[go: up one dir, main page]

JP2001281240A - Water turbidity analyzer - Google Patents

Water turbidity analyzer

Info

Publication number
JP2001281240A
JP2001281240A JP2000094458A JP2000094458A JP2001281240A JP 2001281240 A JP2001281240 A JP 2001281240A JP 2000094458 A JP2000094458 A JP 2000094458A JP 2000094458 A JP2000094458 A JP 2000094458A JP 2001281240 A JP2001281240 A JP 2001281240A
Authority
JP
Japan
Prior art keywords
water
hollow fiber
fiber membrane
quality measuring
sample
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
JP2000094458A
Other languages
Japanese (ja)
Inventor
Yuji Okayasu
祐司 岡安
Akira Shirasaki
亮 白崎
Hiroaki Tanaka
宏明 田中
Kazuyuki Taguchi
和之 田口
Yoshiharu Tanaka
良春 田中
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.)
Fuji Electric Co Ltd
National Research and Development Agency Public Works Research Institute
Original Assignee
Public Works Research Institute
Fuji Electric 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 Public Works Research Institute, Fuji Electric Co Ltd filed Critical Public Works Research Institute
Priority to JP2000094458A priority Critical patent/JP2001281240A/en
Publication of JP2001281240A publication Critical patent/JP2001281240A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

(57)【要約】 【課題】下、排水の各処理プロセスの放流水や河川水、
湖沼水などの環境水の水質監視において、特に溶解性成
分の計測を目的とした水質計測器を使用する場合、試料
中の砂や泥、塵などの濁質が装置内の配管に蓄積し、配
管の閉塞やそれに伴う装置の故障が発生する恐れがあ
る。本発明は、これらの課題を解決した水質計測器を提
供することにある。 【解決手段】水質計測器の前処理部に外圧式中空糸膜モ
ジュールを用いる。さらに、中空糸膜内部にエアを注入
しろ液を逆流させて膜面に付着した濁質を取り除く中空
糸膜モジュールの洗浄機構、配管および本体水槽内に堆
積した砂、泥などを取り除く排泥機構や、藻類が繁殖し
ないように遮光したサンプル水槽などを設け、水質計測
器に安定に試料を供給する。
(57) [Summary] [Problem] Discharged water and river water in each wastewater treatment process,
When monitoring the quality of environmental water such as lake water, especially when using a water quality measuring instrument to measure soluble components, turbidity such as sand, mud, and dust in the sample accumulates in the piping in the device, There is a possibility that the blockage of the pipe and the accompanying failure of the device may occur. An object of the present invention is to provide a water quality measuring instrument that solves these problems. An external pressure type hollow fiber membrane module is used for a pretreatment unit of a water quality measuring instrument. In addition, a washing mechanism for the hollow fiber membrane module that removes suspended matter adhering to the membrane surface by injecting air into the inside of the hollow fiber membrane to reverse the filtrate, and a sludge removing mechanism for removing sand, mud, etc. accumulated in the piping and the main tank. In addition, a sample water tank that is shielded from light to prevent algae from breeding is provided, and a sample is stably supplied to a water quality measuring instrument.

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、 上下水道や排水の
各処理プロセスの水や河川水、湖沼水などの環境水を対
象として、水中の化学成分をモニタリングすること目的
とした水質計測器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water quality measuring instrument for monitoring the chemical components in water for environmental water such as water, river water, lake water, and the like in water, water and wastewater treatment processes. .

【0002】[0002]

【従来の技術】下、排水の各処理プロセスの放流水や河
川水、湖沼水などの環境水の水質監視は水道水源として
の安全性や環境保全という観点から非常に重要である。
その中で現在、水質監視を自動で行う水質計測器が開発
され、実際に適用されている。このような水質計測器と
しては、pH計や伝導度計、遊離塩素計、溶存酸素計、
アンモニア計、UV式有機汚濁計、化学的酸素要求量
(COD)計、全有機炭素(TOC)計、バイオセンサ
を利用した毒物モニタなどがあげられる。
2. Description of the Related Art Monitoring of the quality of environmental water such as effluent water, river water, lake water and the like in each wastewater treatment process is very important from the viewpoint of safety as a tap water source and environmental conservation.
Currently, a water quality measuring instrument for automatically monitoring water quality has been developed and actually applied. Such water quality measuring instruments include pH meter, conductivity meter, free chlorine meter, dissolved oxygen meter,
Examples include an ammonia meter, a UV organic pollution meter, a chemical oxygen demand (COD) meter, a total organic carbon (TOC) meter, and a toxic monitor using a biosensor.

【0003】実際に下、排水の各処理プロセスの放流水
や河川水、湖沼水などの環境水を測定する場合、試料中
に含まれる砂や泥、塵などの濁質を取り除く前処理が必
要である。従来、積層した砂や不織布で試料をろ過し、
濁質を取り除く装置が使用されてきたが、10μm以下
の濁質を除去しきれず、各水質計測器の配管が閉塞して
しまうことや、砂や不織布の補充または交換に手間がか
かるという欠点があった。
In practice, when measuring environmental water such as effluent water, river water, lake water, etc. in each wastewater treatment process, it is necessary to perform a pretreatment to remove turbid substances such as sand, mud, and dust contained in the sample. It is. Conventionally, the sample is filtered with laminated sand or nonwoven fabric,
Devices that remove turbidity have been used. However, they cannot remove turbidity of 10 μm or less, block the piping of each water quality measuring instrument, and have the drawback that it takes time to replenish or replace sand or nonwoven fabric. there were.

【0004】[0004]

【発明が解決しようとする課題】下、排水の各処理プロ
セスの放流水や河川水、湖沼水などの環境水の水質監視
において、特に溶解性成分の計測を目的とした水質計測
器を使用する場合、試料中の砂や泥、塵などの濁質が装
置内の配管に蓄積し、配管の閉塞やそれに伴う装置の故
障が発生する恐れがある。
SUMMARY OF THE INVENTION In monitoring the quality of discharged water, river water, lake water, and other environmental water in each wastewater treatment process, a water quality measuring instrument specifically for measuring soluble components is used. In such a case, turbid substances such as sand, mud, and dust in the sample may accumulate in the piping in the device, which may cause blockage of the piping and a resulting failure of the device.

【0005】本発明は、上記課題を解決するためになさ
れたものであり、水質計測器に安定に試料を供給するこ
とを目的とする。
The present invention has been made to solve the above-mentioned problem, and has as its object to stably supply a sample to a water quality measuring instrument.

【0006】[0006]

【課題を解決するための手段】本発明では、上記課題を
解決するため、請求項1に示すように、サンプル水槽の
前後に設けられ、河川水や地下水などの水道原水や下、
排水処理プロセスの流入水中の化学物質を計測する水質
計測器の前処理部としての除濁装置において、外圧式中
空糸膜モジュールに通水して吸引ろ過するように構成す
るものとする。
According to the present invention, in order to solve the above-mentioned problems, as set forth in claim 1, it is provided before and after a sample water tank to supply raw water such as river water or groundwater, or under water.
A turbidity removal device as a pretreatment unit of a water quality measuring device that measures a chemical substance in the influent water of the wastewater treatment process is configured to pass water through the external pressure type hollow fiber membrane module and perform suction filtration.

【0007】中空糸膜によるろ過方式には、中空糸膜内
部から外部へ向けて試料をろ過する内圧式と中空糸膜外
部から内部へ向け試料をろ過をする外圧式とがある。
下、排水の各処理プロセスの放流水や河川水、湖沼水な
どの環境水といった砂や泥などの濁質の多い試料をろ過
するため、内圧式の中空糸膜では、中空糸膜内部が濁質
ですぐに閉塞してしまう。そこで、本発明では、濁質の
多い試料でも長期間ろ過性能が維持できる外圧式の孔径
0.1μmの中空糸膜モジュールを採用する。
[0007] The filtration method using the hollow fiber membrane includes an internal pressure type in which the sample is filtered from the inside of the hollow fiber membrane to the outside and an external pressure type in which the sample is filtered from the outside of the hollow fiber membrane to the inside.
In order to filter samples with high turbidity such as sand and mud such as effluent water from each wastewater treatment process, river water, and lake water, etc., the internal pressure type hollow fiber membrane has turbidity inside the hollow fiber membrane. Blocks quickly with quality. Therefore, in the present invention, an external pressure type hollow fiber membrane module having a pore diameter of 0.1 μm which can maintain the filtration performance for a long period of time even for a sample having a large amount of turbidity is adopted.

【0008】次に、請求項2に示すように、中空糸膜内
部にエアを注入し、ろ液を逆流させて膜面に付着した濁
質を取り除く中空糸膜モジュールの洗浄機構を設けるこ
ととする。中空糸膜モジュールの表面に付着した濁質を
取り除く洗浄法として、中空糸膜モジュールの下部よ
りエアポンプで気泡を発生させ中空糸膜モジュールを振
動させ膜面に付着した濁質を取り除く方法と、中空糸
膜モジュール内部にエアポンプによりエアを注入し、膜
面に付着した濁質を取り除く方法との2通りがあり、一
般に下、排水の各処理プロセスの放流水や河川水、湖沼
水などの環境水中にはの方法が採用されている。しか
し、前記の環境水中には鉄イオンが多く含まれ、の洗
浄方法では水中の鉄イオンが気泡中の酸素により酸化さ
れて酸化鉄となり、この微粒子が中空糸膜上の微細孔に
入り込み、中空糸膜が早期に目詰まりを起こしてしま
う。そのため、頻繁にクエン酸等の薬液洗浄を行うかま
たは交換しなければならないといった問題があった。本
発明の水質計測器用除濁装置の中空糸膜モジュールの洗
浄機構では、の洗浄方法を採用する。
Next, as set forth in claim 2, air is injected into the hollow fiber membrane, and a washing mechanism is provided for the hollow fiber membrane module for removing the turbidity adhering to the membrane surface by causing the filtrate to flow backward. I do. As a cleaning method for removing turbidity adhered to the surface of the hollow fiber membrane module, a method of generating air bubbles from the lower part of the hollow fiber membrane module with an air pump and vibrating the hollow fiber membrane module to remove turbidity adhered to the membrane surface, There are two methods: removing air adhering to the membrane surface by injecting air into the fiber membrane module with an air pump. Generally, environmental water such as effluent water from each treatment process of wastewater, river water, lake water, etc. The method of is adopted. However, the environmental water contains a lot of iron ions, and in the washing method, iron ions in the water are oxidized by oxygen in bubbles to form iron oxide, and these fine particles enter micropores on the hollow fiber membrane and become hollow. The thread membrane is clogged early. Therefore, there has been a problem that the chemical solution such as citric acid must be frequently cleaned or replaced. In the cleaning mechanism of the hollow fiber membrane module of the water turbidity measuring device of the present invention, the following cleaning method is adopted.

【0009】また、請求項3に示すように、配管および
本体水槽内に堆積した砂、泥などを取り除く排泥機構を
設けることとする。装置の保守面での性能を向上させる
ために、試料を装置に送水する配管と中空糸膜モジュー
ルを収める本体水槽に堆積する砂や泥などの濁質を除去
する目的で、配管の途中に水道水を供給する配管と砂や
泥などの濁質を排出するドレインを設ける。また、本体
水槽の洗浄時に水槽底部に堆積した砂や泥などの濁質が
ドレインに排出されやすくするために、水槽底面を傾斜
させた構造とする。
According to a third aspect of the present invention, there is provided a sludge discharging mechanism for removing sand, mud and the like accumulated in the pipe and the main body water tank. In order to improve the performance of the equipment in terms of maintenance, in order to remove suspended matter such as sand and mud that accumulates in the piping that feeds the sample to the equipment and the main water tank that holds the hollow fiber membrane module, water is supplied in the middle of the piping. A pipe for supplying water and a drain for discharging suspended matter such as sand and mud will be provided. Further, the bottom of the water tank is inclined so that turbid substances such as sand and mud deposited on the bottom of the water tank when the main body water tank is washed are easily discharged to the drain.

【0010】なお、サンプル水槽は遮光し、サンプル水
槽内に藻類などが繁殖できない構造とするのが好適であ
る。
It is preferable that the sample tank is shielded from light and has a structure in which algae and the like cannot propagate in the sample tank.

【0011】[0011]

【発明の実施の形態】本発明の実施例を図1に示す。水
質計用除濁装置は、中空糸膜モジュール1を収納した本
体水槽2とエアポンプ3、試料ろ過用吸引ポンプ4、圧
力センサ5、2方切換え3方電磁弁7、制御部8、ドレ
インバルブ9、10などから構成され、除濁されたろ液
はサンプル水槽6に送られた後、図2に示すように水質
計測器に送られる。
FIG. 1 shows an embodiment of the present invention. The water turbidimeter decontamination device includes a main body water tank 2 containing a hollow fiber membrane module 1, an air pump 3, a sample filtration suction pump 4, a pressure sensor 5, a two-way switching three-way solenoid valve 7, a controller 8, a drain valve 9. , 10 and the like, and the clarified filtrate is sent to the sample tank 6 and then sent to the water quality measuring device as shown in FIG.

【0012】動作は、試料を中空糸膜モジュール1を通
して一定時間試料ろ過用吸引ポンプ4で吸引し、そのろ
液をサンプル水槽6に送る。制御部8のタイマによりろ
過と中空糸膜モジュール1の洗浄が交互に行われる。ろ
過された試料は各水質計測器に送り測定が行われる。こ
のとき、2方切換え3方電磁弁7の試料ろ過用吸引ポン
プ4側は開け、エアポンプ3側を閉じる。また、ドレイ
ンバルブ9の本体水槽2側は開け、ドレイン側は閉じ、
ドレインバルブ10は閉じる。
In operation, the sample is sucked through the hollow fiber membrane module 1 by the sample filtration suction pump 4 for a certain period of time, and the filtrate is sent to the sample water tank 6. Filtration and cleaning of the hollow fiber membrane module 1 are alternately performed by a timer of the control unit 8. The filtered sample is sent to each water quality measuring device to be measured. At this time, the sample filtration suction pump 4 side of the two-way switching three-way solenoid valve 7 is opened, and the air pump 3 side is closed. In addition, the main body water tank 2 side of the drain valve 9 is opened, the drain side is closed,
The drain valve 10 closes.

【0013】図3に中空糸膜モジュールの洗浄方式によ
る中空糸膜モジュールの寿命の違いを示す。縦軸は吸引
圧(Pa )を示し、中空糸膜モジュールが目詰まりの
目安となる。この値が大きくなることは中空糸膜モジュ
ールが目詰まりを起こしていることを示している。破線
は中空糸膜モジュールの下部よりエアポンプで気泡を発
生させ中空糸膜モジュールを振動させ膜面に付着した濁
質を取り除く方法、以下洗浄法、実線は中空糸膜モジ
ュール内部にエアポンプによりエアを注入し、膜面に付
着した濁質を取り除く方法、以下洗浄法を示す。本発
明で使用した中空糸膜モジュールの使用限界は吸引圧約
70kPa であり、洗浄法では約1ヶ月で中空糸膜
モジュールが使用できなくなったのに対し、洗浄法で
は1年以上連続して使用できることがわかった。そこ
で、本発明では洗浄法を採用する。
FIG. 3 shows the difference in the life of the hollow fiber membrane module depending on the method of cleaning the hollow fiber membrane module. The vertical axis is the suction pressure (Pa ) Indicates that the hollow fiber membrane module is a measure of clogging. An increase in this value indicates that the hollow fiber membrane module is clogged. The broken line is a method in which air bubbles are generated from the lower part of the hollow fiber membrane module by an air pump to vibrate the hollow fiber membrane module to remove suspended matter adhered to the membrane surface. Then, a method for removing turbidity adhering to the membrane surface, and a washing method will be described below. The use limit of the hollow fiber membrane module used in the present invention is a suction pressure of about 70 kPa. It was found that the hollow fiber membrane module could not be used in about one month in the cleaning method, but could be used continuously for one year or more in the cleaning method. Therefore, the present invention employs a cleaning method.

【0014】中空糸膜モジュール1の洗浄は、2方切換
え3方電磁弁7の試料ろ過用吸引ポンプ4側を閉じ、エ
アポンプ3側を開きエアポンプ3を作動させ、中空糸膜
モジュール1内部にエア数秒間を注入し、内部のろ液を
逆流させて膜面に付着した濁質を取り除く。また、圧力
センサ5 で中空糸膜モジュール1の目詰まりの指標とな
る試料ろ過用吸引ポンプ4の吸引圧力を常時測定してい
る。もし、設定値以上の吸引圧力となった場合、自動的
に中空糸膜モジュール1の洗浄が行われる。
When the hollow fiber membrane module 1 is washed, the two-way switching three-way solenoid valve 7 is closed on the sample filtration suction pump 4 side, the air pump 3 side is opened, and the air pump 3 is operated. Inject for a few seconds and reverse the internal filtrate to remove turbidity adhering to the membrane surface. The pressure sensor 5 constantly measures the suction pressure of the sample filtration suction pump 4, which is an index of clogging of the hollow fiber membrane module 1. If the suction pressure exceeds the set value, the hollow fiber membrane module 1 is automatically cleaned.

【0015】試料を装置に送水する配管の洗浄は、ドレ
インバルブ9の本体水槽2側を閉じ、ドレイン側を開け
ここに水道水を流して行われる。また、本体水槽2の底
部の洗浄は、ドレインバルブ10とドレインバルブ9の
本体水槽2側を開け、水道水を流して行われる。サンプ
ル水槽6は、図2に示すように空気中の塵が混入しない
ようにふた61により密閉し、さらに藻類の繁殖を防ぐ
ため遮光フィルム60により遮光することにより、長期
間サンプル水槽内の汚れの生成が防止でき、水質計測器
の配管を藻類による閉塞をさせることもなく、安定にろ
過された試料を供給できる。
Washing of a pipe for feeding a sample to the apparatus is performed by closing the main body water tank 2 side of the drain valve 9, opening the drain side, and flowing tap water therethrough. Cleaning of the bottom of the main body water tank 2 is performed by opening the main body water tank 2 side of the drain valves 10 and 9 and flowing tap water. As shown in FIG. 2, the sample tank 6 is sealed with a lid 61 so that dust in the air does not enter, and is shielded from light by a light-shielding film 60 to prevent the growth of algae. Generation can be prevented, and a stable filtered sample can be supplied without blocking the piping of the water quality measuring instrument with algae.

【0016】[0016]

【発明の効果】本発明の水質計測器用除濁装置は、下、
排水の各処理プロセスの放流水や河川水、湖沼水などの
環境水の水質監視において試料中の砂や泥などの濁質を
効率よく取り除くことができ、水質計測器の配管の閉塞
やそれに伴う装置の故障を防ぐことができるので、特に
溶解性成分の計測を目的とした水質計測器に使用でき
る。
According to the present invention, the clarifier for a water quality measuring instrument is as follows.
In monitoring the quality of discharged water, river water, lake water, and other environmental water in each wastewater treatment process, turbidity such as sand and mud in the sample can be efficiently removed. Since the failure of the device can be prevented, it can be used particularly for a water quality measuring instrument for measuring a soluble component.

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

【図1】本発明の水質計測器用除濁装置の構成図FIG. 1 is a configuration diagram of a water turbidity measuring device of the present invention.

【図2】本発明の水質計測器用除濁装置のサンプル水槽
の概略図
FIG. 2 is a schematic diagram of a sample water tank of the clarifier for a water quality measuring instrument of the present invention.

【図3】洗浄方式による中空糸膜モジュールの寿命の違
いを示す図
FIG. 3 is a diagram showing a difference in the life of a hollow fiber membrane module depending on a cleaning method.

【符号の説明】[Explanation of symbols]

1: 中空糸膜モジュール 2: 本体水槽 3: エアポンプ 4: 試料ろ過用吸引ポンプ 5: 圧力センサ 6: サンプル水槽 7: 2方切換え3方電磁弁 8: 制御部 9、10: ドレインバルブ 60: 遮光フィルム 61: ふた 1: hollow fiber membrane module 2: main body water tank 3: air pump 4: sample filtration suction pump 5: pressure sensor 6: sample water tank 7: two-way switching three-way solenoid valve 8: control unit 9, 10: drain valve 60: light shielding Film 61: Lid

───────────────────────────────────────────────────── フロントページの続き (72)発明者 白崎 亮 茨城県つくば市大字旭1番地 建設省土木 研究所内 (72)発明者 田中 宏明 茨城県つくば市大字旭1番地 建設省土木 研究所内 (72)発明者 田口 和之 神奈川県横須賀市長坂2−2−1 株式会 社富士電機総合研究所内 (72)発明者 田中 良春 神奈川県横須賀市長坂2−2−1 株式会 社富士電機総合研究所内 Fターム(参考) 4D006 GA07 HA02 HA19 HA93 JA67A KC03 KC14 KE08Q KE22Q KE23Q KE24Q KE28Q MA01 MA22 PA01 PB04 PB05 PB08 PC80  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Ryo Shirasaki, 1st Asahi, Asahi, Tsukuba, Ibaraki Prefecture Inside the Public Works Research Institute, Ministry of Construction (72) Inventor Hiroaki Tanaka 1st Asahi, Asahi, Tsukuba City, Ibaraki Prefecture, Inside the Public Works Research Institute, Ministry of Construction (72) Inventor Kazuyuki Taguchi 2-2-1 Nagasaka, Yokosuka City, Kanagawa Prefecture Inside Fuji Electric Research Institute, Inc. (72) Inventor Yoshiharu Tanaka 2-2-1 Nagasaka, Yokosuka City, Kanagawa Prefecture F-term in Fuji Electric Research Institute, Inc. (Reference) 4D006 GA07 HA02 HA19 HA93 JA67A KC03 KC14 KE08Q KE22Q KE23Q KE24Q KE28Q MA01 MA22 PA01 PB04 PB05 PB08 PC80

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】サンプル水槽の前後に設けられ、河川水や
地下水などの水道原水や下、排水処理プロセスの流入水
中の化学物質を計測する水質計測器の前処理部としての
除濁装置において、外圧式中空糸膜モジュールに通水し
て吸引ろ過するように構成したことを特徴とする水質計
測器用除濁装置。
1. A turbidity removal device as a pretreatment unit of a water quality measuring device provided before and after a sample water tank and measuring chemical substances in raw water of tap water such as river water and groundwater, and inflow water of a wastewater treatment process, A turbidity separator for a water quality measuring instrument, wherein water is passed through an external pressure type hollow fiber membrane module to perform suction filtration.
【請求項2】請求項1に記載の水質計測器用除濁装置に
おいて、前記中空糸膜内部にエアを注入し、ろ液を逆流
させて膜面に付着した濁質を取り除く中空糸膜モジュー
ルの洗浄機構を備えたことを特徴とする水質計測器用除
濁装置。
2. The hollow fiber membrane module according to claim 1, wherein air is injected into the hollow fiber membrane to reverse the filtrate to remove turbidity adhering to the membrane surface. A clarifier for a water quality measuring instrument, comprising a washing mechanism.
【請求項3】請求項1または2に記載の水質計測器用除
濁装置において、配管および本体水槽内に堆積した砂、
泥などを取り除く排泥機構を備えたことを特徴とする水
質計測器用除濁装置。
3. The water turbidity measuring device according to claim 1, wherein the sand deposited in the pipe and the main body water tank is provided.
A clarifier for water quality measuring instruments, comprising a sludge discharging mechanism for removing mud and the like.
JP2000094458A 2000-03-30 2000-03-30 Water turbidity analyzer Pending JP2001281240A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000094458A JP2001281240A (en) 2000-03-30 2000-03-30 Water turbidity analyzer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000094458A JP2001281240A (en) 2000-03-30 2000-03-30 Water turbidity analyzer

Publications (1)

Publication Number Publication Date
JP2001281240A true JP2001281240A (en) 2001-10-10

Family

ID=18609506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000094458A Pending JP2001281240A (en) 2000-03-30 2000-03-30 Water turbidity analyzer

Country Status (1)

Country Link
JP (1) JP2001281240A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006242749A (en) * 2005-03-03 2006-09-14 Toshiba Corp Pretreatment equipment for water quality measurement
JP2008032691A (en) * 2006-06-29 2008-02-14 Fuji Electric Systems Co Ltd Water quality monitoring system and water quality monitoring method
WO2015146626A1 (en) * 2014-03-27 2015-10-01 栗田工業株式会社 Preprocessing device for online measurement in water system, online measurement device provided with same, and processing method for online measurement
WO2019142402A1 (en) * 2018-01-17 2019-07-25 住友電気工業株式会社 Filtration device and method for washing hollow fiber membrane
CN114624412A (en) * 2022-05-17 2022-06-14 湖南省水产科学研究所 Water quality monitoring device for mixed culture of shrimps and crabs in rice field

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006242749A (en) * 2005-03-03 2006-09-14 Toshiba Corp Pretreatment equipment for water quality measurement
JP2008032691A (en) * 2006-06-29 2008-02-14 Fuji Electric Systems Co Ltd Water quality monitoring system and water quality monitoring method
WO2015146626A1 (en) * 2014-03-27 2015-10-01 栗田工業株式会社 Preprocessing device for online measurement in water system, online measurement device provided with same, and processing method for online measurement
JP2015188769A (en) * 2014-03-27 2015-11-02 栗田工業株式会社 Pretreatment device for online measurement in water system, online measurement device equipped with the same, and pretreatment method for online measurement
WO2019142402A1 (en) * 2018-01-17 2019-07-25 住友電気工業株式会社 Filtration device and method for washing hollow fiber membrane
CN114624412A (en) * 2022-05-17 2022-06-14 湖南省水产科学研究所 Water quality monitoring device for mixed culture of shrimps and crabs in rice field
CN114624412B (en) * 2022-05-17 2022-08-02 湖南省水产科学研究所 Water quality monitoring device for mixed culture of shrimps and crabs in rice field

Similar Documents

Publication Publication Date Title
JP2008032691A (en) Water quality monitoring system and water quality monitoring method
JP4920990B2 (en) Separation membrane cleaning method
CN101475247A (en) Short process flow water treatment technology with hyperfiltration as core and integrated with multiple water purifying technologies
JPWO2012077506A1 (en) Chemical cleaning method for submerged membrane elements
JP3290555B2 (en) Washing method of immersion type membrane cartridge in tank
JP2000140585A (en) Operation of membrane separation apparatus, and membrane separation apparatus
JP2001281240A (en) Water turbidity analyzer
KR100358167B1 (en) An equipment and method for the automatic backwashing of activated carbon process
JP3773337B2 (en) Operation method of organic sewage treatment equipment
KR101309990B1 (en) Water treatment apparatus comprising settling membrane separation tank and water treatment method using thereof
JPH11169851A (en) Water filtration apparatus and method of operating the same
KR101693100B1 (en) Smart Membrane-Filteration Water Treating System
KR100463251B1 (en) Purified system having electro dialysis
JP5059469B2 (en) Method for treating treated water containing iron
JP3333086B2 (en) Water treatment equipment
KR20130080588A (en) Water treatment system of silicon wastewater and method of the same
JP2002119808A (en) Precoat membrane filtration method and apparatus
KR101415678B1 (en) Membrane separation activated sewage treatment method and treatment device
KR101711796B1 (en) Apparatus for sewage treatment using membrane
KR200292228Y1 (en) Reverse osmosis type water treatment system for cold or hot water which have valve means for purifying used water
KR100983312B1 (en) Apparatus for reusing sewage waste water using separation membrane and ozone
CN222024208U (en) A sewage deep treatment device that can both disinfect and remove SS
KR200364038Y1 (en) Advanced drinking water purification system by membrain filtration equipment using demanganese tower
KR200404753Y1 (en) Water quality improvement using fill material of mattress filter
JP7222055B1 (en) MEMBRANE FILTER AND METHOD FOR CLEANING MEMBRANE FILTER

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20051213

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A711

Effective date: 20080317

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20080319

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20080606

RD03 Notification of appointment of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7423

Effective date: 20080606

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080716

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20081111

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20090407