JP3112927B2 - Water purifier - Google Patents

Water purifier

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Publication number
JP3112927B2
JP3112927B2 JP02308549A JP30854990A JP3112927B2 JP 3112927 B2 JP3112927 B2 JP 3112927B2 JP 02308549 A JP02308549 A JP 02308549A JP 30854990 A JP30854990 A JP 30854990A JP 3112927 B2 JP3112927 B2 JP 3112927B2
Authority
JP
Japan
Prior art keywords
water
hollow fiber
cylindrical case
fiber membrane
raw water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP02308549A
Other languages
Japanese (ja)
Other versions
JPH04180887A (en
Inventor
修身 加藤
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
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Filing date
Publication date
Application filed by Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP02308549A priority Critical patent/JP3112927B2/en
Publication of JPH04180887A publication Critical patent/JPH04180887A/en
Application granted granted Critical
Publication of JP3112927B2 publication Critical patent/JP3112927B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、中空糸膜群ならびに活性炭層、および原水
フィルターよりなる浄水器に関する。
Description: TECHNICAL FIELD The present invention relates to a water purifier comprising a group of hollow fiber membranes, an activated carbon layer, and a raw water filter.

[従来の技術] 近年、中空糸膜群と活性炭層を基本構成とする浄水器
が、水道水中の残留塩素による不快な臭いや味を除去し
たり、原水中に浮沈するコロイド状の鉄粉および微細な
ゴミならびに細菌などの異物類を除去するために用いら
れ、その利用範囲は飛躍的に拡大している。
[Prior art] In recent years, a water purifier having a hollow fiber membrane group and an activated carbon layer as a basic configuration has been used to remove unpleasant odors and tastes due to residual chlorine in tap water, and colloidal iron powder floating and sinking in raw water. It is used to remove fine foreign matter and foreign substances such as bacteria, and the range of use has been dramatically expanded.

これら従来の浄水器は、殆んどが被処理水を中空糸膜
の外表面から、膜壁を貫通して中空糸膜内面に通過させ
て、中空糸膜の微細な多孔壁によって上記種々の異物類
を除去するよう構成されている。従って、通水すること
により中空糸膜外表面に上記の異物類が堆積するが、膜
面の大部分が被覆された状態に達すると殆んど濾過能力
を失い、浄水器の寿命は終りに到ってしまう。
In these conventional water purifiers, most of the water to be treated passes from the outer surface of the hollow fiber membrane to the inner surface of the hollow fiber membrane through the membrane wall, and the above-mentioned various types of water are formed by the fine porous wall of the hollow fiber membrane. It is configured to remove foreign matter. Therefore, the above foreign substances accumulate on the outer surface of the hollow fiber membrane by passing water, but when the membrane reaches a state where most of the membrane surface is covered, the filtration ability is almost lost, and the life of the water purifier ends. It will arrive.

このため、浄水処理時のみ効果的に機能し、かつ寿命
の長い浄水器の出現が望まれていたが、この種のものは
従来見られなかった。
For this reason, the appearance of a water purifier that functions effectively only at the time of water purification treatment and has a long service life has been desired, but such a water purifier has not been found before.

[発明が解決しようとする課題] 本発明の浄水器は、このような従来の浄水器の欠点を
改良して、従来品の上記通水方向とは逆向きに、中空糸
膜の内側から外側に向けて通水し、浄水処理時以外は原
水中の異物類が付着堆積しないよう、中空糸膜内表面を
いわゆる一次濾過水により絶えず洗浄できるよう構成せ
しめたものである。
[Problem to be Solved by the Invention] The water purifier of the present invention improves the above-mentioned drawbacks of the conventional water purifier, and reverses the water flow direction of the conventional product from the inside to the outside of the hollow fiber membrane. , And the inner surface of the hollow fiber membrane can be constantly washed with so-called primary filtered water so that foreign substances in the raw water do not adhere and accumulate except during the water purification treatment.

本発明は、中空糸膜の堆積物による被覆が可及的に減
殺されて、累計濾過能力が飛躍的に増強された、寿命の
長い浄水器の提供を目的とするものである。
An object of the present invention is to provide a long-life water purifier in which the coating of the hollow fiber membranes with the deposits is reduced as much as possible, and the cumulative filtration capacity is remarkably enhanced.

[課題を解決するための手段] 本発明は、外周部に二次濾過水通過孔10を有し、両端
部が開口された筒状ケース1、該筒状ケース内に直線状
に集束して収納されかつ両端が開口された中空糸膜群
6、該中空糸膜群の端部と筒状ケースの開口端部を液密
に固定する樹脂固定層9および9′、該筒状ケース外周
面に接しかつ活性炭層7および1個以上の浄化水流出孔
8を有する外筒ケース2よりなり、該筒状ケースの両端
面外側部に原水フィルター5を具備する原水流入キャッ
プ4および一次濾過水流出キャップ12を有し、さらに前
記原水フィルター5が、筒状ケース1の原水流入側の樹
脂固定層9の上面の全面に配設され、且つ少なくとも中
空糸膜内径以下の細孔を有することを特徴とする浄水器
である。
Means for Solving the Problems According to the present invention, a cylindrical case 1 having a secondary filtered water passage hole 10 in an outer peripheral portion and having both ends opened is provided. Hollow fiber membrane group 6 housed and open at both ends, resin fixing layers 9 and 9 'for liquid-tightly fixing the end of the hollow fiber membrane group and the open end of the cylindrical case, outer peripheral surface of the cylindrical case And an outer cylinder case 2 having an activated carbon layer 7 and one or more purified water outflow holes 8, a raw water inflow cap 4 having a raw water filter 5 on both ends of the cylindrical case, and a primary filtered water outflow. It has a cap 12, and the raw water filter 5 is disposed on the entire upper surface of the resin fixing layer 9 on the raw water inflow side of the cylindrical case 1 and has pores at least smaller than the inner diameter of the hollow fiber membrane. It is a water purifier.

本発明で用いられる中空糸膜の素材としては、ポリオ
レフィン系、セルロース系、ポリスルホン系、ポリビニ
ルアルコール系、ポリアクリロニトリル系を始めとして
多孔質の公知の中空糸膜を挙げることが出来る。
Examples of the material of the hollow fiber membrane used in the present invention include known porous hollow fiber membranes such as polyolefin, cellulose, polysulfone, polyvinyl alcohol, and polyacrylonitrile.

また本発明で用いられる活性炭層の素材としては、粒
状活性炭或いは粒状活性炭を微量の粘結剤で固めた成型
活性炭、および活性炭素繊維もしくはそれを微量の粘結
剤で固めた活性炭素繊維成型体などを挙げることが出来
る。
Examples of the material of the activated carbon layer used in the present invention include granular activated carbon or molded activated carbon obtained by solidifying granular activated carbon with a small amount of a binder, and activated carbon fiber or an activated carbon fiber molded product obtained by solidifying the same with a small amount of a binder. And the like.

また筒状ケース1の原水流入側樹脂固定層上面に配設
される原水フィルターとしては、金属または繊維の編織
物で細孔を有するメッシュフィルター、或いはそれらか
らなる不織布様物で実質的に細孔を有するメッシュフィ
ルター、或いはそれらからなる焼結体ならびにセラミッ
クフィルターなどを挙げることが出来る。
The raw water filter disposed on the upper surface of the resin fixing layer on the raw water inflow side of the cylindrical case 1 may be a mesh filter having fine pores made of a knitted or woven fabric of metal or fiber, or a substantially non-woven fabric made of the same. Or a sintered body or a ceramic filter made of them.

[作用] 図面により本発明をさらに詳細に説明する。第1図は
本発明の浄水器の断面を模式的に示すものである。
[Operation] The present invention will be described in more detail with reference to the drawings. FIG. 1 schematically shows a cross section of the water purifier of the present invention.

水道水などの原水は、原水流入口3から流入し、原水
流入キャップ4を経て原水フィルター5を通過し、ここ
で第1段の処理が行なわれ一次濾過水が得られる。
Raw water such as tap water flows in from a raw water inlet 3 and passes through a raw water inflow cap 4 and passes through a raw water filter 5, where the first-stage treatment is performed to obtain primary filtered water.

原水フィルター5の細孔の大きさは、後述する中空糸
膜6の内径以下のものであれば良いが、さらに原水が必
らずフィルター5を通過するように、このフィルター5
の外周面が筒状ケース1上端部の外周面に密接して固着
されているか、或いは原水流入キャップ4の内周面に固
着されていれば良い。
The size of the pores of the raw water filter 5 may be smaller than the inner diameter of the hollow fiber membrane 6, which will be described later.
May be fixed to the outer peripheral surface of the upper end of the cylindrical case 1 closely or to the inner peripheral surface of the raw water inflow cap 4.

原水フィルター5を通過した一次濾過水は、次いで筒
状ケース1上端部の該フィルター5の下部に形成されて
いる樹脂固定層9の表面に開口断面を有する中空糸膜群
6の、各中空糸膜の内側中空部を通過して筒状ケース1
下端部の樹脂固定層9′の開口断面および一次濾過水流
出キャップ12を経て、一次濾過水流出口13より流出す
る。
The primary filtered water that has passed through the raw water filter 5 is then removed from each hollow fiber of the hollow fiber membrane group 6 having an opening cross section on the surface of the resin fixing layer 9 formed below the filter 5 at the upper end of the cylindrical case 1. The cylindrical case 1 passing through the inner hollow portion of the membrane
It flows out from the primary filtered water outlet 13 through the opening cross section of the resin fixing layer 9 'at the lower end and the primary filtered water outflow cap 12.

従って、第1段の処理のみが行なわれた一次濾過水
が、中空糸膜群6や活性炭層7による第2段の処理を受
けることなく直接流出する。
Therefore, the primary filtered water subjected to only the first-stage treatment directly flows out without undergoing the second-stage treatment by the hollow fiber membrane group 6 or the activated carbon layer 7.

本来の浄水器として機能させ、いわゆる浄化水を得る
場合には、一次濾過水流出キャップ12に内蔵されるか、
または該キャップ12以降に接続する開閉弁(図示せず)
を閉じ、上記一次濾過水を上記中空糸膜群6ならびに活
性炭層7を通過させて、第2段の処理を行わせることに
よって得られる。
In order to function as the original water purifier and obtain so-called purified water, it is built in the primary filtered water outflow cap 12,
Or an on-off valve connected to the cap 12 and beyond (not shown)
Is closed, and the primary filtered water is passed through the hollow fiber membrane group 6 and the activated carbon layer 7 to perform the second-stage treatment.

この場合、原水フィルター5を経た一次濾過水が、中
空糸膜6の内側から外側に向って膜壁を貫通して通過し
濾過されて二次濾過水となる。
In this case, the primary filtered water that has passed through the raw water filter 5 passes through the membrane wall from the inside to the outside of the hollow fiber membrane 6 and is filtered to become secondary filtered water.

各中空糸の膜壁には、微細な多孔が形成されており、
これによって、第2段の処理が行なわれる。上記の原水
フィルター5では除去されない、より微細で水中に浮沈
するコロイド状の鉄粉やゴミおよび細菌などが除去さ
れ、ここで二次濾過水が得られることとなる。
Fine porosity is formed on the membrane wall of each hollow fiber,
As a result, the second stage processing is performed. The finer colloidal iron powder, dust, bacteria, and the like that are not removed by the raw water filter 5 and floated and sink in the water are removed, and secondary filtered water is obtained here.

各中空糸膜の内側から外側に膜壁を貫通して流出した
第2段の処理水は、筒状ケース1の外周部に設けられた
二次濾過水通過孔群10を経て、該筒状ケース1の外表面
に密着しかつ外筒ケース2の内面に固着されている活性
炭層7を通過する。
The second-stage treated water flowing out from the inside to the outside of each hollow fiber membrane through the membrane wall passes through a group of secondary filtered water passage holes 10 provided in the outer peripheral portion of the cylindrical case 1, It passes through the activated carbon layer 7 which is in close contact with the outer surface of the case 1 and is fixed to the inner surface of the outer case 2.

この活性炭層7を通過させることにより、第3段の処
理を行ない、二次濾過水中の残留塩素による不快な臭い
や味を除去することが出来る。
By passing through the activated carbon layer 7, the third-stage treatment can be performed to remove unpleasant odors and tastes due to residual chlorine in the secondary filtered water.

活性炭層7は、二次濾過水が必ず活性炭層7を通過す
るように筒状ケース1に密着して固着されることが好ま
しい。
It is preferable that the activated carbon layer 7 is tightly fixed to the cylindrical case 1 so that the secondary filtered water always passes through the activated carbon layer 7.

活性炭層7を通過した第3段の処理水は、浄化水とな
って外筒ケース2の内面と活性炭層7外表面との空間に
形成される空隙部11に集められ、外筒ケース2に設けら
れている浄化水流出孔8から流出する。
The third-stage treated water that has passed through the activated carbon layer 7 becomes purified water, and is collected in a gap 11 formed in the space between the inner surface of the outer cylinder case 2 and the outer surface of the activated carbon layer 7, and is collected by the outer cylinder case 2. It flows out from the provided purified water outflow hole 8.

上記浄化水流出孔8の個数は1ケでも良く、またそれ
以上あっても良い。
The number of the purified water outflow holes 8 may be one or more.

活性炭層7では当然ながら圧力損失を生ずるが、時に
はこの圧力損失が不均一となり、浄化水流出孔8の位置
によっては、圧力損失の少ない流出孔8付近の活性炭層
7からの第3段処理水の流出が多くなる現象が起る。
Although the pressure loss naturally occurs in the activated carbon layer 7, the pressure loss sometimes becomes non-uniform, and depending on the position of the purified water outflow hole 8, the third-stage treated water from the activated carbon layer 7 near the outflow hole 8 having a small pressure loss The phenomenon that the outflow of water increases.

このため活性炭層7での圧力損失を全周に亘って均一
化することが好ましい。例えば、筒状ケース1の二次濾
過水通過孔群10の孔径を浄化水流出孔8付近で上記圧力
損失が均一化するよう漸次変化させるか、または空隙部
11の形状を変化させて流出孔8の位置に関係なく圧力損
失が均一化するような構造とすることも好ましいことで
ある。
For this reason, it is preferable to make the pressure loss in the activated carbon layer 7 uniform over the entire circumference. For example, the hole diameter of the secondary filtered water passage hole group 10 of the cylindrical case 1 is gradually changed so as to make the pressure loss uniform near the purified water outflow hole 8, or the gap portion is formed.
It is also preferable that the shape of 11 is changed so that the pressure loss becomes uniform regardless of the position of the outflow hole 8.

従って単に一次濾過水のみを得る場合は、開閉弁の切
り替え操作、即ち浄化水流出孔8に内蔵または流出孔8
以降に接続している開閉弁を閉じ、一次濾過水流出キャ
ップ12に内蔵または接続されている開閉弁を開くことに
より容易に得ることが出来る。
Therefore, when simply obtaining the primary filtered water, the switching operation of the on-off valve, that is, the built-in or outlet hole 8
This can be easily obtained by closing the on-off valve connected thereafter and opening the on-off valve built in or connected to the primary filtered water outflow cap 12.

また浄化水を得る場合には、これと逆向の弁の開閉操
作を行なえば良い。この弁の開閉を同時に行なうために
三方弁などを使用すれば、容易に達成することが出来
る。
When obtaining purified water, the valve may be opened and closed in the opposite direction. This can be easily achieved by using a three-way valve or the like to simultaneously open and close the valve.

中空糸膜の内表面積には、浄水器としての形態上の制
約から限度があり、この限られた内表面に堆積する種々
の異物類を絶えず洗滌して除去すると、通水抵抗の増大
を防止することが出来る。
The inner surface area of the hollow fiber membrane is limited due to the restrictions on the form as a water purifier, and by continuously washing and removing various foreign matters deposited on the limited inner surface, an increase in water flow resistance is prevented. You can do it.

通常の浄化水と、食器洗浄および野菜ならびに魚類な
どの洗浄その他に用いられる一次濾過水との使用量を比
較すると、圧倒的に後者が大きい。
Comparing the amounts of normal purified water and primary filtered water used for washing dishes, washing vegetables and fish, and the like, the latter is overwhelmingly large.

従って、この一次濾過水に依って、中空糸膜の内表面
に絶えず洗浄し堆積物を除去することに依り、長期に亘
って所望の浄化水を確保することが可能となる。
Therefore, it is possible to secure desired purified water for a long period of time by constantly washing the inner surface of the hollow fiber membrane to remove the deposits by using the primary filtered water.

[実施例] 以下に、第1図に示す構造を有する本発明の浄化器に
依る実施例を示すが、本発明がこれらのみに限定される
ものではない。
[Example] Hereinafter, an example using the purifier of the present invention having the structure shown in Fig. 1 will be described, but the present invention is not limited to these.

実施例1および比較例1 中空糸膜群として、内径270μm、膜厚55μmのポリ
エチレン中空糸膜(三菱レイヨン(株)製EHF−270T)
を用い、該中空糸膜の7776本を集束し、有効中空糸長さ
が123mmとなるように両端を樹脂で固定したものの外周
部に、活性炭素繊維(大阪ガス(株)製A−15)を外径
81mm、内径57mm、長さ123mmに成型した活性炭層を設け
た浄水器を作製し、同一の浄水器を用いて、各々通水方
向の異なる同一の試験条件で通水試験を行った。
Example 1 and Comparative Example 1 As the hollow fiber membrane group, a polyethylene hollow fiber membrane having an inner diameter of 270 μm and a thickness of 55 μm (EHF-270T manufactured by Mitsubishi Rayon Co., Ltd.)
The hollow fiber membrane was bundled with 7,776 fibers, and both ends were fixed with resin so that the effective hollow fiber length was 123 mm. The outer periphery of the hollow fiber membrane was activated carbon fiber (A-15 manufactured by Osaka Gas Co., Ltd.). The outer diameter
A water purifier provided with an activated carbon layer molded to 81 mm, an inner diameter of 57 mm and a length of 123 mm was prepared, and a water flow test was performed using the same water purifier under the same test conditions in different water flow directions.

即ち、一方を本発明と同様に、中空糸膜内面−同外面
−活性炭層の順に通水し、このケースを実施例1とし
た。
That is, water was passed through one side in the order of the inner surface of the hollow fiber membrane, the same outer surface, and the activated carbon layer in the same manner as in the present invention.

また、他方を従来品と同様(本発明とは逆向き)に、
活性炭層−中空糸膜外面−同内面の順に通水し、このケ
ースを比較例1とした。
Also, the other is the same as the conventional product (opposite to the present invention),
Water was passed through the activated carbon layer, the outer surface of the hollow fiber membrane, and the inner surface in this order.

以上の結果を表1に示す。 Table 1 shows the above results.

尚、通水試験は下記の条件に依った。 The water flow test was performed under the following conditions.

原水:名古屋市水 水温:6〜17℃ 通水流速:4/min. 通水量:200/day 中空糸膜内面洗浄水流量:750/day (一次濾過水、実施例1のみ使用) 以上の結果は、本発明の浄水器が、比較例の従来型浄
水器に較べて、多量の通水後に於いても、明らかに高い
流速、流量を示している。
Raw water: Nagoya city Water temperature: 6-17 ° C Flow rate: 4 / min. Flow rate: 200 / day Flow rate of cleaning water inside the hollow fiber membrane: 750 / day (primary filtered water, only used in Example 1) Shows that the water purifier of the present invention has a clearly higher flow rate and flow rate even after passing a large amount of water than the conventional water purifier of the comparative example.

[発明の効果] 本発明の浄水器においては、浄化水を必要としない場
合に開閉弁を切換操作することによって、単に一次濾過
水を得るための第1段の処理のみを行うことができ、こ
の際に中空糸膜内面を素通りする一次濾過水により、膜
内面が洗浄されるので、浄水処理使用時に中空糸膜内表
面に堆積する種々の異物類の多くは、膜表面に殆ど残留
せず、さらには圧力損失の増大が大幅に緩和されるの
で、長期に亘り大量の所望浄化水を確保することが出来
る。
[Effects of the Invention] In the water purifier of the present invention, when the purified water is not required, only the first-stage treatment for obtaining the primary filtered water can be performed by switching the open / close valve, At this time, since the inner surface of the membrane is washed by the primary filtered water that passes through the inner surface of the hollow fiber membrane, most of various foreign substances deposited on the inner surface of the hollow fiber membrane during the water purification treatment hardly remain on the membrane surface. Further, since the increase in pressure loss is greatly reduced, a large amount of desired purified water can be secured over a long period of time.

従って、本発明の浄水器は上記のように従来の浄水器
とは異なった機能、即ち浄化水を得る場合以外は、常に
中空糸膜表面を一次濾過水により洗浄できる構造を有す
るので、従来の浄水器よりも合理的で効率的でありまた
極めて長寿命であるので甚だ経済的である。
Therefore, the water purifier of the present invention has a function different from that of the conventional water purifier as described above, that is, a structure in which the surface of the hollow fiber membrane can always be washed with primary filtered water except when obtaining purified water. It is more economical than water purifiers because it is more reasonable and efficient, and has a very long life.

【図面の簡単な説明】 第1図は本発明の浄水器の構造を示す模式断面図であ
る。 1:筒状ケース 2:外筒ケース 3:原水流入口 4:原水流入キャップ 5:原水フィルター 6:中空糸膜群 7:活性炭層 8:浄化水流出口 9,9′:樹脂固定層 10:二次濾過水通過孔 11:空隙部 12:一次濾過水流出キャップ 13:一次濾過水流出口
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic sectional view showing the structure of the water purifier of the present invention. 1: Cylindrical case 2: Outer case 3: Raw water inlet 4: Raw water inflow cap 5: Raw water filter 6: Hollow fiber membrane group 7: Activated carbon layer 8: Purified water outlet 9,9 ': Resin fixed layer 10: Two Secondary filtered water passage hole 11: Void 12: Primary filtered water outlet cap 13: Primary filtered water outlet

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 1/44 B01D 63/02 B01D 65/02 B01D 65/08 C02F 1/28 Continuation of the front page (58) Field surveyed (Int. Cl. 7 , DB name) C02F 1/44 B01D 63/02 B01D 65/02 B01D 65/08 C02F 1/28

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】外周部に二次濾過水通過孔10を有し、両端
部が開口された筒状ケース1、該筒状ケース内に直線状
に集束して収納されかつ両端が開口された中空糸膜群
6、該中空糸膜群の端部と筒状ケースの開口端部を液密
に固定する樹脂固定層9および9′、該筒状ケース外周
面に接しかつ活性炭層7および1個以上の浄化水流出孔
8を有する外筒ケース2よりなり、該筒状ケースの両端
面外側部に原水フィルター5を具備する原水流入キャッ
プ4および一次濾過水流出キャップ12を有することを特
徴とする浄水器。
1. A cylindrical case 1 having a secondary filtered water passage hole 10 at its outer peripheral portion and having both ends opened. The cylindrical case 1 is linearly bundled and stored in the cylindrical case, and both ends are opened. Hollow fiber membrane group 6, resin fixing layers 9 and 9 'for fixing the ends of the hollow fiber membrane group and the open ends of the cylindrical case in a liquid-tight manner, and activated carbon layers 7 and 1 in contact with the outer peripheral surface of the cylindrical case It comprises an outer cylinder case 2 having at least two purified water outflow holes 8, and a raw water inflow cap 4 having a raw water filter 5 and a primary filtered water outflow cap 12 at the outer side of both end faces of the cylindrical case. Water purifier.
【請求項2】前記原水フィルター5が、筒状ケース1の
原水流入側樹脂固定層9の上面の全面に配設され、且つ
少なくとも中空糸膜内径以下の細孔を有することを特徴
とする浄水器。
2. The water purification apparatus according to claim 1, wherein the raw water filter is disposed on the entire upper surface of the resin fixing layer on the raw water inflow side of the cylindrical case, and has pores at least smaller than the inner diameter of the hollow fiber membrane. vessel.
JP02308549A 1990-11-16 1990-11-16 Water purifier Expired - Fee Related JP3112927B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02308549A JP3112927B2 (en) 1990-11-16 1990-11-16 Water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02308549A JP3112927B2 (en) 1990-11-16 1990-11-16 Water purifier

Publications (2)

Publication Number Publication Date
JPH04180887A JPH04180887A (en) 1992-06-29
JP3112927B2 true JP3112927B2 (en) 2000-11-27

Family

ID=17982368

Family Applications (1)

Application Number Title Priority Date Filing Date
JP02308549A Expired - Fee Related JP3112927B2 (en) 1990-11-16 1990-11-16 Water purifier

Country Status (1)

Country Link
JP (1) JP3112927B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0618476U (en) * 1992-08-08 1994-03-11 株式会社三栄水栓製作所 Water tap with water purifier
GB9222248D0 (en) * 1992-10-23 1992-12-09 Atomic Energy Authority Uk Liquid treatment apparatus
US6589426B1 (en) 1999-09-29 2003-07-08 Zenon Environmental Inc. Ultrafiltration and microfiltration module and system
JP5080781B2 (en) * 2006-11-06 2012-11-21 三菱レイヨン株式会社 Hollow fiber membrane module for degassing and degassing device
JP5805033B2 (en) * 2012-08-24 2015-11-04 トクラス株式会社 Cylindrical carbonaceous body module containing activated carbon or activated carbon raw material and method for producing the same
CN113856314B (en) * 2021-09-28 2022-08-30 重庆昕晟环保科技有限公司 From terminal water purifier of secondary water supply who takes protection

Also Published As

Publication number Publication date
JPH04180887A (en) 1992-06-29

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