JP5019422B2 - Domestic water supply method and apparatus - Google Patents

Domestic water supply method and apparatus Download PDF

Info

Publication number
JP5019422B2
JP5019422B2 JP2006285210A JP2006285210A JP5019422B2 JP 5019422 B2 JP5019422 B2 JP 5019422B2 JP 2006285210 A JP2006285210 A JP 2006285210A JP 2006285210 A JP2006285210 A JP 2006285210A JP 5019422 B2 JP5019422 B2 JP 5019422B2
Authority
JP
Japan
Prior art keywords
water
alkaline
acidic
pipe
water supply
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.)
Expired - Fee Related
Application number
JP2006285210A
Other languages
Japanese (ja)
Other versions
JP2008100174A (en
Inventor
弘次 山中
陽代 鈴木
雅司 藤田
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.)
Organo Corp
Original Assignee
Organo 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 Organo Corp filed Critical Organo Corp
Priority to JP2006285210A priority Critical patent/JP5019422B2/en
Publication of JP2008100174A publication Critical patent/JP2008100174A/en
Application granted granted Critical
Publication of JP5019422B2 publication Critical patent/JP5019422B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Description

本発明は、水道水等の原水を処理して、少なくとも原水、アルカリ性水、酸性水及び純水を生活用水として供給する生活用水供給方法及び装置に関するものである。   The present invention relates to a domestic water supply method and apparatus for processing raw water such as tap water and supplying at least raw water, alkaline water, acidic water and pure water as domestic water.

近年の健康ブームあるいは生活水準の向上に伴い、生活用水として水道水以外に、軟水、純水、酸性水あるいはアルカリ性水の利用が盛んである。特に、純水は、洗濯、食器洗い及び調理用などで使用するのに好適であり、豊富に供給できるシステムが要望されている。また、アルカリ性水は健康のための飲料水として注目を集めており、酸性水はトイレ、食材の殺菌などに好適に利用されている。   With the recent health boom or improvement in living standards, soft water, pure water, acidic water, or alkaline water is actively used as domestic water in addition to tap water. In particular, pure water is suitable for use in washing, dishwashing, cooking, and the like, and there is a demand for a system that can supply abundantly. Alkaline water is attracting attention as drinking water for health, and acidic water is suitably used for sterilization of toilets and foodstuffs.

特開平9−151503号公報には、水道水を浄化する浄化部と、その浄化された水を使途別に水質調整する水質調整部とを有し、水質調整部で水質調整した水を前記使途別に供給する浄化システムが開示されている。この浄化システムによれば、水道水を使用目的に適合した水質に調整した水を適所に供給することができる。   Japanese Patent Application Laid-Open No. 9-151503 has a purifying unit that purifies tap water and a water quality adjusting unit that adjusts the quality of the purified water according to the purpose of use. A supply purification system is disclosed. According to this purification system, it is possible to supply tap water with a water quality adjusted to the purpose of use to an appropriate place.

また、特開2002−143854号公報には、電解槽内に対向して設けられ通水された原水を電気化学処理できる第1電極と第2電極と、前記第1電極に正電位、且つ前記第2電極に負電位を印加する電源部と、前記第1電極と前記第2電極との間に複数のセルを形成するため、前記第1電極と前記第2電極間にそれぞれ間隔をおいて所定の順で並べられた複数のイオン交換膜と、それぞれ流量調整弁が設けられ前記複数のセルのそれぞれに通水できる導入路と、前記複数のセルのそれぞれから処理水を吐出する吐出路とを備えた電気化学的水処理装置であって、前記複数のイオン交換膜が、一価陰イオン選択性陰イオン交換膜、非イオン選択性陰イオン交換膜、非イオン選択性陽イオン交換膜、一価陽イオン選択性陽イオン交換膜から構成され、且つ前記第1電極から前記第2電極までの間にこの順で並べられている電気化学的水処理装置が開示されている。この電気化学的水処理装置によれば、一つの装置で、脱イオン水、Na型の軟水、二価イオンの豊富なミネラル水、アルカリ性水、酸性水と各種の水が容易に生成できる。
特開平9−151503号公報(請求項1) 特開2002−143854号公報(請求項1、図1)
Japanese Patent Application Laid-Open No. 2002-143854 discloses a first electrode and a second electrode that are provided opposite to each other in an electrolytic cell and are capable of electrochemically treating raw water, a positive potential on the first electrode, In order to form a plurality of cells between the power supply unit for applying a negative potential to the second electrode and between the first electrode and the second electrode, there is an interval between the first electrode and the second electrode. A plurality of ion exchange membranes arranged in a predetermined order, an introduction path that is provided with a flow rate adjustment valve and can pass water to each of the plurality of cells, and a discharge path that discharges treated water from each of the plurality of cells A plurality of ion exchange membranes comprising a monovalent anion selective anion exchange membrane, a non-ion selective anion exchange membrane, a non-ion selective cation exchange membrane, Consists of monovalent cation selective cation exchange membranes It is, and electrochemical water treatment device are arranged in this order between the said first electrode to said second electrode is disclosed. According to this electrochemical water treatment apparatus, deionized water, Na-type soft water, mineral water rich in divalent ions, alkaline water, acidic water and various types of water can be easily generated with one apparatus.
JP-A-9-151503 (Claim 1) JP 2002-143854 A (Claim 1, FIG. 1)

しかしながら、特開平9−151503号公報の浄化システムは、異物除去手段、臭気除去手段、有害物質除去手段、適温調整手段、イオン除去手段、ミネラル添加手段、pH調整手段、ガス添加手段などの各手段の設置が必要であり、設置コストが嵩むと共に配管も複雑となるという問題がある。   However, the purification system disclosed in Japanese Patent Application Laid-Open No. 9-151503 has various means such as foreign matter removing means, odor removing means, harmful substance removing means, suitable temperature adjusting means, ion removing means, mineral adding means, pH adjusting means, and gas adding means. There is a problem that the installation cost increases and the piping becomes complicated.

また、特開2002−143854号公報の電気化学的水処理装置は、純水、酸性水及びアルカリ性水は容易に得られるものの、水道水を原水とし、極間距離が大きいため高電圧で運転する必要がある。また、装置構造が複雑であり、イオン交換膜を多用しており、高価である。   In addition, the electrochemical water treatment apparatus disclosed in JP-A-2002-143854 can easily obtain pure water, acidic water and alkaline water, but uses tap water as raw water and operates at a high voltage because of the large distance between the electrodes. There is a need. In addition, the structure of the apparatus is complicated, and ion exchange membranes are frequently used, which is expensive.

従って、本発明の目的は、アルカリ性水、酸性水及び純水を得ることができると共に、電解槽をコンパクト化できる生活用水供給方法及び装置構造が比較的簡易な生活用水供給装置を提供することにある。   Accordingly, an object of the present invention is to provide a domestic water supply apparatus that can obtain alkaline water, acidic water, and pure water, and that has a relatively simple living water supply method and apparatus structure that can make the electrolytic cell compact. is there.

かかる実情において、本発明者は鋭意検討を行った結果、原水を逆浸透膜装置で処理して濃縮水と透過水を得る工程と、電解槽に該逆浸透膜装置から得られる濃縮水を流入し、陰極室からアルカリ性水を、陽極室から酸性水を得る工程と、を有し、原水、透過水、アルカリ性水及び酸性水を生活用水として使用点に供給するようにすれば、アルカリ性水、酸性水及び純水を得ることができると共に、電解槽をコンパクト化できること、また、高価なイオン交換膜を使用していないため、安価に製造できること等を見出し、本発明を完成するに至った。   Under such circumstances, the present inventor has conducted intensive studies, and as a result, processed raw water with a reverse osmosis membrane device to obtain concentrated water and permeated water, and flowed the concentrated water obtained from the reverse osmosis membrane device into an electrolytic cell. A step of obtaining alkaline water from the cathode chamber and acidic water from the anode chamber, and supplying raw water, permeated water, alkaline water and acidic water to the point of use as domestic water, alkaline water, The present inventors have found that acid water and pure water can be obtained and that the electrolytic cell can be made compact, and that an expensive ion exchange membrane is not used, so that it can be manufactured at low cost, and the present invention has been completed.

すなわち、本発明(1)は、原水を逆浸透膜装置で処理して濃縮水と透過水を得る脱塩工程と、電解槽に該逆浸透膜装置から得られる濃縮水を流入し、陰極室からアルカリ性水を、陽極室から酸性水を得る電解工程と、を有し、生活用水として、原水を原水使用点に、透過水を透過水使用点に、該陰極室から得られるアルカリ性水を、アルカリ性水が食材洗浄用として使用されるアルカリ性水使用点に、該陽極室から得られる酸性水を酸性水使用点に供給することを特徴とする生活用水供給方法を提供するものである。 That is, the present invention (1) includes a desalting step of treating raw water with a reverse osmosis membrane device to obtain concentrated water and permeated water, and flowing the concentrated water obtained from the reverse osmosis membrane device into an electrolytic cell, And alkaline water obtained from the cathode chamber, using raw water as the raw water use point, permeate water as the permeate use point, and an electrolysis step for obtaining acidic water from the anode chamber and acidic water from the anode chamber . An object of the present invention is to provide a domestic water supply method characterized by supplying acidic water obtained from the anode chamber to an acidic water use point at an alkaline water use point at which alkaline water is used for cleaning foods .

また、本発明は、逆浸透膜装置と、供給された被処理水を電気分解してアルカリ性水と酸性水とを生成する電解槽を備える生活用水供給装置であって、該逆浸透膜装置の原水側には原水導入配管を、濃縮水側には濃縮水流出配管を、透過水側には透過水流出配管をそれぞれ配し、該電解槽の被処理水流入側には該逆浸透膜装置の濃縮水流出配管を、陰極室にはアルカリ性水流出配管を、陽極室には酸性水流出配管をそれぞれ配し、原水導入配管と原水使用点を接続する原水供給配管と、透過水流出配管と透過水使用点を接続する透過水供給配管と、アルカリ性水流出配管とアルカリ性水が食材洗浄用として使用されるアルカリ性水使用点を接続するアルカリ性水供給配管と、酸性水流出配管と酸性水使用点を接続する酸性水供給配管と、をそれぞれ配するものであることを特徴とする本発明(1)の生活用水供給方法を実施するための生活用水供給装置を提供するものである。 The present invention is also a domestic water supply device comprising a reverse osmosis membrane device and an electrolytic cell for electrolyzing the supplied treated water to produce alkaline water and acidic water, wherein the reverse osmosis membrane device A raw water introduction pipe is arranged on the raw water side, a concentrated water outflow pipe is arranged on the concentrated water side, a permeate outflow pipe is arranged on the permeate side, and the reverse osmosis membrane device is arranged on the treated water inflow side of the electrolytic cell. Concentrated water outflow piping, alkaline water outflow piping in the cathode chamber, acidic water outflow piping in the anode chamber, raw water supply piping connecting the raw water introduction piping and raw water use point, permeate outflow piping, Permeated water supply pipe connecting the permeated water use point, alkaline water outflow pipe and alkaline water supply pipe connecting alkaline water use point where alkaline water is used for washing food , acidic water outflow pipe and acidic water use point Connect the acidic water supply pipe, There is provided a domestic water supply system for carrying out the domestic water supply method of the present invention (1), characterized in that the respective distribution.

本発明の生活用水供給方法によれば、アルカリ性水、酸性水及び純水を得ることができると共に、電解槽をコンパクト化できる。また、本発明の生活用水供給装置によれば、高価なイオン交換膜を使用していないため安価に製造できる。   According to the domestic water supply method of the present invention, alkaline water, acidic water and pure water can be obtained, and the electrolytic cell can be made compact. Moreover, according to the domestic water supply apparatus of this invention, since an expensive ion exchange membrane is not used, it can manufacture at low cost.

本発明の生活用水供給方法及び装置(以下、2つの発明を言う場合、単に「本発明において」と言うことがある。)において、原水は生活用水として使用される水道水等の水である。水道水には通常、カルシウムイオンやマグネシウムイオン等の2価のカチオンの他、ナトリウムイオン、カリウムイオン、塩化物イオン、硝酸イオン、硫酸イオン等の強電解質、炭酸イオン、シリカ等の弱電解質等の不純物が種々の比率で含まれている。   In the domestic water supply method and apparatus of the present invention (hereinafter, two inventions are simply referred to as “in the present invention”), the raw water is water such as tap water used as domestic water. Tap water usually contains divalent cations such as calcium ion and magnesium ion, strong electrolyte such as sodium ion, potassium ion, chloride ion, nitrate ion and sulfate ion, weak electrolyte such as carbonate ion and silica, etc. Impurities are included in various ratios.

本発明において、生活用水としては、ダイニング、洗面所、バスルームなどで使用される人間が生活を営むために必要となる各種用水であり、飲料用水を含むものである。このため、生活用水が使用される場所としては、一戸建て住宅、集合住宅、仮設住宅などの各種住宅の他、会社の事務所、工場、実験室、研究所、病院、宿泊施設などの人が活動する場所も含むものである。   In the present invention, the water for daily use is various types of water that is necessary for a human being used in a dining room, a washroom, a bathroom, etc. to live a life, and includes drinking water. For this reason, people living in water such as single-family houses, apartment houses, and temporary houses, as well as company offices, factories, laboratories, research laboratories, hospitals, and lodging facilities are active. The place to do is also included.

次ぎに、本発明の実施の形態における生活用水供給方法及び生活用水供給装置を図1を参照して説明する。本例の生活用水供給装置50は、逆浸透膜装置10と、供給された被処理水を電気分解してアルカリ性水と酸性水とを生成する電解槽20を備えるものであって、逆浸透膜装置10の原水側には原水導入配管aを、濃縮水側には濃縮水流出配管cを、透過水側には透過水流出配管bをそれぞれ配し、電解槽20の被処理水流入側には逆浸透膜装置10の濃縮水流出配管cを、陰極室にはアルカリ性水流出配管dを、陽極室には酸性水流出配管eをそれぞれ配し、原水導入配管aと原水使用点を接続する原水供給配管Aと、透過水流出配管bと透過水使用点を接続する透過水供給配管Bと、アルカリ性水流出配管dとアルカリ性水使用点を接続するアルカリ性水供給配管Dと、酸性水流出配管eと酸性水使用点を接続する酸性水供給配管Eと、をそれぞれ配するものである。   Next, a domestic water supply method and a domestic water supply apparatus according to an embodiment of the present invention will be described with reference to FIG. The domestic water supply device 50 of this example includes a reverse osmosis membrane device 10 and an electrolytic cell 20 that electrolyzes the supplied water to be treated to generate alkaline water and acidic water. The apparatus 10 is provided with a raw water introduction pipe a on the raw water side, a concentrated water outflow pipe c on the concentrated water side, and a permeate outflow pipe b on the permeate side. Has a concentrated water outlet pipe c of the reverse osmosis membrane device 10, an alkaline water outlet pipe d in the cathode chamber, and an acidic water outlet pipe e in the anode chamber, and connects the raw water introduction pipe a and the raw water use point. Raw water supply pipe A, permeated water outflow pipe b, permeated water supply pipe B connecting permeate use point, alkaline water outflow pipe d, alkaline water supply pipe D connecting alkaline water use point, and acidic water outflow pipe e. Acidic water supply pipe E connecting the acidic water use point, It is intended to distribution, respectively.

逆浸透膜装置(RO)10としては、特に制限されず、公知の逆浸透膜装置が使用できる。RO膜としては、3.9MPa以上の高圧膜から0.98MPa以下の超低圧膜まで種々のタイプのものを使用することができる。また、RO膜としては、酢酸セルロース及びその誘導体の膜あるいは合成高分子膜が使用できる。また、逆浸透膜装置は、通常工業的に利用可能な型式に膜を収納した装置(モジュール)として使用される。モジュールの形態としては、中空糸型、スパイラル型、平板型、チューブ型及びホローファイバー型などが挙げられる。   The reverse osmosis membrane device (RO) 10 is not particularly limited, and a known reverse osmosis membrane device can be used. Various types of RO membranes can be used, from high pressure membranes of 3.9 MPa or higher to ultralow pressure membranes of 0.98 MPa or lower. Further, as the RO membrane, a membrane of cellulose acetate and its derivatives or a synthetic polymer membrane can be used. The reverse osmosis membrane device is usually used as a device (module) in which the membrane is housed in a type that can be industrially used. Examples of the module form include a hollow fiber type, a spiral type, a flat plate type, a tube type, and a hollow fiber type.

電解槽20は、供給された被処理水を電気分解してアルカリ性水と酸性水とを生成するものであれば、特に制限されず、公知の電解槽を使用することができる。電解槽20は、例えば直流電源に接続された一組のチタン基板に白金メッキを施した電極を対向させて陽極および陰極とし、該電極間に形成される空間を電解室とし、該電解室に被処理水導入管と陽極側に接続された酸性水排出管と陰極側に設置されたアルカリ水排出管を有し、電解室に被処理水を通水しながら、前記電極間に電流密度0.1〜10A/dm程度の電流を通電して、陽極付近から酸性水を、陰極付近からアルカリ性水を排出するものを例示することができる。電解室にポリエチレン、ポリプロピレン、セラミックスなどの多孔質膜を配して電解室を陽極側を陽極室とし、陰極側を陰極室に分割する隔膜式電解槽を用いても良い。更に、これらの電解槽において、複数組の陽極と陰極を配置し、それらの電極に並列または直列に直流電流を通電する複槽式電解槽を用いることもできる。また、カルシウムイオンやマグネシウムイオンの塩や水酸化物が陰極に析出するのを防止するために、通電中に陽極と陰極の極性を20分〜1時間程度の間隔で定期的に反転し、かつ反転に同期させて酸性水およびアルカリ水排出管を切り替える極性反転機構を備えた電解槽であってもよい。 The electrolyzer 20 is not particularly limited as long as it supplies electrolyzed supplied water to produce alkaline water and acidic water, and a known electrolyzer can be used. The electrolytic cell 20 has, for example, a pair of titanium substrates connected to a direct current power source and electrodes that are plated with platinum facing each other as an anode and a cathode, and a space formed between the electrodes serves as an electrolysis chamber. A treated water introduction pipe, an acidic water discharge pipe connected to the anode side, and an alkaline water discharge pipe installed on the cathode side, while passing the treated water into the electrolysis chamber, the current density between the electrodes was 0 An example is one in which a current of about 1 to 10 A / dm 2 is applied to discharge acidic water from the vicinity of the anode and alkaline water from the vicinity of the cathode. A diaphragm type electrolytic cell may be used in which a porous film such as polyethylene, polypropylene, or ceramic is disposed in the electrolysis chamber, and the electrolysis chamber is divided into an anode chamber on the anode side and a cathode chamber on the cathode side. Further, in these electrolytic cells, it is also possible to use a multi-tank electrolytic cell in which a plurality of sets of anodes and cathodes are arranged and a direct current is passed in parallel or in series with these electrodes. Further, in order to prevent calcium ions and magnesium ion salts and hydroxides from depositing on the cathode, the polarity of the anode and the cathode is periodically reversed at intervals of about 20 minutes to 1 hour during energization, and It may be an electrolytic cell provided with a polarity reversing mechanism that switches between acid water and alkaline water discharge pipes in synchronization with reversal.

次ぎに、本例の生活用水供給装置50を用いて生活用水を供給する方法を説明する。生活用水供給装置50を用いて生活用水を製造するには、原水を逆浸透膜装置10で処理して濃縮水と透過水を得るI工程と、電解槽20に逆浸透膜装置10から得られる濃縮水を流入し、陰極室からアルカリ性水を、陽極室から酸性水を得るII工程と、を有し、原水、透過水、アルカリ性水及び酸性水を生活用水として使用点に供給する。   Next, a method for supplying domestic water using the domestic water supply apparatus 50 of this example will be described. In order to produce domestic water using the domestic water supply device 50, the raw water is processed by the reverse osmosis membrane device 10 to obtain concentrated water and permeate, and the electrolytic cell 20 is obtained from the reverse osmosis membrane device 10. The step of supplying concentrated water and supplying alkaline water from the cathode chamber and acidic water from the anode chamber, and supplying raw water, permeated water, alkaline water and acidic water to the point of use as domestic water.

I工程において得られるRO透過水は、原水中の不純物イオン等が除去され、純水として使用点に供給される。純水は洗濯、食器洗い、調理用として好適である。I工程において得られるRO濃縮水は、原水中の不純物が濃縮されている。例えばRO回収率が65%の場合、RO濃縮水中のイオン濃度は、原水中のイオン濃度の3倍近くになる。RO濃縮水は電解槽20に送られる。   The RO permeated water obtained in step I is supplied to the point of use as pure water after removing impurity ions and the like in the raw water. Pure water is suitable for washing, dishwashing and cooking. In the RO concentrated water obtained in the step I, impurities in the raw water are concentrated. For example, when the RO recovery rate is 65%, the ion concentration in the RO concentrated water is nearly three times the ion concentration in the raw water. The RO concentrated water is sent to the electrolytic cell 20.

II工程において、電解槽20に、濃縮水流出配管cを通してRO濃縮水を通水し、陰極と陽極に直流電位を印加する。電解槽20に通水、通電すると、陽極水流出配管eから排出される陽極出口水は、陽極反応によって酸素ガスが発生するため、酸素や次亜塩素酸を含み、酸化力や殺菌力を有するため、酸性水として利用することができる。また、陰極水流出配管hから排出される陰極出口水は、陰極反応によって水素ガスが発生するため、還元性を有するアルカリ性水として利用することができる。   In step II, RO concentrated water is passed through the concentrated water outflow pipe c into the electrolytic cell 20, and a DC potential is applied to the cathode and the anode. When water is passed through the electrolyzer 20 and energized, the anode outlet water discharged from the anode water outflow pipe e contains oxygen and hypochlorous acid and has an oxidizing power and a sterilizing power because oxygen gas is generated by the anode reaction. Therefore, it can be used as acidic water. Further, the cathode outlet water discharged from the cathode water outflow pipe h can be used as alkaline water having reducibility because hydrogen gas is generated by the cathode reaction.

本発明においては、電解槽20の被処理水としてイオン濃度の高いRO濃縮水を用いるため、低電圧で運転することができる。また、電解槽20の被処理水として、RO濃縮水ではなく、例えば原水を使用した場合、同じpHのアルカリ性水や酸性水を得るためには、装置が大きくならざるを得ない。生活用水供給装置は、通常設置容積が制限されるため、装置がコンパクト化できることは大きな利点である。   In the present invention, RO concentrated water having a high ion concentration is used as the water to be treated in the electrolytic cell 20, so that it can be operated at a low voltage. Further, when raw water is used as the water to be treated in the electrolytic cell 20 instead of RO concentrated water, for example, the apparatus must be large in order to obtain alkaline water or acidic water having the same pH. Since the domestic water supply device normally has a limited installation volume, it is a great advantage that the device can be made compact.

II工程で得られたアルカリ性水は調理用、食材洗浄用に好適に使用される。RO濃縮水を電気分解して得られたアルカリ性水は、原水を電気分解して得られた同じpH値のアルカリ性水と比較して、理由は不明ではあるが、野菜の洗浄効果が高い。酸性水はトイレ、食材殺菌に好適に使用される。また、原水は従前通り、生活用水として使用することができ、また、純水、アルカリ性水及び酸性水が採取できない場合の緊急用水として使用できる。具体的には、原水供給配管Aは、全ての生活用水使用点に供給可能に別配管しておくことが好ましい。   The alkaline water obtained in step II is suitably used for cooking and cleaning foods. Alkaline water obtained by electrolyzing RO concentrated water has a high vegetable washing effect, although the reason is unknown, compared with alkaline water having the same pH value obtained by electrolyzing raw water. Acidic water is suitably used for toilets and food sterilization. Moreover, raw water can be used as domestic water as before, and can also be used as emergency water when pure water, alkaline water and acidic water cannot be collected. Specifically, the raw water supply pipe A is preferably separately piped so that it can be supplied to all domestic water use points.

次ぎに、本発明の他の実施の形態における生活用水供給方法及び生活用水供給装置について図2を参照して説明する。図2において、図1と同一構成要素には同一符号を付して、その説明を省略し異なる点について主に説明する。すなわち、図2において、図1と異なる点は、酸性水供給配管Eの途中に上流側から下流側に向けて、酸性水貯留槽21及び酸性水供給ポンプ24を、アルカリ性水供給配管Dの途中にアルカリ性水貯留槽22及びアルカリ性水供給ポンプ25を、透過水供給配管Bの途中に透過水貯留槽23及び透過水供給ポンプ26をそれぞれ備え、酸性水貯留槽21の下流側の酸性水供給配管と酸性水貯留槽21が酸性水戻り配管27で接続され、アルカリ性水貯留槽22の下流側のアルカリ性水供給配管とアルカリ性水貯留槽22がアルカリ性水戻り配管28で接続され、透過水貯留槽23の下流側の透過水供給配管と透過水貯留槽23が透過水戻り配管29で接続された生活用水供給装置50aとした点にある。   Next, a domestic water supply method and a domestic water supply apparatus according to another embodiment of the present invention will be described with reference to FIG. In FIG. 2, the same components as those in FIG. 1 are denoted by the same reference numerals, description thereof will be omitted, and different points will be mainly described. That is, FIG. 2 is different from FIG. 1 in that the acidic water storage tank 21 and the acidic water supply pump 24 are arranged in the middle of the alkaline water supply pipe D in the middle of the acidic water supply pipe E from the upstream side toward the downstream side. Are provided with an alkaline water storage tank 22 and an alkaline water supply pump 25, and a permeated water storage tank 23 and a permeated water supply pump 26 in the middle of the permeated water supply pipe B, respectively. And the acidic water storage tank 21 are connected by the acidic water return pipe 27, the alkaline water supply pipe downstream of the alkaline water storage tank 22 and the alkaline water storage tank 22 are connected by the alkaline water return pipe 28, and the permeated water storage tank 23 is connected. The permeated water supply pipe 50 and the permeated water storage tank 23 are connected to each other by a permeated water return pipe 29.

すなわち、該各工程で得られた酸性水、アルカリ性水及び透過水は、それぞれの貯留槽に流入し、各々の供給ポンプにより、該貯留槽から使用点に供給されると共に、該使用点で使用される量を超える供給水は、該貯留槽に戻される。このため、それぞれの生活用水を使用点に安定して供給することができる。また、各貯留槽21〜23において、高水位を検出して装置を自動的に停止する手段、低水位を検出して装置を自動的に稼動する手段を付設しておくことで、利便性が一層高まる。   That is, the acidic water, alkaline water and permeated water obtained in each step flow into the respective storage tanks, and are supplied from the storage tanks to the point of use by the respective supply pumps and used at the point of use. Supply water in excess of the amount to be returned is returned to the reservoir. For this reason, each domestic water can be stably supplied to a use point. Further, in each of the storage tanks 21 to 23, convenience is provided by adding a means for automatically stopping the apparatus by detecting a high water level and a means for automatically operating the apparatus by detecting a low water level. Increased further.

本発明において、逆浸透膜装置10の前段には、原水から残留塩素やトリハロメタン等の有機成分、更に酸化鉄、シリカなどの微粒子を除去する前処理装置を設置することが、逆浸透膜装置10の膜面を防止することができる点で好ましい。前処理装置の具体例としては、活性炭や膜分離装置などが挙げられる。   In the present invention, the reverse osmosis membrane device 10 is provided with a pretreatment device for removing organic components such as residual chlorine and trihalomethane from the raw water, and fine particles such as iron oxide and silica, from the raw water. It is preferable in that the film surface can be prevented. Specific examples of the pretreatment device include activated carbon and a membrane separation device.

本例の生活用水供給装置50、50aを用いて生活用水を製造すれば、アルカリ性水、酸性水及び純水を得ることができると共に、電解槽をコンパクト化できる。   If domestic water is manufactured using the domestic water supply devices 50 and 50a of this example, alkaline water, acidic water and pure water can be obtained, and the electrolytic cell can be made compact.

本発明において、アルカリ性水貯留槽22及び透過水貯留槽23には、殺菌設備を付設することが、貯留槽中におけるアルカリ性水及び透過水の微生物による腐敗を防止することができる点で好ましい。殺菌設備としては、紫外線照射方法あるいは貯留槽及び貯留槽出口配管中に銀付きフィルターを設置する方法などが挙げられる。   In the present invention, it is preferable that the alkaline water storage tank 22 and the permeated water storage tank 23 are provided with a sterilization facility from the viewpoint of preventing decay of alkaline water and permeated water in the storage tank by microorganisms. Examples of the sterilization facility include an ultraviolet irradiation method or a method of installing a filter with silver in a storage tank and a storage tank outlet pipe.

本発明において、逆浸透膜装置10は、前段と後段の多段であってもよい。すなわち、前段の逆浸透膜装置から得られる濃縮水を、後段の逆浸透膜装置の被処理水とすることで、RO透過水(純水)の回収を高めることができる。また、逆浸透膜前段に昇圧ポンプを設置する場合には、濃縮水の一部を該ポンプ上流に循環させることでも、RO透過水(純水)の回収を高めることができる。   In the present invention, the reverse osmosis membrane device 10 may be a multistage of a front stage and a rear stage. That is, recovery of RO permeated water (pure water) can be enhanced by using the concentrated water obtained from the upstream reverse osmosis membrane device as the treated water of the downstream reverse osmosis membrane device. Moreover, when installing a pressure | voltage rise pump in the front | former stage of a reverse osmosis membrane, collection | recovery of RO permeated water (pure water) can be improved also by circulating a part of concentrated water upstream of this pump.

次ぎに、実施例を挙げて本発明を更に具体的に説明するが、これは単に例示であって本発明を制限するものではない。   Next, the present invention will be described more specifically with reference to examples. However, this is merely an example and does not limit the present invention.

図2に示す生活用水供給装置のフロー図に従い、1280L/日の水道水を、逆浸透膜装置に供給し、RO濃縮水を電解槽に供給し、下記の運転条件下で処理して酸性水、アルカリ性水及び透過水を得た。その結果、酸性水390L/日、アルカリ性水;52L/日、RO透過水(純水)を838L/日を得た。なお、水道水は活性炭+精密ろ過フィルター(D−4形+FUカートリッジ、オルガノ社製)を通したものを使用した。   In accordance with the flow chart of the domestic water supply device shown in FIG. 2, 1280 L / day of tap water is supplied to the reverse osmosis membrane device, RO concentrated water is supplied to the electrolytic cell, and the acid water is treated under the following operating conditions. Alkaline water and permeated water were obtained. As a result, 390 L / day of acidic water, alkaline water; 52 L / day, and 838 L / day of RO permeated water (pure water) were obtained. In addition, the tap water used what passed the activated carbon + microfiltration filter (D-4 form + FU cartridge, the organo company make).

<逆浸透膜装置>
・RO膜モジュール(RE2012−LP×3本;セハン社製)
・水道水供給量;1280L/日
・ RO濃縮水量;442L/日、RO透過水量;838L/日
・ RO回収率;65%
<Reverse osmosis membrane device>
・ RO membrane module (RE2012-LP x 3; manufactured by Sehan)
・ Tap water supply amount: 1280 L / day ・ RO concentrated water amount: 442 L / day, RO permeate water amount: 838 L / day ・ RO recovery rate: 65%

<電解槽>
・電気分解装置(隔膜付き複槽式;オルガノ社製)
・通電電流値;0.8A
・平均印加電圧;4.0V
・ 被処理水;RO濃縮水量;442L/日
・ 酸性水量;390L/日
・ アルカリ性水量;52L/日
<Electrolytic cell>
・ Electrolysis device (double tank type with diaphragm; manufactured by Organo)
・ Conducting current value: 0.8A
・ Average applied voltage: 4.0V
・ Water to be treated; RO concentrated water volume: 442 L / day ・ Acidic water volume: 390 L / day ・ Alkaline water volume: 52 L / day

<貯留槽>
・ 酸性水貯留槽及びアルカリ性水貯留槽の容量;それぞれ50L
・ 透過水貯留槽の容量;150L
<Reservoir>
・ Capacity of acidic water storage tank and alkaline water storage tank; 50L each
・ Capacity of permeate storage tank: 150L

本実施の形態における生活用水供給装置のフロー図である。It is a flowchart of the domestic water supply apparatus in this Embodiment. 他の実施の形態における生活用水供給装置のフロー図である。It is a flowchart of the domestic water supply apparatus in other embodiment.

符号の説明Explanation of symbols

10 逆浸透膜装置
a〜e、A、B、D、E 配管
20 電解槽
21 酸性水貯留槽
22 アルカリ性水貯留槽
23 透過水貯留槽
24〜26 ポンプ
27〜29 戻り配管
50、50a 生活用水供給装置
DESCRIPTION OF SYMBOLS 10 Reverse osmosis membrane apparatus ae, A, B, D, E Piping 20 Electrolysis tank 21 Acidic water storage tank 22 Alkaline water storage tank 23 Permeated water storage tank 24-26 Pump 27-29 Return piping 50, 50a Water supply for domestic use apparatus

Claims (5)

原水を逆浸透膜装置で処理して濃縮水と透過水を得る脱塩工程と、電解槽に該逆浸透膜装置から得られる濃縮水を流入し、陰極室からアルカリ性水を、陽極室から酸性水を得る電解工程と、を有し、生活用水として、原水を原水使用点に、透過水を透過水使用点に、該陰極室から得られるアルカリ性水を、アルカリ性水が食材洗浄用として使用されるアルカリ性水使用点に、該陽極室から得られる酸性水を酸性水使用点に供給することを特徴とする生活用水供給方法。 A desalination step in which raw water is treated with a reverse osmosis membrane device to obtain concentrated water and permeated water, and concentrated water obtained from the reverse osmosis membrane device is flowed into an electrolytic cell, and alkaline water from the cathode chamber and acidic water from the anode chamber An electrolysis step for obtaining water, and as raw water for daily use, raw water is used as a raw water use point, permeate is used as a permeate use point, alkaline water obtained from the cathode chamber is used for washing foods A water supply method for domestic use, characterized in that acidic water obtained from the anode chamber is supplied to the acidic water usage point at the alkaline water usage point. 該脱塩工程で得られた透過水、及び該電解工程で得られたアルカリ性水及び酸性水は、それぞれの貯留槽に流入し、該貯留槽から使用点に供給されると共に、該使用点で使用される量を超える供給水は、該貯留槽に戻されることを特徴とする請求項1記載の生活用水供給方法。   The permeated water obtained in the desalting step and the alkaline water and acidic water obtained in the electrolysis step flow into the respective storage tanks and are supplied from the storage tanks to the point of use. The domestic water supply method according to claim 1, wherein supply water exceeding the amount used is returned to the storage tank. 逆浸透膜装置と、
供給された被処理水を電気分解してアルカリ性水と酸性水とを生成する電解槽を備える生活用水供給装置であって、
該逆浸透膜装置の原水側には原水導入配管を、濃縮水側には濃縮水流出配管を、透過水側には透過水流出配管をそれぞれ配し、
該電解槽の被処理水流入側には該逆浸透膜装置の濃縮水流出配管を、陰極室にはアルカリ性水流出配管を、陽極室には酸性水流出配管をそれぞれ配し、
原水導入配管と原水使用点を接続する原水供給配管と、
透過水流出配管と透過水使用点を接続する透過水供給配管と、
アルカリ性水流出配管とアルカリ性水が食材洗浄用として使用されるアルカリ性水使用点を接続するアルカリ性水供給配管と、
酸性水流出配管と酸性水使用点を接続する酸性水供給配管と、をそれぞれ配するものであることを特徴とする請求項1又は2いずれか1項記載の生活用水供給方法を実施するための生活用水供給装置。
A reverse osmosis membrane device;
A water supply device for daily life comprising an electrolyzer that electrolyzes the supplied treated water to produce alkaline water and acidic water,
The reverse osmosis membrane device is provided with a raw water introduction pipe on the raw water side, a concentrated water outflow pipe on the concentrated water side, and a permeate outflow pipe on the permeate side,
Concentrated water outflow piping of the reverse osmosis membrane device is arranged on the treated water inflow side of the electrolytic cell, alkaline water outflow piping is arranged in the cathode chamber, and acidic water outflow piping is arranged in the anode chamber, respectively.
A raw water supply pipe connecting the raw water introduction pipe and the raw water use point;
A permeate supply pipe connecting the permeate outflow pipe and the permeate use point;
An alkaline water supply pipe for connecting an alkaline water outlet pipe and an alkaline water use point where alkaline water is used for cleaning foods ;
3. The water supply method for domestic use according to claim 1, wherein an acid water outflow pipe and an acid water supply pipe connecting the acid water use point are respectively arranged. Domestic water supply device.
該透過水供給配管の途中に透過水貯留槽を、該アルカリ性水供給配管の途中にアルカリ性水貯留槽を、該酸性水供給配管の途中に酸性水貯留槽をそれぞれ備え、該透過水貯留槽の下流側の透過水供給配管と該透過水貯留槽が透過水戻り配管で接続され、該アルカリ性水貯留槽の下流側のアルカリ性水供給配管と該アルカリ性水貯留槽がアルカリ性水戻り配管で接続され、該酸性水貯留槽の下流側の酸性水供給配管と該酸性水貯留槽が酸性水戻り配管で接続されることを特徴とする請求項3記載の生活用水供給装置。   A permeated water storage tank is provided in the middle of the permeated water supply pipe, an alkaline water storage tank is provided in the middle of the alkaline water supply pipe, and an acidic water storage tank is provided in the middle of the acidic water supply pipe. A downstream permeate water supply pipe and the permeate water storage tank are connected by a permeate return pipe, an alkaline water supply pipe downstream of the alkaline water storage tank and the alkaline water storage tank are connected by an alkaline water return pipe, The domestic water supply apparatus according to claim 3, wherein the acidic water supply pipe on the downstream side of the acidic water storage tank and the acidic water storage tank are connected by an acidic water return pipe. 該逆浸透膜装置の前段には、該原水から有機成分を除去する前処理装置を設置したことを特徴とする請求項3又は4記載の生活用水供給装置。   The water supply device for domestic use according to claim 3 or 4, wherein a pretreatment device for removing organic components from the raw water is installed in a front stage of the reverse osmosis membrane device.
JP2006285210A 2006-10-19 2006-10-19 Domestic water supply method and apparatus Expired - Fee Related JP5019422B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2006285210A JP5019422B2 (en) 2006-10-19 2006-10-19 Domestic water supply method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2006285210A JP5019422B2 (en) 2006-10-19 2006-10-19 Domestic water supply method and apparatus

Publications (2)

Publication Number Publication Date
JP2008100174A JP2008100174A (en) 2008-05-01
JP5019422B2 true JP5019422B2 (en) 2012-09-05

Family

ID=39434905

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2006285210A Expired - Fee Related JP5019422B2 (en) 2006-10-19 2006-10-19 Domestic water supply method and apparatus

Country Status (1)

Country Link
JP (1) JP5019422B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5564174B2 (en) * 2008-03-31 2014-07-30 株式会社神鋼環境ソリューション Purification method and apparatus for purification of water containing metal components
JP5486170B2 (en) * 2008-07-16 2014-05-07 オルガノ株式会社 Domestic water supply system with hot water storage system
CN101962217A (en) * 2010-09-27 2011-02-02 杨思博 Method for preparing electrolysis water by electrolyzing dual-quality water

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06226259A (en) * 1993-02-04 1994-08-16 Takenori Hayakawa Water feeding system and water feeding device used in same
JP2003334433A (en) * 2002-05-16 2003-11-25 Kurita Water Ind Ltd Continuous dissolving device, continuous dissolving method and apparatus for supplying gas-dissolved water
JP2006272031A (en) * 2005-03-28 2006-10-12 Toto Ltd Apparatus for producing drinking water

Also Published As

Publication number Publication date
JP2008100174A (en) 2008-05-01

Similar Documents

Publication Publication Date Title
JP3716042B2 (en) Acid water production method and electrolytic cell
US6458257B1 (en) Microorganism control of point-of-use potable water sources
KR101831743B1 (en) Electrolysis device and apparatus for producing electrolyzed ozonated water
JP6017911B2 (en) Artificial dialysis water production equipment for personal dialysis
JP5486170B2 (en) Domestic water supply system with hot water storage system
JP5714060B2 (en) Dialysate preparation water production equipment
CN108633269B (en) Water treatment device, device for producing water for dialysate preparation, and hydrogen-rich water supply device
EP1149054A1 (en) Microorganism control of point-of-use potable water sources
JP4929430B2 (en) Electrolyzed water production apparatus and electrolyzed water production method
JPWO2015087536A1 (en) Method for producing oxidized water for sterilization
JP5019422B2 (en) Domestic water supply method and apparatus
JP6171047B1 (en) Electrolyzed water production apparatus and operation method thereof
US20130092530A1 (en) Apparatus for producing electrolytic reduced water and control method thereof
KR20120114900A (en) Apparatus for producing reducing water by electrolysis
JP4896657B2 (en) Domestic water supply method and apparatus
JPH11235590A (en) Ionized water generator
JP5093437B2 (en) Bacteria control method for fuel cell system
KR101108142B1 (en) Clean water system for functional water
JP2004249221A (en) Desalinizing method of seawater or the like using alkali ionized water generator and apparatus therefor
KR101644275B1 (en) Electrolysis device and water treatment method using the device
CN215855269U (en) Water purification system
CN215288100U (en) Water purification system
EP4026607A1 (en) Apparatus for producing acidic aqueous solution and method for producing acidic aqueous solution
JPH11221566A (en) Production of electrolytic water
JP3357598B2 (en) Ionized water generator and method for producing weakly alkaline ionized water and weakly acidic sterilized water

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20090423

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20101022

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20111220

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20120216

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20120307

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20120426

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: 20120606

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20120607

R150 Certificate of patent or registration of utility model

Ref document number: 5019422

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150622

Year of fee payment: 3

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees