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JP2001149921A - Water treating device - Google Patents

Water treating device

Info

Publication number
JP2001149921A
JP2001149921A JP33442999A JP33442999A JP2001149921A JP 2001149921 A JP2001149921 A JP 2001149921A JP 33442999 A JP33442999 A JP 33442999A JP 33442999 A JP33442999 A JP 33442999A JP 2001149921 A JP2001149921 A JP 2001149921A
Authority
JP
Japan
Prior art keywords
residual chlorine
water
filter cartridge
time
reverse osmosis
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
JP33442999A
Other languages
Japanese (ja)
Inventor
Hiroyoshi Koyama
裕喜 小山
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.)
Organo Corp
Original Assignee
Organo Corp
Japan Organo 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 Organo Corp, Japan Organo Co Ltd filed Critical Organo Corp
Priority to JP33442999A priority Critical patent/JP2001149921A/en
Publication of JP2001149921A publication Critical patent/JP2001149921A/en
Pending legal-status Critical Current

Links

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To decide an exact replacement time of an activated carbon filter cartridge of a residual chlorine removing device used in a front stage of a pure water production device utilizing a reverse osmosis membrane. SOLUTION: This water treating device is provided with a residual chlorine meter 13 for measuring residual chlorine concentration in feed water, and an arithmetic device of a control part 30 obtains the total quantity of removed residual chlorine by the product of measured residual chlorine concentration and the feed water quantity decided by an open time of a water feed valve 11, and the integrated amount is made to a chlorine treated quantity by the filter cartridge of the residual chlorine removing device 10. When the total chlorine treated quantity is over treating performance of the filter cartridge, an alarm informing the fact is generated and the filter cartridge is exchanged. The reliability of the device and the economicity of the operation are attained by detecting the exchange time of the filter cartridge neither too earlier nor too later.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、水処理装置に関
し、特に、逆浸透膜を有する純水製造装置等の水処理装
置に好適に利用される残留塩素除去装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment apparatus, and more particularly to a residual chlorine removal apparatus suitably used for a water treatment apparatus such as a pure water production apparatus having a reverse osmosis membrane.

【0002】[0002]

【従来の技術】小型の水処理装置として、逆浸透膜を利
用する逆浸透式純水製造装置(以下、単に純水製造装置
と呼ぶ)が知られている。逆浸透膜は、水をはじめ、種
々の液体の膜分離に適用できる。小型純水製造装置に
は、合成高分子膜を浸透膜として利用し、且つ、市水を
給水として利用するものが多い。このような小型純水製
造装置では、一般に合成高分子膜は塩素等の酸化剤によ
って劣化するので、この逆浸透膜を保護する目的で、市
水中の残留塩素を除去する残留塩素除去装置を純水装置
の前段に設けている。
2. Description of the Related Art As a small water treatment apparatus, a reverse osmosis type pure water production apparatus using a reverse osmosis membrane (hereinafter simply referred to as a pure water production apparatus) is known. Reverse osmosis membranes can be applied to membrane separation of various liquids including water. Many small-sized pure water production apparatuses use a synthetic polymer membrane as a permeable membrane and use city water as water supply. In such a small-sized pure water production apparatus, a synthetic polymer membrane is generally deteriorated by an oxidizing agent such as chlorine. Therefore, in order to protect the reverse osmosis membrane, a residual chlorine removal apparatus for removing residual chlorine in city water is used. Provided before the water system.

【0003】残留塩素除去装置としては、活性炭を利用
した活性炭濾過装置、例えば活性炭フィルタカートリッ
ジが利用される。このような活性炭を利用する残留塩素
除去装置は、その処理能力に寿命があり、特に、活性炭
フィルタカートリッジは除去能力が小さいので、頻繁に
カートリッジの交換が必要となる。
[0003] As a residual chlorine removing apparatus, an activated carbon filtering apparatus using activated carbon, for example, an activated carbon filter cartridge is used. Such a residual chlorine removing apparatus using activated carbon has a long life in its processing ability. In particular, since the activated carbon filter cartridge has a small removing ability, the cartridge needs to be frequently replaced.

【0004】[0004]

【発明が解決しようとする課題】一般に、カートリッジ
等の交換時期は、装置の通水開始日から何ヶ月後に交換
を行う等、日数に基づいて管理される。しかし、純水製
造装置の稼働状況は、ユーザによって大きく異なり、ま
た、ユーザ内においても、時期によって異なる場合があ
る。更に、市水中の残留塩素濃度は、地域や日時によっ
ても大きく異なる。このため、カートリッジの交換時期
を単に日数で管理することには、処理能力以下の時点で
交換をしてカートリッジの無駄使いになったり、或い
は、処理能力以上の稼働によって逆浸透膜の劣化を生じ
たりする等の不具合があった。
Generally, the replacement time of a cartridge or the like is managed on the basis of the number of days, for example, how many months after the start of water flow of the apparatus, the replacement is performed. However, the operation status of the pure water production apparatus differs greatly depending on the user, and may also differ within the user depending on the time. Furthermore, the concentration of residual chlorine in city water varies greatly depending on the region and the date and time. For this reason, simply managing the replacement time of the cartridge by the number of days may result in wasteful use of the cartridge by replacing the cartridge at a point below the processing capacity, or deterioration of the reverse osmosis membrane due to operation exceeding the processing capacity. Troubles such as

【0005】本発明は、上記に鑑み、活性炭を利用して
市水等から残留塩素を除去する残留塩素除去装置の管理
を効果的に行うことができ、もって後段に配置される純
水製造装置等に使用される逆浸透膜の劣化を効果的に且
つ経済的に防止できる水処理装置を提供することを目的
とする。
[0005] In view of the above, the present invention can effectively manage a residual chlorine removing device that removes residual chlorine from city water or the like using activated carbon, and thus a pure water production device disposed at a subsequent stage. It is an object of the present invention to provide a water treatment apparatus that can effectively and economically prevent the degradation of a reverse osmosis membrane used for the purpose.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に、本発明の水処理装置は、給水中の残留塩素を除去す
る残留塩素除去装置を備え、該残留塩素除去装置によっ
て残留塩素が除去された給水を処理して所望の水質の水
を供給する水処理装置において、前記残留塩素除去装置
に供給される給水中の残留塩素濃度と装置の稼働時間と
に基づいて前記残留塩素除去装置による塩素処理量を演
算する演算装置と、前記演算された塩素処理量が所定値
に達した際に所定の信号を発生する信号発生装置とを備
えることを特徴とする。
In order to achieve the above object, a water treatment apparatus according to the present invention includes a residual chlorine removing apparatus for removing residual chlorine in feed water, and the residual chlorine removing apparatus removes residual chlorine. In the water treatment apparatus for processing the supplied water and supplying water of a desired quality, the residual chlorine removal apparatus based on the residual chlorine concentration in the feed water supplied to the residual chlorine removal apparatus and the operation time of the apparatus. It is characterized by comprising an arithmetic unit for calculating the amount of chlorination, and a signal generator for generating a predetermined signal when the calculated amount of chlorination reaches a predetermined value.

【0007】本発明の水処理装置によると、残留塩素除
去装置に供給される給水中の残留塩素濃度と、装置の稼
働時間とによって、残留塩素除去装置が除去した残留塩
素量が得られ、この塩素量が残留塩素除去装置の処理能
力に達した時点で信号を発生するので、直ちに残留塩素
除去装置のカートリッジ交換等のメンテナンスを行うこ
とができる。このため、後段に配設される純水製造装置
等に使用される逆浸透膜等の損傷を伴うことなく、且
つ、経済的に残留塩素除去装置を運転することが出来
る。
[0007] According to the water treatment apparatus of the present invention, the amount of residual chlorine removed by the residual chlorine removing device can be obtained by the residual chlorine concentration in the feed water supplied to the residual chlorine removing device and the operation time of the device. Since a signal is generated when the amount of chlorine reaches the processing capacity of the residual chlorine removing device, maintenance such as replacement of the cartridge of the residual chlorine removing device can be performed immediately. Therefore, the residual chlorine removing device can be economically operated without causing damage to the reverse osmosis membrane and the like used in the pure water production device and the like provided at the subsequent stage.

【0008】本発明の水処理装置は、残留塩素によって
障害が生じやすい、いかなる型式の水処理装置にも利用
でき、特に、逆浸透膜を利用した純水製造装置に用いる
ことが好ましい。ここで、給水中の残留塩素濃度は、予
め手分析等によって測定しておき、その測定値をもって
給水中の残留塩素濃度を常に一定と仮定して運転しても
よいが、通常は、残留塩素計を設置し、給水中の残留塩
素濃度を定期的に測定するのが望ましい。前記残留塩素
計は定期的に前記残留塩素濃度を測定し、前記演算装置
は、残留塩素濃度が測定された都度、これと装置の稼働
時間とに基づいて残留塩素の処理量を積算することが好
ましい。この場合、特にきめ細かな交換時期を検知する
等の管理が可能である。
[0008] The water treatment apparatus of the present invention can be used for any type of water treatment apparatus which is liable to be damaged by residual chlorine, and is particularly preferably used for a pure water production apparatus using a reverse osmosis membrane. Here, the residual chlorine concentration in the feedwater may be measured in advance by manual analysis or the like, and the measured value may be used to operate assuming that the residual chlorine concentration in the feedwater is always constant. It is desirable to install a meter and measure the residual chlorine concentration in the water supply periodically. The residual chlorine meter periodically measures the residual chlorine concentration, and each time the residual chlorine concentration is measured, the arithmetic unit may integrate the residual chlorine concentration based on the measured residual chlorine concentration and the operation time of the device. preferable. In this case, it is possible to perform management such as detecting a minutely replacement time.

【0009】[0009]

【発明の実施の形態】以下、図面を参照し本発明の実施
形態例に基づいて本発明を更に詳細に説明する。図1
は、本発明の第1の実施形態例に係る水処理装置の要部
を示すブロック図である。本水処理装置は、給水から残
留塩素を除去する活性炭フィルタカートリッジとして構
成される残留塩素除去装置10と、この残留塩素除去装
置10の後段に配設される、逆浸透膜モジュールとして
構成される純水製造装置20と、全体の制御を行う制御
部30とから構成される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail with reference to the drawings based on embodiments of the present invention. FIG.
FIG. 1 is a block diagram showing a main part of a water treatment apparatus according to a first embodiment of the present invention. The present water treatment apparatus includes a residual chlorine removing device 10 configured as an activated carbon filter cartridge for removing residual chlorine from feed water, and a pure chlorine configured as a reverse osmosis membrane module disposed downstream of the residual chlorine removing device 10. It is composed of a water production apparatus 20 and a control unit 30 for performing overall control.

【0010】残留塩素除去装置10の給水側には、給水
弁11と、給水弁11の出口配管12に接続された残留
塩素計13とが付属する。残留塩素除去装置13の出口
配管14には給水ポンプ21が接続され、残留塩素が除
去された給水は、給水ポンプ21によって逆浸透膜モジ
ュール20に供給される。逆浸透膜モジュール20は、
内部に配設された逆浸透膜によって給水を濾過し、逆浸
透膜を透過した透過水は、配管22を経由して純水の利
用場所に供給される。一方、逆浸透膜によって濃縮され
た水は、配管23を経由して廃棄される。
On the water supply side of the residual chlorine removing device 10, a water supply valve 11 and a residual chlorine meter 13 connected to an outlet pipe 12 of the water supply valve 11 are attached. A feed water pump 21 is connected to the outlet pipe 14 of the residual chlorine removing device 13, and the feed water from which the residual chlorine has been removed is supplied to the reverse osmosis membrane module 20 by the feed water pump 21. Reverse osmosis membrane module 20,
The feedwater is filtered by a reverse osmosis membrane disposed inside, and the permeated water that has passed through the reverse osmosis membrane is supplied to a pure water use location via a pipe 22. On the other hand, the water concentrated by the reverse osmosis membrane is discarded via the pipe 23.

【0011】制御部30は、純水利用場所からの制御信
号によって、本水処理装置の運転を開始し、給水弁11
を開にすると同時に給水ポンプ21を運転する。制御部
30は、所定の時間間隔をおいて残留塩素計13による
残留塩素濃度の測定を行い、これを内部の演算装置に入
力する。制御部30は、また、給水弁11の開となる時
間を累積し、残留塩素除去装置の稼働時間としている。
The control unit 30 starts operation of the water treatment apparatus according to a control signal from a pure water use place, and
Is opened and the water supply pump 21 is operated at the same time. The control unit 30 measures the residual chlorine concentration by the residual chlorine meter 13 at predetermined time intervals, and inputs this to an internal arithmetic unit. The control unit 30 also accumulates the time when the water supply valve 11 is opened, and sets the accumulated time as the operating time of the residual chlorine removing device.

【0012】残留塩素計13としては、回転微少電極ポ
ーラログラフ法を利用した残留塩素計が使用される。こ
の形式の残留塩素計は、連続的に残留塩素の濃度測定が
可能であるが、市水における残留塩素濃度の変動は緩や
かであるので、実用的には例えば1日に1回の測定で足
りる。
As the residual chlorine meter 13, a residual chlorine meter utilizing a rotary microelectrode polarographic method is used. This type of residual chlorine meter can continuously measure the concentration of residual chlorine, but since the residual chlorine concentration in city water fluctuates slowly, practically, for example, measurement once a day is sufficient. .

【0013】制御部30の演算装置は、残留塩素除去装
置のフィルタカートリッジの処理能力を、残留塩素除去
可能量として予め記憶している。演算装置は、水処理装
置の1日における給水弁開の延べ時間をその日の装置稼
働時間として記憶し、これと装置に固有の1時間当たり
の給水流量との積をその日の給水処理量とする。残留塩
素計13で測定した残留塩素濃度と、この給水処理量と
を掛け合わせたものをその日の残留塩素除去量として記
憶し、その毎日の累積量をフィルタカートリッジによる
残留塩素除去の実処理量とする。この残留塩素除去の実
処理量と、先に記憶されたフィルタカートリッジの処理
能力とを比較し、実処理量が処理能力を上回ると、その
旨の警報を発生しフィルタカートリッジの交換時期の到
来を知らせる。
The arithmetic unit of the control unit 30 stores in advance the processing capacity of the filter cartridge of the residual chlorine removing device as a residual chlorine removable amount. The arithmetic unit stores the total time of opening the water supply valve of the water treatment device in one day as the operation time of the device on that day, and uses the product of this and the water supply flow rate per hour peculiar to the device as the water supply treatment amount of the day. . The product obtained by multiplying the residual chlorine concentration measured by the residual chlorine meter 13 and the amount of the supplied water is stored as the residual chlorine removal amount for the day, and the cumulative amount for each day is calculated as the actual residual chlorine removal amount by the filter cartridge. I do. The actual processing amount of the residual chlorine removal is compared with the previously stored processing capacity of the filter cartridge. If the actual processing amount exceeds the processing capacity, an alarm to that effect is generated and the time to replace the filter cartridge arrives. Inform.

【0014】上記実施形態例の水処置装置によると、フ
ィルタカートリッジの処理能力に正確に対応するフィル
タカートリッジの交換時期を決定できるので、純水製造
装置の逆浸透膜を劣化させることなく、且つ、経済的に
その交換時期が決定できる。交換頻度は、装置の種類や
給水の水質等によっても異なるが、例えば2〜3ヶ月に
1回程度となる。
According to the water treatment apparatus of the above embodiment, the replacement time of the filter cartridge corresponding to the processing capacity of the filter cartridge can be determined accurately, so that the reverse osmosis membrane of the pure water production apparatus is not deteriorated, and The exchange time can be determined economically. The replacement frequency varies depending on the type of the apparatus, the quality of water supplied, and the like, but is, for example, about once every two to three months.

【0015】上記実施形態例では、給水量が給水弁の開
時間に比例し、また、単位時間当たりの給水流量は装置
に固有であることに着目して、給水弁の開時間を計測す
ることによって給水量の測定に代えている。掛かる構成
によって、流量計を設置することなく給水量の測定が可
能である。なお、給水弁の開時間の計測に代えて、給水
ポンプの運転時間を装置の稼働時間として計測してもよ
い。また、本実施形態例では、時間当たりの給水量は装
置に固有の処理能力量としてあるが、この給水量は、装
置に固有の処理能力量を、計測された給水圧力又はポン
プの吐出側圧力によって修正して求めてもよい。
In the above embodiment, the open time of the water supply valve is measured by paying attention to the fact that the amount of water supply is proportional to the opening time of the water supply valve and that the flow rate of water supply per unit time is unique to the apparatus. Instead of measuring water supply. With this configuration, the amount of water supply can be measured without installing a flow meter. Instead of measuring the opening time of the water supply valve, the operation time of the water supply pump may be measured as the operation time of the device. Further, in the present embodiment, the water supply amount per time is a processing capacity amount specific to the device, but this water supply amount is obtained by measuring the processing capacity amount specific to the device by the measured water supply pressure or the discharge side pressure of the pump. May be determined by correction.

【0016】残留塩素計による残留塩素濃度の測定は、
給水の性質を考慮した上で任意の時間間隔で行うことが
出来る。また、連続的な測定であってもよい。この場
合、所定値以上の変動があったときに、その都度演算装
置を動作させてそれまでの塩素処理量を求め、これを積
算する。逆浸透膜としては、例えば酢酸セルロース系膜
や合成高分子膜が好適に用いられる。また、フィルタカ
ートリッジとしては、活性炭に限らず、亜硫酸カルシウ
ム等を用いてもよい。
The measurement of the residual chlorine concentration by the residual chlorine meter is as follows.
It can be performed at arbitrary time intervals in consideration of the nature of water supply. Further, continuous measurement may be performed. In this case, when there is a change equal to or more than the predetermined value, the arithmetic unit is operated each time to obtain the amount of chlorine treatment up to that time, and this is integrated. As the reverse osmosis membrane, for example, a cellulose acetate membrane or a synthetic polymer membrane is suitably used. Further, the filter cartridge is not limited to activated carbon, but may be calcium sulfite or the like.

【0017】以上、本発明をその好適な実施形態例に基
づいて説明したが、本発明の水処理装置は、上記実施形
態例の構成にのみ限定されるものではなく、上記実施形
態例の構成から種々の修正及び変更を施したものも、本
発明の範囲に含まれる。
Although the present invention has been described based on the preferred embodiment, the water treatment apparatus of the present invention is not limited to the configuration of the above-described embodiment, but the configuration of the above-described embodiment. Various modifications and changes made from are also included in the scope of the present invention.

【0018】また、上述の実施形態例では、給水中の残
留塩素濃度を水処理装置に組み込まれた残留塩素計13
によって測定したが、残留塩素計13を省略し、給水中
の残留塩素濃度を適宜の手段で予め測定しておき、その
測定値を用いて、給水中の残留塩素濃度を一定として運
転してもよい。
In the above-described embodiment, the residual chlorine concentration in the feed water is measured by the residual chlorine meter 13 incorporated in the water treatment apparatus.
The residual chlorine meter 13 is omitted, the residual chlorine concentration in the feedwater is measured in advance by appropriate means, and the residual chlorine concentration in the feedwater is kept constant by using the measured value. Good.

【0019】[0019]

【発明の効果】以上、説明したように、本発明の水処理
装置によると、後段の装置に対して残留塩素に起因する
影響を与えることなく、残留塩素除去装置のメンテナン
スの時期を残留塩素除去装置自身の処理能力に合わせて
正確に決定できるので、水処理装置の運転に際して、そ
の信頼性を損なうことなく、且つ、経済的に運転できる
効果がある。
As described above, according to the water treatment apparatus of the present invention, the maintenance of the residual chlorine removing apparatus can be performed without affecting the subsequent apparatus due to the residual chlorine. Since the water treatment apparatus can be accurately determined in accordance with the processing capacity of the apparatus itself, there is an effect that the water treatment apparatus can be operated economically without impairing its reliability.

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

【図1】本発明の一実施形態例に係る水処理装置のブロ
ック図。
FIG. 1 is a block diagram of a water treatment apparatus according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10:残留塩素除去装置 11:給水弁 12:給水弁出口配管 13:残留塩素計 14:残留塩素除去装置出口配管 20:純水製造装置 21:給水ポンプ 22:透過水配管 23:濃縮水配管 30:制御部 10: Residual chlorine removing device 11: Water supply valve 12: Water supply valve outlet piping 13: Residual chlorine meter 14: Residual chlorine removing device outlet piping 20: Pure water production device 21: Water supply pump 22: Permeated water piping 23: Concentrated water piping 30 : Control unit

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 給水中の残留塩素を除去する残留塩素除
去装置を備え、該残留塩素除去装置によって残留塩素が
除去された給水を処理して所望の水質の水を供給する水
処理装置において、 前記残留塩素除去装置に供給される給水中の残留塩素濃
度と装置の稼働時間とに基づいて前記残留塩素除去装置
による塩素処理量を演算する演算装置と、前記演算され
た塩素処理量が所定値に達した際に所定の信号を発生す
る信号発生装置とを備えることを特徴とする水処理装
置。
1. A water treatment device comprising a residual chlorine removing device for removing residual chlorine in feed water, wherein the water treatment device supplies the water having a desired quality by treating the feed water from which the residual chlorine has been removed by the residual chlorine removing device. An arithmetic unit for calculating the amount of chlorination by the residual chlorine removal device based on the residual chlorine concentration in the feed water supplied to the residual chlorine removal device and the operation time of the device; and the calculated chlorination amount is a predetermined value. And a signal generating device for generating a predetermined signal when the temperature reaches a predetermined value.
JP33442999A 1999-11-25 1999-11-25 Water treating device Pending JP2001149921A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33442999A JP2001149921A (en) 1999-11-25 1999-11-25 Water treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33442999A JP2001149921A (en) 1999-11-25 1999-11-25 Water treating device

Publications (1)

Publication Number Publication Date
JP2001149921A true JP2001149921A (en) 2001-06-05

Family

ID=18277289

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33442999A Pending JP2001149921A (en) 1999-11-25 1999-11-25 Water treating device

Country Status (1)

Country Link
JP (1) JP2001149921A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008007741A1 (en) * 2006-07-12 2008-01-17 Toyota Jidosha Kabushiki Kaisha Fuel cell system
WO2008007740A1 (en) * 2006-07-12 2008-01-17 Toyota Jidosha Kabushiki Kaisha Fuel cell system
JP2009019773A (en) * 2007-07-13 2009-01-29 Schwaebische Huettenwerke Automotive Gmbh & Co Kg Adjustment valve for adjusting supply volume of positive displacement pump
JP2009037830A (en) * 2007-08-01 2009-02-19 Aisin Seiki Co Ltd Fuel cell system
WO2011105566A1 (en) * 2010-02-26 2011-09-01 株式会社日立製作所 Seawater desalting system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008007741A1 (en) * 2006-07-12 2008-01-17 Toyota Jidosha Kabushiki Kaisha Fuel cell system
WO2008007740A1 (en) * 2006-07-12 2008-01-17 Toyota Jidosha Kabushiki Kaisha Fuel cell system
JP2008021499A (en) * 2006-07-12 2008-01-31 Toyota Motor Corp Fuel cell system
US8808932B2 (en) 2006-07-12 2014-08-19 Toyota Jidosha Kabushiki Kaisha Fuel cell system
JP2009019773A (en) * 2007-07-13 2009-01-29 Schwaebische Huettenwerke Automotive Gmbh & Co Kg Adjustment valve for adjusting supply volume of positive displacement pump
JP2009037830A (en) * 2007-08-01 2009-02-19 Aisin Seiki Co Ltd Fuel cell system
WO2011105566A1 (en) * 2010-02-26 2011-09-01 株式会社日立製作所 Seawater desalting system

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