JPH11188246A - Washing method for hollow fiber membrane - Google Patents

Washing method for hollow fiber membrane

Info

Publication number
JPH11188246A
JPH11188246A JP35904697A JP35904697A JPH11188246A JP H11188246 A JPH11188246 A JP H11188246A JP 35904697 A JP35904697 A JP 35904697A JP 35904697 A JP35904697 A JP 35904697A JP H11188246 A JPH11188246 A JP H11188246A
Authority
JP
Japan
Prior art keywords
water
hollow fiber
fiber membrane
electrolytic
cleaning
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
JP35904697A
Other languages
Japanese (ja)
Inventor
Yoshihiro Shimizu
善弘 清水
Noritake Sumida
憲武 隅田
Ichiro Oshima
一郎 大島
Yoko Fukushima
容子 福島
Takeo Abe
剛夫 安部
Rie Tamaru
理恵 田丸
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.)
Sharp Corp
Original Assignee
Sharp 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 Sharp Corp filed Critical Sharp Corp
Priority to JP35904697A priority Critical patent/JPH11188246A/en
Publication of JPH11188246A publication Critical patent/JPH11188246A/en
Pending legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an inexpensive and simple washing method for a hollow fiber membrane for alkali treating device removing transmission substance deposited on the inside of the hollow fiber membrane with an economical method and besides perfectly killing bacteria in the hollow fiber membrane disabled to remove them. SOLUTION: In a water treating device which has a water purifying part having the hollow fiber membrane 2 as one of the constitutional elements and an electrolysis bath 3 for producing electrolyzed water, electrolyzed acidic water and other adjusted water are continuously passed through the membrane 2 from the direction opposite to it at a time of water purification treatment, and the membrane 2 is washed by back-washing of the adjusted water.

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】本発明は中空糸膜を構成要素
の一つとして持つ浄水処理部と水の電解槽を備え持つ整
水機の中空糸膜の洗浄方法に関し、更に詳しくは電解酸
性水とその他の調整水を連続して中空糸膜に通水し中空
糸膜の瀘過寿命を延長させる方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of cleaning a hollow fiber membrane of a water purifier having a water purification treatment section having a hollow fiber membrane as one of constituent elements and a water electrolysis tank, and more particularly to an electrolytic acid water. And the other conditioned water is continuously passed through the hollow fiber membrane to extend the filtration life of the hollow fiber membrane.

【0002】[0002]

【従来の技術】従来の中空糸膜モジュールは食品分野や
医療分野、水処理分野などをはじめとして様々な方面で
利用されている。これらの中空糸膜モジュールは湿式法
若しくは乾式法と呼ばれる方法で製膜された後モジュー
ル化される。中空糸膜は一般的には通常湿潤した環境で
使用され、中空糸内の細孔に水中の不純物や微生物など
を捕集し、これらを除去する。
2. Description of the Related Art Conventional hollow fiber membrane modules are used in various fields such as food, medical, and water treatment fields. These hollow fiber membrane modules are formed into a module after being formed by a method called a wet method or a dry method. The hollow fiber membrane is generally used in a humid environment, and collects impurities and microorganisms in water in pores in the hollow fiber and removes them.

【0003】しかし、長期間使用していると、汚染物質
などの膜壁面への堆積物、またモジュール内における微
生物の増殖によって処理能力の低下、製品品質の低下を
招く。そこで堆積物を剥がしたり、細孔を開口して処理
能力を回復させ、菌や黴などの微生物の増殖を防ぐ中空
糸膜の洗浄手段が必要となる。
However, when used for a long period of time, deposits on the membrane wall surface such as contaminants and the growth of microorganisms in the module cause a reduction in processing capacity and a reduction in product quality. Therefore, it is necessary to remove the sediment or open the pores to restore the processing ability, and to provide a means for cleaning the hollow fiber membrane that prevents the growth of microorganisms such as bacteria and fungi.

【0004】従って、化学的な殺菌消壱液を洗浄液とし
て用いる方法として、特開平5−168873号公報に
開示されているような次亜塩素酸、水酸化ナトリウムな
どの水溶液を、中空糸膜が浄水処理する場合と逆の方向
から通水させる方法や特開平9−52027号公報に開
示されているような天然抗菌剤を含有した洗浄液で逆洗
する方法が提案されている。
Accordingly, as a method of using a chemical sterilizing solution as a cleaning solution, an aqueous solution of hypochlorous acid, sodium hydroxide or the like as disclosed in Japanese Patent Application Laid-Open No. 5-168873 is used. There have been proposed a method of passing water from the opposite direction to the case of performing water purification treatment, and a method of backwashing with a cleaning solution containing a natural antibacterial agent as disclosed in JP-A-9-52027.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、化学的
な殺菌消毒液を洗浄液として用いる方法は、微生物の繁
殖を防止する効果は期待できるが、これらの殺菌消毒液
は人体に対して毒性があるため、これらが中空糸膜中に
残留しないように、完全に除去しなければならない。
However, although a method using a chemical disinfectant as a cleaning solution can be expected to prevent the growth of microorganisms, these disinfectants are toxic to the human body. Must be completely removed so that they do not remain in the hollow fiber membrane.

【0006】また、天然抗菌剤を含有した洗浄液は人体
に対する毒性は低くなるものの、天然抗菌剤はその値段
が高くつくし、また、その殺菌力が水中に含まれる全て
の雑菌に効くかどうかは疑わしい。
Although a cleaning solution containing a natural antibacterial agent has low toxicity to the human body, the natural antibacterial agent is expensive, and it is doubtful whether its bactericidal activity is effective against all bacteria contained in water. .

【0007】本発明は経済的な方法で中空糸膜の内面に
堆積した瀘過物質を除去し、更に、除去しきれなかった
中空糸膜内の雑菌を完全に死滅させる浄水用中空糸膜の
洗浄方法を提供することにある。
According to the present invention, there is provided a hollow fiber membrane for water purification which removes filter substances deposited on the inner surface of the hollow fiber membrane by an economical method, and furthermore, completely eliminates various bacteria in the hollow fiber membrane which could not be removed. It is to provide a cleaning method.

【0008】[0008]

【課題を解決するための手段】本発明の中空糸膜の洗浄
方法は上記目的を達成するためのものであり、第1の発
明は中空糸膜を構成要素の一つとして持っている浄水部
と電解水を生成する電解槽を有する整水器で、電解酸性
水とその他の調整水を、浄水処理をしている時と逆の方
向から、中空糸膜に連続して通水するものである。
Means for Solving the Problems The method for cleaning a hollow fiber membrane according to the present invention is intended to achieve the above object, and the first invention is a water purification section having a hollow fiber membrane as one of the constituent elements. A water conditioner having an electrolysis tank that generates electrolyzed water, and continuously passes electrolyzed acidic water and other conditioned water through the hollow fiber membrane from the opposite direction of the water purification process. is there.

【0009】また、第2の発明は、その他の調整水で中
空糸膜を逆洗した後に電解酸性水を通水する時、屯解酸
性水は浄水処理使用時と同じ方向から中空糸膜に通水す
るものである。
Further, the second invention is characterized in that when the hollow fiber membrane is backwashed with other conditioned water and then the electrolytic acid water is passed through, the deionized acidic water is applied to the hollow fiber membrane in the same direction as when using the water purification treatment. It allows water to flow.

【0010】そして、第3の発明は上記の中空糸膜を洗
浄するための調整水として人体に害のない生体適合性の
洗浄剤を含んだものやまた単なる水道水を使用するもの
である。
[0010] In a third aspect of the present invention, the conditioning water for cleaning the hollow fiber membrane contains a biocompatible cleaning agent which is harmless to the human body, or simply uses tap water.

【0011】更に、第4の発明は、その他の調整水は1
種類のみと限るものでなく、必要であれば何種類用いて
もかまわない、つまり電解酸性水と合わせてに二種類以
上あるものである。
Further, in the fourth invention, the other adjusted water is 1
The type is not limited to the type, and any type may be used if necessary. That is, there are two or more types in combination with the electrolytic acidic water.

【0012】また、第5の発明は、中空糸膜の洗浄目的
で用いる酸性水のpH(酸、アルカリ度)は2から6の
範囲に収まるようにするものである。
According to a fifth aspect of the present invention, the pH (acid, alkalinity) of the acidic water used for cleaning the hollow fiber membrane falls within the range of 2 to 6.

【0013】更に、電解酸性水の殺菌力を向上させる目
的で電解液として電解槽に供給される原水中に食塩を添
加するものである。
Further, in order to improve the sterilizing power of the electrolytic acidic water, salt is added to raw water supplied to the electrolytic cell as an electrolytic solution.

【0014】本発明で示す中空糸膜の洗浄方法では、洗
浄用の調整水で中空糸膜を逆洗することにより、中空糸
膜側壁に堆積した残留物や中空糸膜の細孔に捕集された
水道水中の不純物や微生物は除去される。この時、洗浄
用の調整水として水道水を用いた場合、水道水には残留
塩素が含まれているので、逆洗によって除去しきれなか
った一部の微生物は死滅すると考えられる。
In the method for cleaning a hollow fiber membrane according to the present invention, the hollow fiber membrane is back-washed with a conditioning water for cleaning, so that the residue deposited on the side wall of the hollow fiber membrane and the pores of the hollow fiber membrane are collected. Impurities and microorganisms in the treated tap water are removed. At this time, if tap water is used as the conditioning water for washing, since the tap water contains residual chlorine, it is considered that some microorganisms that could not be completely removed by backwashing will die.

【0015】ところが、除去しきれず死滅しない微生物
が中空糸膜内に残留しているので、この微生物を完全に
死滅させる目的で電解酸性水を中空糸膜中に通水させ
る。そして電解酸性水を中空糸膜に通水させる場合は浄
水使用時と逆方向からでも同じ方向からでもどちらの方
向からでもよい。逆方向から電解酸性水を通水する場合
は逆洗を行いながら残留微生物の殺菌を同時に行う。
However, since microorganisms that cannot be completely removed and do not die remain in the hollow fiber membrane, electrolytic acid water is passed through the hollow fiber membrane in order to completely kill the microorganisms. When the electrolytic acid water is passed through the hollow fiber membrane, it may be from the opposite direction or the same direction as when using purified water, or from any direction. When passing the electrolytic acid water from the opposite direction, the residual microorganisms are simultaneously sterilized while performing back washing.

【0016】しかし、中空糸膜を逆洗処理すると中空糸
膜側壁の細孔の方向性を変えてしまうので、多少物理的
ダメージが残ることが知られている。よって電解酸性水
だけでも順方向から行うことで、中空糸膜の寿命をより
延命させることが期待できる。中空糸膜に残留する微生
物の殺菌目的で使用する電解酸性水のpHは2から6ま
での範囲に収まるようにし、好ましくはpH2.7前後
がよい。また電解液として電解槽に供給される水道水中
に食塩を添加することにより、電解効率を向上させ、電
解酸性水の殺菌力を向上させることが可能となる。
However, it is known that when the hollow fiber membrane is backwashed, the directionality of the pores on the side wall of the hollow fiber membrane is changed, so that some physical damage remains. Therefore, it can be expected that the life of the hollow fiber membrane can be further prolonged by performing the treatment from the forward direction using only the electrolytic acidic water. The pH of the electrolytic acid water used for the purpose of sterilizing microorganisms remaining in the hollow fiber membrane is adjusted to fall within a range of 2 to 6, and preferably around pH 2.7. Further, by adding salt to tap water supplied to the electrolytic cell as an electrolytic solution, it is possible to improve the electrolysis efficiency and improve the sterilizing power of the electrolyzed acidic water.

【0017】電解酸性水の殺菌能力の特徴として抗菌ス
ペクトルが広いということ、原料が水道水だけ、若しく
は水道水と食塩だけなので人体に比較的安全なことがあ
げらわる。更に電解酸性水の殺菌力の持続時間が短いこ
とが知られている。つまり、電解酸性水の殺菌力はある
程度時間が経つと消滅するので、もし電解酸性水の殺菌
力の人体への影響を懸念する場合でも、本発明の方法で
中空糸膜の洗浄を行ってしばらく放置しておけば電解酸
性水の殺菌力は完全に消滅し、安全に浄水処理した水を
飲むことができる。
The characteristics of the sterilizing ability of the electrolytic acid water are that it has a broad antibacterial spectrum and that it is relatively safe for the human body because the raw material is only tap water or only tap water and salt. Furthermore, it is known that the duration of the sterilizing power of the electrolytic acid water is short. In other words, the sterilizing power of the electrolytic acidic water disappears after a certain period of time, so even if the sterilizing power of the electrolytic acidic water is concerned about the effect on the human body, the hollow fiber membrane may be washed by the method of the present invention for a while. If left untreated, the sterilizing power of the electrolyzed acidic water will completely disappear, and you can safely drink purified water.

【0018】[0018]

【発明の実施の形態】以下本発明の中空糸膜の洗浄方法
の実施の形態を図面と共に説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the method for cleaning a hollow fiber membrane of the present invention will be described below with reference to the drawings.

【0019】本発明の中空糸膜の洗浄方法の第1の実施
の形態を、活性炭と中空糸膜で構成される浄化部と浄化
処理された水を電気分解する電解槽を備え持つ整水器に
おける中空糸膜の洗浄について、図1、図2、図3を用
いて説明する。
The first embodiment of the method for cleaning a hollow fiber membrane according to the present invention is directed to a water conditioner provided with a purifying section composed of activated carbon and a hollow fiber membrane and an electrolytic cell for electrolyzing purified water. The washing of the hollow fiber membrane in the above will be described with reference to FIGS. 1, 2 and 3. FIG.

【0020】図1はこの整水器で電解水を生成する時の
水の経路を示しており、この整水器で電解アルカリ水を
取水する場合は、活性炭1、中空糸膜2を経由してきた
水が電解処理される。この整水器には図1で示すよう
に、活性炭1の前に三方弁11、活性炭1と中空糸膜2
の間に三方弁12、中空糸膜2と電解槽3との間に三方
弁13、14、電解アルカリ水を生成するに伴って生成
する電解酸性水を中空糸膜2の方へ返すための三方弁1
5が設置されている。
FIG. 1 shows a water path when electrolytic water is generated by the water conditioner. When the electrolytic water is taken by the water conditioner, the water passes through the activated carbon 1 and the hollow fiber membrane 2. The water is electrolyzed. As shown in FIG. 1, this water conditioner has a three-way valve 11, an activated carbon 1 and a hollow fiber membrane 2 before an activated carbon 1.
Between the three-way valve 12 and the hollow fiber membrane 2 and the electrolytic cell 3, and three-way valves 13 and 14 between the hollow fiber membrane 2 and the electrolytic cell 3 for returning the electrolytic acid water generated as the electrolytic alkaline water is generated to the hollow fiber membrane 2. Three-way valve 1
5 are installed.

【0021】この整水器の中空糸膜を洗浄する場合、先
ず図2で示す経路により中空糸膜2を水道水で逆洗し、
次に図3に示す経路により中空糸膜2を電解酸性水で逆
洗する。水道水による逆洗により中空糸膜2の側壁に堆
積した残留物や中空糸膜2の細孔に補集されている水道
水中の不純物は洗い流される。また、電解酸性水による
逆洗により、水道水逆洗で除去しきれなかった細菌や微
生物を完全に死滅させることができる。
When the hollow fiber membrane of the water conditioner is washed, first, the hollow fiber membrane 2 is backwashed with tap water along the route shown in FIG.
Next, the hollow fiber membrane 2 is backwashed with electrolytic acid water along the route shown in FIG. Residues deposited on the side wall of the hollow fiber membrane 2 by backwashing with tap water and impurities in tap water collected in pores of the hollow fiber membrane 2 are washed away. In addition, by backwashing with electrolytic acid water, bacteria and microorganisms that cannot be completely removed by tap water backwash can be completely killed.

【0022】次に本発明の中空糸膜の洗浄方法の第2の
実施の形態を、活性炭と中空糸膿で構成される浄化部と
浄化処理された水を電気分解する電解槽を備え持つ整水
器における中空糸膜の洗浄について、図4、図5、図6
を用いて説明する。
Next, a second embodiment of the method for cleaning a hollow fiber membrane according to the present invention is directed to a method for cleaning a hollow fiber membrane comprising a purifying section composed of activated carbon and hollow fiber and an electrolytic cell for electrolyzing purified water. About cleaning of the hollow fiber membrane in the water vessel, FIGS.
This will be described with reference to FIG.

【0023】図4はこの整水器で電解水を生成する時の
水の経路を示しており、活性炭5の前に三方弁16、活
性炭5と中空糸膜の間に三方弁17、18、中空糸膜6
と電解槽7との間に三方弁19、20、電解アルカリ水
を生成するに伴って生成する電解酸性水を中空糸膜6の
方へ返すための三方弁21が設置されている。
FIG. 4 shows a water path when electrolyzed water is generated by the water conditioner. A three-way valve 16 is provided before the activated carbon 5 and three-way valves 17 and 18 are provided between the activated carbon 5 and the hollow fiber membrane. Hollow fiber membrane 6
Three-way valves 19 and 20 and a three-way valve 21 for returning electrolytic acid water generated as the alkaline water is generated toward the hollow fiber membrane 6 are provided between the electrolyzer 7 and the electrolytic cell 7.

【0024】この整水器の中空糸膜6を洗浄する場合、
先ず図5で示す経路により中空糸膜6を水道水で逆洗
し、次に図6に示す経路により中空糸膜6に電解酸性水
を順方向から供給する。
When washing the hollow fiber membrane 6 of this water conditioner,
First, the hollow fiber membrane 6 is backwashed with tap water along the route shown in FIG. 5, and then electrolytic acidic water is supplied to the hollow fiber membrane 6 from the forward direction through the route shown in FIG.

【0025】上記第1の実施の形態の場合は、電解酸性
水を中空糸膜2に浄水処理をしている場合と逆方向から
供給するので、水道水逆洗で除去しきれなかった不純物
や、除去しきれずまた死滅していない細菌や微生物を逆
洗で除去しながらまた酸性水の力で殺菌をするというメ
リットがあるが、中空糸膜2の細孔は順方向から供給さ
れる水道水中の不純物を補集しやすいような方向性を持
った細孔が中空糸膜の側壁に多数有り、逆洗を行うこと
で、その方向性に変化が生じたり、また、物理的な損傷
は逃れられない。
In the case of the first embodiment, the electrolytic acid water is supplied from the opposite direction to the case where the hollow fiber membrane 2 is subjected to the water purification treatment. There is an advantage that bacteria and microorganisms that cannot be completely removed and are not killed are removed by backwashing and sterilized by the power of acidic water, but the pores of the hollow fiber membrane 2 are supplied in tap water supplied from the forward direction. There are many pores on the side wall of the hollow fiber membrane that have a directional property so that impurities can be easily collected. By performing backwashing, the directional property may change and physical damage may be avoided. I can't.

【0026】よって、第2の実施の形態では、電解酸性
水を順方向から供給することで上記第1の実施の形態の
場合よりも中空糸膜6の物理的な損傷を抑えるので、中
空糸膜6がより長寿命になることが期待できる。
Therefore, in the second embodiment, the supply of electrolytic acid water from the forward direction suppresses the physical damage of the hollow fiber membrane 6 as compared with the case of the first embodiment. It can be expected that the film 6 will have a longer life.

【0027】上記中空糸膜の洗浄方法において、電解酸
性水の殺菌力には生物が生存しにくい酸性という条件と
水道水中に存在している塩化物イオンが電解酸化を受け
ることによって生成する溶存塩素やその他の塩素活性種
が寄与していると考えられている。よって、塩化物イオ
ンの濃度が大きい水を用いて生成した電解酸性水はより
大きな殺菌効果が期待できる。
In the above-mentioned method for cleaning the hollow fiber membrane, the sterilizing power of the electrolytic acidic water is limited to the condition that the organism is difficult to survive and the dissolved chlorine generated by the chloride ions present in the tap water undergoing electrolytic oxidation. And other chlorine active species are thought to contribute. Therefore, electrolytic acid water generated using water having a high chloride ion concentration can be expected to have a greater bactericidal effect.

【0028】図7にはより強力な殺菌力を付与した電解
酸性水で中空糸膜を逆洗する場合の水道水のフロー図
を、図8にはより強力な殺菌力を付与した電解酸性水を
中空糸膜に順方向から供給する場合の水道水のフロー図
を示す。
FIG. 7 is a flow chart of tap water in the case where the hollow fiber membrane is backwashed with electrolytic acid water to which stronger sterilizing power is applied, and FIG. 8 is electrolytic water to which stronger sterilizing power is applied. Is a flow diagram of tap water when water is supplied to a hollow fiber membrane from a forward direction.

【0029】本発明の中空糸膜の洗浄方法で、上記のよ
り強力な殺菌力を持つ電解酸性水を利用する場合は、通
常、図1の取水経路を持つ整水器で電解アルカリ水を得
る整水器の中空糸膜2に図2で示す水道水逆洗を行った
後、図7で示す電解酸性水逆洗を連続して行う。また
は、通常図4の取水経路を持つ整水器で電解アルカリ水
を得る整水器の中空糸膜6に図5で示す水道水逆洗を行
った後、図8で示す電解酸性水による洗浄を連続して行
えば良い。
In the method for cleaning a hollow fiber membrane of the present invention, when the above-mentioned electrolytic acid water having a stronger sterilizing power is used, usually, the electrolytic alkaline water is obtained by a water conditioner having a water intake path shown in FIG. After the tap water backwash shown in FIG. 2 is performed on the hollow fiber membrane 2 of the water conditioner, the electrolytic acid water backwash shown in FIG. 7 is continuously performed. Alternatively, after the tap water backwash shown in FIG. 5 is performed on the hollow fiber membrane 6 of the water conditioner for obtaining electrolytic alkaline water with the water conditioner having the water intake path shown in FIG. May be performed continuously.

【0030】[0030]

【発明の効果】本発明の中空糸膜洗浄方法は上記のよう
な構成であるから、水道水などの原水で中空糸膜モジュ
ールを逆洗した後、電解酸性水で処理を行うので、逆洗
で除去しきれなかった中空糸膜中の細菌や黴などの微生
物を殺菌することができる。また、電解酸性水は抗菌ス
ペクトルが広く、そして、原料が水道水だけ、若しくは
水道水と食塩だけなので人体に比較的安全である。
Since the hollow fiber membrane cleaning method of the present invention has the above-described configuration, the hollow fiber membrane module is backwashed with raw water such as tap water and then treated with electrolytic acid water. Microorganisms such as bacteria and fungi in the hollow fiber membrane that could not be removed by the method can be sterilized. Electrolytic acid water has a broad antibacterial spectrum and is relatively safe for the human body because the raw material is only tap water or only tap water and salt.

【0031】更に、電解酸性水の殺菌力の持続時間は短
く、つまり、電解酸性水の殺菌力はある程度時間が経つ
と消滅するので、もし電解酸性水の殺菌力の人体への影
響を懸念する場合でも、本発明の方法で中空糸膜の洗浄
を行ってしばらく放置しておけば電解酸性水の殺菌力は
完全に消滅し、安全に浄水処理した水を飲むことができ
る。また、電解酸性水は電解槽が備えられている整水器
であれば簡単に造ることができるのでコスト的にも有利
である。
Furthermore, the sterilizing power of the electrolytic acid water has a short duration, that is, the sterilizing power of the electrolytic acid water disappears after a certain period of time. Therefore, there is a concern that the sterilizing power of the electrolytic acid water may affect the human body. Even in this case, if the hollow fiber membrane is washed by the method of the present invention and left for a while, the sterilizing power of the electrolytic acid water completely disappears, and the purified water can be safely drunk. In addition, the electrolytic acid water can be easily prepared as long as it is a water conditioner provided with an electrolytic cell, and is therefore advantageous in terms of cost.

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

【図1】本発明の中空糸膜の洗浄方法の第1の実施の実
施形態を示すアルカリ整水器の電解アルカリ水の取水経
路の説明図である。
FIG. 1 is an explanatory diagram of a water intake path of electrolytic alkaline water of an alkaline water conditioner, showing a first embodiment of a method for cleaning a hollow fiber membrane of the present invention.

【図2】本発明の中空糸膜の洗浄方法の第1の実施の形
態を示すアルカリ整水器の中空糸膜の水道水逆洗の取水
経路の説明図である。
FIG. 2 is an explanatory view of a water intake path of tap water back washing of the hollow fiber membrane of the alkaline water purifier, showing the first embodiment of the method for cleaning a hollow fiber membrane of the present invention.

【図3】本発明の中空糸膜の洗浄方法の第1の実施の形
態を示すアルカリ整水器の中空糸膜の電解酸性水逆洗の
取水経路の説明図である。
FIG. 3 is an explanatory diagram of a water intake path for backwashing of the hollow fiber membrane of the alkaline water purifier with electrolytic acidic water, showing the first embodiment of the method for cleaning a hollow fiber membrane of the present invention.

【図4】本発明の中空糸膜の洗浄方法の第2の実施の形
態を示すアルカリ整水器の電解アルカリ水の取水経路の
説明図である。
FIG. 4 is an explanatory view of a water intake path of electrolytic alkaline water of an alkaline water conditioner, showing a second embodiment of the method for cleaning a hollow fiber membrane of the present invention.

【図5】本発明の中空糸膜の洗浄方法の第2の実施の形
態を示すアルカリ整水器の中空糸膜の水道水逆洗の取水
経路の説明図である。
FIG. 5 is an explanatory view of a water intake path of tap water backwashing of a hollow fiber membrane of an alkali water regulator, showing a second embodiment of the method for cleaning a hollow fiber membrane of the present invention.

【図6】本発明の中空糸膜の洗浄方法の第2の実施の形
態を示すアルカリ整水器の中空糸膜を電解酸性水で洗浄
する時の取水経路の説明図である。
FIG. 6 is an explanatory view of a water intake path when the hollow fiber membrane of the alkaline water purifier is washed with electrolytic acid water, showing the second embodiment of the method for cleaning a hollow fiber membrane of the present invention.

【図7】本発明の中空糸膜の洗浄方法の第1の実施の形
態のアルカリ整水器の中空糸膜を殺菌力を強化した電解
酸性水で逆洗する時の取水経路の説明図である。
FIG. 7 is an explanatory view of a water intake path when the hollow fiber membrane of the alkaline water purifier of the first embodiment of the method for cleaning a hollow fiber membrane of the present invention is backwashed with electrolytic acid water having enhanced sterilizing power. is there.

【図8】本発明の中空糸膜の洗浄方法の第2の実施の形
態のアルカリ整水器の中空糸膜を殺菌力を強化した電解
酸性水で洗浄する時の取水経路を示す。
FIG. 8 shows a water intake path when the hollow fiber membrane of the alkaline water purifier according to the second embodiment of the method for cleaning a hollow fiber membrane of the present invention is washed with electrolytic acid water having enhanced sterilizing power.

【符号の説明】[Explanation of symbols]

1,5 活性炭 2,6 中空糸膜 3,7 電解槽 11,12,13,14,15 アルカリ整水器の三方
弁 16,17,18,19,20,21 アルカリ整水器
の三方弁
1,5 Activated carbon 2,6 Hollow fiber membrane 3,7 Electrolyzer 11,12,13,14,15 Three-way valve of alkaline water regulator 16,17,18,19,20,21 Three-way valve of alkaline water regulator

───────────────────────────────────────────────────── フロントページの続き (72)発明者 福島 容子 大阪府大阪市阿倍野区長池町22番22号 シ ャープ株式会社内 (72)発明者 安部 剛夫 大阪府大阪市阿倍野区長池町22番22号 シ ャープ株式会社内 (72)発明者 田丸 理恵 大阪府大阪市阿倍野区長池町22番22号 シ ャープ株式会社内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yoko Fukushima 22-22 Nagaikecho, Abeno-ku, Osaka City, Osaka Inside Sharp Corporation (72) Inventor Takeo Abe 22-22 Nagaikecho, Abeno-ku, Osaka City, Osaka Sharp (72) Inventor Rie Tamaru 22-22 Nagaikecho, Abeno-ku, Osaka-shi, Osaka Sharp Corporation

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 中空糸膜を構成要素の一つとして持って
いる浄水部と電解水を生成する電解槽を有する整水器に
おいて、電解酸性水とその他の調整水を、浄水処理をし
ている時と逆の方向から、中空糸膜に連続して通水する
ことを特徴とする中空糸膜の洗浄方法。
In a water purifier having a water purification section having a hollow fiber membrane as one of its constituent elements and an electrolytic tank for producing electrolytic water, electrolytic acid water and other conditioned water are subjected to water purification treatment. A method for cleaning a hollow fiber membrane, comprising continuously passing water through the hollow fiber membrane from a direction opposite to the direction in which the hollow fiber membrane is located.
【請求項2】 中空糸膜を構成要素の一つとして持って
いる浄水部と電解水を生成する電解槽を有する整水器に
おいて、中空糸膜を洗浄するための調整水を、最初に浄
水処理をしている時と逆の方向から中空糸膜に通水し、
次に浄水処理をしている時と同じ方向から電解酸性水を
通水することを特徴とする中空糸膜の洗浄方法。
2. In a water purifier having a water purification section having a hollow fiber membrane as one of the constituent elements and an electrolysis tank for producing electrolyzed water, firstly, conditioned water for washing the hollow fiber membrane is purified by water purification. Water is passed through the hollow fiber membrane from the opposite direction when
Next, a method for cleaning a hollow fiber membrane, comprising passing electrolytic acid water from the same direction as during the water purification treatment.
【請求項3】 上記調整水として水道水などの原水を使
用することを特徴とする請求項1または請求項2記載の
中空糸膜の洗浄方法。
3. The method for cleaning a hollow fiber membrane according to claim 1, wherein raw water such as tap water is used as the conditioning water.
【請求項4】 上記電解酸性水のpHは2.0から6.
0の間に調整されていることを特徴とする請求項1また
は請求項2記載の中空糸膜の洗浄方法。
4. The pH of the electrolytic acidic water is 2.0 to 6.
The method for cleaning a hollow fiber membrane according to claim 1, wherein the adjustment is performed between 0 and 3.
【請求項5】 上記電解酸性水を調整する時、電解液と
して電解槽に供給される原水に食塩を添加することを特
徴とする請求項1または請求項2記載の中空糸膜の洗浄
方法。
5. The method for cleaning a hollow fiber membrane according to claim 1, wherein, when adjusting the electrolytic acid water, salt is added to raw water supplied to an electrolytic cell as an electrolytic solution.
JP35904697A 1997-12-26 1997-12-26 Washing method for hollow fiber membrane Pending JPH11188246A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35904697A JPH11188246A (en) 1997-12-26 1997-12-26 Washing method for hollow fiber membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35904697A JPH11188246A (en) 1997-12-26 1997-12-26 Washing method for hollow fiber membrane

Publications (1)

Publication Number Publication Date
JPH11188246A true JPH11188246A (en) 1999-07-13

Family

ID=18462466

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35904697A Pending JPH11188246A (en) 1997-12-26 1997-12-26 Washing method for hollow fiber membrane

Country Status (1)

Country Link
JP (1) JPH11188246A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003093848A (en) * 2001-09-21 2003-04-02 Japan Organo Co Ltd Membrane washing apparatus and membrane washing method
JP2003536057A (en) * 2000-06-09 2003-12-02 ビヨ・メリウー How to use filtration means to prepare analytical samples from very large samples
JP2005118707A (en) * 2003-10-17 2005-05-12 Ngk Insulators Ltd Water cleaning system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003536057A (en) * 2000-06-09 2003-12-02 ビヨ・メリウー How to use filtration means to prepare analytical samples from very large samples
JP4792590B2 (en) * 2000-06-09 2011-10-12 ビヨ・メリウー Use of filtration means to prepare analytical samples from very large amounts of samples
JP2003093848A (en) * 2001-09-21 2003-04-02 Japan Organo Co Ltd Membrane washing apparatus and membrane washing method
JP2005118707A (en) * 2003-10-17 2005-05-12 Ngk Insulators Ltd Water cleaning system

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