total flow rate was 2.0 L / min, and both the cathode 6 side and the anode 7 side were 1.0 L.
/ Min. In addition, calcium lactate was used as an additive, and after adjusting to 1 mol / L with pure water, it was added to the negative 6-electrode side so as to be 10 −3 mol / L using a metering pump.
Table 4 shows the characteristics of the alkaline ionized water obtained from the cathode 6 side and the acidic ionized water obtained from the anode 7 side by this experiment.

【0028】[0028]

【表4】 [Table 4]

【0029】表より明らかなように、本実施例の整水機
14は、原水の特性にかかわらず常に一定の特性のアル
カリイオン水を得ることができる。また、得られる水量
は実施例1に比較して約2倍となるため、アルカリイオ
ン水のみが必要な場合には有効な手段である。
As is clear from the table, the water conditioner 14 of this embodiment can always obtain alkaline ionized water having a constant characteristic regardless of the characteristic of the raw water. In addition, the amount of water obtained is about twice as large as that in Example 1, so this is an effective means when only alkaline ionized water is required.

【0030】次に、図5を用いて、本発明の第3の実施
例を説明する。整水機15は、水道水中に含まれるカル
キや有機物を除去するための活性炭フィルタ2と、、雑
菌や微粒子を取り除くための0.1μmの中空糸フィル
タ3と、、イオンや溶存気体を取り除く逆浸透フィルタ
4と、得られた純水に所望の物質を添加し調整するため
の添加装置5と、調整された水を陽極7側で電解して酸
性イオン水を生成し、純水と同時に生成する濃縮水を陰
極6側で電解してアルカリイオン水を生成するための電
解槽8とから構成されており、第2の実施例に示す電解
槽8の極性を反転させたものである。
Next, a third embodiment of the present invention will be described with reference to FIG. The water conditioner 15 includes an activated carbon filter 2 for removing chlorine and organic substances contained in tap water, a 0.1 μm hollow fiber filter 3 for removing bacteria and fine particles, and a reverse filter for removing ions and dissolved gas. The permeation filter 4, an addition device 5 for adding and adjusting a desired substance to the obtained pure water, and the adjusted water is electrolyzed on the anode 7 side to generate acidic ionized water, which is generated at the same time as pure water. The electrolyzer 8 for electrolyzing the concentrated water to generate alkaline ionized water on the side of the cathode 6 is the inversion of the polarity of the electrolyzer 8 shown in the second embodiment.

【0031】本実施例の整水機15を用い、3種類の水
道水を用いて実際にイオン水生成実験を行った。尚、実
験は炭酸量、硬度、残留塩素、pHに注目して行った。
また、前記3種類の水道水の特性は、上述の第1および
第2の実施例に用いた表2に示すものと同様である。
Using the water conditioner 15 of this embodiment, an ion water production experiment was actually conducted using three types of tap water. The experiment was conducted by paying attention to the amount of carbonic acid, hardness, residual chlorine and pH.
Further, the characteristics of the three types of tap water are the same as those shown in Table 2 used in the above-mentioned first and second examples.

【0032】実験条件として、電解電流は1A、総流量
2.0L/min、陰極6側、陽極7側ともに1.0L
/minとした。また添加剤としては塩化カルシウムを
用い、純水で1mol/Lに調整した後、定量ポンプを
用いて陽極7側へ10-3mol/Lになるよう添加し
た。この実験によって陽極7側から得られた酸性イオン
水、陰極6側から得られたアルカリイオン水の特性を表
5に示す。
As experimental conditions, the electrolysis current was 1 A, the total flow rate was 2.0 L / min, and both the cathode 6 side and the anode 7 side were 1.0 L.
/ Min. Further, calcium chloride was used as an additive, and after adjusting to 1 mol / L with pure water, it was added to the anode 7 side so as to be 10 −3 mol / L using a metering pump. Table 5 shows the characteristics of acidic ionized water obtained from the anode 7 side and alkaline ionized water obtained from the cathode 6 side by this experiment.

【0033】[0033]

【表5】 [Table 5]

【0034】表より明らかなように、本実施例の整水機
15は、原水の特性にかかわらず常に一定の特性の酸性
イオン水を得ることができる。また、得られる水量は実
施例1に比較して約2倍となるため、酸性イオン水のみ
が必要な場合には有効な手段である。
As is clear from the table, the water purifier 15 of this embodiment can always obtain acidic ionized water having a constant characteristic regardless of the characteristic of the raw water. In addition, the amount of water obtained is about twice as large as that in Example 1, so that it is an effective means when only acidic ionized water is required.

【0035】[0035]

【発明の効果】以上説明したことから明かなように、本
発明の整水機は、原水に含まれるイオンや溶存気体に影
響を受けることなく、所望のアルカリイオン水、酸性イ
オン水を安定して得ることができる。
As is clear from the above description, the water purifier of the present invention stabilizes desired alkaline ionized water and acidic ionized water without being affected by ions or dissolved gas contained in raw water. Can be obtained.

【0036】また、アルカリ水のみが必要な時は、純水
に任意の物質を添加した水を電解槽の陰極側で、濃縮水
を陽極側で電解することにより、より多量の所望のアル
カリ水を安定して得ることができる。
When only alkaline water is required, a larger amount of the desired alkaline water can be obtained by electrolyzing water prepared by adding an arbitrary substance to pure water on the cathode side of the electrolytic cell and electrolyzing concentrated water on the anode side. Can be stably obtained.

【0037】また同様に、酸性イオン水のみが必要な時
はは、純水に任意の物質を添加した水を電解槽の陽極側
で、濃縮水を陰極側で電解することにより、より多量の
所望の酸性イオン水を安定して得ることができる。
Similarly, when only acidic ionized water is required, a larger amount of water can be obtained by electrolyzing water prepared by adding an arbitrary substance to pure water on the anode side of the electrolytic cell and concentrated water on the cathode side. The desired acidic ionized water can be stably obtained.

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

【図1】本発明の整水機の構成を具体化した第1の実施
例を示す図である。
FIG. 1 is a diagram showing a first embodiment embodying the configuration of a water purifier according to the present invention.

【図2】本発明の整水機に搭載される逆浸透フィルタの
構造を示す図である。
FIG. 2 is a diagram showing a structure of a reverse osmosis filter mounted on the water purifier of the present invention.

【図3】図2に示す逆浸透フィルタの要部の断面図であ
る。
FIG. 3 is a cross-sectional view of a main part of the reverse osmosis filter shown in FIG.

【図4】本発明の整水機の第2の実施例の構成を示す図
である。
FIG. 4 is a diagram showing the configuration of a second embodiment of the water purifier of the present invention.

【図5】本発明の整水機の第3の実施例の構成を示す図
である。
FIG. 5 is a diagram showing a configuration of a third embodiment of a water purifier according to the present invention.

【図6】従来の整水機の構成を示す図である。FIG. 6 is a diagram showing a configuration of a conventional water conditioning machine.

【符号の説明】 4 逆浸透フィルタ 5 添加装置 6 陰極 7 陽極 8 電解槽 9 隔膜 10 逆浸透膜[Explanation of Codes] 4 Reverse Osmosis Filter 5 Addition Device 6 Cathode 7 Anode 8 Electrolyzer 9 Septum 10 Reverse Osmosis Membrane

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 水道水等の原水を通過させて純水を得る
ことが可能な逆浸透膜と、 その逆浸透膜により得られる純水に対して任意の物質を
添加し、所望の水に調整する添加装置と、 その添加装置により調整された水を電解する電解槽とを
備えたことを特徴とする整水機。
1. A reverse osmosis membrane capable of obtaining pure water by passing raw water such as tap water, and an arbitrary substance is added to pure water obtained by the reverse osmosis membrane to obtain a desired water. A water purifier comprising an adding device for adjusting and an electrolytic cell for electrolyzing water adjusted by the adding device.
【請求項2】 前記逆浸透膜が原水を純水と濃縮水とに
分ける機能を有し、更には前記電解層が前記添加装置に
より調整された水を陰極側で電解し、且つ前記濃縮水を
陽極側で電解することを特徴とする請求項1記載の整水
機。
2. The reverse osmosis membrane has a function of dividing raw water into pure water and concentrated water, and further, the electrolytic layer electrolyzes water adjusted by the adding device on the cathode side, and the concentrated water The water purifier according to claim 1, wherein the water is electrolyzed on the anode side.
【請求項3】 前記逆浸透膜が原水を純水と濃縮水とに
分ける機能を有し、更には前記電解層が前記添加装置に
より調整された水を陽極側で電解し、且つ前記濃縮水を
陰極側で電解することを特徴とする請求項1記載の整水
機。
3. The reverse osmosis membrane has a function of dividing raw water into pure water and concentrated water, and further, the electrolytic layer electrolyzes water adjusted by the addition device on the anode side, and the concentrated water The water purifier according to claim 1, wherein the water is electrolyzed on the cathode side.
JP7937193A 1993-04-06 1993-04-06 Water conditioning machine Pending JPH06285467A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7937193A JPH06285467A (en) 1993-04-06 1993-04-06 Water conditioning machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7937193A JPH06285467A (en) 1993-04-06 1993-04-06 Water conditioning machine

Publications (1)

Publication Number Publication Date
JPH06285467A true JPH06285467A (en) 1994-10-11

Family

ID=13688022

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7937193A Pending JPH06285467A (en) 1993-04-06 1993-04-06 Water conditioning machine

Country Status (1)

Country Link
JP (1) JPH06285467A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004505770A (en) * 2000-08-11 2004-02-26 エイチツーオー・テクノロジーズ・リミテッド Water treatment system under the sink
JP2007307502A (en) * 2006-05-19 2007-11-29 Ichiro Shoda Method for generating electrolytic water and electrolytic water generator
JP2008178845A (en) * 2007-01-26 2008-08-07 Kotobuki Kakoki Kk Electrolyzed hypochlorous water production apparatus
WO2016095229A1 (en) * 2014-12-19 2016-06-23 深圳市同盛绿色科技有限公司 Water treatment system and ph adjustment device therefor
CN105776651A (en) * 2014-12-19 2016-07-20 深圳市同盛绿色科技有限公司 Water treatment system
CN109553226A (en) * 2019-01-15 2019-04-02 天津碧水源膜材料有限公司 Producing water is weakly alkaline nanofiltration water purifier and purifier

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004505770A (en) * 2000-08-11 2004-02-26 エイチツーオー・テクノロジーズ・リミテッド Water treatment system under the sink
JP2007307502A (en) * 2006-05-19 2007-11-29 Ichiro Shoda Method for generating electrolytic water and electrolytic water generator
JP4641003B2 (en) * 2006-05-19 2011-03-02 一郎 庄田 Electrolyzed water generation method and electrolyzed water generator
JP2008178845A (en) * 2007-01-26 2008-08-07 Kotobuki Kakoki Kk Electrolyzed hypochlorous water production apparatus
WO2016095229A1 (en) * 2014-12-19 2016-06-23 深圳市同盛绿色科技有限公司 Water treatment system and ph adjustment device therefor
CN105776651A (en) * 2014-12-19 2016-07-20 深圳市同盛绿色科技有限公司 Water treatment system
CN105776651B (en) * 2014-12-19 2018-09-25 深圳市同盛绿色科技有限公司 A kind of water treatment system
CN109553226A (en) * 2019-01-15 2019-04-02 天津碧水源膜材料有限公司 Producing water is weakly alkaline nanofiltration water purifier and purifier

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