JPH09155343A - Water purifier - Google Patents

Water purifier

Info

Publication number
JPH09155343A
JPH09155343A JP7346313A JP34631395A JPH09155343A JP H09155343 A JPH09155343 A JP H09155343A JP 7346313 A JP7346313 A JP 7346313A JP 34631395 A JP34631395 A JP 34631395A JP H09155343 A JPH09155343 A JP H09155343A
Authority
JP
Japan
Prior art keywords
water
tank
exchange resin
anion exchange
purification tank
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
JP7346313A
Other languages
Japanese (ja)
Inventor
Yoshie Tanizaki
美江 谷崎
Yukio Kobayashi
幸男 小林
Hiroyuki Okazaki
博行 岡崎
Atsuko Nishi
温子 西
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co 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 Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP7346313A priority Critical patent/JPH09155343A/en
Publication of JPH09155343A publication Critical patent/JPH09155343A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Water By Ion Exchange (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To make safe and palatable drinking water from raw water over a long period of time by providing two or more first water purifying tanks packed with a chloride ion type strong basic anion exchange resin and providing a second water purifying tank packed with activated carbon and hollow yarn membranes purifying primary filtered water. SOLUTION: Raw water is passed through a first water purifying tank 1a packed with an anion exchange resin by a raw water supply control mechanism 7. Next, the primary filtered water issued from the first water purifying tank 1a is passed through a second water purifying tank 2 from a primary filtered water supply control mechanism 9 to be emitted from a purified water emitting port 13. At that time, when the life of the anion exchange resin of the first water purifying tank 1a is detected on the basis of an integrated flow rate by a liquid flow sensor 5, the supply of water to the first water purifying tank 1a is stopped by the raw water supply control mechanism 7 and the supply of water is changed over to a first water purifying tank 1b and a sodium chloride aq. soln. is supplied to the first water purifying tank 1a from a sodium chloride dissolving tank 10 by a regeneration soln. supply mechanism 8 to simultaneously perform the regeneration of the anion exchange resin of the first water purifying tank 1a.

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、水を浄化し飲用に
供するための浄水器に関する。
TECHNICAL FIELD The present invention relates to a water purifier for purifying water for drinking.

【0002】[0002]

【従来の技術】上水道の普及により殆どの飲用水には、
水道水が用いられているが、上水道の未整備或いは嗜好
上の理由等により井戸水も用いられている。しかしなが
ら、井戸水のなかには、飲用水としての水質基準を満た
さないものがあり、特に硝酸性窒素及び亜硝酸性窒素の
項目と大腸菌群、一般細菌といった細菌に関する項目で
基準を越える場合が多い。また、井戸水は、臭気、色度
の項目で水質上問題となることも多い。
2. Description of the Related Art Due to the spread of water supply, most drinking water is
Although tap water is used, well water is also used due to undeveloped water supply or preference. However, some well water does not meet the water quality standards for drinking water, and in particular, the items of nitrate nitrogen and nitrite nitrogen and the items of bacteria such as coliform bacteria and general bacteria often exceed the standards. In addition, well water often causes problems in terms of water quality in terms of odor and chromaticity.

【0003】井戸水の汚染物質のうち、細菌は、多孔質
中空糸膜での膜濾過により、また、臭気や色度成分は、
活性炭により除去することが可能であることから、多孔
質中空糸膜や活性炭を単独で或いは組み合わせて濾材と
した浄水器が井戸水の浄化にも適用されるが、硝酸性窒
素及び亜硝酸性窒素は、かかる濾材によっては除去され
ず、硝酸性窒素及び亜硝酸性窒素の除去に有効なアニオ
ン交換樹脂を濾材として併用した浄水器も検討されてい
る。
Among the pollutants in well water, bacteria are produced by membrane filtration with a porous hollow fiber membrane, and odor and chromaticity components are
Since it can be removed by activated carbon, a water purifier that uses a porous hollow fiber membrane or activated carbon alone or in combination as a filter medium is also applicable to the purification of well water, but nitric nitrogen and nitrite nitrogen are A water purifier using an anion exchange resin, which is not removed by such a filter medium and is effective for removing nitrate nitrogen and nitrite nitrogen, as a filter medium is also under study.

【0004】アニオン交換樹脂を浄水器の濾材とする場
合、アニオン交換樹脂は、硝酸性窒素及び亜硝酸性窒素
をイオン交換により除去するが、浄水器内に充填した限
られた量のアニオン交換樹脂量では、比較的短時間でイ
オン交換基が飽和して寿命に達してしまい、頻繁なアニ
オン交換樹脂の交換及び再生を必要とする。
When an anion exchange resin is used as a filter medium for a water purifier, the anion exchange resin removes nitrate nitrogen and nitrite nitrogen by ion exchange, but a limited amount of anion exchange resin filled in the water purifier is used. In terms of quantity, the ion-exchange groups saturate in a relatively short period of time and reach the end of their lives, requiring frequent exchange and regeneration of the anion-exchange resin.

【0005】[0005]

【発明が解決しようとする課題】本発明の目的は、濾材
として寿命の短いアニオン交換樹脂を有効に用いて硝酸
性窒素及び亜硝酸性窒素を含む井戸水等の原水から長期
にわたり安全で美味しい飲料水を得る浄水器を提供する
ことにある。
The object of the present invention is to effectively use an anion exchange resin having a short life as a filter medium, and to obtain safe and delicious drinking water from raw water such as well water containing nitrate nitrogen and nitrite nitrogen for a long period of time. It is to provide a water purifier to obtain.

【0006】[0006]

【課題を解決するための手段】本発明は、塩化物イオン
型強塩基性アニオン交換樹脂が充填された第1浄水槽を
二つ以上備えると共に第1浄水槽からの一次濾過水を浄
化する活性炭及び中空糸膜が充填された第2浄水槽を備
え、一つの第1浄水槽への原水通水時に他の第1浄水槽
への通水を停止させる原水供給制御機構と、通水停止状
態にある第1浄水槽のアニオン交換樹脂の再生時に塩化
ナトリウム水溶液を供給する再生液供給機構と、通水の
第1浄水槽からの一次濾過水のみを選択し第2浄水槽へ
供給し、通水停止の第1浄水槽の再生廃液を排出させる
一次濾過水供給制御機構とを設けたことを特徴とする浄
水器にある。
The present invention comprises two or more first water purification tanks filled with a chloride ion type strongly basic anion exchange resin and activated carbon for purifying primary filtered water from the first water purification tank. And a second water purification tank filled with a hollow fiber membrane, and a raw water supply control mechanism for stopping the water passage to the other first water purification tank when the raw water is passed to one first water purification tank, and a water passage stop state In the first water purification tank, the regeneration liquid supply mechanism that supplies an aqueous sodium chloride solution when regenerating the anion exchange resin, and only the primary filtered water from the first water purification tank that supplies water are selected and supplied to the second water purification tank. It is a water purifier characterized by being provided with a primary filtered water supply control mechanism for discharging the recycled waste liquid of the first water purification tank whose water is stopped.

【0007】[0007]

【発明の実施の形態】本発明の浄水器は、塩化物イオン
型強塩基性アニオン交換樹脂が充填された第1浄水槽と
活性炭及び中空糸膜が充填された第2浄水槽を備え、第
1浄水槽は、塩化物イオン型強塩基性アニオン交換樹脂
がそれぞれ充填された二つ以上の槽で構成される。
BEST MODE FOR CARRYING OUT THE INVENTION The water purifier of the present invention comprises a first water purification tank filled with a chloride ion type strongly basic anion exchange resin and a second water purification tank filled with activated carbon and a hollow fiber membrane. One water purification tank is composed of two or more tanks each filled with a chloride ion type strongly basic anion exchange resin.

【0008】第1浄水槽に充填されるアニオン交換樹脂
は、原水中の硝酸性窒素及び亜硝酸性窒素をイオン交換
によって除去するものであり、塩化ナトリウムにより再
生可能な塩化物イオン型で、原水のpHに影響されない
強塩基性のアニオン交換樹脂を用いる。
The anion exchange resin filled in the first water purification tank is for removing nitrate nitrogen and nitrite nitrogen in raw water by ion exchange, and is a chloride ion type reproducible with sodium chloride, A strongly basic anion exchange resin that is not affected by the pH of

【0009】第2浄水槽に充填される活性炭は、原水中
の臭気、色度成分その他有機物を除去するものであり、
ヤシガラ活性炭、骨炭、木炭等の天然物系活性炭、ピッ
チ、石油コークス、樹脂やゴムの焼成物等からの合成活
性炭が用いられ、活性炭の賦活も水蒸気賦活、化学的賦
活等任意の方法が用いられ、形態も、粉末状、粒状、繊
維状等のいずれでもよい。好ましくは粒状のヤシガラ活
性炭が用いられ、また銀を添着して抗菌性を付与した活
性炭も好ましく用いられる。
The activated carbon filled in the second water purifying tank removes odors, chromaticity components and other organic substances in the raw water,
Natural product type activated carbon such as coconut shell activated carbon, bone charcoal, charcoal, pitch, petroleum coke, synthetic activated carbon from burned material of resin or rubber, etc. are used, and activation of activated carbon may be performed by steam activation, chemical activation or any other method. The shape may be any of powder, granules, fibers, and the like. Granular coconut husk activated carbon is preferably used, and activated carbon to which silver is impregnated to impart antibacterial properties is also preferably used.

【0010】また、第2浄水槽に充填される中空糸膜
は、原水中の大腸菌、一般細菌等の細菌類やその他微小
物を除去するものであり、セルロース系、ポリオレフィ
ン系、ポリスルフォン系、ポリビニルアルコール系、ポ
リメチルメタクリレート系等の高分子物質からなる多孔
質中空糸膜が用いられ、またエチレン−ビニルアルコー
ル共重合体等で親水化された多孔質中空糸膜が好ましく
用いられる。
The hollow fiber membrane filled in the second water purification tank is for removing bacteria such as Escherichia coli and general bacteria in raw water and other minute substances, and is composed of cellulose, polyolefin, polysulfone, A porous hollow fiber membrane made of a polymeric substance such as polyvinyl alcohol or polymethyl methacrylate is used, and a porous hollow fiber membrane hydrophilized with an ethylene-vinyl alcohol copolymer or the like is preferably used.

【0011】本発明の浄水器においては、原水供給制御
機構と、再生液供給機構と、一次濾過水供給制御機構と
を設ける。
In the water purifier of the present invention, a raw water supply control mechanism, a regenerated liquid supply mechanism, and a primary filtered water supply control mechanism are provided.

【0012】原水供給制御機構は、一つの第1浄水槽へ
の原水通水時に他の第1浄水槽への通水を停止させる機
能を有し、切り換え弁で構成し、流量センサーによるア
ニオン交換樹脂のイオン交換能が失われた状態(寿命)
の検知により今まで通水していた第1浄水槽から他の使
用可能な状態にあるアニオン交換樹脂を含む第1浄水槽
への切り換えが手動または自動的に行われる。
The raw water supply control mechanism has a function of stopping the passage of water to the other first water purification tank when the raw water is passed to one first water purification tank. Loss of ion exchange capacity of resin (life)
By the detection of the above, the switching from the first water purifying tank, which has been passing water until now, to the first water purifying tank containing another usable anion exchange resin is performed manually or automatically.

【0013】再生液供給機構は、アニオン交換樹脂の再
生時に塩化ナトリウム水溶液を通水停止状態にある第1
浄水槽へ供給する機能を有し、切り換え弁で構成し、原
水供給制御機構による原水の切り換えに対応させて手動
または連動させて自動的に塩化ナトリウム水溶液を通水
停止状態にある第1浄水槽へ供給する。アニオン交換樹
脂の再生は、供給される塩化ナトリウム水溶液によりア
ニオン交換樹脂に吸着された硝酸性窒素及び亜硝酸性窒
素をイオン交換基から遊離させることにより行われ、塩
化ナトリウム水溶液の供給は、アニオン交換樹脂のイオ
ン交換容量及び塩化ナトリウム量に基づき設定する流量
制御部で制御され、アニオン交換樹脂の再生終了後に、
塩化ナトリウム水溶液の供給が停止される。
The regenerating liquid supply mechanism is a first recirculating liquid supply mechanism in which the passage of the aqueous sodium chloride solution is stopped when the anion exchange resin is regenerated.
The first water purification tank that has a function of supplying water to the water purification tank, is composed of a switching valve, and is in a stopped state of automatically passing sodium chloride aqueous solution either manually or in conjunction with switching the raw water by the raw water supply control mechanism. Supply to. Regeneration of the anion exchange resin is carried out by releasing the nitrate nitrogen and nitrite nitrogen adsorbed on the anion exchange resin from the ion exchange group by the supplied sodium chloride aqueous solution, and the sodium chloride aqueous solution is supplied by the anion exchange resin. It is controlled by the flow rate control unit that is set based on the ion exchange capacity and sodium chloride amount of the resin, and after the regeneration of the anion exchange resin is completed,
The supply of the aqueous sodium chloride solution is stopped.

【0014】また、再生液供給機構は、通水停止状態に
ある第1浄水槽のアニオン交換樹脂の再生に用いる塩化
ナトリウム水溶液を生成する塩化ナトリウム溶解槽を備
えており、原水の一部を分流させ、この分流水を用いて
投入された塩化ナトリウムを溶解する塩化ナトリウム溶
解槽と接続してもよいが、第1浄水槽から第2浄水槽へ
供給する一次濾過水からの分流水を用いて塩化ナトリウ
ムを溶解する塩化ナトリウム溶解槽と接続されることが
好ましい。また、この再生液供給機構は、塩化ナトリウ
ムを存在させない状態で用いることにより洗浄水供給機
構としても作用する。塩化ナトリウムとしては、入手が
容易で安全性、溶解性も優れることから食塩が好ましく
用いられる。
Further, the regenerant supply mechanism is provided with a sodium chloride dissolving tank for producing an aqueous sodium chloride solution used for regenerating the anion exchange resin of the first water purifying tank in a state where water flow is stopped, and part of the raw water is diverted. Although it may be connected to a sodium chloride dissolution tank that dissolves sodium chloride that has been input using this divided water, by using the divided water from the primary filtered water supplied from the first water purification tank to the second water purification tank It is preferably connected to a sodium chloride dissolving tank for dissolving sodium chloride. Further, this regenerant supply mechanism also functions as a wash water supply mechanism when used in a state where sodium chloride is not present. As sodium chloride, sodium chloride is preferably used because it is easily available, safe, and highly soluble.

【0015】一次濾過水供給制御機構は、通水中の第1
浄水槽からの一次濾過水のみを選択して第2浄水槽へ供
給し、通水停止の第1浄水槽の再生廃液を排出させる機
能を有し、切り換え弁で構成し、原水供給制御機構によ
る原水の切り換え及び再生液供給機構による塩化ナトリ
ウム水溶液の供給に対応させて手動または連動させて自
動的に一次濾過水の第2浄水槽への供給及び再生廃液の
浄水器外への排出を行う。
The primary filtered water supply control mechanism is the first
It has a function of selecting only the primary filtered water from the water purification tank and supplying it to the second water purification tank, and discharging the regenerated waste liquid of the first water purification tank whose water flow is stopped. In response to the switching of raw water and the supply of the aqueous sodium chloride solution by the regeneration liquid supply mechanism, the primary filtration water is automatically supplied to the second water purification tank and the regeneration waste liquid is discharged to the outside of the water purifier in association with the manual operation.

【0016】本発明の浄水器においては、原水流入口か
ら第2浄水槽に至るまでの流路に流量センサー及び定流
量弁を設ける。流量センサーは、積算流量を検出し、所
定の積算流量に基づいてアニオン交換樹脂の寿命を検知
するためのもので、浄水の水質を一定の基準に維持する
上でのアニオン交換樹脂の寿命の検知手段として機能
し、定流量弁は、流量を一定に保ち安定した浄化を行わ
せる浄化安定手段として機能する。
In the water purifier of the present invention, a flow sensor and a constant flow valve are provided in the flow path from the raw water inlet to the second water tank. The flow rate sensor detects the accumulated flow rate and detects the life of the anion exchange resin based on the predetermined accumulated flow rate. It detects the life of the anion exchange resin when maintaining the quality of purified water to a certain standard. The constant flow valve functions as a means, and functions as a purification stabilizing means that keeps the flow rate constant and performs stable purification.

【0017】また、流量センサーからの検出信号によ
り、原水供給制御機構にて今まで通水中の第1浄水槽へ
の原水の通水を停止させ他の使用可能なアニオン交換樹
脂を含む第1浄水槽への原水の通水に切り換えるように
すると共に、予め通水中の第1浄水槽におけるアニオン
交換樹脂の寿命状態を表示させるようにすることが好ま
しく、アニオン交換樹脂の再生時期の到来を点灯、音声
等で知らせる表示部を浄水器に設けることが好ましい。
Further, in response to the detection signal from the flow rate sensor, the raw water supply control mechanism stops the passage of the raw water to the first water purifying tank which has been so far passed, and the first purified water containing another usable anion exchange resin. It is preferable that the life of the anion exchange resin in the first water purification tank during water passage is displayed in advance while switching to the passage of raw water to the tank, and the arrival of the regeneration time of the anion exchange resin is lit up. It is preferable that the water purifier be provided with a display portion that informs by voice or the like.

【0018】[0018]

【実施例】以下、本発明を図面で示す実施例により具体
的に説明する。図1は、本発明の浄水器の一例の構成図
であり、図2は、本発明の浄水器の他の例の構成図であ
る。図中、1は第1浄水槽、1aは第1浄水槽、1bは
第1浄水槽、2は第2浄水槽、3は原水流入口、4は分
流・流量制御部、5は液流センサー、6は定流量弁、7
は原水供給制御機構、8は再生液供給機構、9は一次濾
過水供給制御機構、10は塩化ナトリウム溶解槽、11
は分流部、12は流量制御部、13は浄水吐水口、14
は再生廃液排出口を表す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to the embodiments shown in the drawings. FIG. 1 is a block diagram of an example of the water purifier of the present invention, and FIG. 2 is a block diagram of another example of the water purifier of the present invention. In the figure, 1 is a first water purification tank, 1a is a first water purification tank, 1b is a first water purification tank, 2 is a second water purification tank, 3 is a raw water inlet, 4 is a diversion / flow controller, 5 is a liquid flow sensor. , 6 is a constant flow valve, 7
Is a raw water supply control mechanism, 8 is a regenerant supply mechanism, 9 is a primary filtered water supply control mechanism, 10 is a sodium chloride dissolution tank, 11
Is a flow dividing section, 12 is a flow rate control section, 13 is a purified water discharge port, and 14 is
Indicates a recycled waste liquid discharge port.

【0019】図1において、原水は、原水流入口3より
供給し、流路に設けた液流センサー5、定流量弁6を経
て原水供給制御機構7によってアニオン交換樹脂充填の
第1浄水槽1aに通水される。第1浄水槽1aからの一
次濾過水は、原水供給制御機構7と連動する一次濾過水
供給制御機構9によって活性炭及び中空糸膜充填の第2
浄水槽2に通水され、第2浄水槽2からの浄水は、浄水
吐水口13から吐水される。液流センサー5での積算流
量により第1浄水槽1aのアニオン交換樹脂の寿命を検
知したときは、原水供給制御機構7によって第1浄水槽
1aへの通水が停止されると共に第1浄水槽1bへの通
水に切り換えられ、第1浄水槽1bからの一次濾過水
は、原水供給制御機構7と連動する一次濾過水供給制御
機構9によって第2浄水槽2に通水される。
In FIG. 1, raw water is supplied from a raw water inlet 3, passes through a liquid flow sensor 5 and a constant flow valve 6 provided in a flow path, and a raw water supply control mechanism 7 controls a first water purification tank 1a filled with an anion exchange resin. Is passed to. The primary filtered water from the first water purification tank 1a is secondarily filled with activated carbon and hollow fiber membranes by the primary filtered water supply control mechanism 9 which works in conjunction with the raw water supply control mechanism 7.
Water is passed through the water purification tank 2, and the purified water from the second water purification tank 2 is discharged from the purified water outlet 13. When the life of the anion exchange resin of the first water purification tank 1a is detected by the integrated flow rate of the liquid flow sensor 5, the raw water supply control mechanism 7 stops the water flow to the first water purification tank 1a and the first water purification tank 1a. The primary filtered water from the first purified water tank 1b is switched to the water flowing to the first purified water tank 1b, and is passed to the second purified water tank 2 by the primary filtered water supply control mechanism 9 which works in conjunction with the raw water supply control mechanism 7.

【0020】一方、通水が停止され、再生を要するアニ
オン交換樹脂含有の第1浄水槽1には、塩化ナトリウム
水溶液が再生液供給機構8によって供給される。再生液
供給機構8は、第1浄水槽から第2浄水槽へ供給する一
次濾過水からの分流水による塩化ナトリウム溶解槽10
と接続される。
On the other hand, the sodium chloride aqueous solution is supplied by the regenerant supply mechanism 8 to the first water purifying tank 1 containing the anion exchange resin, which is required to be regenerated and whose water flow is stopped. The regenerant liquid supply mechanism 8 is a sodium chloride dissolving tank 10 that is a branched water from the primary filtered water supplied from the first purified water tank to the second purified water tank.
Connected to

【0021】塩化ナトリウム水溶液は、一次濾過水供給
制御機構9から第2浄水槽2へ供給される一次濾過水の
流路に設けた分流部11で分流され流量制御部12を経
た一次濾過水と投入された塩化ナトリウムとで塩化ナト
リウム溶解槽10にて生成される。また、分流の一次濾
過水は、塩化ナトリウムを存在させずそのまま再生後の
洗浄水としても第1浄水槽1に供給される。一次濾過水
量及び塩化ナトリウム量は、再生及び洗浄に必要な量だ
けとすることが好ましく流量制御部12及び投入量で設
定する。第1浄水槽1でのアニオン交換樹脂の再生廃液
及び洗浄水は、一次濾過水供給制御機構9によって再生
廃液排出口14から浄水器外へ排出される。
The aqueous solution of sodium chloride is divided by the flow dividing section 11 provided in the flow path of the primary filtered water supplied from the primary filtered water supply control mechanism 9 to the second purified water tank 2 to the primary filtered water which has passed through the flow rate control section 12. It is generated in the sodium chloride dissolving tank 10 with the added sodium chloride. Further, the split-flow primary filtered water is supplied to the first water purification tank 1 as washing water after being regenerated as it is without the presence of sodium chloride. The amount of primary filtered water and the amount of sodium chloride are preferably only those required for regeneration and washing, and are set by the flow rate controller 12 and the input amount. The recycled waste liquid of the anion exchange resin and the cleaning water in the first water purification tank 1 are discharged from the recycled waste liquid discharge port 14 to the outside of the water purifier by the primary filtered water supply control mechanism 9.

【0022】図1においては、第1浄水槽1aへの原水
の通水時に第1浄水槽1bへの塩化ナトリウム水溶液を
供給して再生する状態を示し、原水の第1浄水槽及び第
2浄水槽にての浄化と第1浄水槽におけるアニオン交換
樹脂の再生を同時に行うことができる。
FIG. 1 shows a state in which an aqueous sodium chloride solution is supplied to the first water purification tank 1b to regenerate the raw water when the raw water is passed to the first water purification tank 1a. The purification in the tank and the regeneration of the anion exchange resin in the first water purification tank can be performed at the same time.

【0023】また、図2においては、再生を要するアニ
オン交換樹脂含有の第1浄水槽1へ塩化ナトリウム水溶
液を供給する再生液供給機構8は、第1浄水槽1へ供給
される原水の流路に設けた分流・流量制御部4で分流さ
れた原水による塩化ナトリウム溶解槽10に接続され
る。
In FIG. 2, the regenerant supply mechanism 8 for supplying the aqueous sodium chloride solution to the first water purification tank 1 containing anion exchange resin that requires regeneration is a flow path for the raw water supplied to the first water purification tank 1. It is connected to a sodium chloride dissolving tank 10 for raw water divided by the diversion / flow rate control unit 4 provided in.

【0024】図1または図2において、原水供給制御機
構7、再生液供給機構8及び一次濾過水供給制御機構9
は、それぞれ切り換え弁で構成し、各機構は、それぞれ
連動しており、手動によりまたは電磁弁等を用いた自動
化にとり一体的に作動する。
In FIG. 1 or 2, raw water supply control mechanism 7, reclaimed liquid supply mechanism 8 and primary filtered water supply control mechanism 9
Are each composed of a switching valve, and the respective mechanisms are interlocked with each other and operate integrally either manually or for automation using a solenoid valve or the like.

【0025】[0025]

【発明の効果】本発明の浄水器によれば、濾材として寿
命の短いアニオン交換樹脂の充填槽を複数備えることに
より、アニオン交換樹脂の機能発揮と再生とを可能とし
てアニオン交換樹脂を有効に用い、硝酸性窒素及び亜硝
酸性窒素を含む井戸水等の原水から長期にわたり安全で
美味しい飲料水を得ることができ、本発明の浄水器は、
経済的にも有利なるものである。
EFFECTS OF THE INVENTION According to the water purifier of the present invention, by providing a plurality of anion exchange resin filling tanks having a short life as a filter medium, the function and regeneration of the anion exchange resin can be performed and the anion exchange resin is effectively used. , It is possible to obtain safe and delicious drinking water from raw water such as well water containing nitrate nitrogen and nitrite nitrogen for a long period of time, and the water purifier of the present invention is
It is also economically advantageous.

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

【図1】本発明の浄水器の一例の構成図である。FIG. 1 is a configuration diagram of an example of a water purifier of the present invention.

【図2】本発明の浄水器の他の例の構成図である。FIG. 2 is a configuration diagram of another example of the water purifier of the present invention.

【符号の説明】[Explanation of symbols]

1 第1浄水槽 1a 第1浄水槽 1b 第1浄水槽 2 第2浄水槽 3 原水流入口 4 分流・流量制御部 5 液流センサー 6 定流量弁 7 原水供給制御機構 8 再生液供給機構 9 一次濾過水供給制御機構 10 塩化ナトリウム溶解槽 11 分流部 12 流量制御部 13 浄水吐水口 14 再生廃液排出口 1 1st water purification tank 1a 1st water purification tank 1b 1st water purification tank 2 2nd water purification tank 3 Raw water inflow port 4 Dividing / flow rate control unit 5 Liquid flow sensor 6 Constant flow valve 7 Raw water supply control mechanism 8 Regeneration liquid supply mechanism 9 Primary Filtered water supply control mechanism 10 Sodium chloride dissolution tank 11 Flow dividing section 12 Flow rate control section 13 Purified water spouting port 14 Recycled waste liquid discharge port

───────────────────────────────────────────────────── フロントページの続き (72)発明者 西 温子 東京都中央区京橋二丁目3番19号 三菱レ イヨン株式会社内 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Nishi Atsuko 2-3-19 Kyobashi, Chuo-ku, Tokyo Inside Mitsubishi Rayon Co., Ltd.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 塩化物イオン型強塩基性アニオン交換樹
脂が充填された第1浄水槽を二つ以上備えると共に第1
浄水槽からの一次濾過水を浄化する活性炭及び中空糸膜
が充填された第2浄水槽を備え、一つの第1浄水槽への
原水通水時に他の第1浄水槽への通水を停止させる原水
供給制御機構と、通水停止状態にある第1浄水槽のアニ
オン交換樹脂の再生時に塩化ナトリウム水溶液を供給す
る再生液供給機構と、通水の第1浄水槽からの一次濾過
水のみを選択し第2浄水槽へ供給し、通水停止の第1浄
水槽の再生廃液を排出させる一次濾過水供給制御機構と
を設けたことを特徴とする浄水器。
1. At least two first water purification tanks filled with a chloride ion type strongly basic anion exchange resin are provided.
It is equipped with a second water purification tank filled with activated carbon and hollow fiber membranes that purifies the primary filtered water from the water purification tank, and stops the passage of water to the other first water purification tank when the raw water is passed to one first water purification tank. A raw water supply control mechanism for controlling, a regeneration liquid supply mechanism for supplying an aqueous sodium chloride solution at the time of regenerating the anion exchange resin of the first water purification tank in a water supply stopped state, and only the primary filtered water from the first water purification tank for water passage. A water purifier characterized by comprising a primary filtered water supply control mechanism for selecting and supplying the second waste water to the second water tank and discharging the recycled waste liquid of the first water tank whose water supply is stopped.
【請求項2】 再生液供給機構が、第1浄水槽からの一
次濾過水を用いる塩化ナトリウム溶解槽を備えている請
求項1記載の浄水器。
2. The water purifier according to claim 1, wherein the regeneration liquid supply mechanism includes a sodium chloride dissolving tank that uses the primary filtered water from the first water purifying tank.
【請求項3】 原水流入口から第2浄水槽に至るまでの
流路に流量センサー及び定流量弁を設けた請求項1また
は請求項2記載の浄水器。
3. The water purifier according to claim 1 or 2, wherein a flow sensor and a constant flow valve are provided in a flow path from the raw water inlet to the second water purification tank.
JP7346313A 1995-12-13 1995-12-13 Water purifier Pending JPH09155343A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7346313A JPH09155343A (en) 1995-12-13 1995-12-13 Water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7346313A JPH09155343A (en) 1995-12-13 1995-12-13 Water purifier

Publications (1)

Publication Number Publication Date
JPH09155343A true JPH09155343A (en) 1997-06-17

Family

ID=18382562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7346313A Pending JPH09155343A (en) 1995-12-13 1995-12-13 Water purifier

Country Status (1)

Country Link
JP (1) JPH09155343A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009273968A (en) * 2008-05-12 2009-11-26 Kawamoto Pump Mfg Co Ltd Water purifying apparatus
JP2014184391A (en) * 2013-03-22 2014-10-02 Taiheiyo Cement Corp Method for regenerating amphoteric ion exchange resin
CN113387413A (en) * 2021-05-19 2021-09-14 中核四0四有限公司 Ion exchange method for uranium-containing wastewater treatment in nitric acid and carbonic acid mixed system
CN114804244A (en) * 2022-04-07 2022-07-29 阳光氢能科技有限公司 Water treatment system for electrolysis and hydrogen production system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009273968A (en) * 2008-05-12 2009-11-26 Kawamoto Pump Mfg Co Ltd Water purifying apparatus
JP2014184391A (en) * 2013-03-22 2014-10-02 Taiheiyo Cement Corp Method for regenerating amphoteric ion exchange resin
CN113387413A (en) * 2021-05-19 2021-09-14 中核四0四有限公司 Ion exchange method for uranium-containing wastewater treatment in nitric acid and carbonic acid mixed system
CN114804244A (en) * 2022-04-07 2022-07-29 阳光氢能科技有限公司 Water treatment system for electrolysis and hydrogen production system

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