JPH09187766A - Clarification apparatus for drinking water - Google Patents

Clarification apparatus for drinking water

Info

Publication number
JPH09187766A
JPH09187766A JP315596A JP315596A JPH09187766A JP H09187766 A JPH09187766 A JP H09187766A JP 315596 A JP315596 A JP 315596A JP 315596 A JP315596 A JP 315596A JP H09187766 A JPH09187766 A JP H09187766A
Authority
JP
Japan
Prior art keywords
fiber membrane
hollow fiber
raw water
membrane filter
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.)
Withdrawn
Application number
JP315596A
Other languages
Japanese (ja)
Inventor
Kimihisa Takada
公久 高田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Shibaura Machinery Corp
Original Assignee
IHI Shibaura Machinery Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by IHI Shibaura Machinery Corp filed Critical IHI Shibaura Machinery Corp
Priority to JP315596A priority Critical patent/JPH09187766A/en
Publication of JPH09187766A publication Critical patent/JPH09187766A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To rapidly supply clean water by decreasing the frequency of cleaning of a hollow fiber membrane filter and continuing supplying of clean water for a long time. SOLUTION: In a clarification apparatus for clean water wherein the clean water is formed by filtering raw water supplied by driving a pump 1 by means of a hollow fiber membrane filter 4 and a cleaning means for cleaning the hollow fiber membrane filter 4 is installed, and bleed-off circuit 20 provided with a circulation path 18 for circulating a part of the raw water sucked by means of a pump 1 from the ejection side of the pump 1 to the suction side and a flow rate control valve 19 for controlling the flow rate of the raw water flowing this circulation path 18 is installed. When filtering performance of the hollow fiber membrane filter 4 is decreased as impurities in the raw water are stuck on the surface of the hollow fiber membrane, pressure of the raw water supplied to the hollow fiber membrane filter 4 side is elevated by downing the divergence of the flow rate control valve 19 and the amt. of supplying is increased to recover the amt. of formation of clean water and to decrease the frequency of cleaning of the hollow fiber membrane filter 4.

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、飲料水用浄化装置
に関する。
TECHNICAL FIELD The present invention relates to a drinking water purifying apparatus.

【0002】[0002]

【従来の技術】近年、震災などの緊急時において、汚濁
された水(以下、原水という。)を飲料水として利用で
きるように浄化するための様々な飲料水用浄化装置が開
発されている。このような飲料水用浄化装置のなかで、
原水を濾過するフィルタ装置として、中空糸膜フィルタ
を用いたものが知られている。中空糸膜フィルタは、
0.1μm程度の微細な粒子を捕えることができ、1〜
数μmの大きさの大腸菌などの細菌を確実に除菌するこ
とができる。
2. Description of the Related Art In recent years, various drinking water purification devices have been developed for purifying polluted water (hereinafter referred to as raw water) so that it can be used as drinking water in an emergency such as an earthquake. . Among such drinking water purifiers,
A filter device using a hollow fiber membrane filter is known as a filter device for filtering raw water. The hollow fiber membrane filter is
Capable of capturing fine particles of about 0.1 μm,
It is possible to surely remove bacteria such as Escherichia coli having a size of several μm.

【0003】中空糸膜フィルタを用いた飲料水用浄化装
置では、濾過した水を逆流させたりエアバブリングを行
う洗浄手段を備えており、中空糸膜フィルタにおける各
中空糸膜の表面に原水中の夾雑物などが付着して濾過性
能が低下した場合には、洗浄手段により中空糸膜フィル
タを洗浄して濾過性能を回復させる。
A drinking water purifying apparatus using a hollow fiber membrane filter is equipped with a cleaning means for backflowing filtered water or performing air bubbling, and the surface of each hollow fiber membrane in the hollow fiber membrane filter contains raw water. When contaminants or the like are attached and the filtration performance is lowered, the hollow fiber membrane filter is washed by the washing means to restore the filtration performance.

【0004】[0004]

【発明が解決しようとする課題】しかし、中空糸膜フィ
ルタの洗浄には1回の洗浄について数分〜10分程度の
時間を要し、この洗浄時には原水の濾過が一時的に中断
され、原水を濾過することにより生成される浄水の供給
も一時的に中断される。従って、中空糸膜フィルタの洗
浄を頻繁に行う場合には、浄水の迅速な供給という要望
に充分に応えることができない。
However, it takes several minutes to 10 minutes per washing to wash the hollow fiber membrane filter, and during this washing, the filtration of the raw water is temporarily interrupted. The supply of purified water generated by filtering the water is also temporarily interrupted. Therefore, when the hollow fiber membrane filter is frequently washed, it is not possible to sufficiently meet the demand for quick supply of purified water.

【0005】[0005]

【課題を解決するための手段】請求項1記載の発明は、
電動機により駆動されるポンプと、このポンプにより吸
入された原水が流れる原水供給用パイプと、この原水供
給用パイプの吐出側端部に接続された中空糸膜フィルタ
と、この中空糸膜フィルタで濾過された浄水が流れる浄
水用パイプと、前記中空糸膜フィルタを洗浄する洗浄手
段とを備えた飲料水用浄化装置において、前記ポンプに
より吸入された原水の一部をこのポンプの吐出側から吸
入側へ還流させる還流通路とこの還流通路内を流れる原
水の流量を制御する流量制御弁とを備えたブリードオフ
回路を設けている。このような飲料水用浄化装置を使用
して浄水を生成する場合には、最初に、流量制御弁の開
度を中空糸膜フィルタの濾過量に適した還流量となるよ
うにセットし、ポンプの運転を開始する。中空糸膜フィ
ルタにより原水の濾過が行われ、中空糸膜の表面に原水
中の夾雑物が付着して濾過性能が低下し、生成される浄
水の量が減少した場合には、流量制御弁の開度を絞るこ
とにより還流通路を通って還流される原水の量を減ら
し、中空糸膜フィルタ側へ供給される原水の水圧を高く
するとともに供給される原水の量を増やし、生成される
浄水の量を回復させる。引き続き浄水の生成を行ない、
中空糸膜の表面に原水中の夾雑物がさらに付着して生成
される浄水の量が再び減少した場合には、流量制御弁の
開度をさらに絞ることにより生成される浄水の量を再び
回復させる。このようにして、生成される浄水の量が減
少した場合には流量制御弁の開度を次第に絞って生成さ
れる浄水の量を回復させるという操作を繰り返し、浄水
の生成量が所定量まで低下するとともに中空糸膜フィル
タ側の水圧が所定の圧力に達した後に、洗浄手段により
中空糸膜フィルタを洗浄する。このようにすれば、中空
糸膜の表面に原水中の夾雑物が付着して浄水の生成量が
減少した場合に直ちに中空糸膜フィルタを洗浄しなくて
もよく、初期の原水設定量を略均一に長時間にわたって
供給することができ、従って、浄水の供給を初期設定状
態で長時間継続して行うことができる。
According to the first aspect of the present invention,
A pump driven by an electric motor, a raw water supply pipe through which raw water sucked by this pump flows, a hollow fiber membrane filter connected to the discharge side end of this raw water supply pipe, and a filtration with this hollow fiber membrane filter. In a drinking water purifying apparatus including a purified water pipe through which the purified water flows and a cleaning unit that cleans the hollow fiber membrane filter, a part of the raw water sucked by the pump is sucked from the discharge side of the pump. A bleed-off circuit is provided, which includes a return passage for returning the flow to the return passage and a flow control valve for controlling the flow rate of the raw water flowing in the return passage. When producing purified water using such a purifying device for drinking water, first, the opening of the flow control valve is set to a reflux amount suitable for the filtration amount of the hollow fiber membrane filter, and the pump is set. Start driving. When the raw water is filtered by the hollow fiber membrane filter and foreign matter in the raw water adheres to the surface of the hollow fiber membrane to lower the filtration performance and reduce the amount of purified water produced, the flow control valve By reducing the opening, the amount of raw water recirculated through the recirculation passage is reduced, the water pressure of the raw water supplied to the hollow fiber membrane filter side is increased, and the amount of the raw water supplied is increased, resulting in the purified water produced. Restore the amount. Continue to produce purified water,
When the amount of purified water generated by the contamination of raw water further adhering to the surface of the hollow fiber membrane decreases again, the amount of purified water generated is recovered again by further narrowing the opening of the flow control valve. Let In this way, when the amount of purified water produced decreases, the operation of gradually narrowing the opening of the flow control valve to recover the amount of purified water produced is repeated, and the amount of produced purified water decreases to a prescribed amount. At the same time, after the water pressure on the hollow fiber membrane filter side reaches a predetermined pressure, the hollow fiber membrane filter is washed by the washing means. In this way, if the impurities in the raw water adhere to the surface of the hollow fiber membrane and the amount of purified water produced decreases, it is not necessary to immediately wash the hollow fiber membrane filter, and the initial raw water set amount is substantially The water can be uniformly supplied for a long time, and therefore, the purified water can be continuously supplied for a long time in the initial setting state.

【0006】[0006]

【発明の実施の形態】本発明の一実施の形態を図面に基
づいて説明する。図1は本発明の飲料水用浄化装置の全
体構造を示すブロック図である。まず、電動機(図示せ
ず)により駆動されるポンプ1が設けられており、ポン
プ1には原水供給用パイプ2が接続されている。この原
水供給用パイプ2はポンプ1により吸入された原水が流
れるもので、原水の吸入側端部にはフィルタ3が取り付
けられており、吐出側端部には複数個の中空糸膜フィル
タ4を収納したフィルタケース5が接続されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a block diagram showing the overall structure of the drinking water purifying apparatus of the present invention. First, a pump 1 driven by an electric motor (not shown) is provided, and a raw water supply pipe 2 is connected to the pump 1. This raw water supply pipe 2 is a pipe through which the raw water sucked by the pump 1 flows, and a filter 3 is attached to the suction side end of the raw water, and a plurality of hollow fiber membrane filters 4 are attached to the discharge side end. The stored filter case 5 is connected.

【0007】前記中空糸膜フィルタ4は、中心部に中心
穴を有するマカロニ状の中空糸の壁面に多数のスリット
状穴をあけた多数の中空糸膜4aを芯体(図示せず)の
回りに束ねたものであり、水が中空糸膜4aのスリット
状穴を通過して中空糸膜4aの外周面から中空糸膜4a
の中心穴へ至る際に、略0.1μm以上の細菌や夾雑物
などの通過を阻止する性能を有する。前記フィルタケー
ス5内は図2に示すように、前記中空糸膜フィルタ4を
差し込む差込穴6が形成された仕切板7により上下に仕
切られており、下方が原水が供給される原水用空間8と
され、上方が原水を前記中空糸膜フィルタ4で濾過する
ことにより生成された浄水が集められる浄水用空間9と
されている。
In the hollow fiber membrane filter 4, a large number of hollow fiber membranes 4a in which a large number of slit-shaped holes are formed in the wall surface of a macaroni-shaped hollow fiber having a central hole at the center are provided around a core body (not shown). The water is passed through the slit-shaped holes of the hollow fiber membrane 4a to pass from the outer peripheral surface of the hollow fiber membrane 4a to the hollow fiber membrane 4a.
When it reaches the center hole, it has the ability to block passage of bacteria and contaminants of approximately 0.1 μm or more. As shown in FIG. 2, the inside of the filter case 5 is vertically divided by a partition plate 7 in which an insertion hole 6 for inserting the hollow fiber membrane filter 4 is formed, and a lower portion is a space for raw water to which raw water is supplied. 8, and the upper part is a water purification space 9 in which purified water generated by filtering raw water with the hollow fiber membrane filter 4 is collected.

【0008】前記フィルタケース5には、前記原水用空
間8に連通する3個の接続口10a,10b,10c
と、前記浄水用空間9に連通する1個の接続口10dと
が形成されている。第一接続口10aには前記原水供給
用パイプ2の吐出側端部が接続され、第二接続口10b
には一端にブロワ11が接続されたエア供給パイプ12
の他端が接続され、第三接続口10cには逆流洗浄のバ
ブリング時にオーバーフローした原水や空気を排出する
排出用パイプ13が接続されている。第四接続口10d
には、生成された浄水を排水する浄水用パイプ14が接
続されている。
The filter case 5 has three connection ports 10a, 10b, 10c communicating with the raw water space 8.
And one connection port 10d communicating with the water purification space 9 are formed. The discharge side end of the raw water supply pipe 2 is connected to the first connection port 10a, and the second connection port 10b.
An air supply pipe 12 having a blower 11 connected to one end
The other end is connected, and the third connection port 10c is connected to a discharge pipe 13 for discharging raw water and air that have overflowed at the time of bubbling in backwashing. Fourth connection port 10d
A water purification pipe 14 for draining the generated purified water is connected to the.

【0009】前記原水供給用パイプ2の途中からは、後
述する洗浄手段による前記中空糸膜フィルタ4の洗浄時
に、原水用空間8内の水を中空糸膜4aの表面から剥離
された夾雑物とともに排水するための洗浄用排水パイプ
15が分岐されている。また、前記浄水用パイプ14の
途中には、一端にコンプレッサ16が接続されたエア供
給パイプ17が接続されている。
From the middle of the raw water supply pipe 2, when the hollow fiber membrane filter 4 is washed by a washing means which will be described later, the water in the raw water space 8 is removed together with the impurities separated from the surface of the hollow fiber membrane 4a. A cleaning drain pipe 15 for draining is branched. Further, an air supply pipe 17 having a compressor 16 connected to one end thereof is connected in the middle of the water purification pipe 14.

【0010】前記原水供給パイプ2には、前記ポンプ1
により吸入された原水の一部をポンプ1の吸入側へ還流
させる還流通路であるバイパス通路18が、前記ポンプ
1の吐出側と吸入側とを連通させて設けられている。こ
のバイパス通路18の途中には、バイパス通路18内を
流れる原水の流量を制御する流量制御弁である手動式の
ニードル弁19が設けられている。そして、これらのバ
イパス通路18とニードル弁19とによりブリードオフ
回路20が形成されている。
The raw water supply pipe 2 is provided with the pump 1
A bypass passage 18 which is a return passage for returning a part of the raw water sucked by the pump 1 to the suction side of the pump 1 is provided to connect the discharge side and the suction side of the pump 1 to each other. A manual needle valve 19 which is a flow rate control valve for controlling the flow rate of the raw water flowing through the bypass passage 18 is provided in the middle of the bypass passage 18. The bypass passage 18 and the needle valve 19 form a bleed-off circuit 20.

【0011】ここで、前記洗浄手段は、前記中空糸膜4
aの表面に付着している夾雑物を剥離させるもので、前
記ブロワ11やエア供給パイプ12、及び、前記コンプ
レッサ16やエア供給パイプ17、エア供給パイプ1
2,17の途中に配置された各種のバルブ等により形成
されている。
Here, the cleaning means is the hollow fiber membrane 4
The foreign matter adhering to the surface of a is peeled off. The blower 11, the air supply pipe 12, the compressor 16, the air supply pipe 17, and the air supply pipe 1 are removed.
It is formed by various valves and the like arranged in the middle of Nos. 2 and 17.

【0012】つぎに、それぞれの前記パイプ2,15,
12,13,14,17の途中に配置されている各種の
部品などについて説明する。前記原水供給用パイプ2の
途中には、圧力計21、手動式のニードル弁22、モー
タ駆動式の弁23が配置されている。前記洗浄用排水パ
イプ15の途中には、モータ駆動式の弁24が配置され
ている。前記エア供給用パイプ12の途中には、エア用
フローメータ25、電磁弁26、逆止弁27が配置され
ている。前記排出用パイプ13の途中には、モータ駆動
式の弁28が配置されている。前記浄水用パイプ14の
途中には、圧力計29、手動式のニードル弁30、活性
炭フィルタ31、モータ駆動式の弁32、水用フローメ
ータ33、手動式のボール弁34が配置されている。前
記エア供給パイプ17の途中には、フィルタレギュレー
タ35、エアフィルタ36、電磁弁37、逆止弁38が
配置されている。
Next, each of the pipes 2, 15 and
Various parts arranged in the middle of 12, 13, 14, and 17 will be described. A pressure gauge 21, a manual needle valve 22, and a motor driven valve 23 are arranged in the middle of the raw water supply pipe 2. A motor-driven valve 24 is arranged in the middle of the cleaning drain pipe 15. An air flow meter 25, a solenoid valve 26, and a check valve 27 are arranged in the middle of the air supply pipe 12. A motor-driven valve 28 is arranged in the middle of the discharge pipe 13. A pressure gauge 29, a manual needle valve 30, an activated carbon filter 31, a motor-driven valve 32, a water flow meter 33, and a manual ball valve 34 are arranged in the middle of the water purification pipe 14. A filter regulator 35, an air filter 36, a solenoid valve 37, and a check valve 38 are arranged in the middle of the air supply pipe 17.

【0013】このような構成において、この飲料水用浄
化装置を使用して浄水を生成する場合には、最初に、ニ
ードル弁19の開度を中空糸膜フィルタ4の濾過量に適
した還流量となるようにセットし、ポンプ1の運転を開
始する。ポンプ1の運転を開始すると、ポンプ1により
吸入された原水が原水供給用パイプ2内を流れてフィル
タケース5の原水用空間8内へ供給され、原水の一部は
バイパス通路18を通ってポンプ1の吸入側へ還流され
る。原水用空間8内へ供給された原水は中空糸膜フィル
タ4により細菌や夾雑物等の流入が阻止されて浄水とな
り、この浄水はフィルタケース5の浄水用空間9に集め
られた後に浄水用排水パイプ14内を流れて給水され
る。浄水用排水パイプ14内を流れる浄水はその途中で
活性炭フィルタ31により溶解物が吸着され、臭気物質
やその他の溶解物が除去される。ポンプ1の運転は電動
機駆動であるため、低騒音、低振動が達成される。
In the case of producing purified water by using this drinking water purifying apparatus with such a constitution, first, the opening degree of the needle valve 19 is adjusted to the reflux amount suitable for the filtration amount of the hollow fiber membrane filter 4. Then, the operation of the pump 1 is started. When the operation of the pump 1 is started, the raw water sucked by the pump 1 flows through the raw water supply pipe 2 and is supplied into the raw water space 8 of the filter case 5, and a part of the raw water is pumped through the bypass passage 18. 1 is returned to the suction side. The raw water supplied into the raw water space 8 is purified by the hollow fiber membrane filter 4 from blocking the inflow of bacteria, contaminants, etc., and this purified water is collected in the clean water space 9 of the filter case 5 and then discharged for purification. Water is supplied by flowing through the pipe 14. As for the purified water flowing through the purified water drain pipe 14, the dissolved matter is adsorbed by the activated carbon filter 31 on the way, and odorous substances and other dissolved matters are removed. Since the pump 1 is driven by an electric motor, low noise and low vibration are achieved.

【0014】このようにして浄水の生成を続けると、中
空糸膜4aの表面に夾雑物が付着することにより中空糸
膜フィルタ4の濾過性能が低下し、図3のAに示すよう
に浄水の生成量が次第に減少する。
When the purified water is continuously produced in this manner, contaminants are attached to the surface of the hollow fiber membrane 4a to lower the filtration performance of the hollow fiber membrane filter 4, and as shown in FIG. The amount produced decreases gradually.

【0015】浄水の生成量が所定量まで低下したとき
は、ブリードオフ回路20のニードル弁19の開度を絞
り込む。すると、バイパス通路18を通って還流される
原水が少なくなるとともに中空糸膜フィルタ4側へ供給
される原水の水圧が高まるとともに量が増え、浄水の生
成量が回復する。ニードル弁19の開度をそのままにし
て浄水の生成を続けると、中空糸膜4aの表面に夾雑物
がさらに付着することにより中空糸膜フィルタ4の濾過
性能が低下し、図3のBに示すように浄水の生成量が次
第に減少する。
When the amount of purified water produced falls to a predetermined amount, the opening of the needle valve 19 of the bleed-off circuit 20 is narrowed down. Then, the amount of raw water recirculated through the bypass passage 18 is reduced, the water pressure of the raw water supplied to the hollow fiber membrane filter 4 is increased, and the amount thereof is increased. Continuing to generate purified water with the opening of the needle valve 19 kept as it is, contaminants further adhere to the surface of the hollow fiber membrane 4a, so that the filtration performance of the hollow fiber membrane filter 4 deteriorates, as shown in FIG. 3B. Thus, the amount of purified water produced gradually decreases.

【0016】浄水の生成量が再び所定量まで低下したと
きは、ブリードオフ回路20のニードル弁19の開度を
さらに絞り込む。すると、バイパス通路18を通って還
流される原水がさらに少なくなるとともに、中空糸膜フ
ィルタ4側へ供給される原水の水圧がさらに高くなると
ともに量がさらに増え、浄水の生成量が再び回復する。
ニードル弁19の開度をそのままの状態にして浄水の生
成を続けると、中空糸膜4aの表面に夾雑物がさらに付
着することにより中空糸膜フィルタ4の濾過性能が低下
し、図3のCに示すように浄水の生成量が次第に減少す
る。そして、浄水の生成量が所定量まで低下して所定の
圧力に達したら、洗浄手段により中空糸膜フィルタ4の
洗浄を行い、この洗浄が終了した後は、ブリードオフ回
路20のニードル弁19の開度を当初の状態に戻して浄
水の生成を再開する。
When the amount of purified water produced again falls to a predetermined amount, the opening of the needle valve 19 of the bleed-off circuit 20 is further narrowed. Then, the raw water recirculated through the bypass passage 18 is further reduced, the water pressure of the raw water supplied to the hollow fiber membrane filter 4 side is further increased, the amount thereof is further increased, and the production amount of purified water is recovered again.
Continuing to generate purified water with the opening degree of the needle valve 19 kept as it is, foreign matter further adheres to the surface of the hollow fiber membrane 4a, whereby the filtration performance of the hollow fiber membrane filter 4 deteriorates, and C of FIG. As shown in, the amount of purified water produced gradually decreases. When the generated amount of purified water drops to a predetermined amount and reaches a predetermined pressure, the hollow fiber membrane filter 4 is washed by the washing means, and after this washing is completed, the needle valve 19 of the bleed-off circuit 20 Return the opening to the initial state and restart the production of purified water.

【0017】従って、このブリードオフ回路20を設け
ない場合に比べて、中空糸膜フィルタ4を洗浄する頻度
が例えば1/3となり、浄水の生成を長時間連続して行
うことができ、浄水の迅速な供給という要望に充分に応
えることができる。
Therefore, compared with the case where the bleed-off circuit 20 is not provided, the frequency of cleaning the hollow fiber membrane filter 4 becomes, for example, 1/3, and purified water can be continuously generated for a long time, and the purified water can be continuously produced. It can fully meet the demand for quick supply.

【0018】つぎに、中空糸膜フィルタ4の洗浄につい
て説明する。この洗浄時には、弁23,32を閉弁させ
るとともに、電磁弁37を開弁させてコンプレッサ16
を駆動させる。コンプレッサ16の駆動により、第四接
続口10dから浄水用空間9内へ高圧空気が供給され、
浄水用空間9内に溜っていた浄水が中空糸膜4aの中心
穴から外周へ向けて濾過時とは逆向きに流れ、中空糸膜
4aの表面に付着している夾雑物が剥離される。続いて
コンプレッサ16の駆動を停止し、電磁弁26,28を
開弁させてブロワ11を駆動させる。ブロワ11の駆動
により第二接続口10bから原水用空間8内へ空気が供
給され、原水用空間8内に溜っていた原水に対してエア
バブリングが行われ、気泡によって中空糸膜4aの表面
に付着している夾雑物の剥離が促進される。そして、エ
アバブリングの実施後ブロワ11の駆動を停止し、弁2
4を開弁することにより、原水用空間8内の水が中空糸
膜4aの表面から剥離された夾雑物とともに洗浄用排水
パイプ15から排水される。なお、この洗浄時において
ブロワ11やコンプレッサ16により供給された空気
は、排出用パイプ13を通って排出される。
Next, the cleaning of the hollow fiber membrane filter 4 will be described. During this cleaning, the valves 23 and 32 are closed and the solenoid valve 37 is opened to open the compressor 16
Drive. By driving the compressor 16, high-pressure air is supplied from the fourth connection port 10d into the water purification space 9,
The purified water accumulated in the water purification space 9 flows from the center hole of the hollow fiber membrane 4a toward the outer periphery in the opposite direction to that at the time of filtration, and the contaminants adhering to the surface of the hollow fiber membrane 4a are peeled off. Then, the drive of the compressor 16 is stopped, the electromagnetic valves 26 and 28 are opened, and the blower 11 is driven. Air is supplied from the second connection port 10b into the raw water space 8 by driving the blower 11, air bubbling is performed on the raw water that has accumulated in the raw water space 8, and air bubbles are applied to the surface of the hollow fiber membrane 4a. The peeling of adhering impurities is promoted. After the air bubbling is performed, the drive of the blower 11 is stopped and the valve 2
By opening the valve 4, the water in the raw water space 8 is drained from the cleaning drain pipe 15 together with the contaminants separated from the surface of the hollow fiber membrane 4a. The air supplied by the blower 11 and the compressor 16 during this cleaning is discharged through the discharge pipe 13.

【0019】なお、本実施の形態においては、浄水の生
成量が所定量まで低下した場合には、それを確認した作
業者がブリードオフ回路20のニードル弁19を手動で
開度調節する場合を例に挙げて説明したが、浄水の生成
量をセンサで確認し、その確認結果に基づいてニードル
弁19の開度を自動的に調節するようにしてもよい。
In the present embodiment, when the amount of purified water produced falls to a predetermined amount, an operator who confirms the amount of purified water may manually adjust the opening of the needle valve 19 of the bleed-off circuit 20. Although described as an example, the amount of purified water generated may be confirmed by a sensor, and the opening degree of the needle valve 19 may be automatically adjusted based on the confirmation result.

【0020】[0020]

【発明の効果】本発明によれば、中空糸膜の表面に原水
中の夾雑物が付着して中空糸膜フィルタの濾過性能が低
下したために生成される浄水の量が減少した場合には、
流量制御弁の開度を絞ることにより還流通路を通って還
流される原水の量を減らし、中空糸膜フィルタ側へ供給
される原水の水圧を高くするとともに供給される原水の
量を増やすことにより生成される浄水の量を回復させる
ことができ、そして、浄水の生成量が減少した場合に流
量制御弁の開度を絞って生成される浄水の量を回復させ
るという操作を繰り返すことにより、洗浄手段による中
空糸膜フィルタの洗浄頻度を低下させることができ、こ
れにより、浄水の供給を長時間継続して行うことがで
き、浄水の迅速な供給という要望に応えることができ
る。
EFFECTS OF THE INVENTION According to the present invention, when the amount of purified water produced decreases due to the contaminants in the raw water adhering to the surface of the hollow fiber membrane and the filtration performance of the hollow fiber membrane filter is reduced,
By reducing the opening of the flow control valve to reduce the amount of raw water recirculated through the recirculation passage, increasing the water pressure of the raw water supplied to the hollow fiber membrane filter side and increasing the amount of raw water supplied. The amount of purified water produced can be recovered, and when the amount of produced purified water decreases, the operation of reducing the opening of the flow control valve to recover the amount of purified water produced will be repeated. The cleaning frequency of the hollow fiber membrane filter by the means can be reduced, whereby the purified water can be continuously supplied for a long time, and it is possible to meet the demand for the rapid supply of the purified water.

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

【図1】本発明の一実施の形態を示すブロック図であ
る。
FIG. 1 is a block diagram showing an embodiment of the present invention.

【図2】フィルタケースの構造とこのフィルタケース内
への中空糸膜フィルタの収納構造を示す縦断側面図であ
る。
FIG. 2 is a vertical cross-sectional side view showing a structure of a filter case and a structure for housing a hollow fiber membrane filter in the filter case.

【図3】ブリードオフ回路の弁の開度と浄水の生成量と
の関係を示すグラフである。
FIG. 3 is a graph showing the relationship between the valve opening of the bleed-off circuit and the amount of purified water produced.

【符号の説明】[Explanation of symbols]

1 ポンプ 2 原水供給用パイプ 4 中空糸膜フィルタ 14 浄水用パイプ 18 還流通路 19 流量制御弁 20 ブリードオフ回路 1 Pump 2 Raw Water Supply Pipe 4 Hollow Fiber Membrane Filter 14 Water Purification Pipe 18 Reflux Passage 19 Flow Control Valve 20 Bleed-off Circuit

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 電動機により駆動されるポンプと、この
ポンプにより吸入された原水が流れる原水供給用パイプ
と、この原水供給用パイプの吐出側端部に接続された中
空糸膜フィルタと、この中空糸膜フィルタで濾過された
浄水が流れる浄水用パイプと、前記中空糸膜フィルタを
洗浄する洗浄手段とを備えた飲料水用浄化装置におい
て、前記ポンプにより吸入された原水の一部をこのポン
プの吐出側から吸入側へ還流させる還流通路とこの還流
通路内を流れる原水の流量を制御する流量制御弁とを備
えたブリードオフ回路を設けたことを特徴とする飲料水
用浄化装置。
1. A pump driven by an electric motor, a raw water supply pipe through which raw water sucked by this pump flows, a hollow fiber membrane filter connected to the discharge side end of this raw water supply pipe, and this hollow In a drinking water purification device comprising a water purification pipe through which purified water filtered by a fiber membrane filter flows, and a cleaning means for cleaning the hollow fiber membrane filter, part of the raw water sucked by the pump is A drinking water purifying device comprising a bleed-off circuit provided with a return passage for returning from a discharge side to a suction side and a flow control valve for controlling a flow rate of raw water flowing in the return passage.
JP315596A 1996-01-11 1996-01-11 Clarification apparatus for drinking water Withdrawn JPH09187766A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP315596A JPH09187766A (en) 1996-01-11 1996-01-11 Clarification apparatus for drinking water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP315596A JPH09187766A (en) 1996-01-11 1996-01-11 Clarification apparatus for drinking water

Publications (1)

Publication Number Publication Date
JPH09187766A true JPH09187766A (en) 1997-07-22

Family

ID=11549470

Family Applications (1)

Application Number Title Priority Date Filing Date
JP315596A Withdrawn JPH09187766A (en) 1996-01-11 1996-01-11 Clarification apparatus for drinking water

Country Status (1)

Country Link
JP (1) JPH09187766A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019018162A (en) * 2017-07-19 2019-02-07 株式会社クラレ Cleaning method of hollow fiber membrane filtering device, and the hollow fiber membrane filtering device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019018162A (en) * 2017-07-19 2019-02-07 株式会社クラレ Cleaning method of hollow fiber membrane filtering device, and the hollow fiber membrane filtering device

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