JPH0929237A - Water purifier - Google Patents

Water purifier

Info

Publication number
JPH0929237A
JPH0929237A JP20187695A JP20187695A JPH0929237A JP H0929237 A JPH0929237 A JP H0929237A JP 20187695 A JP20187695 A JP 20187695A JP 20187695 A JP20187695 A JP 20187695A JP H0929237 A JPH0929237 A JP H0929237A
Authority
JP
Japan
Prior art keywords
water
exchange resin
water purifying
cation exchange
activated carbon
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
JP20187695A
Other languages
Japanese (ja)
Inventor
Yukio Kobayashi
幸男 小林
Masanao Kobuke
正直 小泓
Hiroyuki Okazaki
博行 岡崎
Masahiko Taneike
昌彦 種池
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 JP20187695A priority Critical patent/JPH0929237A/en
Publication of JPH0929237A publication Critical patent/JPH0929237A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To effectively remove chlorine, dissolving ionic toxic substance, etc., by providing the first water purifying tank in which a mixture of a cation exchange resin and an active carbon is used as a filter medium and the second water purifying tank in which a hollow fiber membrane is used as a filter medium, in a water purifier in which the active carbon, the cation exchange resin and the hollow fiber membrance are used as the filter medium. SOLUTION: The first water purifying tank 2 and the second water purifying tank 7 are arranged in the main body container 1 of a water purifier and a flow rate sensor 9 and a controlling and displaying part 10 are provided between both the water purifying tanks 2 and 7. In addition, a mixture of a cation exchange resin and an active carbon is stored in the first water purifying tank 2 and a hollow fiber membrane is stored in the second water purifying tank 7 located on the downstream of the first water purifying tank, respectively as filter medium, and chlorine, trihalomethane, dissolving ionic toxic substances, agrochemicals, etc., are eliminated in the first water purifying tank 2 and bacteria and micro toxic substances, etc., are eliminated in the second water purifying tank 7. In this instance, a calcium salt type is used as the cation exchange resin, and a natural stone wherein calcium carbonate and/or soluble silicic acid are main components is filled in the first water purifying tank and/or the second water purifying tank.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、水の安全性やおいしさ
を損なう物質を除去する浄水器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purifier for removing substances that impair the safety and taste of water.

【0002】[0002]

【従来の技術】活性炭は、水道水に含まれる残留塩素を
吸着除去することから、水道水の浄化を目的とした浄水
器において、活性炭が濾過材として用いられているが、
活性炭を濾過材とする浄水器においては、使用後長時間
の通水停止状態とした場合、活性炭層に雑菌が繁殖し、
通水再開時に雑菌が流出するという問題がある。
2. Description of the Related Art Activated carbon is used as a filtering material in a water purifier for the purpose of purifying tap water because activated carbon adsorbs and removes residual chlorine contained in tap water.
In a water purifier that uses activated carbon as a filter medium, when the water flow is stopped for a long time after use, various bacteria propagate in the activated carbon layer,
There is a problem that miscellaneous bacteria will flow out when water is restarted.

【0003】また、多孔質中空糸膜は、膜濾過により細
菌を捕捉しうることから、活性炭に多孔質中空糸膜を濾
過材として併用した、雑菌の流出の問題がない浄水器も
知られているが、かかる多孔質中空糸膜を濾過材とする
浄水器においても、水道の配管から溶出する鉛等の重金
属の陽イオンや硝酸性窒素、亜硝酸性窒素等の陰イオン
等の溶解イオン性有害物質の除去には、あまり有効では
ないというのが現状である。
Further, since the porous hollow fiber membrane can capture bacteria by membrane filtration, there is also known a water purifier using activated carbon in combination with the porous hollow fiber membrane as a filter material and having no problem of outflow of various bacteria. However, even in a water purifier using such a porous hollow fiber membrane as a filtering material, dissolved ionicity such as cations of heavy metals such as lead and anions such as nitrate nitrogen and nitrite nitrogen, which are eluted from water pipes At present, it is not very effective in removing harmful substances.

【0004】溶解イオン性有害物質の除去については、
活性炭収納ユニット、分離濾過膜収納ユニット及びイオ
ン交換樹脂収納ユニットを組み合わせた浄水器(実開平
3−7989号公報)や容器に収納したフィルター、活
性炭及びイオン交換樹脂に順次水道水を通す浄水器(特
開昭61−257282号公報)等が提案され、活性炭
により塩素、トリハロメタン、農薬及び溶解イオン性有
害物質の除去、イオン交換樹脂により溶解イオン性有害
物質の除去を、それぞれ行うことが知られている。
Regarding the removal of dissolved ionic harmful substances,
A water purifier that combines an activated carbon storage unit, a separation filtration membrane storage unit, and an ion exchange resin storage unit (No. Kaikai 3-7989), a filter stored in a container, a water purifier that sequentially passes tap water through the activated carbon and ion exchange resin ( JP-A 61-257282) is proposed, and it is known that chlorine, trihalomethane, pesticides and dissolved ionic toxic substances are removed by activated carbon, and dissolved ionic toxic substances are removed by an ion exchange resin. There is.

【0005】しかしながら、上記提案の浄水器では、イ
オン交換樹脂を活性炭の上流側に配置した場合は、水道
水に含まれる塩素の影響でイオン交換樹脂が酸化分解さ
れ、活性炭で除去しきれなかった分解物が流出して濾過
水に臭気を発生させたりする。また、イオン交換樹脂を
活性炭の下流側に配置した場合は、イオン交換樹脂に含
まれる分解物、低分子物質が流出して濾過水に臭気を発
生させたりする。
However, in the above proposed water purifier, when the ion exchange resin is arranged on the upstream side of the activated carbon, the ion exchange resin is oxidatively decomposed by the effect of chlorine contained in tap water and cannot be completely removed by the activated carbon. The decomposed product may flow out and cause odor in the filtered water. Further, when the ion exchange resin is arranged on the downstream side of the activated carbon, decomposed products and low molecular weight substances contained in the ion exchange resin flow out to generate odor in the filtered water.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、活性
炭、中空糸膜及び陽イオン交換樹脂を濾過材として用い
て、水道水に含まれる塩素、トリハロメタン、農薬、溶
解イオン性有害物質、細菌等が効果的に除去された、安
全でおいしい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 use chlorine, trihalomethane, pesticides, dissolved ionic toxic substances and bacteria contained in tap water by using activated carbon, hollow fiber membranes and cation exchange resins as filter media. It is intended to provide a water purifier that obtains safe and delicious water from which water etc. has been effectively removed.

【0007】[0007]

【課題を解決するための手段】本発明は、活性炭、陽イ
オン交換樹脂及び中空糸膜を濾過材とする浄水器におい
て、陽イオン交換樹脂と活性炭との混合物を濾過材とす
る第1浄水槽及びその下流に配置された中空糸膜を濾過
材とする第2浄水槽を備えたことを特徴とする浄水器に
ある。
The present invention provides a water purifier using activated carbon, a cation exchange resin and a hollow fiber membrane as a filtering material, and a first water purification tank using a mixture of the cation exchange resin and activated carbon as a filtering material. And a second water purification tank having a hollow fiber membrane arranged downstream thereof as a filtering material.

【0008】本発明の浄水器は、第1浄水槽及びその下
流に配置された第2浄水槽とを備えて構成され、第1浄
水槽には、陽イオン交換樹脂と活性炭との混合物が濾過
材として収納され、第2浄水槽には、中空糸膜が濾過材
として収納される。
The water purifier of the present invention comprises a first water purification tank and a second water purification tank arranged downstream of the first water purification tank. The first water purification tank filters a mixture of a cation exchange resin and activated carbon. The hollow fiber membrane is stored as a filtering material in the second water purification tank.

【0009】本発明の浄水器の第1浄水槽において、陽
イオン交換樹脂と活性炭との混合物により、塩素、トリ
ハロメタン、溶解イオン性有害物質、農薬等の除去を行
い、第2浄水槽において、中空糸膜により、細菌、微細
有害物質等の除去を行う。
In the first water tank of the water purifier of the present invention, chlorine, trihalomethane, dissolved ionic toxic substances, pesticides, etc. are removed by a mixture of cation exchange resin and activated carbon, and the second water tank is hollow. Bacteria, fine harmful substances, etc. are removed by a thread film.

【0010】第1浄水槽においては、活性炭が、陽イオ
ン交換樹脂を酸化分解する原水の水道水に含まれる塩素
を除去すると同時に、陽イオン交換樹脂に含まれる分解
物、低分子物質を吸着除去し、陽イオン交換樹脂を有効
に機能させて溶解イオン性有害物質の除去を充分に行わ
せ、陽イオン交換樹脂の酸化分解物等による着色、臭気
等のない濾過水を得ることができる。
In the first water purification tank, the activated carbon removes chlorine contained in the tap water of the raw water which oxidizes and decomposes the cation exchange resin, and at the same time, adsorbs and removes decomposition products and low-molecular substances contained in the cation exchange resin. Then, the cation exchange resin can be effectively functioned to sufficiently remove the dissolved ionic toxic substance, and filtered water having no odor and the like due to coloring by the oxidative decomposition product of the cation exchange resin can be obtained.

【0011】本発明の浄水器に用いる陽イオン交換樹脂
は、強酸性陽イオン交換樹脂、弱酸性陽イオン交換樹脂
のいずれでもよいが、水道水には、例えば配水管に用い
られる鉛管から鉛等の重金属陽イオンが溶出し、しかも
その多くが中性塩として溶解しているので、中性塩を分
解吸着する強酸性陽イオン交換樹脂を用いることが好ま
しい。
The cation exchange resin used in the water purifier of the present invention may be either a strongly acidic cation exchange resin or a weakly acidic cation exchange resin. In tap water, for example, lead pipes used in water pipes, lead, etc. Since the heavy metal cations are dissolved and most of them are dissolved as neutral salts, it is preferable to use a strong acid cation exchange resin that decomposes and adsorbs the neutral salts.

【0012】陽イオン交換樹脂は、そのイオン型がカル
シウム塩型であることが好ましく、カルシウム塩型の陽
イオン交換樹脂を用いることにより、イオン交換により
濾過水に放出されたカルシウムイオンが、濾過水におい
しさを与えるといわれ、また、飲用により人体に補充さ
れることから健康面でも好ましい濾過水を得ることがで
きる。
The cation exchange resin preferably has an ionic type of a calcium salt type. By using the calcium salt type cation exchange resin, the calcium ions released into the filtered water by ion exchange can be filtered. It is said to give an odor, and since it is replenished to the human body by drinking, it is possible to obtain filtered water which is preferable from a health standpoint.

【0013】また、本発明の浄水器に用いる活性炭は、
通常浄水器に使用しうる活性炭であれば、特に制限され
るものではなく、ヤシガラ、骨、木等の天然物活性炭、
ピッチ系、石油コークス系、樹脂またはゴム系等の合成
活性炭等が挙げられ、活性炭の賦活も水蒸気賦活法、化
学的賦活法等任意の方法によってもよい。また、粉末
状、粒状、繊維状等のいずれの形態であってもよい。さ
らに、活性炭は、銀等の抗菌性金属をメッキ等により添
着されたものであってもよい。
The activated carbon used in the water purifier of the present invention is
It is not particularly limited as long as it is an activated carbon that can be usually used in a water purifier, coconut husk, bone, natural activated carbon such as wood,
Pitch-based, petroleum coke-based, resin or rubber-based synthetic activated carbon and the like can be mentioned, and activated carbon may be activated by any method such as steam activation or chemical activation. Further, it may be in any form such as powder, granules and fibres. Further, the activated carbon may be one in which an antibacterial metal such as silver is attached by plating or the like.

【0014】本発明の浄水器に用いる活性炭として、2
種以上を混合して用いることもでき、活性炭が2種以上
の活性炭の混合物であることは、吸着能力の範囲を広
げ、水道水に含まれる各種物質への対応範囲を拡大して
吸着寿命を、混合される他の活性炭或いは陽イオン交換
樹脂とバランスさせるうえで好ましいことである。
As the activated carbon used in the water purifier of the present invention, 2
It is also possible to mix and use more than one kind, and the fact that the activated carbon is a mixture of two or more types of activated carbon broadens the range of adsorption capacity and expands the range of correspondence to various substances contained in tap water to improve the adsorption life. However, it is preferable to balance with other activated carbon or cation exchange resin to be mixed.

【0015】本発明の浄水器においては、第1浄水槽の
濾過材が陽イオン交換樹脂と活性炭との混合物であるこ
とが必要であるが、陽イオン交換樹脂と活性炭との混合
物が下式を満足する混合比率C/Rの混合物であること
が好ましい。 1≦C/R≦8 但し、Cは活性炭重量(g)、Rは陽イオン交換樹脂容
積(ml)を示す。
In the water purifier of the present invention, it is necessary that the filter material of the first water purification tank is a mixture of cation exchange resin and activated carbon, and the mixture of cation exchange resin and activated carbon has the following formula. It is preferable that the mixture has a satisfactory mixing ratio C / R. 1 ≦ C / R ≦ 8 where C is the activated carbon weight (g) and R is the cation exchange resin volume (ml).

【0016】陽イオン交換樹脂と活性炭との混合物が前
記式を満足する混合比率C/Rの混合物であるときは、
陽イオン交換樹脂と活性炭の各吸着能力がほぼ揃い、吸
着寿命に著しい差を生じさせることがないので、混合物
の一方のみの吸着能力の低下に基づく不完全吸着を避け
ることができる。
When the mixture of cation exchange resin and activated carbon is a mixture having a mixing ratio C / R satisfying the above formula,
Since the adsorption capacities of the cation exchange resin and the activated carbon are almost the same and there is no significant difference in the adsorption life, it is possible to avoid incomplete adsorption due to the reduction of the adsorption capacity of only one of the mixtures.

【0017】本発明の浄水器においては、第2浄水槽に
は、濾過材として中空糸膜を用いるが、本発明の浄水器
に用いる中空糸膜は、通常浄水器に使用しうる多孔質中
空糸膜であれば、特に制限されるものではなく、ポリエ
チレン等のポリオレフィン系、ポリスルホン系等の中空
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、ポリビニルアルコール等により親水化されてい
てもよく、通水性を向上させるうえで中空糸膜が親水化
されていることは好ましいことである。
In the water purifier of the present invention, a hollow fiber membrane is used as a filtering material in the second water purifying tank, but the hollow fiber membrane used in the water purifier of the present invention is a porous hollow that can be used in ordinary water purifiers. The fiber membrane is not particularly limited as long as it is a polyolefin-based hollow fiber membrane such as polyethylene or polysulfone-based, and is hydrophilized with an ethylene-vinyl alcohol copolymer or polyvinyl alcohol. It is also preferable that the hollow fiber membrane is hydrophilized in order to improve water permeability.

【0018】また、本発明の浄水器においては、第1浄
水槽及び/または第2浄水槽に、炭酸カルシウム及び/
または溶性ケイ酸を主成分とする天然石を充填すること
もでき、濾過水中に微量に溶出する炭酸カルシウム及び
/または溶性ケイ酸が天然水様のおいしさを与える。
Also, in the water purifier of the present invention, calcium carbonate and / or
Alternatively, natural stone mainly composed of soluble silicic acid can be filled, and a small amount of calcium carbonate and / or soluble silicic acid which is eluted in the filtered water gives the taste of natural water.

【0019】本発明の浄水器においては、前記の第1浄
水槽及び第2浄水槽を備えるが、第1浄水槽と第2浄水
槽の間に、流量センサー、または定流量弁と圧力スイッ
チの検知手段を設けることが好ましく、これら手段を第
1浄水槽及び第2浄水槽の双方の濾過材の圧力損失の影
響が少ない位置に設けることにより、流量センサーの積
算濾過流量、または一定流量で流れていることを検知で
きる圧力スイッチの積算稼動時間から、第1浄水槽及び
第2浄水槽における濾過材の寿命を把握することができ
る。検知手段の流量センサー、または圧力スイッチから
の信号は、制御及び表示部に光や音に変換して表示し濾
過材の寿命状態を知らせる。
The water purifier of the present invention is provided with the above-mentioned first water purification tank and second water purification tank, but between the first water purification tank and the second water purification tank, there is a flow sensor or a constant flow valve and a pressure switch. It is preferable to provide detection means, and by providing these means at positions where the influence of the pressure loss of the filtration media of both the first water purification tank and the second water purification tank is small, the flow rate is integrated by the flow rate sensor or at a constant flow rate. It is possible to grasp the life of the filter medium in the first water purification tank and the second water purification tank from the cumulative operating time of the pressure switch that can detect that the water is being discharged. The signal from the flow sensor of the detection means or the pressure switch is converted into light or sound and displayed on the control and display unit to indicate the life state of the filter medium.

【0020】[0020]

【作用】本発明の浄水器における第1浄水槽の濾過材を
陽イオン交換樹脂と活性炭との混合物としたことによ
り、陽イオン交換樹脂と活性炭とがそれぞれ阻害される
ことなく機能を発揮し、塩素、トリハロメタン、溶解イ
オン性有害物質、農薬等の除去を行い、かつ着色、臭気
等のない濾過水とし、さらに第2浄水槽の濾過材の中空
糸膜により細菌、微細有害物質の除去を行い、安全でお
いしい水を得る。
[Function] By using the mixture of the cation exchange resin and the activated carbon as the filter material of the first water purification tank in the water purifier of the present invention, the cation exchange resin and the activated carbon exert their functions without being hindered, Chlorine, trihalomethane, dissolved ionic toxic substances, pesticides, etc. are removed, and filtered water with no coloring or odor is removed, and bacteria and fine toxic substances are removed by the hollow fiber membrane of the filter material of the second water purification tank. Get safe, delicious water.

【0021】[0021]

【実施例】以下、本発明を図面に示した実施例により具
体的に説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to the embodiments shown in the drawings.

【0022】(実施例1)図1は本発明の浄水器の例の
断面図である。
(Embodiment 1) FIG. 1 is a sectional view of an example of a water purifier according to the present invention.

【0023】浄水器は、その本体容器1内に第1浄水槽
2及び第2浄水槽7が配置され、第1浄水槽2及び第2
浄水槽7の間に流量センサー9及び制御及び表示部10
が設けられ、それぞれ配水管にて連通している。第1浄
水槽2の底部には原水の水道水の流入口6を備え、第1
浄水槽2の上部から流出の濾過水は、流量センサー9を
経由し、第2浄水槽7の底部から流入して第2浄水槽7
の上部から流出し、吐出水流出口11より浄水として吐
出する。流量センサー9による信号の制御及び表示部1
0は本体容器1の外方より見えるように設けてある。
In the water purifier, the first water purification tank 2 and the second water purification tank 7 are arranged in the main body container 1, and the first water purification tank 2 and the second water purification tank 2 are arranged.
A flow rate sensor 9 and a control and display unit 10 between the water purification tanks 7.
Are provided and communicate with each other through water pipes. At the bottom of the first water purification tank 2, a tap water inlet 6 for raw water is provided.
The filtered water flowing out from the upper part of the water purification tank 2 passes through the flow rate sensor 9 and flows in from the bottom part of the second water purification tank 7 into the second water purification tank 7
Out of the upper part of the water and is discharged from the discharge water outlet 11 as purified water. Signal control and display unit 1 by the flow sensor 9
0 is provided so that it can be seen from the outside of the main body container 1.

【0024】第1浄水槽2の濾過材のカルシウム塩型陽
イオン交換樹脂としては、アンバーライトIR−120
B(オルガノ社製陽イオン交換樹脂)を下記の方法でカ
ルシウム塩型としたものを用いた。
As the calcium salt type cation exchange resin for the filter material of the first water purification tank 2, Amberlite IR-120 is used.
B (a cation exchange resin manufactured by Organo Corporation) in the form of calcium salt was used by the following method.

【0025】アンバーライトIR−120Bを1リット
ルガラス漏斗に入れ4N塩酸水溶液1.5リットル(イ
オン交換樹脂の交換容量の約3倍当量、以下括弧内の当
量数は対イオン交換樹脂の交換容量)を200ミリリッ
トル/分の通水速度で通水した。その後イオン交換水1
0リットルを200ミリリットル/分の通水速度で通水
して洗浄した後、3N水酸化ナトリウム水溶液2リット
ル(約3倍当量)を200ミリリットル/分の通水速度
で通水し、イオン交換樹脂のイオン型をナトリウム塩型
とした。
Amberlite IR-120B was placed in a 1-liter glass funnel and 1.5 liters of 4N hydrochloric acid aqueous solution (about 3 times equivalent amount of ion-exchange resin exchange capacity, the number of equivalents in parentheses below is the exchange capacity of counter-ion exchange resin). Was passed at a water flow rate of 200 ml / min. Then deionized water 1
After washing 0 liter of water with a water flow rate of 200 ml / min and washing, 2 liter of a 3N sodium hydroxide aqueous solution (about 3 times equivalent) was passed at a water flow rate of 200 ml / min to obtain an ion exchange resin. The ionic form of was changed to the sodium salt form.

【0026】さらに、イオン交換水10リットルを20
0ミリリットル/分の通水速度で通水して洗浄した後、
4N塩酸水溶液1.5リットル(約3倍当量)を通水
後、イオン交換水10リットルを通水して洗浄した。そ
の後3モル/リットルの塩化カルシウム水溶液1リット
ル(約3倍当量)を100ミリリットル/分の通水速度
で通水し、イオン交換水10リットルを200ミリリッ
トル/分の通水速度で通水して洗浄した。得られたイオ
ン交換樹脂は、そのイオン型が、塩化カルシウム水溶液
及びイオン交換水の通水液のキレート滴定法によるカル
シウムイオン濃度の測定より、1.92当量/リットル
のカルシウム塩型に変換されていた。
Further, 10 liters of ion-exchanged water is added to 20
After washing by passing water at a water flow rate of 0 ml / min,
After passing 4 liters of a 4N hydrochloric acid aqueous solution (about 3 times equivalent), 10 liters of ion-exchanged water was passed for washing. Then, 1 liter of a 3 mol / liter calcium chloride aqueous solution (about 3 times equivalent) was passed at a water flow rate of 100 ml / min, and 10 liters of ion-exchanged water was passed at a water flow rate of 200 ml / min. Washed. The ion type of the obtained ion exchange resin was converted to a calcium salt type of 1.92 equivalents / liter by the measurement of the calcium ion concentration by the chelate titration method of the aqueous solution of calcium chloride and the flowing solution of the ion exchanged water. It was

【0027】また、第1浄水槽2の濾過材の活性炭とし
ては、クラレコールT−SB48/100(クラレケミ
カル社製活性炭)を用いた。
As the activated carbon of the filter material of the first water purification tank 2, Kuraray Coal T-SB48 / 100 (activated carbon manufactured by Kuraray Chemical Co., Ltd.) was used.

【0028】第1浄水槽2には、その下方に150メッ
シュのナイロンメッシュを樹脂枠に貼付した支持体3を
設けて前記カルシウム塩型陽イオン交換樹脂300ミリ
リットルと活性炭450gの混合物からなる濾過材5を
充填して、濾過材5が流出しないよう上方に支持体3と
同様の構造の支持体4を設けた。
The first water purification tank 2 is provided with a support 3 below which a nylon mesh of 150 mesh is attached to a resin frame, and a filtration material comprising a mixture of 300 ml of the calcium salt type cation exchange resin and 450 g of activated carbon. 5, a support 4 having the same structure as the support 3 was provided above so that the filtering material 5 would not flow out.

【0029】第2浄水槽7の濾過材の中空糸膜8として
は、親水化ポリエチレン製多孔質中空糸膜を用い、2液
型ポリウレタン樹脂で中空糸膜の端部を開放状態にして
固定して第2浄水槽7に収納した。
As the hollow fiber membrane 8 of the filter material of the second water purification tank 7, a porous hollow fiber membrane made of hydrophilic polyethylene is used, and the end of the hollow fiber membrane is fixed with a two-component polyurethane resin in an open state. And stored in the second water purification tank 7.

【0030】第1浄水槽2と第2浄水槽7とをつなぐ配
水管の途中に羽根車式の流量センサー9を設け、流量セ
ンサー9の出力信号により制御及び表示部10の制御部
で流量を積算して濾過材の寿命表示をするようにした。
An impeller type flow rate sensor 9 is provided in the middle of the water pipe connecting the first water purification tank 2 and the second water purification tank 7, and the flow rate is controlled by the output signal of the flow rate sensor 9 and the control unit of the display unit 10 controls the flow rate. The life of the filter material is indicated by adding up.

【0031】かかる構成として作製した浄水器に通水速
度4リットル/分で通水試験をし、下記の測定を行っ
た。
The water purifier thus constructed was subjected to a water flow test at a water flow rate of 4 liters / minute, and the following measurements were carried out.

【0032】(1)残留塩素除去能力 2.0±0.2ppmの塩素を含有する水を8000リ
ットル通水したときの吐出水の残留塩素濃度をo−トリ
ジン法により測定した。
(1) Residual Chlorine Removal Ability The residual chlorine concentration of discharge water when 8000 liters of water containing 2.0 ± 0.2 ppm of chlorine was passed was measured by the o-tolidine method.

【0033】(2)除菌能力 Pseudomonas diminuta IFO1
4213 1.7×107ケ/ミリリットルを含む水を
6リットル通水したときの吐出水の菌数を 測定し
た。
(2) Sterilizing ability Pseudomonas diminuta IFO1
The number of bacteria in the discharged water was measured when 6 liters of water containing 4213 1.7 × 10 7 cells / ml was passed.

【0034】(3)鉛除去能力 鉛濃度として150ppbの塩化鉛水溶液を8000リ
ットル通水したときの吐出水の鉛濃度を測定した。
(3) Lead removal capacity The lead concentration in discharge water was measured when 8000 liters of a lead chloride aqueous solution of 150 ppb was passed.

【0035】(4)トリハロメタン除去能力 クロロホルムを60ppbに調製した水溶液を8000
リットル通水したときの吐出水のクロロホルム濃度を測
定した。
(4) Removal capacity of trihalomethane: An aqueous solution prepared by adjusting chloroform to 60 ppb is used as 8000.
The chloroform concentration of the discharged water when liter was passed was measured.

【0036】(5)濾過材寿命表示 流量センサーの信号は、積算流量が8000リットルの
時点を濾過材の寿命と設定して表示したが、寿命時の積
算流量を市販の積算流量計で実測した。
(5) Filtration Material Life Display The signal of the flow rate sensor was displayed by setting the life of the filtration material at the time when the cumulative flow rate was 8000 liters, and the cumulative flow rate at the end of life was measured by a commercially available cumulative flow meter. .

【0037】浄水器の通水試験の結果を表1に示した
が、本実施例の浄水器は、残留塩素、細菌、鉛及びトリ
ハロメタンのいずれに対しても高い除去能力を示した。
また、濾過材寿命表示における結果から判るように、流
量センサーにより測定した流量と市販の積算流量計によ
り実測した流量は、ほぼ同じで、流量センサーによって
も正確な測定が可能であった。
The results of the water flow test of the water purifier are shown in Table 1. The water purifier of this example showed a high removal ability for residual chlorine, bacteria, lead and trihalomethane.
Further, as can be seen from the results of the filter medium life display, the flow rate measured by the flow rate sensor and the flow rate actually measured by the commercially available integrating flowmeter were almost the same, and accurate measurement was possible by the flow rate sensor.

【0038】(実施例2)実施例1の浄水器における第
1浄水槽2の濾過材5の活性炭を、クラレコールT−S
B48/100(クラレケミカル社製活性炭)と低賦活
炭を1:1の重量比で混合したものに代えた以外は、実
施例1と同様にして作製した浄水器に実施例1と同様の
通水試験をし、その結果を表1に示した。
(Embodiment 2) The activated carbon of the filter medium 5 of the first water purification tank 2 in the water purifier of Embodiment 1 was replaced with Kuraray Coal TS.
A water purifier prepared in the same manner as in Example 1 was used, except that B48 / 100 (activated carbon manufactured by Kuraray Chemical Co., Ltd.) and low-activated carbon were mixed in a weight ratio of 1: 1. A water test was conducted and the results are shown in Table 1.

【0039】本実施例の浄水器は、残留塩素及び細菌の
いずれに対しても高い除去能力を示し、鉛の除去能力は
僅かに低下するが、トリハロメタンに対し高い除去能力
を示した。
The water purifier of this example showed a high removal ability for both residual chlorine and bacteria, and a slight reduction in lead removal ability, but a high removal ability for trihalomethanes.

【0040】[0040]

【表1】 [Table 1]

【0041】(実施例3)実施例1の浄水器における第
1浄水槽2の濾過材5の混合物に石灰石200gを追加
した以外は、実施例1と同様にして作製した浄水器に名
古屋市水道水を用いて実施例1と同様の通水試験をし、
その結果を表2に示した。
(Example 3) A water purifier manufactured in the same manner as in Example 1 except that 200 g of limestone was added to the mixture of the filter media 5 in the first water purification tank 2 in the water purifier of Example 1 was used by Nagoya City Waterworks. The same water flow test as in Example 1 was performed using water,
The results are shown in Table 2.

【0042】本実施例の浄水器は、残留塩素、細菌、鉛
及びトリハロメタンのいずれに対しても高い除去能力を
示した。また、滴定法により測定したカルシウムイオン
濃度は原水の水道水では6.7mg/リットルであった
が、吐出水では増加したカルシウムイオン濃度を示し
た。
The water purifier of this example showed a high removal ability for residual chlorine, bacteria, lead and trihalomethane. The calcium ion concentration measured by the titration method was 6.7 mg / liter in the tap water of the raw water, but the calcium ion concentration increased in the discharged water.

【0043】[0043]

【表2】 [Table 2]

【0044】[0044]

【発明の効果】本発明の浄水器は、陽イオン交換樹脂と
活性炭との混合物からなる濾過材と中空糸膜からなる濾
過材とを組み合わせたことにより、水道水に含まれる塩
素、トリハロメタン、農薬、溶解イオン性有害物質、細
菌等を効果的に除去することができ、また、炭酸カルシ
ウム及び/または溶性ケイ酸を主成分とする天然石の添
加によりカルシウムイオンを増加させることができ、安
全でおいしい水を得ることを可能とする。さらに、濾過
材の寿命を検知しうるようにすることにより、より安全
性を高めると共に除去能力を効率よく発揮させることが
可能である。
EFFECTS OF THE INVENTION The water purifier of the present invention is a combination of a filter material composed of a mixture of a cation exchange resin and activated carbon and a filter material composed of a hollow fiber membrane. , It is possible to effectively remove dissolved ionic harmful substances, bacteria, etc. Also, it is possible to increase calcium ions by adding natural stones containing calcium carbonate and / or soluble silicic acid as a main component, which is safe and delicious. Allows you to get water. Further, by making it possible to detect the life of the filter medium, it is possible to further enhance safety and efficiently exhibit the removal ability.

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

【図1】本発明の浄水器の例の断面図である。FIG. 1 is a cross-sectional view of an example of a water purifier of the present invention.

【符号の説明】[Explanation of symbols]

1 本体容器 2 第1浄水槽 3 支持体 4 支持体 5 濾過材 6 原水流入口 7 第2浄水槽 8 中空糸膜 9 流量センサー 10 制御及び表示部 11 吐出水流出口 1 Main Container 2 First Water Purification Tank 3 Support 4 Support 5 Filter Material 6 Raw Water Inlet 7 Second Water Purification Tank 8 Hollow Fiber Membrane 9 Flow Sensor 10 Control and Display 11 Discharge Water Outlet

───────────────────────────────────────────────────── 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 1/68 520 C02F 1/68 520K 530 530B 540 540A 540C 540D (72)発明者 種池 昌彦 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─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Internal reference number FI Technical indication C02F 1/68 520 C02F 1/68 520K 530 530B 540 540A 540C 540D (72) Inventor Masahiko Taneike Tokyo 2-3-19 Kyobashi, Chuo-ku Mitsubishi Rayon Co., Ltd.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 活性炭、陽イオン交換樹脂及び中空糸膜
を濾過材とする浄水器において、陽イオン交換樹脂と活
性炭との混合物を濾過材とする第1浄水槽及びその下流
に配置された中空糸膜を濾過材とする第2浄水槽を備え
たことを特徴とする浄水器。
1. A water purifier using activated carbon, a cation exchange resin and a hollow fiber membrane as a filter medium, wherein a first water tank using a mixture of a cation exchange resin and activated carbon as a filter medium and a hollow arranged downstream thereof. A water purifier characterized by comprising a second water purification tank using a fiber membrane as a filtering material.
【請求項2】 陽イオン交換樹脂がカルシウム塩型であ
る請求項1記載の浄水器。
2. The water purifier according to claim 1, wherein the cation exchange resin is a calcium salt type.
【請求項3】 活性炭が2種以上の活性炭の混合物であ
る請求項1記載の浄水器。
3. The water purifier according to claim 1, wherein the activated carbon is a mixture of two or more types of activated carbon.
【請求項4】 陽イオン交換樹脂と活性炭との混合物が
下式を満足する混合比率C/Rの混合物である請求項1
記載の浄水器。 1≦C/R≦8 但し、Cは活性炭重量(g)、Rは陽イオン交換樹脂容
積(ml)を示す。
4. A mixture of a cation exchange resin and activated carbon is a mixture having a mixing ratio C / R satisfying the following formula.
Water purifier as described. 1 ≦ C / R ≦ 8 where C is the activated carbon weight (g) and R is the cation exchange resin volume (ml).
【請求項5】 第1浄水槽及び/または第2浄水槽に炭
酸カルシウム及び/または溶性ケイ酸を主成分とする天
然石を充填した請求項1記載の浄水器。
5. The water purifier according to claim 1, wherein the first water purification tank and / or the second water purification tank is filled with natural stone containing calcium carbonate and / or soluble silicic acid as a main component.
【請求項6】 第1浄水槽と第2浄水槽との間に、流量
センサー、または定流量弁と圧力スイッチを設けた請求
項1記載の浄水器。
6. The water purifier according to claim 1, wherein a flow sensor, or a constant flow valve and a pressure switch are provided between the first water purification tank and the second water purification tank.
JP20187695A 1995-07-17 1995-07-17 Water purifier Pending JPH0929237A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20187695A JPH0929237A (en) 1995-07-17 1995-07-17 Water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20187695A JPH0929237A (en) 1995-07-17 1995-07-17 Water purifier

Publications (1)

Publication Number Publication Date
JPH0929237A true JPH0929237A (en) 1997-02-04

Family

ID=16448340

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20187695A Pending JPH0929237A (en) 1995-07-17 1995-07-17 Water purifier

Country Status (1)

Country Link
JP (1) JPH0929237A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003006381A1 (en) * 2001-07-12 2003-01-23 Dynaflo Co., Ltd. Water purifier

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003006381A1 (en) * 2001-07-12 2003-01-23 Dynaflo Co., Ltd. Water purifier
US6909101B2 (en) 2001-07-12 2005-06-21 Yoichi Nishioka Water purifying apparatus

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