JPH08294689A - Sterilizing and washing mechanism of apparatus having reverse osmosis membrane treatment tank - Google Patents

Sterilizing and washing mechanism of apparatus having reverse osmosis membrane treatment tank

Info

Publication number
JPH08294689A
JPH08294689A JP12726395A JP12726395A JPH08294689A JP H08294689 A JPH08294689 A JP H08294689A JP 12726395 A JP12726395 A JP 12726395A JP 12726395 A JP12726395 A JP 12726395A JP H08294689 A JPH08294689 A JP H08294689A
Authority
JP
Japan
Prior art keywords
treatment tank
reverse osmosis
osmosis membrane
bypass circuit
silver
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
JP12726395A
Other languages
Japanese (ja)
Inventor
Tatsuo Okazaki
龍夫 岡崎
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP12726395A priority Critical patent/JPH08294689A/en
Publication of JPH08294689A publication Critical patent/JPH08294689A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE: To prevent the loss of sterilizing power after the sterilization of org. matter by changing over a reverse osmosis membrane treated water pipeline to a bypass circuit to perform anion exchange treatment and subsequently electrolyzing reverse osmosis membrane treated water to perform sterilization and washing. CONSTITUTION: When an artificial dyalitic apparatus 1 is operated, the changeover valves 9, 13 of a supply pipeline 8 are opened toward a machinery main body 2 and reverse osmosis membrane treated water is supplied to the machinery main body 2 to be subjected to artificial analysis. When the artificial dyalitic apparatus is sterilized and washed, the changeover valves 9, 13 are opened toward a bypass circuit 10. Whereupon, reverse osmosis membrane treated water flows to an anion exchange treatment tank 11 and chlorine ions are substituted with hydrogen ions to remove chlorine. Subsequently, the treated water is introduced into a silver electrolytic cell 12 to be electrolized. Herein, silver ions are eluted to form sterilizig water containing silver hydroxide and having strong sterilizing power and this water is sent to the machinery main body 2 from the bypass circuit 10 to sterilize and wash the same.

Description

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

【0001】[0001]

【発明の利用分野】本発明は人工血液透析装置やIC洗
浄装置のように、機器の用途上、流体供給管路に逆浸透
膜処理槽を具備し、逆浸透膜処理をした水等を利用して
所定の処理をする機器の殺菌・洗浄機構に関する。
BACKGROUND OF THE INVENTION The present invention has a reverse osmosis membrane treatment tank in a fluid supply line for use of equipment such as an artificial hemodialysis apparatus and an IC cleaning apparatus, and uses water and the like subjected to reverse osmosis membrane treatment. The present invention relates to a sterilization / cleaning mechanism for equipment that performs predetermined processing.

【0002】[0002]

【従来の技術】人工透析装置やIC洗浄装置のように純
度の高い水を使用する装置は、一般に、逆浸透膜処理装
置を具備し、逆浸透膜処理をした水を使用して機器本体
の目的の作業を行っている。この種の装置はその性質
上、必要に応じて機器本体及び逆浸透膜を殺菌・洗浄す
る必要がある。
2. Description of the Related Art A device using high-purity water, such as an artificial dialysis device or an IC cleaning device, is generally equipped with a reverse osmosis membrane treatment device and uses water subjected to the reverse osmosis membrane treatment of the equipment main body. You are doing the work you want. Due to the nature of this type of device, it is necessary to sterilize and clean the device body and reverse osmosis membrane as necessary.

【0003】従来、人工血液透析装置等の殺菌・洗浄に
は次亜塩素酸ナトリウムを用いた洗浄液を使用し、この
洗浄液を外部から装置の水回路に流して逆浸透膜や機器
本体を殺菌・洗浄していた。
Conventionally, a cleaning solution using sodium hypochlorite has been used for sterilization / cleaning of an artificial hemodialysis machine and the like, and this cleaning solution is supplied from the outside to the water circuit of the system to sterilize the reverse osmosis membrane and the equipment body. I was cleaning.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、次亜塩
素酸ナトリウムを用いた洗浄液は有機物との化学反応に
より殺菌力を失ってしまうため、所定の殺菌・洗浄効果
を得るには高濃度で使用しなければならない。また、従
来は、装置の外部から洗浄液を流し込んでいたため、洗
浄液の流水量を当該装置の逆浸透膜に適合した通水量に
調整しなければならず、流量調整に注意を払わなければ
ならなかった。
However, since a cleaning solution using sodium hypochlorite loses its bactericidal power due to a chemical reaction with an organic substance, it must be used at a high concentration to obtain a predetermined bactericidal / cleaning effect. There must be. Further, in the past, since the cleaning liquid was poured from the outside of the device, the amount of water flowing through the cleaning liquid had to be adjusted to a water flow amount that was suitable for the reverse osmosis membrane of the device, and attention had to be paid to the flow rate adjustment. It was

【0005】従って、本発明の第1の目的は逆浸透膜処
理槽を有し、この逆浸透膜処理槽で生成した処理水を利
用して目的の作業を行う各種装置において、逆浸透膜処
理水の流路切り換えで、機器本体及び/または逆浸透膜
が銀電解殺菌水によって殺菌・洗浄され、しかも、有機
物を殺菌した後も殺菌力が失われない前記装置を提供す
ることにある。
Therefore, a first object of the present invention is to provide a reverse osmosis membrane treatment tank in various devices for performing a desired work by utilizing the treated water produced in the reverse osmosis membrane treatment tank. It is an object of the present invention to provide the above apparatus in which the main body of the device and / or the reverse osmosis membrane is sterilized and washed with silver electrolytic sterilizing water by switching the water flow path, and the sterilizing power is not lost even after sterilizing the organic matter.

【0006】本発明の他の目的は、殺菌・洗浄水のpH
を制御する手段をさらに具備した前記装置を提供するこ
とにある。
Another object of the present invention is to sterilize / wash water pH.
It is an object of the present invention to provide the device further comprising means for controlling.

【0007】[0007]

【課題を解決するための手段】上記第1の目的を達成す
るために、逆浸透膜処理槽を備え、この処理槽で調整し
た逆浸透膜処理水を利用して目的の作業を行う装置の殺
菌・洗浄機構において、逆浸透膜処理槽と機器本体間の
処理水供給管路に、切換弁によって流路が切換えられる
バイパス回路を形成するとともに、このバイパス回路に
陰イオン交換処理槽と銀電解槽を上流・下流の関係に介
装して前記切換弁により機器本体へ殺菌・洗浄用の銀電
解水供給路が形成されるように構成したことを特徴とす
る。好ましくは、、さらに、前記バイパス回路の銀電解
槽下流側から切換弁を介して前記逆浸透膜処理槽へ銀電
解水供給路を形成してもよく、この場合は、銀電解槽下
流側の切換弁は機器本体と逆浸透膜処理槽に択一的に開
くようにしてもよく、また、両方へ開くようにしてもよ
い。
In order to achieve the above-mentioned first object, a reverse osmosis membrane treatment tank is provided, and an apparatus for performing a desired work by utilizing the reverse osmosis membrane treated water adjusted in this treatment tank. In the sterilization / cleaning mechanism, a bypass circuit whose flow path is switched by a switching valve is formed in the treated water supply pipe between the reverse osmosis membrane treatment tank and the main body of the equipment, and an anion exchange treatment tank and silver electrolysis are formed in this bypass circuit. It is characterized in that the tank is interposed in an upstream / downstream relationship so that the switching valve forms a silver electrolyzed water supply path for sterilization / washing to the apparatus body. Preferably, a silver electrolyzed water supply path may be further formed from the silver electrolysis tank downstream side of the bypass circuit to the reverse osmosis membrane treatment tank via a switching valve. The switching valve may be opened selectively to the device body and the reverse osmosis membrane treatment tank, or may be opened to both.

【0008】上記第2の目的を達成するために、本発明
は上記の装置において、さらに、殺菌・洗浄水を調整す
る前記バイパス回路に、該回路を通る流体のpHを制御
するpH調整手段を設けたことを特徴とする。
In order to achieve the above-mentioned second object, the present invention is the above-mentioned device, wherein the bypass circuit for adjusting sterilizing / washing water further comprises pH adjusting means for controlling the pH of the fluid passing through the circuit. It is characterized by being provided.

【0009】前記バイパス回路に設けるpH調整手段に
は、陽イオン交換槽、pH調整溶液添加部、あるいは有
隔膜または無隔膜の電解槽などがある。
Examples of the pH adjusting means provided in the bypass circuit include a cation exchange tank, a pH adjusting solution adding section, and a membrane-separated or membrane-less electrolytic cell.

【0010】陽イオン交換槽は、バイパス回路から分岐
したバイパスに介装され、陽イオン処理水を前記陰イオ
ン交換処理槽の前または後、もしくは、銀電解槽の前ま
たは後の処理水に混合するようになっている。
The cation exchange tank is interposed in a bypass branched from the bypass circuit, and the cation-treated water is mixed with the treated water before or after the anion-exchange treatment tank or before or after the silver electrolytic cell. It is supposed to do.

【0011】[0011]

【作用】逆浸透膜処理槽を通った処理水は、通常は人工
透析装置等の機器本体に供給され、機器本来の目的に適
した作業に使用される。機器本体を殺菌・洗浄するとき
は、逆浸透膜処理水管路の切換弁をバイパス回路側へ開
くと逆浸透膜処理水がバイパス回路の陰イオン交換処理
槽において陰イオン交換され、塩素を除去した水に調整
される。次いで、この水は銀電極を陽極とする銀電解槽
で電解され、水中に銀イオンが溶出する。一般に水道水
などの塩素を含む水に銀イオンを溶出させると、Agイ
オンがClイオンと結合して塩化銀が生成されるが、本
発明では陰イオン交換により塩素を除去した水にAgイ
オンを溶出するのでAgイオンは水中のOHイオンと結
合し、殺菌力がより強い水酸化銀(AgOH)が生成さ
れる。かくして水酸化銀を含む殺菌力の強い水が、バイ
パス回路から機器本体へ通水されることにより、機器本
体が殺菌・洗浄される。
The treated water that has passed through the reverse osmosis membrane treatment tank is usually supplied to the main body of the equipment such as the artificial dialysis machine and used for the work suitable for the original purpose of the equipment. When sterilizing and cleaning the equipment body, open the switching valve of the reverse osmosis membrane treated water pipeline to the bypass circuit side, and the reverse osmosis membrane treated water is anion-exchanged in the anion-exchange treatment tank of the bypass circuit to remove chlorine. Adjusted to water. Next, this water is electrolyzed in a silver electrolytic cell having a silver electrode as an anode, and silver ions are eluted in the water. Generally, when silver ions are eluted into water containing chlorine such as tap water, Ag ions are combined with Cl ions to form silver chloride. In the present invention, Ag ions are added to water from which chlorine has been removed by anion exchange. As it elutes, Ag ions combine with OH ions in water to produce silver hydroxide (AgOH) having stronger bactericidal activity. Thus, the water having a strong sterilizing power containing silver hydroxide is passed from the bypass circuit to the device body, so that the device body is sterilized and washed.

【0012】他方、バイパス回路の銀電解槽下流側切換
弁を操作して逆浸透膜処理槽への銀電解水供給路を開く
と、殺菌水が逆浸透膜処理槽へ通水され、逆浸透膜が殺
菌・洗浄される。
On the other hand, when the silver electrolysis tank downstream side switching valve of the bypass circuit is operated to open the silver electrolyzed water supply passage to the reverse osmosis membrane treatment tank, sterilizing water is passed to the reverse osmosis membrane treatment tank and reverse osmosis is performed. The membrane is sterilized and washed.

【0013】バイパス回路にpH調整手段を設けた場合
は、殺菌水のpHを所望の値に制御することが可能にな
る。pH調整手段が陽イオン交換処理槽である場合は、
陰イオン交換処理の前の水の一部を陽イオン交換処理に
よりpHを下げた後、陰イオン交換の前の水に混合する
か、もしくは陰イオン交換処理後の一部を陽イオン交換
処理して陰イオン交換処理水に混合することにより、銀
電解槽へ供給される塩素除去処理水のpHが制御され
る。この水を銀電解槽で電解することによって殺菌水の
pHが調整される。
If the bypass circuit is provided with a pH adjusting means, it becomes possible to control the pH of the sterilized water to a desired value. When the pH adjusting means is a cation exchange treatment tank,
After lowering the pH of a portion of the water before the anion exchange treatment by the cation exchange treatment, mix it with the water before the anion exchange treatment or treat the portion after the anion exchange treatment with the cation exchange treatment. By mixing with the anion-exchange treated water, the pH of the chlorine-removed treated water supplied to the silver electrolytic cell is controlled. The pH of the sterilized water is adjusted by electrolyzing this water in a silver electrolytic cell.

【0014】陰イオン交換処理水の一部を陽イオン交換
処理した後、銀電解槽下流の銀電解水に混合することに
より、殺菌水のpHが制御され、機器本体または逆浸透
処理槽がpH制御された殺菌水によって殺菌・洗浄され
る。
After part of the anion exchange-treated water is subjected to cation exchange treatment, the pH of the sterilized water is controlled by mixing with the silver electrolyzed water downstream of the silver electrolyzer, and the pH of the equipment body or the reverse osmosis treatment tank is controlled. Sterilized and washed with controlled sterilized water.

【0015】pH調整溶液添加部から、銀電解槽の上流
側の陰イオン交換処理水、または、銀電解槽の下流側の
銀電解水にpH調整溶液を添加することによっても殺菌
水のpHが調整される。
The pH of the sterilizing water can also be adjusted by adding the pH adjusting solution from the pH adjusting solution adding section to the anion-exchange treated water on the upstream side of the silver electrolytic cell or the silver electrolytic water on the downstream side of the silver electrolytic cell. Adjusted.

【0016】さらに、陰イオン交換処理槽と銀電解槽の
間にpH値調整用の有隔膜または無隔膜電解槽を介装し
た場合は、pH調整用の電解によって陰イオン交換処理
水のpHが調整される。
Furthermore, when a diaphragm or non-diaphragm electrolyzer for pH value adjustment is interposed between the anion exchange treatment tank and the silver electrolytic cell, the pH of the anion exchange treated water is adjusted by electrolysis for pH adjustment. Adjusted.

【0017】逆浸透膜処理槽の排水管から切換弁を介し
てバイパス回路に切換通路を形成した場合は、殺菌・洗
浄の際に、切換弁を操作して切換通路を開くことによ
り、逆浸透膜の殺菌・洗浄水供給路が、バイパス回路に
合流し、ミネラルを含む水が銀電解槽に供給されて電解
効率を向上させるほか、供給原水の全量が有効利用され
る。また、Clイオン等を含む逆浸透膜処理排水がバイ
パス回路で陰イオン交換されることにより、水中のCl
イオン等がOHイオンに置換され、pHが高く調整され
る。さらに、逆浸透膜処理槽への殺菌水供給回路が銀電
解槽を通る循環回路になることにより、逆浸透膜は、次
第に銀Agイオン濃度の高い殺菌水によって自動的に繰
返して殺菌・洗浄される。
When a switching passage is formed in the bypass circuit from the drain pipe of the reverse osmosis membrane treatment tank via the switching valve, the reverse osmosis is opened by operating the switching valve during sterilization / cleaning. The membrane sterilization / washing water supply channel joins the bypass circuit, water containing minerals is supplied to the silver electrolyzer to improve electrolysis efficiency, and the entire raw water supply is effectively used. In addition, reverse osmosis membrane treatment wastewater containing Cl ions and the like is anion-exchanged in a bypass circuit, so that Cl in water is dissolved.
Ions and the like are replaced with OH ions, and the pH is adjusted to a high level. Furthermore, the sterilizing water supply circuit to the reverse osmosis membrane treatment tank becomes a circulation circuit that passes through the silver electrolysis tank, so that the reverse osmosis membrane is automatically and repeatedly sterilized and washed by sterilizing water having a high silver Ag ion concentration. It

【0018】[0018]

【実施例】以下、本発明の実施例を説明する。本発明は
逆浸透膜処理槽を一体に具備し、この処理槽で調整した
逆浸透膜処理水を利用して目的の作業を行う装置に適用
されるもので、ここでは血液の人工透析装置を例示して
説明する。
Embodiments of the present invention will be described below. The present invention is provided with an integrated reverse osmosis membrane treatment tank, and is applied to an apparatus for performing a target work by using the reverse osmosis membrane treated water adjusted in this treatment tank. Here, an artificial dialysis apparatus for blood is used. An example will be described.

【0019】この種の人工透析装置1は、供給原水を逆
浸透膜処理して処理水を機器本体2に供給し、排水をド
レン等に捨てる逆浸透膜処理槽3を一体に具備し、逆浸
透膜処理により水中のおよそ90%の不純成分を除去し
た後、この処理水を機器本体3の透析液供給部4に供給
し、透析原液5を添加して透析液に調整するとともに、
調整された透析液が監視装置6を介して透析器7に導入
され、血液の人工透析に供された後、外部に排水される
ようになっている。このため、逆浸透膜処理槽2の処理
水出口と機器本体2の透析液供給部4は逆浸透膜処理水
の供給管路8で接続されている。
The artificial dialysis apparatus 1 of this type is integrally provided with a reverse osmosis membrane treatment tank 3 for performing reverse osmosis membrane treatment of supply raw water to supply treated water to the apparatus main body 2 and discarding waste water to a drain or the like. After removing about 90% of the impure component in the water by the osmotic membrane treatment, this treated water is supplied to the dialysate supply unit 4 of the device body 3, and the dialyzing stock solution 5 is added to adjust the dialysate.
The adjusted dialysate is introduced into the dialyzer 7 via the monitoring device 6, is used for artificial dialysis of blood, and is then drained to the outside. Therefore, the treated water outlet of the reverse osmosis membrane treatment tank 2 and the dialysate supply unit 4 of the device body 2 are connected by the reverse osmosis membrane treated water supply pipe line 8.

【0020】この処理水供給管路8を利用して殺菌・洗
浄液供給ラインを形成するため、供給管路8に、切換弁
9を介して供給管路8から分岐され、供給管路8に合流
するバイパス回路10が形成されているとともに、この
バイパス回路10に、陰イオン交換処理槽11と銀電解
槽12が上流・下流の位置関係で直列に介装されている
。尚、図ではより好ましい実施例としてバイパス回路
10と供給管路8の合流部にも切換弁13を設け、非利
用時はバイパス回路10が供給管路8から完全に閉鎖さ
れるようにしてある。
In order to form a sterilizing / cleaning liquid supply line by using the treated water supply pipe line 8, the supply pipe line 8 is branched from the supply pipe line 8 via the switching valve 9 and merges with the supply pipe line 8. The bypass circuit 10 is formed, and an anion exchange treatment tank 11 and a silver electrolytic tank 12 are interposed in series in the bypass circuit 10 in the upstream / downstream positional relationship. In the drawing, as a more preferred embodiment, a switching valve 13 is provided also at the confluence of the bypass circuit 10 and the supply pipe line 8 so that the bypass circuit 10 is completely closed from the supply pipe line 8 when not in use. .

【0021】陰イオン交換処理槽11は切換弁9によっ
てバイパス回路10に流路を切換えられた逆浸透膜処理
水の塩素を除去するためのもので、これにより、下流側
の銀電解槽12には塩素を取り除いた処理水が供給され
るようになっている。
The anion exchange treatment tank 11 is for removing chlorine of the reverse osmosis membrane treated water whose flow path is switched to the bypass circuit 10 by the switching valve 9, whereby the silver electrolysis tank 12 on the downstream side is removed. Is supplied with treated water from which chlorine has been removed.

【0022】銀電解槽12は、少なくとも陽極に銀電極
を使用し、陽極と陰極間に電流を印加して槽内の水に銀
イオンを溶出させる目的で使用されており、図の実施例
では陽極・陰極の両極12a、12bに銀電極を使用
し、両銀電極に印加する電流の極性を転換して連続的に
銀電解が行われるようにしている。
The silver electrolytic cell 12 uses at least a silver electrode for the anode, and is used for the purpose of applying a current between the anode and the cathode to elute silver ions into the water in the cell. In the illustrated embodiment, Silver electrodes are used for both the anode and cathode electrodes 12a and 12b, and the polarity of the current applied to both silver electrodes is changed so that silver electrolysis can be continuously performed.

【0023】他方、バイパス回路10の銀電解槽12の
下流側から切換弁14を介して前記逆浸透膜処理槽3に
供給路15が設けられており、切換弁14を供給路15
側に開くことにより、バイパス回路の水が逆浸透膜処理
槽3に流れるようになっている。銀電解槽下流側の切換
弁は機器本体と逆浸透膜処理槽に択一的に開くようにし
てもよく、また、図のように三方弁を使用して両方へ開
くようにしてもよい。
On the other hand, a supply passage 15 is provided in the reverse osmosis membrane treatment tank 3 from the downstream side of the silver electrolytic cell 12 of the bypass circuit 10 via the switching valve 14, and the switching valve 14 is connected to the supply path 15.
By opening to the side, the water in the bypass circuit flows into the reverse osmosis membrane treatment tank 3. The switching valve on the downstream side of the silver electrolytic cell may be selectively opened to the device main body and the reverse osmosis membrane treatment tank, or may be opened to both sides by using a three-way valve as shown in the figure.

【0024】かくして、図1の実施例では人工透析装置
1の作動時は供給管路8の切換弁9、13を機器本体側
に開き逆浸透膜処理水が装置本体に供給されて、人工透
析を行う。
Thus, in the embodiment of FIG. 1, when the artificial dialysis apparatus 1 is in operation, the switching valves 9 and 13 of the supply line 8 are opened to the main body of the equipment, and the reverse osmosis membrane-treated water is supplied to the main body of the artificial dialysis. I do.

【0025】透析終了後等に人工透析装置1を殺菌・洗
浄する際は、切換弁9、13をバイパス回路10側に開
くと、逆浸透処理水が陰イオン交換処理槽11に流れ、
ここで水中の塩素イオンが水素イオンに置換され、塩素
が除かれる。この場合、陰イオン交換処理槽11では逆
浸透膜処理水を陰イオン交換するので、陰イオン交換処
理が効率良く行われる。
When sterilizing and washing the artificial dialysis device 1 after dialysis, etc., when the switching valves 9 and 13 are opened to the bypass circuit 10 side, the reverse osmosis treated water flows into the anion exchange treatment tank 11,
Here, chlorine ions in water are replaced with hydrogen ions to remove chlorine. In this case, since the reverse osmosis membrane-treated water is anion-exchanged in the anion-exchange treatment tank 11, the anion-exchange treatment is efficiently performed.

【0026】陰イオン交換された処理水は下流側の銀電
解槽12では陰イオン交換により塩素が除かれた処理水
に銀イオンが溶出する。この場合、銀電解槽12では陰
イオン交換により塩素が除かれた処理水に銀イオンが溶
出するので、銀電解槽12の水は水酸化銀を効率良く含
み、殺菌力が強い水になる。かくして、この殺菌水がバ
イパス回路10から機器本体2に導入されて機器本体2
が殺菌・洗浄される。
In the anion-exchanged treated water, silver ions are eluted into the treated water from which chlorine has been removed by anion exchange in the downstream silver electrolytic cell 12. In this case, in the silver electrolysis tank 12, silver ions are eluted into the treated water from which chlorine has been removed by anion exchange, so the water in the silver electrolysis tank 12 contains silver hydroxide efficiently and becomes water with a strong sterilizing power. Thus, this sterilizing water is introduced from the bypass circuit 10 into the device body 2 and the device body 2
Are sterilized and washed.

【0027】バイパス回路10の銀電解槽12の下流側
に設けた切換弁14を供給路15側に開くと前記殺菌水
が供給路15を介して逆浸透膜処理槽3に導入され、処
理槽3、特にその内部の逆浸透膜(図示せず)が殺菌・
洗浄される。
When the switching valve 14 provided on the downstream side of the silver electrolysis tank 12 of the bypass circuit 10 is opened to the supply passage 15 side, the sterilizing water is introduced into the reverse osmosis membrane treatment tank 3 through the supply passage 15 and the treatment tank. 3, especially the reverse osmosis membrane (not shown) inside the
To be washed.

【0028】本発明の装置はバイパス回路10の任意の
場所で処理水のpHを調整し、殺菌水のpHを制御でき
るようにするのが望ましい。
The apparatus of the present invention preferably adjusts the pH of the treated water anywhere in the bypass circuit 10 so that the pH of the sterilized water can be controlled.

【0029】このために、図2の実施例では、バイパス
回路10の陰イオン交換処理槽11と銀電解槽12の間
の管路に流量比調整部材16を介してバイパス17を形
成し、このバイパス17に陽イオン交換処理槽18を介
装し、陰イオン交換処理水の一部を陽イオン交換してp
Hを下げ、この処理水を陰イオン交換処理水に合流させ
て処理水全体のpHを調整できるようにしている。
For this reason, in the embodiment shown in FIG. 2, a bypass 17 is formed in the conduit between the anion exchange treatment bath 11 and the silver electrolysis bath 12 of the bypass circuit 10 via the flow rate adjusting member 16. The bypass 17 is provided with a cation exchange treatment tank 18, and a part of the anion exchange treated water is cation exchanged to p.
By lowering H, the treated water is joined to the anion exchange treated water so that the pH of the whole treated water can be adjusted.

【0030】図3の実施例は同じ目的で陰イオン交換処
理槽11下流側と銀電解槽12下流側の間に流量比調整
部材16を介してバイパス17を形成するとともに、こ
のバイパス17に陽イオン交換処理槽18を介装してい
る。この実施例では陰イオン交換処理水の一部を陽イオ
ン交換し、この陽イオン交換処理水を銀電解水に混合し
て殺菌水のpHを調整するようにしている。
In the embodiment of FIG. 3, for the same purpose, a bypass 17 is formed between the downstream side of the anion exchange treatment tank 11 and the downstream side of the silver electrolysis tank 12 via the flow ratio adjusting member 16, and the bypass 17 is positively connected. An ion exchange treatment tank 18 is provided. In this embodiment, a part of the anion-exchange treated water is cation-exchanged, and the cation-exchange treated water is mixed with silver electrolyzed water to adjust the pH of the sterilizing water.

【0031】さらに、図4の実施例はバイパス回路10
の陰イオン交換処理槽11の上流側に陽イオン交換処理
槽18を介装したバイパス17を形成し、一部の水を陽
イオン交換した後、合流させ、予めpH制御した水を陰
イオン交換処理して結果的に殺菌水のpHが所望の値に
なるようにしている。
Further, the embodiment of FIG. 4 has the bypass circuit 10
The bypass 17 having the cation exchange treatment tank 18 interposed is formed on the upstream side of the anion exchange treatment tank 11 of FIG. Treatment is performed so that the pH of the sterilized water eventually reaches a desired value.

【0032】図5の実施例は、バイパス回路10にpH
調整溶液供給部19を設け、pH調整溶液をバイパス回
路10の処理水に添加してpH調整をするものである。
この場合、pH調整溶液供給部19は図5のように銀電
解槽12の上流側と下流側の双方に設置する場合に限ら
ず、いずれか一方にのみ設置してもよい。
In the embodiment shown in FIG. 5, the bypass circuit 10 has a pH value.
The adjustment solution supply unit 19 is provided, and the pH adjustment solution is added to the treated water of the bypass circuit 10 to adjust the pH.
In this case, the pH adjusting solution supply unit 19 is not limited to being installed on both the upstream side and the downstream side of the silver electrolysis tank 12 as shown in FIG. 5, and may be installed on only one of them.

【0033】図6の実施例は、バイパス回路10の陰イ
オン交換処理槽11と銀電解槽12の間に別の電解槽2
0を介装し、電解槽20の電解でpH調整した水を銀電
解槽12で電解することによって殺菌水が所望のpHに
なるようにしている。この電解槽20は図6のように、
有隔膜電解槽を使用した場合を例示しているが、無隔膜
電解槽でもよい。有隔膜電解槽を使用するときは、陰極
室の水と陽極室の水の排水混合比を変えることによって
もpH調整が可能になる。
In the embodiment shown in FIG. 6, another electrolytic bath 2 is provided between the anion exchange treatment bath 11 and the silver electrolytic bath 12 of the bypass circuit 10.
The pH of the sterilized water is adjusted to a desired pH by electrolyzing water in the silver electrolysis tank 12 in which the pH is adjusted by electrolysis in the electrolysis tank 20. As shown in FIG. 6, this electrolytic cell 20 is
Although the case of using the diaphragm electrolyzer is illustrated, a non-diaphragm electrolyzer may be used. When using the diaphragm electrolyzer, the pH can be adjusted also by changing the drainage mixing ratio of water in the cathode chamber and water in the anode chamber.

【0034】図1乃至図6の実施例は、逆浸透膜処理槽
3の非利用側排水が排水管路21からドレン22へ直接
排水されるようになっているが、図7に例示するよう
に、排水管路21から切換弁23を介して分岐させた管
路24を前記バイパス回路10に好ましくは合流弁25
を介して接続し、機器本体あるいは、逆浸透膜の殺菌・
洗浄の際に、切換弁23をバイパス回路10側に開い
て、逆浸透膜処理槽3の非利用側排水がバイパス回路1
0に流れるようにするのがより好ましい。逆浸透膜処理
槽3から排水される非利用側の水には電解質のミネラル
等が含まれているのでこの水をバイパス回路10に合流
させることにより、銀電解槽12及び電解槽20の電解
効率が良くなる。また、排水も利用されるので水の有効
利用にもなる。
1 to 6, the non-use side drainage of the reverse osmosis membrane treatment tank 3 is drained directly from the drainage pipe 21 to the drain 22, but as shown in FIG. In addition, a conduit 24 branched from the drainage conduit 21 via a switching valve 23 is preferably joined to the bypass circuit 10 by a merging valve 25.
Sterilization of the device body or reverse osmosis membrane
At the time of cleaning, the switching valve 23 is opened to the bypass circuit 10 side so that the non-use side drainage of the reverse osmosis membrane treatment tank 3 is bypass circuit 1.
It is more preferable that the flow rate be zero. Since the water on the non-use side drained from the reverse osmosis membrane treatment tank 3 contains electrolyte minerals and the like, it is possible to combine this water with the bypass circuit 10 so that the electrolysis efficiency of the silver electrolytic cell 12 and the electrolytic cell 20 is increased. Will get better. In addition, since the drainage is also used, the water can be effectively used.

【0035】尚、図7は図1に対応するものであるが、
本発明は図2乃至図6のものを図7と同様の構成にする
ことを含むものである。また、図の実施例では逆浸透膜
処理槽を備えた人工透析装置を例示して説明したが、本
発明はこれに限らず、例えば、IC洗浄装置のように逆
浸透膜処理槽を具備し、この装置で生成した逆浸透膜処
理水を利用する装置全般に適用されるものである。
Although FIG. 7 corresponds to FIG. 1,
The present invention includes the configuration of FIGS. 2 to 6 similar to that of FIG. Further, in the illustrated embodiment, the artificial dialysis device including the reverse osmosis membrane treatment tank has been described as an example, but the present invention is not limited to this, and the reverse osmosis membrane treatment tank such as an IC cleaning device is provided. The present invention is applicable to all devices using the reverse osmosis membrane treated water generated by this device.

【0036】[0036]

【効果】本発明は逆浸透膜処理槽を具備する各種装置の
逆浸透膜処理水管路のバイパス回路に銀殺菌水を生成す
る装置が併設されているので、流路の切換えで機器本体
または逆浸透膜を銀殺菌水で殺菌・洗浄することができ
る。
[Effect] According to the present invention, since a device for producing silver sterilizing water is provided in the bypass circuit of the reverse osmosis membrane treated water pipe of various devices equipped with the reverse osmosis membrane treatment tank, the device main body or reverse The osmotic membrane can be sterilized and washed with silver sterilized water.

【0037】とくに、本発明では、銀殺菌水生成装置が
陰イオン交換処理により塩素を除去した水に銀イオンを
溶出させるので生成される銀殺菌水は殺菌力の強い水酸
化銀殺菌となり、低い濃度でも高い殺菌効果が得られ
る。
In particular, in the present invention, since the silver sterilizing water generator elutes silver ions into water from which chlorine has been removed by anion exchange treatment, the silver sterilizing water produced is highly sterilizing silver hydroxide sterilizing and is low. A high bactericidal effect can be obtained even at a high concentration.

【0038】殺菌水を生成するバイパス回路にpH調整
手段を設けることにより殺菌水のpHを所望の値に制御
することができる。
The pH of the sterilized water can be controlled to a desired value by providing a pH adjusting means in the bypass circuit for generating the sterilized water.

【0039】逆浸透膜処理槽の非利用側排水を殺菌水生
成用のバイパス回路に合流させることにより、殺菌水生
成の電解効率が向上、水の有効利用が図れるほか、pH
を高く調整することができる。また、銀イオン濃度のよ
り高い水酸化銀殺菌水を供給することも可能になる。
By merging the waste water on the non-use side of the reverse osmosis membrane treatment tank with the bypass circuit for sterilizing water production, the electrolysis efficiency of sterilizing water production is improved, and the effective use of water can be achieved.
Can be adjusted higher. It is also possible to supply silver hydroxide sterilized water having a higher silver ion concentration.

【0040】殺菌水供給回路が逆浸透膜処理水の供給路
に組み込まれているので装置に適合した水圧の殺菌水が
自動供給されることになる。
Since the sterilizing water supply circuit is incorporated in the reverse osmosis membrane-treated water supply path, sterilizing water having a water pressure suitable for the apparatus is automatically supplied.

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

【図1】 本発明の一実施例を示す装置の概略構成図FIG. 1 is a schematic configuration diagram of an apparatus showing an embodiment of the present invention.

【図2】 本発明の他の実施例を示す装置の概略構成図FIG. 2 is a schematic configuration diagram of an apparatus showing another embodiment of the present invention.

【図3】 本発明の他の実施例を示す装置の概略構成図FIG. 3 is a schematic configuration diagram of an apparatus showing another embodiment of the present invention.

【図4】 本発明の他の実施例を示す装置の概略構成図FIG. 4 is a schematic configuration diagram of an apparatus showing another embodiment of the present invention.

【図5】 本発明の他の実施例を示す装置の概略構成図FIG. 5 is a schematic configuration diagram of an apparatus showing another embodiment of the present invention.

【図6】 本は積め他の実施例を示す装置の概略構成図FIG. 6 is a schematic configuration diagram of an apparatus showing another embodiment of stacking books.

【図7】 本発明の他の実施例を示す装置の概略構成図FIG. 7 is a schematic configuration diagram of an apparatus showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…人工透析装置、 2…機器本体、 3…逆浸透膜処
理槽、 4…透析液供給部、 5…透析原液、 6…監
視装置、 7…透析器、 8…供給管路、 9、13、
14、23…切換弁、 10…バイパス回路、 11…
陰イオン交換処理槽、 12…銀電解槽、 15…供給
路、 16…流量比調整部材、 17…バイパス、 1
8…陽イオン交換処理槽、 19…pH調整溶液供給
部、 20…電解槽、 21…排水管路、 22…ドレ
ン。
DESCRIPTION OF SYMBOLS 1 ... Artificial dialysis device, 2 ... Equipment main body, 3 ... Reverse osmosis membrane treatment tank, 4 ... Dialysate supply part, 5 ... Dialysis stock solution, 6 ... Monitoring device, 7 ... Dialyzer, 8 ... Supply pipeline, 9, 13 ,
14, 23 ... Switching valve, 10 ... Bypass circuit, 11 ...
Anion exchange treatment tank, 12 ... Silver electrolysis tank, 15 ... Supply path, 16 ... Flow rate adjusting member, 17 ... Bypass, 1
8 ... Cation exchange treatment tank, 19 ... pH adjusting solution supply section, 20 ... Electrolyte tank, 21 ... Drainage line, 22 ... Drain.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/50 520 C02F 1/50 520P 531 531E 540 540Z 550 550H 560 560E 560D 560F 1/66 510 1/66 510K 530 530G 540 540D 540C 540E 540G ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C02F 1/50 520 C02F 1/50 520P 531 531E 540 540Z 550 550H 560 560E 560D 560F 1/66 510 1 / 66 510K 530 530G 540 540D 540C 540E 540G

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 逆浸透膜処理槽を備え、この処理槽で調
整した逆浸透膜処理水を利用して目的の作業を行う装置
の殺菌・洗浄機構において、逆浸透膜処理槽と機器本体
間の処理水供給管路に、切換弁によって流路が切換えら
れるバイパス回路を形成するとともに、このバイパス回
路に陰イオン交換処理槽と銀電解槽を上流・下流の関係
に介装して前記切換弁により機器本体へ殺菌・洗浄用の
銀電解水供給路が形成されるようしたことを特徴とす
る、逆浸透膜処理槽を有する装置の殺菌・洗浄機構
1. A sterilization / cleaning mechanism for an apparatus that comprises a reverse osmosis membrane treatment tank and uses the reverse osmosis membrane-treated water prepared in this treatment tank to perform a desired operation. A bypass circuit, whose flow path is switched by a switching valve, is formed in the treated water supply pipe of the above, and an anion exchange treatment tank and a silver electrolytic cell are interposed in the bypass circuit in an upstream / downstream relationship, and the switching valve is provided. A sterilization / cleaning mechanism for a device having a reverse osmosis membrane treatment tank, characterized in that a silver electrolyzed water supply path for sterilization / cleaning is formed in the main body of the device.
【請求項2】 逆浸透膜処理槽を備え、この処理槽で調
整した逆浸透膜処理水を利用して目的の作業を行う装置
の殺菌・洗浄機構において、逆浸透膜処理槽と機器本体
間の処理水供給管路に、切換弁によって流路が切換えら
れるバイパス回路を形成するとともに、このバイパス回
路に陰イオン交換処理槽と銀電解槽を上流・下流の関係
に介装して前記切換弁により機器本体へ殺菌・洗浄用の
銀電解水供給路が形成されるように構成し、さらに、前
記バイパス回路の銀電解槽下流側から切換弁を介して前
記逆浸透膜処理槽へ銀電解水供給路を形成したことを特
徴とする、逆浸透膜処理槽を有する装置の殺菌・洗浄機
2. A sterilization / cleaning mechanism for an apparatus that comprises a reverse osmosis membrane treatment tank and uses the reverse osmosis membrane-treated water prepared in this treatment tank to perform a desired operation, wherein the reverse osmosis membrane treatment tank and the equipment body are connected to each other. A bypass circuit, whose flow path is switched by a switching valve, is formed in the treated water supply pipe of the above, and an anion exchange treatment tank and a silver electrolytic cell are interposed in the bypass circuit in an upstream / downstream relationship, and the switching valve is provided. Is configured so that a silver electrolyzed water supply path for sterilization and cleaning is formed in the main body of the equipment, and further, silver electrolyzed water is supplied to the reverse osmosis membrane treatment tank from the downstream side of the silver electrolysis tank of the bypass circuit via a switching valve. A sterilization / cleaning mechanism for an apparatus having a reverse osmosis membrane treatment tank, characterized by forming a supply path
【請求項3】 前記パイパス回路の陰イオン交換処理槽
と銀電解槽間の管路に流量比調整部材を介してバイパス
を形成し、このバイパス回路に陽イオン交換処理槽を介
装した請求項1または2記載の逆浸透膜処理槽を有する
装置の殺菌・洗浄機構
3. A bypass is formed in the conduit between the anion exchange treatment tank of the bypass circuit and the silver electrolytic cell through a flow rate adjusting member, and a cation exchange treatment tank is interposed in the bypass circuit. Sterilization / cleaning mechanism of an apparatus having a reverse osmosis membrane treatment tank according to 1 or 2
【請求項4】 前記バイパス回路の陰イオン交換処理槽
下流側管路から流量比調整部材を介して銀電解槽下流側
管路へバイパスを形成し、このバイパスに陽イオン交換
処理槽を介装した請求項1または2記載の逆浸透膜処理
槽を有する装置の殺菌・洗浄機構
4. A bypass is formed from the anion exchange treatment tank downstream side pipe line of the bypass circuit to the silver electrolytic cell downstream side pipe line via a flow ratio adjusting member, and the cation exchange treatment tank is interposed in this bypass. 3. A sterilization / cleaning mechanism for an apparatus having a reverse osmosis membrane treatment tank according to claim 1 or 2.
【請求項5】 前記バイパス回路の陰イオン交換処理槽
の上流側管路に流量比調整部材を介してバイパスを形成
し、このバイパスに陽イオン交換処理槽を介装した請求
項1または2記載の逆浸透膜処理槽を有する装置の殺菌
・洗浄機構
5. The method according to claim 1, wherein a bypass is formed in the upstream side pipe line of the anion exchange treatment tank of the bypass circuit via a flow ratio adjusting member, and the cation exchange treatment tank is interposed in the bypass. Sterilization and cleaning mechanism for equipment with reverse osmosis membrane treatment tank
【請求項6】 前記バイパス回路の陰イオン交換処理槽
の下流側管路にpH調整溶液添加部を設けた請求項1ま
たは2記載の逆浸透膜処理槽を有する装置の殺菌・洗浄
機構
6. A sterilization / cleaning mechanism for an apparatus having a reverse osmosis membrane treatment tank according to claim 1 or 2, wherein a pH adjusting solution addition section is provided in a downstream side pipe line of the anion exchange treatment tank of the bypass circuit.
【請求項7】 前記バイパス回路の陰イオン交換処理槽
と前記銀電解槽の間にpH調整用の有隔膜または無隔膜
の電解槽を介装したことを特徴とする請求項1または2
記載の逆浸透膜処理槽を有する装置の殺菌・洗浄機構
7. The electrolytic cell having a diaphragm or a non-diaphragm for pH adjustment is interposed between the anion exchange treatment tank of the bypass circuit and the silver electrolysis tank.
Sterilization / cleaning mechanism of device having reverse osmosis membrane treatment tank described
【請求項8】 逆浸透膜処理槽の排水管から前記バイパ
ス回路の銀電解槽上流側に、切換弁を介して管路を接続
したことをさらに特徴とする請求項2、3、4、5また
は6記載の逆浸透膜処理槽を有する装置の殺菌・洗浄機
8. A pipe line is further connected from the drain pipe of the reverse osmosis membrane treatment tank to the upstream side of the silver electrolysis tank of the bypass circuit via a switching valve. Or a sterilization / cleaning mechanism for an apparatus having a reverse osmosis membrane treatment tank according to 6
JP12726395A 1995-04-27 1995-04-27 Sterilizing and washing mechanism of apparatus having reverse osmosis membrane treatment tank Pending JPH08294689A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12726395A JPH08294689A (en) 1995-04-27 1995-04-27 Sterilizing and washing mechanism of apparatus having reverse osmosis membrane treatment tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12726395A JPH08294689A (en) 1995-04-27 1995-04-27 Sterilizing and washing mechanism of apparatus having reverse osmosis membrane treatment tank

Publications (1)

Publication Number Publication Date
JPH08294689A true JPH08294689A (en) 1996-11-12

Family

ID=14955709

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12726395A Pending JPH08294689A (en) 1995-04-27 1995-04-27 Sterilizing and washing mechanism of apparatus having reverse osmosis membrane treatment tank

Country Status (1)

Country Link
JP (1) JPH08294689A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0826636A1 (en) * 1996-08-27 1998-03-04 Nihon Trim Co. Limited Water containing dissolved electrolytic hydrogen, and method and apparatus of production thereof
JP2002263649A (en) * 2001-03-05 2002-09-17 Toto Ltd Sterilizing water production
US6623695B2 (en) 1997-12-04 2003-09-23 Steris Corporation Chemical modification of electrochemically activated solutions for improved performance
JP2007325983A (en) * 2006-06-06 2007-12-20 Toray Ind Inc Water purifier

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0826636A1 (en) * 1996-08-27 1998-03-04 Nihon Trim Co. Limited Water containing dissolved electrolytic hydrogen, and method and apparatus of production thereof
US6623615B1 (en) 1996-08-27 2003-09-23 Nihon Trim Co., Ltd. Electrolytic hydrogen dissolved water and method and apparatus of production thereof
US6623695B2 (en) 1997-12-04 2003-09-23 Steris Corporation Chemical modification of electrochemically activated solutions for improved performance
JP2002263649A (en) * 2001-03-05 2002-09-17 Toto Ltd Sterilizing water production
JP4671160B2 (en) * 2001-03-05 2011-04-13 Toto株式会社 Sterilization water generator
JP2007325983A (en) * 2006-06-06 2007-12-20 Toray Ind Inc Water purifier

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