JP2000061462A - Method of controlling ph and hardness of water - Google Patents

Method of controlling ph and hardness of water

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Publication number
JP2000061462A
JP2000061462A JP10249132A JP24913298A JP2000061462A JP 2000061462 A JP2000061462 A JP 2000061462A JP 10249132 A JP10249132 A JP 10249132A JP 24913298 A JP24913298 A JP 24913298A JP 2000061462 A JP2000061462 A JP 2000061462A
Authority
JP
Japan
Prior art keywords
water
exchange resin
cation exchange
functional group
hardness
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
JP10249132A
Other languages
Japanese (ja)
Inventor
Yuji Tsukita
祐二 槻田
Hironori Hatono
広典 鳩野
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.)
Toto Ltd
Original Assignee
Toto 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 Toto Ltd filed Critical Toto Ltd
Priority to JP10249132A priority Critical patent/JP2000061462A/en
Publication of JP2000061462A publication Critical patent/JP2000061462A/en
Pending legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PROBLEM TO BE SOLVED: To produce water having a desirable effect and performance on the hair, skin, or the like by suitably mixing water which have passed through cation exchange resin the end of whose functional group is sodium, cation exchange resin of hydrogen, and anion exchange resin of hydroxyl group respectively to control pH and hardness of the mixed water. SOLUTION: City water fed as raw water is distributed to respective pipelines by a branch valve. The distribution to the pipelines is done by suitably operating the branch valve by a user. That is, city water to be fed as raw water is divided into parts passing through cation exchange resin the end of whose functional group is sodium type, cation exchange resin of hydrogen type, anion exchange resin of hydroxyl type, and a city water/raw water bypass for causing city water to flow as it is without treating any longer respectively through pipelines by the command from a control panel. As a result, soft water of neutral pH, soft water of weak acidic pH, water of alkaline pH, and city water/raw water can be used according to the appropriate use object to the user.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、毛髪や肌などに対
して大変好ましい効果・効能を有し、かつ水周り機器と
その周辺の汚れを付着しにくくするための水を多量に作
るための方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention has a very favorable effect and effect on hair, skin, and the like, and is for producing a large amount of water for making it difficult for dirt to adhere to the equipment around water and its surroundings. Regarding the method.

【0002】[0002]

【従来の技術】水には酸性水とアルカリ性水があり、ま
たカルシウムイオンやマグネシウムイオンを多量に含ん
だ硬水とこれらの含有量が少ない軟水があり、弱酸性水
は肌や髪のpHに近いために刺激が少なく、美容によい
とされ、アルカリ性水は健康によいため料理等に用いる
とよく、また有機物の分解・洗浄に効果があるとされ、
また硬水はミネラルウォーターとして飲用に供され、軟
水は石けんの泡立ちがよいため洗濯に適する。このよう
に、使用目的によって要求される水の性質は異なるので
ある。
2. Description of the Related Art Water includes acidic water and alkaline water, hard water containing a large amount of calcium ions and magnesium ions and soft water containing a small amount of these ions, and weak acidic water is close to the pH of skin and hair. Therefore, it is said that it is less irritating and is good for beauty, and alkaline water is good for health, so it is good to use it for cooking, etc.
Hard water is used as mineral water for drinking, and soft water is suitable for washing because the soap has a good foaming property. Thus, the properties of water required depend on the purpose of use.

【0003】従来、美容と防汚の両方に効果的な水の作
成方法は存在しなかったが、高純度水を熱媒体とする冷
却機器の金属の腐食を抑制するために、水のpHを制御
する方法としては、例えば特公平8−9030がある。
Conventionally, there has been no method for producing water effective for both beauty and antifouling, but in order to suppress corrosion of metal of cooling equipment using high-purity water as a heat medium, the pH of water is adjusted. As a control method, there is, for example, Japanese Patent Publication No. 8-9030.

【0004】[0004]

【発明が解決しようとする課題】しかし従来の方法で
は、以下のごとく問題がある。すなわち特公平8−90
30では、循環水が陽イオン交換樹脂と陰イオン交換樹
脂の混合槽を常に通過することになるため、陰イオン除
去が不要の場合においても陰イオン除去が行われ用途に
よっては無駄な場合がある。また、混合槽を用いた場合
は、樹脂の利用効率がやや低くなるために多くの再生剤
が必要となるという欠点があった。
However, the conventional method has the following problems. That is, Japanese Patent Publication 8-90
In the case of 30, the circulating water always passes through the mixing tank of the cation exchange resin and the anion exchange resin. Therefore, even if the anion removal is unnecessary, the anion removal is performed and may be useless depending on the application. . Further, when a mixing tank is used, there is a drawback that a large amount of a regenerant is required because the utilization efficiency of the resin is slightly lowered.

【0005】本発明は、上記従来の技術の問題を解決す
るものであり、毛髪や肌などに対して大変好ましい効果
・効能を有し、かつ水周り機器とその周辺の汚れを付着
しにくくするための水を多量に作るための方法を提供す
ることを目的とする。
The present invention solves the above-mentioned problems of the prior art, has very favorable effects and effects on hair and skin, and makes it difficult for dirt to adhere to the equipment around water and its surroundings. The purpose is to provide a method for producing a large amount of water.

【0006】[0006]

【課題を解決するための手段およびその作用・効果】上
記課題を解決するためになされた本発明は、官能基末端
がナトリウム型の陽イオン交換樹脂と、官能基末端が水
素型の陽イオン交換樹脂と、官能基末端が水酸基型の陰
イオン交換樹脂を通じた水を適宜混合することによって
水のpH、硬度を制御することとした。
MEANS FOR SOLVING PROBLEMS AND ACTIONS AND EFFECTS OF THE PROBLEMS The present invention made to solve the above problems is a cation exchange resin having a sodium group at a functional group terminal and a hydrogen type cation exchange resin having a functional group terminal. It was decided to control the pH and hardness of water by appropriately mixing the resin and water that has passed through an anion exchange resin having a hydroxyl group at the functional group terminal.

【0007】官能基末端がナトリウム型の陽イオン交換
樹脂と、官能基末端が水素型の陽イオン交換樹脂と、官
能基末端が水酸基型の陰イオン交換樹脂を通じた水を適
宜混合することによって、使用者は自由に水のpH、硬
度を制御する事ができるため、毛髪や肌などに対して大
変好ましい美容効果・効能を有し、また水周り機器への
防汚効果を有する弱酸性水や、有機物の分解・洗浄に効
果があるとされるアルカリ性水、また石けんの泡立ちが
よく、金属石けん汚れが付着しにくくなり、水周り機器
や肌、髪への美容に対しても効果的な軟水を、自在に作
成・制御することが可能となる。
By appropriately mixing water through a cation exchange resin having a sodium group at the functional group end, a cation exchange resin having a hydrogen group at the functional group end, and water passed through an anion exchange resin having a hydroxyl group at the functional group end, Since the user can freely control the pH and hardness of water, weak acidic water that has very favorable cosmetic effects and effects on hair and skin, and has an antifouling effect on equipment around water is also available. Alkaline water, which is said to be effective in decomposing and cleaning organic substances, and soap that foams well, makes it difficult for metal soap stains to adhere, and is also effective for beauty around equipment, skin, and hair. Can be freely created and controlled.

【0008】また陽イオン交換樹脂と陰イオン交換樹脂
の混合槽を使用せず、それぞれ単独の樹脂槽を用いるこ
とによって、利用者の用途に適した所望の水を作れるた
め、樹脂を無駄に使用することがなく、樹脂の利用効率
も良くなる。
[0008] Further, by using a separate resin tank for each of the cation-exchange resin and the anion-exchange resin, it is possible to produce the desired water suitable for the user's purpose. There is no need to do so, and the resin utilization efficiency is improved.

【0009】上記軟水の効果は、例えば石けん、シャン
プーを使用する場合に水道水中のカルシウム、マグネシ
ウムと石けん成分が結合して金属石けんを生成するが、
軟水であることにより金属石鹸を肌や髪に残留すること
を防ぐことが出来るため、肌や髪のかさかさ感、ぱさつ
き感等をなくすことに起因する。
The effect of the above soft water is, for example, when soap and shampoo are used, calcium and magnesium in tap water are combined with soap components to form metal soap,
The soft water can prevent the metal soap from remaining on the skin and hair, and thus causes the bulky feeling and the feeling of dryness of the skin and hair to be eliminated.

【0010】本発明による水のpH、硬度制御方法は、
あらゆる水周り機器に対しても応用可能である。例えば
給湯・給水器具、水栓金具、シャワー設備、浴槽設備、
簡易型サウナ、便器、洗面化粧台、温水洗浄便座、キッ
チン、食器洗浄機などに応用できる。
The method for controlling the pH and hardness of water according to the present invention is
It can also be applied to all types of equipment around water. For example, hot water supply / water supply equipment, faucet fittings, shower equipment, bathtub equipment,
It can be applied to simple saunas, toilets, vanities, hot water toilet seats, kitchens, dishwashers, etc.

【0011】本発明におけるイオン交換樹脂は、陽イオ
ン交換樹脂は強酸性型、弱酸性型のどちらでも構わな
い。また陽イオン交換樹脂はキレート樹脂も含んでい
る。同様に、陰イオン交換樹脂は強塩基型、弱塩基型の
どちらでも構わない。
The cation exchange resin in the present invention may be either a strong acid type or a weak acid type. The cation exchange resin also contains a chelate resin. Similarly, the anion exchange resin may be either a strong base type or a weak base type.

【0012】本発明の好ましい態様においては、前記水
のpH、硬度を制御する方法において、イオン交換樹脂
を通じない水を混合する手段も備える。
[0012] In a preferred aspect of the present invention, the method for controlling the pH and hardness of the water also comprises means for mixing water that does not pass through the ion exchange resin.

【0013】前記水のpH、硬度を制御する方法におい
て、イオン交換樹脂を通じない水を混合する手段も備え
ることによって、利用者の水の種類の選択肢がより広が
ることになる。すなわち、利用者は例えば一般家庭にお
ける用途の場合には、通常蛇口から吐出する水道水が望
まれる場合もあるため、水道水原水を吐出する機構も含
まれることが望ましい。
In the method of controlling the pH and hardness of water, by providing a means for mixing water that does not pass through the ion exchange resin, the choice of water types for the user can be further expanded. That is, in the case of use in a general household, for example, a user may desire tap water that is normally discharged from a tap, and therefore it is desirable to include a mechanism that discharges raw tap water.

【0014】また、上述した如くイオン交換樹脂を通じ
た水をお互いに混合するのみならず、水道水原水とも混
合するという方法を含むことにより、より利用できる水
の種類が増すことになる。
Further, by including the method of mixing not only the water that has passed through the ion exchange resin with each other as described above, but also mixing with the tap water raw water, the types of water that can be used are increased.

【0015】[0015]

【発明の実施の形態】以上説明した本発明の構成・作用
を一層明らかにするために、以下本発明の好適な実施例
について説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Preferred embodiments of the present invention will be described below in order to further clarify the constitution and operation of the present invention described above.

【0016】(実施例)図1は本発明を達成するための
装置である。まず原水として供給される水道水(図1で
は水道水原水として示した)は分岐バルブによって各配
管に分岐される。各配管への分岐は、使用者が制御パネ
ルを適切に操作することによって行われる。すなわち、
原水として供給される水道水はそれぞれ、官能基末端が
ナトリウム型の陽イオン交換樹脂(図1ではNa型陽イ
オン交換樹脂と示した)、官能基末端が水素型の陽イオ
ン交換樹脂(図1ではH型陽イオン交換樹脂と示し
た)、官能基末端が水酸型の陰イオン交換樹脂(図1で
はOH型陰イオン交換樹脂と示した)、そして水道水を
何も処理せずに原水のままで流すための水道水原水バイ
パスに、制御パネルからの命令によって各配管を通じて
分岐される。
(Embodiment) FIG. 1 shows an apparatus for achieving the present invention. First, tap water supplied as raw water (shown as tap water raw water in FIG. 1) is branched into each pipe by a branch valve. The branch to each pipe is performed by the user appropriately operating the control panel. That is,
Each of the tap water supplied as raw water has a sodium cation exchange resin with a functional group terminal (shown as Na type cation exchange resin in FIG. 1) and a hydrogen type cation exchange resin with a functional group terminal (FIG. 1). H-type cation exchange resin), an anion exchange resin whose functional group end is a hydroxyl type (shown as OH type anion exchange resin in Fig. 1), and tap water without any treatment. It is branched through each pipe to the tap water raw water bypass for flowing as it is by the command from the control panel.

【0017】官能基末端がナトリウム型の陽イオン交換
樹脂を通過した水は、官能基末端がナトリウム型の陽イ
オン交換樹脂にあらかじめ吸着していたナトリウムイオ
ンと、水道水原水中のカルシウム、マグネシウムなどの
陽イオンがイオン交換反応を起こすことによって、水道
水原水中のカルシウム、マグネシウムなどの陽イオンは
官能基末端がナトリウム型の陽イオン交換樹脂に吸着さ
れ、もともと官能基末端がナトリウム型の陽イオン交換
樹脂に吸着していたナトリウムイオンが放出される。そ
の結果、pHが中性の軟水が得られる。
The water which has passed through the sodium-type cation exchange resin whose functional group end is the sodium ion which has been adsorbed in advance on the sodium-type cation exchange resin whose functional group end is the same as calcium and magnesium in the tap water raw water. When the cations cause an ion exchange reaction, the cations such as calcium and magnesium in the tap water raw water are adsorbed on the sodium-type cation exchange resin whose functional group ends are originally sodium-type cation exchange resins. The sodium ions adsorbed on are released. As a result, soft water having a neutral pH is obtained.

【0018】同様に、官能基末端が水素型の陽イオン交
換樹脂を通過した水は、官能基末端が水素型の陽イオン
交換樹脂にあらかじめ吸着していた水素イオンと、水道
水原水中のカルシウム、マグネシウムなどの陽イオンが
イオン交換反応を起こすことによって、水道水原水中の
カルシウム、マグネシウムなどの陽イオンは官能基末端
が水素型の陽イオン交換樹脂に吸着され、もともと官能
基末端が水素型の陽イオン交換樹脂に吸着していた水素
イオンが放出される。その結果、pHが弱酸性の軟水が
得られる。
Similarly, water having passed through a cation exchange resin whose functional group end is a hydrogen type has hydrogen ions adsorbed in advance on a cation exchange resin whose functional group end is a hydrogen type, calcium in tap water raw water, Cations such as magnesium and magnesium in tap water are adsorbed by a cation exchange resin whose functional group end is a hydrogen type by causing a cation such as magnesium to undergo an ion exchange reaction. The hydrogen ions adsorbed on the ion exchange resin are released. As a result, soft water having a weakly acidic pH is obtained.

【0019】同様に、官能基末端が水酸型の陰イオン交
換樹脂を通過した水は、官能基末端が水酸型の陰イオン
交換樹脂にあらかじめ吸着していた水酸イオンと、水道
水原水中の炭酸イオン、硝酸イオン、硫酸イオンなどの
陰イオンがイオン交換反応を起こすことによって、水道
水原水中の炭酸イオン、硝酸イオン、硫酸イオンなどの
陰イオンは官能基末端が水酸型の陰イオン交換樹脂に吸
着され、もともと官能基末端が水酸型の陰イオン交換樹
脂に吸着していた水酸イオンが放出される。その結果、
pHがアルカリ性の水が得られる。
Similarly, the water having passed through the hydroxyl group-type anion exchange resin having a functional group end is mixed with the hydroxide ion previously adsorbed on the hydroxyl group-type anion exchange resin having a functional group terminal and the tap water raw water. Anions such as carbonate ions, nitrate ions, and sulfate ions in water of the tap water cause anion exchange reaction, so that anions such as carbonate ions, nitrate ions, and sulfate ions in tap water have a hydroxyl group at the functional group end. Hydroxyl ions, which were originally adsorbed on the resin and were originally adsorbed on the hydroxide type anion exchange resin whose functional group ends are released, are released. as a result,
Water with an alkaline pH is obtained.

【0020】分岐バルブで分岐された水のうちで唯一、
水道水原水バイパスを通った水は、上記例のようなイオ
ン交換反応を起こすことなく、水道水原水がそのまま後
段に通水される。
The only water branched by the branch valve is
The water that has passed the tap water raw water bypass is directly passed to the latter stage of the tap water raw water without causing the ion exchange reaction as in the above example.

【0021】上記の如くそれぞれの樹脂、バイパスを通
って得られた水は後段の混合バルブに集められ、処理水
として使用に供される。
The water obtained through the respective resins and bypasses as described above is collected in a mixing valve in the subsequent stage and used as treated water.

【0022】すなわち、上記の如く得られたpHが中性
の軟水、pHが弱酸性の軟水、pHがアルカリ性の水、
そして水道水原水(pHは中性で、カルシウム、マグネ
シウムの濃度が高い硬水)が、使用者の適当な利用目的
のために制御パネルから入力された命令に応じて、混合
バルブで適当に混合され、処理水となって使用に供され
る。
That is, the above-obtained soft water having neutral pH, soft water having weakly acidic pH, and water having alkaline pH,
Then, the tap water raw water (hard water having a neutral pH and high concentration of calcium and magnesium) is appropriately mixed by the mixing valve according to the instruction input from the control panel for the user's proper purpose of use. , Treated water and used.

【0023】利用者が水道水を何も処理せず、原水のま
ま使用したい場合には、やはり制御パネルからの命令に
よって、水道水をイオン交換樹脂に通じることなく、す
べて水道水原水バイパスに通じればよい。
When the user does not process tap water and wants to use the raw water as it is, the instruction from the control panel also allows the tap water to be directly connected to the tap water raw water bypass without passing to the ion exchange resin. Good.

【0024】図2は以上のような機構により生成した水
の、pHと硬度成分の濃度を示したものである。
FIG. 2 shows the pH and the concentration of the hardness component of the water produced by the above mechanism.

【0025】すなわち、本発明に示す図1の機構によっ
て、図形ABCDの内部の範囲におけるpH、硬度成分
の濃度を有する水を自在に生成することができる。
That is, by the mechanism shown in FIG. 1 according to the present invention, it is possible to freely generate water having a pH and a hardness component concentration within the range of the figure ABCD.

【0026】例えば、図1に示すNa型陽イオン交換樹
脂とH型陽イオン交換樹脂と、水道水原水バイパスを用
いて、それぞれに適当な量だけ通水し、後に混合するこ
とによって、図2における図形ABCの内部の範囲にお
けるpH、硬度成分の濃度を有する水を自在に生成する
ことができる。
For example, by using the Na-type cation exchange resin and the H-type cation exchange resin shown in FIG. 1 and tap water raw water bypasses, water is passed through in an appropriate amount, respectively, and then mixed. It is possible to freely generate water having the pH and the concentration of the hardness component in the range inside the figure ABC in FIG.

【0027】これは、図形ABCの頂点Aの部分のp
H、硬度の水をNa型陽イオン交換樹脂が、頂点Bの部
分のpH、硬度の水をH型陽イオン交換樹脂が、そして
頂点Cの部分のpH、硬度の水は水道水原水バイパス
を、それぞれ通じた水が生成するためである。
This is p at the vertex A of the figure ABC.
The water of H and hardness is Na type cation exchange resin, the pH of the vertex B is the H type cation exchange resin, and the water of hardness is the pH and hardness of the vertex C is tap water raw water bypass. , Because the water that flows through each is generated.

【0028】同様に、図1に示すNa型陽イオン交換樹
脂とOH型陰イオン交換樹脂と、水道水原水バイパスを
用いて、それぞれに適当な量だけ通水し、後に混合する
ことによって、図2における図形ADCの内部の範囲に
おけるpH、硬度成分の濃度を有する水を自在に生成す
ることができる。
Similarly, by using Na-type cation exchange resin and OH-type anion exchange resin shown in FIG. 1 and tap water raw water bypass, respectively, an appropriate amount of water is passed through, and after mixing, It is possible to freely generate water having the pH and the concentration of the hardness component within the range of the figure ADC in 2.

【0029】これは、図形ADCの頂点Aの部分のp
H、硬度の水をNa型陽イオン交換樹脂が、頂点Dの部
分のpH、硬度の水をOH型陰イオン交換樹脂が、そし
て頂点Cの部分のpH、硬度の水は水道水原水バイパス
を、それぞれ通じた水が生成するためである。
This is p at the vertex A of the figure ADC.
The water of H and hardness is Na type cation exchange resin, the pH of vertex D is the OH type anion exchange resin of the hardness water, and the pH and hardness of vertex C is the tap water raw water bypass. , Because the water that flows through each is generated.

【0030】以上のような機構により、使用者は、例え
ば洗顔、洗髪、有機物などの汚れ落としなどといった自
分の使用目的に応じた水を自在に多量に生成し、利用す
ることが可能となる。
With the above-described mechanism, the user can freely generate and use a large amount of water according to his / her purpose of use, for example, face washing, hair washing, stain removal of organic substances and the like.

【0031】[0031]

【発明の効果】以上に説明した如く本発明によれば、水
のpH、硬度制御方法を用いることによって、毛髪や肌
などに対して大変好ましい効果・効能を有し、かつ水周
り機器とその周辺の汚れを付着しにくくするための水を
多量に作るための方法を提供することができる。
As described above, according to the present invention, by using the method of controlling the pH and hardness of water, it has very favorable effects and effects on hair, skin, etc. It is possible to provide a method for producing a large amount of water for making it difficult for dirt to adhere to the surrounding area.

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

【図1】本発明における、水のpH、硬度制御方法を具
現化するための装置を示す図
FIG. 1 is a diagram showing an apparatus for embodying a method for controlling pH and hardness of water according to the present invention.

【図2】図1の装置によって生成される水のpH、硬度
成分の濃度の範囲を示す図
FIG. 2 is a diagram showing pH and concentration ranges of hardness components of water produced by the apparatus of FIG.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 官能基末端がナトリウム型の陽イオン交
換樹脂と、官能基末端が水素型の陽イオン交換樹脂と、
官能基末端が水酸基型の陰イオン交換樹脂を通じた水を
適宜混合することによって水のpH、硬度を制御する方
法。
1. A cation exchange resin having a sodium group at a functional group end, and a cation exchange resin having a hydrogen group at a functional group end,
A method of controlling the pH and hardness of water by appropriately mixing water that has passed through an anion exchange resin whose functional group end is a hydroxyl group.
【請求項2】 イオン交換樹脂を通じない水を混合する
手段も備えることを特徴とする、請求項1に記載の水の
pH、硬度を制御する方法。
2. The method for controlling pH and hardness of water according to claim 1, further comprising means for mixing water that does not pass through the ion exchange resin.
JP10249132A 1998-08-19 1998-08-19 Method of controlling ph and hardness of water Pending JP2000061462A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10249132A JP2000061462A (en) 1998-08-19 1998-08-19 Method of controlling ph and hardness of water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10249132A JP2000061462A (en) 1998-08-19 1998-08-19 Method of controlling ph and hardness of water

Publications (1)

Publication Number Publication Date
JP2000061462A true JP2000061462A (en) 2000-02-29

Family

ID=17188412

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10249132A Pending JP2000061462A (en) 1998-08-19 1998-08-19 Method of controlling ph and hardness of water

Country Status (1)

Country Link
JP (1) JP2000061462A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006061828A (en) * 2004-08-26 2006-03-09 Isao Midorikawa Method for producing acid water and alkaline water
US7931810B2 (en) 2006-01-27 2011-04-26 Millipore Corporation Water purification system and method
JP2011530395A (en) * 2008-08-09 2011-12-22 ユード ヴァッサーアオフベライトゥング ゲー・エム・ベー・ハー Modifiable control unit for softening equipment
JP2012501247A (en) * 2008-09-02 2012-01-19 ユード ヴァッサーアオフベライトゥング ゲー・エム・ベー・ハー Pending evaluation of measurements in an automatic water softening system when a given operating condition occurs
JP2013535322A (en) * 2010-07-26 2013-09-12 ビーダブリューティー アクティエンゲゼルシャフト Method and system for treating water
WO2022268461A1 (en) * 2021-06-22 2022-12-29 Gambro Lundia Ab Acidic and alkaline cleaning of ion exchange systems, such as water purifiers, by ion exchange resin

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006061828A (en) * 2004-08-26 2006-03-09 Isao Midorikawa Method for producing acid water and alkaline water
US7931810B2 (en) 2006-01-27 2011-04-26 Millipore Corporation Water purification system and method
US8146752B2 (en) 2006-01-27 2012-04-03 Emd Millipore Corporation Water purification system and method
US8177977B2 (en) 2006-01-27 2012-05-15 Emd Millipore Corporation Water purification system and method
JP2011530395A (en) * 2008-08-09 2011-12-22 ユード ヴァッサーアオフベライトゥング ゲー・エム・ベー・ハー Modifiable control unit for softening equipment
US8709241B2 (en) 2008-08-09 2014-04-29 Judo Wasseraufbereitung Gmbh Retrofittable control unit for a softening apparatus
JP2012501247A (en) * 2008-09-02 2012-01-19 ユード ヴァッサーアオフベライトゥング ゲー・エム・ベー・ハー Pending evaluation of measurements in an automatic water softening system when a given operating condition occurs
US8668830B2 (en) 2008-09-02 2014-03-11 Judo Wasseraufbereitung Gmbh Interruption of measured variable analyses in an automatic water softening system when defined operating situations are present
JP2013535322A (en) * 2010-07-26 2013-09-12 ビーダブリューティー アクティエンゲゼルシャフト Method and system for treating water
EP2598446B1 (en) * 2010-07-26 2019-12-04 BWT Aktiengesellschaft Process and system for treating water
WO2022268461A1 (en) * 2021-06-22 2022-12-29 Gambro Lundia Ab Acidic and alkaline cleaning of ion exchange systems, such as water purifiers, by ion exchange resin

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