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JP2008032691A - Water quality monitoring system and water quality monitoring method - Google Patents

Water quality monitoring system and water quality monitoring method Download PDF

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JP2008032691A
JP2008032691A JP2007147231A JP2007147231A JP2008032691A JP 2008032691 A JP2008032691 A JP 2008032691A JP 2007147231 A JP2007147231 A JP 2007147231A JP 2007147231 A JP2007147231 A JP 2007147231A JP 2008032691 A JP2008032691 A JP 2008032691A
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water
biosensor
water quality
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cleaning
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Takashi Inui
貴誌 乾
Katsuji Yokoyama
勝治 横山
Yoshiharu Tanaka
良春 田中
Hideo Kanai
秀夫 金井
Nobuhisa Kato
修久 加藤
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Fuji Electric Co Ltd
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Fuji Electric Systems Co Ltd
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本発明は、河川や上下水道などの水を対象として、水中の有害物質などの化学成分をモニタリングする水質監視システムおよび水質監視方法に関する。   The present invention relates to a water quality monitoring system and a water quality monitoring method for monitoring chemical components such as harmful substances in water for water such as rivers and water and sewage systems.

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。現在、水質監視を自動で行う水質計測器が開発され、実際に適用され始めている。このような水質計測器としては、pH計、伝導度計、遊離塩素計、濁度計、着色度計、溶存酸素(DO)計、酸化還元電位(ORP)計、アンモニア計、硝酸イオン計、リン酸イオン計、全窒素/全リン(T−N/T−P)計、汚泥濃度(MLSS)計、UV式有機汚濁計、化学的酸素要求量(COD)計、生物学的酸素要求量(BOD)計、全有機炭素(TOC)計、揮発性有機化合物(VOC)計、(MLSS)計、バイオセンサなどが挙げられる。   Monitoring of the quality of environmental water such as effluent from each treatment process of sewage and river water and lake water is very important from the viewpoint of safety as a tap water source and environmental conservation. Currently, water quality measuring instruments that automatically monitor water quality have been developed and are actually being applied. As such a water quality measuring instrument, a pH meter, a conductivity meter, a free chlorine meter, a turbidity meter, a coloring meter, a dissolved oxygen (DO) meter, a redox potential (ORP) meter, an ammonia meter, a nitrate ion meter, Phosphate ion meter, total nitrogen / total phosphorus (TN / TP) meter, sludge concentration (MLSS) meter, UV organic pollution meter, chemical oxygen demand (COD) meter, biological oxygen demand (BOD) meter, total organic carbon (TOC) meter, volatile organic compound (VOC) meter, (MLSS) meter, biosensor and the like.

なお、本明細書において、「バイオセンサ」とは、試料水中の測定対象化学物質を認識する分子識別素子であって、酵素や抗体などの生体機能性材料や微生物、細胞など生体そのものを利用し、これらの生物材料を多孔性高分子膜に化学的に包括または共有結合させることにより固定化した膜と、電気化学的検出器などのトランスデューサとを組み合わせて生物材料の分子識別信号を電気信号に変換して、試料水中に含まれる種々の化学物質の測定を行うセンサを意味する。バイオセンサは、試料水を生物材料の固定化膜に接触させ、これによって生ずる生化学反応により生成または消費される物質の濃度変化を検出器で電流や電圧などの電気的な出力(以下、「センサ出力」という)の変化に変換して測定する。例えば、特許文献1には、水中の有害物質検出を目的としたバイオセンサ応用毒物モニタが記載されている。   In this specification, a “biosensor” is a molecular identification element that recognizes a chemical substance to be measured in sample water, and uses biological functional materials such as enzymes and antibodies, and living organisms such as microorganisms and cells. The biomaterial molecular identification signal is converted into an electrical signal by combining a membrane in which these biological materials are chemically encapsulated or covalently bonded to a porous polymer membrane and a transducer such as an electrochemical detector. It means a sensor that converts and measures various chemical substances contained in sample water. A biosensor is a method in which sample water is brought into contact with an immobilized membrane of biological material, and a concentration change of a substance generated or consumed by a biochemical reaction caused thereby is detected by an electric output (hereinafter referred to as “current” or “voltage”). It is converted to a change in sensor output) and measured. For example, Patent Document 1 describes a biosensor-applied toxic monitor for the purpose of detecting harmful substances in water.

このような水質監視において、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、水質計測器の配管閉塞やポンプ等の送液装置故障防止のため、試料水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、不織布、あるいはスクリーンで試料水をろ過し、濁質を取り除く、除濁装置が使用されてきたが、このような除濁装置では、10μm以下の濁質を除去しきれないという問題があった。   In such water quality monitoring, especially when using a water quality measuring device for the purpose of measuring soluble components, in order to prevent clogging of piping of the water quality measuring device and failure of a liquid feeding device such as a pump, Pretreatment is necessary to remove turbidity such as mud and dust. Conventionally, a turbidity removal device has been used that removes turbidity by filtering sample water with laminated sand, nonwoven fabric, or screen, but such turbidity removal device cannot remove turbidity of 10 μm or less. There was a problem.

そのため、常時試料水を通水し、連続監視を行う水質計測器においては、例えば、特許文献2に記載されているような、サブマイクロメーターオーダーの阻止粒径を持つろ過膜を用いた膜ろ過装置を使用する必要がある。しかしながら、上記膜ろ過装置は、雨天時や雪解け時の河川、湖沼水、あるいは下排水といった濁質の負荷が高い水を処理する場合、ろ過膜表面の目詰まりにより、ろ過性能が極めて悪くなり、処理水量が低下したり、処理水の水質が低下したりすることがある。よって、後段の水質計測器の測定値が変動したり、測定不能状態となったりするという問題がある。   For this reason, in a water quality measuring instrument that continuously passes sample water and performs continuous monitoring, for example, a membrane filtration using a filtration membrane having a submicrometer order blocking particle size as described in Patent Document 2 It is necessary to use the device. However, when the above membrane filtration device treats water with high turbidity load such as rivers, lake water, or sewage when it rains or melts, the filtration performance becomes extremely bad due to clogging of the filtration membrane surface, The amount of treated water may decrease or the quality of treated water may deteriorate. Therefore, there is a problem that the measured value of the water quality measuring device at the latter stage fluctuates or becomes unable to be measured.

そこで、膜ろ過装置への濁質負荷を低減するため、サブミリメーターオーダーの粒径を持つ濁質を除去可能な、スクリーンや不織布を用いた除濁装置を膜ろ過装置の前段に併設することが望ましい。また、膜ろ過装置の自動保守運転方法として、エアあるいは水道水による逆流洗浄、膜表面のエアスクラビング、試料水にポンプやプロペラ等の機械的手段で上方ないし側方水流を付与し、そのせん断力による膜表面の洗浄、ろ過水槽の水道水洗浄等が検討されている(非特許文献1)。   Therefore, in order to reduce the load of turbidity on the membrane filtration device, a turbidity removal device using a screen or non-woven fabric that can remove turbidity with a particle size on the order of submillimeters can be installed in front of the membrane filtration device. desirable. In addition, automatic maintenance operation methods for membrane filtration devices include backwashing with air or tap water, air scrubbing on the membrane surface, and applying upward or lateral water flow to the sample water by mechanical means such as a pump or propeller, and its shear force. Cleaning of the membrane surface by water, tap water cleaning of filtration water tanks, etc. have been studied (Non-Patent Document 1).

さらに、試料水中の濁質による配管閉塞・装置故障以外の測定妨害要因として、カルシウムイオン等の硬度成分の析出や大気中の雑菌繁殖による配管閉塞やセンサ素子表面汚染が挙げられる。この場合、濁質のようなろ過膜による除去は困難なため、特許文献3に記載されているような、装置内の薬液洗浄等の化学的除去法、あるいは、特許文献4や特許文献5に記載されているような、ワイパー、ジェット水流による汚染部位の洗浄等の物理的除去法が検討されている。
特公平7-85072号公報 特開2001-281240号公報 特開2000-146893号公報 特開平9-54076号公報 特開平7-181130号公報 イヌイ・ティ(Inui T)、外3名,「硝化細菌バイオセンサを用いた有害物質監視の下水道システムへの適用(Application of toxicity monitor using nitrifying bacteria biosensor to sewerage systems)」,ウォータ・サイエンス・アンド・テクノロジ(Water science and technology),2002年,第45巻,第4/5号,p.271−278
Furthermore, measurement obstruction factors other than pipe blockage due to turbidity in the sample water and device failure include precipitation of hardness components such as calcium ions, pipe blockage due to bacterial growth in the air, and sensor element surface contamination. In this case, since removal with a filtration membrane such as turbidity is difficult, a chemical removal method such as chemical solution cleaning in the apparatus as described in Patent Document 3, or Patent Document 4 and Patent Document 5 As described, physical removal methods such as cleaning of contaminated sites with a wiper or a jet water stream are being studied.
Japanese Patent Publication No. 7-85072 JP 2001-281240 A JP 2000-146893 A JP-A-9-54076 JP-A-7-181130 Inui T, 3 others, “Application of toxicity monitor using nitrifying bacteria biosensor to sewerage systems”, Water Science and Technology (Water science and technology), 2002, 45, 4/5, p. 271-278

上記のような除濁機能を持つ前処理装置と水質計測器を用いて、濁質負荷の高い試料水の溶解性成分について安定した連続監視を継続するには、保守作業の簡易化、保守頻度の低減等が求められる。また、装置の導入にあたっては、保守費用の低減が求められる。しかしながら、保守頻度を低減するために、前処理装置を1か月以上連続運転すると、前処理装置では、例えば、ろ過膜表面への汚泥堆積量が多くなり、手作業による洗浄作業に多大な時間を要するという問題がある。また、例えば、ろ過膜内での雑菌繁殖による目詰まりのため、膜表面に堆積した汚泥を除去しただけではろ過膜を再使用できない場合があるという問題がある。そのため、保守頻度が高くなることにより、保守費用が増大し、装置導入が困難な状況となっていた。   In order to continue stable continuous monitoring of the soluble components of sample water with high turbidity load using the pretreatment device and water quality measuring instrument with the turbidity function as described above, the maintenance work is simplified and the maintenance frequency is reduced. Reduction is required. In addition, the introduction of the device requires a reduction in maintenance costs. However, if the pretreatment device is continuously operated for one month or more in order to reduce the maintenance frequency, the pretreatment device, for example, increases the amount of sludge deposited on the surface of the filtration membrane, which requires a lot of time for manual cleaning work. There is a problem that requires. Further, for example, there is a problem that the filtration membrane may not be reused only by removing the sludge accumulated on the membrane surface due to clogging due to propagation of various bacteria in the filtration membrane. For this reason, the maintenance frequency increases, so that the maintenance cost increases and it is difficult to introduce the apparatus.

また、バイオセンサでは、長期間連続運転している間に、固定化膜の表面上に析出物や生物性の汚れが付着する。これら析出物や生物性の汚れの付着量が増加すると、センサ出力が低下し、有害物質を検出するのに必要な検出感度が得られなくなり、有害物質を正確に検出することができなくなる。そのため、バイオセンサのセンサ出力の校正を行って、センサ出力が低下しても有害物質が正確に検出できるようにしている。また、センサ出力が一定の値よりも低下した場合は、固定化膜を交換する必要があり、試料水中に雑菌や析出物が多く含まれている場合はその頻度が多くなり、費用が増加するという問題がある。   In addition, in the biosensor, precipitates and biological dirt adhere to the surface of the immobilized membrane during continuous operation for a long period of time. When the amount of deposits and biological dirt attached increases, the sensor output decreases, the detection sensitivity necessary for detecting the harmful substances cannot be obtained, and the harmful substances cannot be detected accurately. For this reason, the sensor output of the biosensor is calibrated so that harmful substances can be accurately detected even if the sensor output decreases. Also, if the sensor output falls below a certain value, it is necessary to replace the immobilized membrane. If the sample water contains many germs and precipitates, the frequency will increase and the cost will increase. There is a problem.

そこで本発明は、上記の問題点に鑑み、簡易な保守作業で、且つ低減された保守頻度および費用で、水質監視システムを長期にわたって連続的に運転することができる水質監視システムおよび水質監視方法を提供することを目的とする。   In view of the above problems, the present invention provides a water quality monitoring system and a water quality monitoring method capable of continuously operating a water quality monitoring system over a long period of time with simple maintenance work and reduced maintenance frequency and cost. The purpose is to provide.

上記の目的を達成するために、本発明に係る水質監視システムは、監視対象となる水源から試料水を連続的に採取する採水装置と、この採水装置で採取した試料水中の濁質を連続的に除去する前処理装置と、この前処理装置で前処理された試料水中の有害物質を連続的に検出する水質計測器と、この水質計測器の定期的な校正の間、前記採水装置の運転を停止するとともに、前記水質計測器への試料水の通水を停止し、前記前処理装置または前記水質計測器を洗浄するように制御する運転制御装置とを備えたことを特徴とするものである。   In order to achieve the above object, a water quality monitoring system according to the present invention includes a water sampling device that continuously collects sample water from a water source to be monitored, and turbidity in the sample water collected by the water sampling device. A pretreatment device for continuous removal; a water quality measuring device for continuously detecting harmful substances in the sample water pretreated by the pretreatment device; and during the periodic calibration of the water quality measuring device, An operation control device for stopping the operation of the apparatus, stopping the flow of the sample water to the water quality measuring instrument, and controlling the pretreatment device or the water quality measuring instrument to be washed. To do.

前記前処理装置としては、試料水中の汚濁を膜でろ過する膜分離手段と、この膜分離手段と前記水質計測器との間の試料水が流れる部分に水を流して洗浄を行う第1の洗浄手段とを備えたものが好ましい。この場合、前記運転制御装置は、前記水質計測器の定期的な校正の間、前記第1の洗浄手段を運転するように制御することが好ましい。   As the pretreatment device, a membrane separation means for filtering the contamination in the sample water with a membrane, and a cleaning is performed by flowing water through a portion where the sample water flows between the membrane separation means and the water quality measuring instrument. What provided the washing | cleaning means is preferable. In this case, it is preferable that the operation control device performs control so that the first cleaning unit is operated during the periodic calibration of the water quality measuring instrument.

前記水質計測器としては、バイオセンサと、このバイオセンサ内の試料水が流れる部分に水または空気を流して洗浄を行う第2の洗浄手段とを備えたものが好ましい。この場合、前記運転制御装置としては、前記バイオセンサの定期的な校正で異常と判断した場合に、第2の洗浄手段を運転するように制御することが好ましい。   The water quality measuring instrument preferably includes a biosensor and a second cleaning unit that performs cleaning by flowing water or air through a portion of the biosensor in which sample water flows. In this case, it is preferable that the operation control device performs control so that the second cleaning unit is operated when it is determined that there is an abnormality in the periodic calibration of the biosensor.

本発明は、別の態様として、水質監視方法であって、監視対象となる水源から採水装置にて試料水を連続的に採取し、この採取した試料水中の濁質を前処理装置で連続的に除去し、この前処理された試料水中の有害物質を水質計測器で連続的に検出する水質監視工程と、前記水質計測器の定期的な校正の間、前記採水装置の採水運転を停止し、前記水質計測器への試料水の通水を停止し、前記前処理装置または前記水質計測器を洗浄する校正工程とを含むことを特徴とする。   Another aspect of the present invention is a water quality monitoring method, in which sample water is continuously collected from a water source to be monitored by a water collection device, and turbidity in the collected sample water is continuously collected by a pretreatment device. The water sampling operation of the water sampling apparatus during the water quality monitoring step of continuously detecting harmful substances in the pre-treated sample water with a water quality measuring instrument and the periodic calibration of the water quality measuring instrument And a calibration step of stopping the water flow of the sample water to the water quality measuring instrument and washing the pretreatment device or the water quality measuring instrument.

前記前処理装置は、試料水中の汚濁を膜でろ過する膜分離手段を備えるものが好ましく、前記校正工程は、前記膜分離手段と前記水質計測器との間の試料水が流れる部分に水を流して洗浄を行う第1の洗浄を行うことを含むことが好ましい。   The pretreatment device is preferably provided with a membrane separation means for filtering the contamination in the sample water with a membrane, and the calibration step is performed by supplying water to a portion where the sample water flows between the membrane separation means and the water quality measuring instrument. It is preferable to include performing the 1st washing | cleaning which flows and wash | cleans.

前記水質計測器は、バイオセンサを備えるものが好ましく、前記校正工程は、前記バイオセンサの校正において異常と判断した場合、前記バイオセンサ内の試料水が流れる部分に水または空気を流して洗浄を行う第2の洗浄を行うことを含むことが好ましい。   The water quality measuring instrument is preferably equipped with a biosensor, and when the calibration process determines that there is an abnormality in the calibration of the biosensor, the sample is washed by flowing water or air through the portion where the sample water flows in the biosensor. It is preferable to include performing the 2nd washing | cleaning to perform.

また、本発明に係る水質監視システムは、別の形態として、監視対象となる水源から試料水を連続的に採取する採水装置と、この採水装置で採取した試料水中の有害物質を連続的に検出するバイオセンサであって、微生物を固定した膜と溶存酸素を測定する溶存酸素電極とを備えたバイオセンサと、このバイオセンサ内の試料水が流れる部分に水または空気を流して洗浄を行う洗浄手段と、このバイオセンサを定期的に校正する際、センサ出力の低下により異常と判断した場合に、前記洗浄手段を運転するように制御する運転制御装置とを備えたことを特徴とする。   Further, the water quality monitoring system according to the present invention, as another form, continuously collects a water sampling device that continuously collects sample water from a water source to be monitored, and harmful substances in the sample water collected by this water sampling device. In this biosensor, a biosensor equipped with a membrane to which microorganisms are fixed and a dissolved oxygen electrode for measuring dissolved oxygen is washed, and water or air is passed through a portion where the sample water flows in the biosensor for cleaning. A cleaning unit that performs the cleaning, and an operation control device that controls the cleaning unit to operate when it is determined to be abnormal due to a decrease in sensor output when the biosensor is periodically calibrated. .

また、本発明に係る水質監視方法は、別の形態として、監視対象となる水源から採水装置にて試料水を連続的に採取し、この採取した試料水中の有害物質を、微生物を固定した膜と溶存酸素を測定する溶存酸素電極とを備えたバイオセンサで連続的に検出する水質監視工程と、前記バイオセンサを定期的に校正する際、センサ出力の低下により異常と判断した場合に、このバイオセンサ内の試料水が流れる部分に水または空気を流して洗浄する校正工程とを含むことを特徴とする。   Further, the water quality monitoring method according to the present invention, as another form, continuously collects sample water from a water source to be monitored with a water sampling device, and fixes microorganisms to harmful substances in the collected sample water. A water quality monitoring step for continuously detecting with a biosensor having a membrane and a dissolved oxygen electrode for measuring dissolved oxygen, and when calibrating the biosensor periodically, when it is judged abnormal due to a decrease in sensor output, And a calibration step of washing by flowing water or air in a portion where the sample water flows in the biosensor.

このように、水質監視システムを長期にわたって連続的に運転しても、水質計測器を定期的に校正する間、採水装置の運転を停止するとともに、前処理装置または水質計測器を洗浄することで、採水装置内の濁質の一部が重力により脱離し、濁質の蓄積を防止できるとともに、前処理装置内または水質計測器内での雑菌の繁殖を防止することができる。よって、下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の水質監視システムに要求される、保守作業の簡易化、保守頻度および費用の低減が可能であり、濁質負荷の高い試料水の場合においても、水質計測器への試料水の安定供給、および水質計測器の測定精度の維持が容易に可能となる。   In this way, even if the water quality monitoring system is operated continuously over a long period of time, the water sampling device should be stopped and the pretreatment device or the water quality measuring device washed while the water quality measuring device is periodically calibrated. Thus, part of the turbidity in the water sampling apparatus is detached due to gravity, and accumulation of turbidity can be prevented, and propagation of germs in the pretreatment apparatus or the water quality measuring instrument can be prevented. Therefore, it is possible to simplify the maintenance work, reduce the frequency and cost of maintenance required for the water quality monitoring system of each sewage treatment process, environmental water such as river water, lake water, etc. Even in the case of high sample water, the stable supply of sample water to the water quality measuring instrument and the maintenance of the measurement accuracy of the water quality measuring instrument can be easily performed.

特に、前処理装置の洗浄として、前処理装置の膜分離手段と水質計測器との間の試料水が流れる部分に水を流して洗浄を行う第1の洗浄を行うことで、バイオセンサを汚染する雑菌の温床となっている部分を定期的に洗浄することができ、水質計測器の測定精度を、簡易な保守作業で、且つ少ない保守頻度および保守費用で、容易に維持することができる。   In particular, as the cleaning of the pretreatment device, the biosensor is contaminated by performing the first washing in which the sample water flows between the membrane separation means of the pretreatment device and the water quality measuring device to perform the washing. Therefore, it is possible to periodically wash the portion that is a hotbed of various germs, and to easily maintain the measurement accuracy of the water quality measuring instrument with simple maintenance work and with less maintenance frequency and maintenance cost.

さらに、前処理装置内で繁殖した雑菌がバイオセンサ内に流入して滞留し、測定精度が低下することがあるが、現行の水質計測器の自動洗浄機構はバイオセンサ周辺の配管の硬度成分付着防止を目的とした酸洗浄のみであり、バイオセンサ内のセンサ素子表面の薬液洗浄といった化学的自動洗浄は、バイオセンサで用いる微生物の脆弱性のため不可能であり、測定精度を復帰させることが困難である。そのため、雑菌繁殖場所となっている前処理装置の洗浄頻度を高くする必要があるが、その間は試料水を通水しないため、測定の連続性が失われたり、上記洗浄後に洗浄水がバイオセンサに通水されると、バイオセンサが有害物質流入時と同様の応答を示して誤警報を発したりするという問題がある。そこで、バイオセンサが校正で異常と判断された場合、バイオセンサ内の試料水が流れる部分に水または空気を流して洗浄を行う第2の洗浄を行うことで、バイオセンサ内に滞留する雑菌の他、同様にセンサ出力を低下させる析出物や生物性の汚れを物理的に除去することができ、測定精度を維持することができる。   In addition, germs that have propagated in the pretreatment device may flow into and stay in the biosensor, reducing the measurement accuracy. However, the automatic cleaning mechanism of the current water quality measuring instrument adheres to the hardness component of the piping around the biosensor. It is only acid cleaning for the purpose of prevention, and chemical automatic cleaning such as chemical cleaning of the sensor element surface in the biosensor is impossible due to the vulnerability of microorganisms used in the biosensor, and the measurement accuracy can be restored. Have difficulty. Therefore, it is necessary to increase the cleaning frequency of the pretreatment device that is a breeding place for bacteria, but during that time sample water is not passed, so the continuity of measurement is lost, or the cleaning water is washed after the cleaning. When the water is passed through the biosensor, there is a problem in that the biosensor shows a response similar to that at the time of inflow of harmful substances and issues a false alarm. Therefore, when the biosensor is determined to be abnormal by calibration, the second cleaning is performed by flowing water or air through the portion where the sample water in the biosensor flows, so that the germs staying in the biosensor can be removed. In addition, it is possible to physically remove precipitates and biological stains that similarly reduce the sensor output, and maintain measurement accuracy.

また、微生物膜と溶存酸素電極とを備えたバイオセンサにおいて、長期間連続運転している間に、微生物膜の表面上に析出物や生物性の汚れが付着し、酸素の通過量が減少することから、溶存酸素電極で測定される酸素量が減少し、センサ出力が低下する。このセンサ出力の低下は、バイオセンサを定期的に校正する際に、その校正値から検知することができる。そして、センサ出力が異常であると判断した場合に、バイオセンサ内の試料水が流れる部分に水または空気を流すことで、析出物や生物性の汚れが除去され、センサ出力を元の状態に戻すことができる。よって、微生物膜を交換すべき値までセンサ出力が低下するのを防ぐことができ、保守頻度を少なくし、費用を低減することができる。また、微生物膜に供給する酸素の量を維持できることから、微生物の寿命低下を防止し、この点からも費用を低減することができる。   In addition, in a biosensor equipped with a microbial membrane and a dissolved oxygen electrode, precipitates and biological dirt adhere to the surface of the microbial membrane during continuous operation for a long period of time, reducing the amount of oxygen passing through. For this reason, the amount of oxygen measured by the dissolved oxygen electrode is reduced, and the sensor output is reduced. This decrease in sensor output can be detected from the calibration value when the biosensor is periodically calibrated. When it is determined that the sensor output is abnormal, the precipitate or biological dirt is removed by flowing water or air through the portion of the biosensor where sample water flows, and the sensor output is restored to the original state. Can be returned. Therefore, it is possible to prevent the sensor output from being lowered to a value at which the microbial membrane should be replaced, to reduce the maintenance frequency and to reduce the cost. In addition, since the amount of oxygen supplied to the microbial membrane can be maintained, it is possible to prevent a decrease in the life of the microbial organism and to reduce costs in this respect.

以下、添付図面を参照して、本発明に係る水質監視システムおよび水質監視方法の一実施の形態について説明する。図1は、本発明に係る水質監視システムの一実施の形態の概略的な構成を示す模式図である。図2は、図1中に示すバイオセンサの内部構造を示す模式図である。図3は、図2中に示す微生物膜と溶存酸素電極の構成を示す模式図である。図4は、図1中に示すバイオセンサの周辺構成を示す模式図である。   Hereinafter, an embodiment of a water quality monitoring system and a water quality monitoring method according to the present invention will be described with reference to the accompanying drawings. FIG. 1 is a schematic diagram showing a schematic configuration of an embodiment of a water quality monitoring system according to the present invention. FIG. 2 is a schematic diagram showing the internal structure of the biosensor shown in FIG. FIG. 3 is a schematic diagram showing the configuration of the microbial membrane and the dissolved oxygen electrode shown in FIG. FIG. 4 is a schematic diagram showing a peripheral configuration of the biosensor shown in FIG.

図1に示すように、本実施の形態の水質監視システムは、監視対象となる水源から試料水を採取する採水装置1と、試料水中から濁質を除去する前処理装置2と、試料水中の有害物質を検出する水質計測器3と、水質監視システムの運転を自動的に制御する運転制御装置4とから主に構成される。   As shown in FIG. 1, the water quality monitoring system of the present embodiment includes a water sampling device 1 that collects sample water from a water source to be monitored, a pretreatment device 2 that removes turbidity from the sample water, and sample water. It is mainly composed of a water quality measuring device 3 that detects the harmful substances and an operation control device 4 that automatically controls the operation of the water quality monitoring system.

(1.採水装置)
採水装置1としては、水中ポンプが用いられる。採水装置1は連続的に水源から試料水を採取し、前処理装置2に通水する。なお、採水装置1は、常時運転を行うと、水中ポンプ内の流路に濁質が次第に蓄積することにより流路が閉塞し、採水停止となり、多大な労力を要する水中ポンプ内部の保守作業を行わなければならない場合がある。そこで、水質計測器3が定期的な校正を行っている間は試料水を水質計測器3に通水する必要がないことから、上記の校正中は採水装置1の運転を停止し、間欠運転とすることで、ポンプ内の濁質の一部を重力により脱離させることができ、保守頻度を低下させることができる。
(1. Water sampling device)
As the water sampling apparatus 1, a submersible pump is used. The water sampling device 1 continuously collects sample water from the water source and passes the sample water through the pretreatment device 2. In addition, when the water sampling apparatus 1 is always operated, turbidity gradually accumulates in the flow path in the submersible pump, which closes the flow path, stops water sampling, and maintenance of the submersible pump requires much labor. You may have to do work. Therefore, since it is not necessary to pass the sample water through the water quality measuring instrument 3 while the water quality measuring instrument 3 performs the periodic calibration, the operation of the water sampling apparatus 1 is stopped during the above calibration, and intermittently. By setting the operation, a part of the turbidity in the pump can be desorbed by gravity, and the maintenance frequency can be reduced.

(2.前処理装置)
前処理装置2は、膜ろ過装置11と、その前段のスクリーン12とから主に構成される。このように2段の構成にすることで、膜ろ過装置11の濁質負荷を低減でき、保守頻度を低下することができる。なお、監視対象となる水源の濁質負荷が低い場合は、スクリーン12を設けずに、膜ろ過装置11単体の構成にしてもよい。
(2. Pretreatment device)
The pretreatment device 2 is mainly composed of a membrane filtration device 11 and a screen 12 at the preceding stage. Thus, by setting it as a 2 step | paragraph structure, the turbid load of the membrane filtration apparatus 11 can be reduced, and a maintenance frequency can be reduced. In addition, when the turbidity load of the water source to be monitored is low, the screen 12 may not be provided and the configuration of the membrane filtration device 11 alone may be used.

スクリーン12には、防食性の高いステンレス等の材料が使用され、ろ過面には横方向のスリットが形成される。スクリーン12では、採水装置1からの試料水をスクリーン12の上部に導水し、スクリーンのろ過面上を自然落下させることにより、固液分離が行われる。ろ過面上に補足された濁質は、水流および重力によりスクリーン排水槽71に落下して排出される。一方、ろ過水は、スクリーン12内部のスクリーンろ過水槽72に貯水される。スクリーンろ過水槽72内のろ過水は、給水ポンプ58により、膜ろ過装置11に供給される。スクリーンろ過水槽72内の余剰ろ過水は、オーバーフロー配管(図示省略)を経由してスクリーン排水槽71に排出される。上記スリットは0.1〜1mm幅であることが好ましい。これにより、粒径0.1〜1mm以上の濁質をろ過して除去することができる。   The screen 12 is made of a material such as stainless steel having a high anticorrosion property, and a horizontal slit is formed on the filtration surface. In the screen 12, the sample water from the water sampling device 1 is guided to the upper part of the screen 12, and solid-liquid separation is performed by allowing the sample water to fall naturally on the filtration surface of the screen. The suspended matter trapped on the filtration surface falls to the screen drainage tank 71 due to water flow and gravity and is discharged. On the other hand, the filtered water is stored in a screen filtered water tank 72 inside the screen 12. The filtrate in the screen filtration water tank 72 is supplied to the membrane filtration device 11 by the water supply pump 58. Excess filtered water in the screen filtered water tank 72 is discharged to the screen drain tank 71 via an overflow pipe (not shown). The slit is preferably 0.1 to 1 mm wide. Thereby, the suspended matter with a particle size of 0.1-1 mm or more can be filtered and removed.

スクリーン12の保守法としては、スクリーン12のろ過面裏側に取り付けたブラシ(図示省略)をモーターで常時運転、あるいはタイマーを付与して間欠運転させ、付着した濁質を除去する方法(以下、「スクリーン裏面ブラシ洗浄」という)が用いられる。さらに、水道水配管63から定期的に試料水に替えて水道水を導水し、スクリーン12のろ過面表側を洗浄する方法(以下、「スクリーン表面水道水洗浄」という)が用いられる。スクリーン表面水道水洗浄の二次的効果として、導水した水道水が後段の膜ろ過装置11の原水槽52に通水されることから、膜ろ過装置11のろ過膜表面を水道水で洗浄することが可能となる。   As a maintenance method for the screen 12, a brush (not shown) attached to the back side of the filtration surface of the screen 12 is always operated with a motor or intermittently operated with a timer to remove adhering turbidity (hereinafter, “ Screen backside brush cleaning ”is used. Further, a method of periodically guiding the tap water instead of the sample water from the tap water pipe 63 and cleaning the front side of the filtration surface of the screen 12 (hereinafter referred to as “screen surface tap water cleaning”) is used. As a secondary effect of the screen surface tap water cleaning, since the introduced tap water is passed through the raw water tank 52 of the subsequent membrane filtration device 11, the membrane surface of the membrane filtration device 11 is washed with tap water. Is possible.

膜ろ過装置11としては、ろ過膜として中空糸膜を数百本程度束ねた膜モジュール51が用いられる。この膜モジュール51は、スクリーン12からの試料水が充填される原水槽52内に配置され、膜モジュール51の一端が原水槽52のフランジ(以下、水槽フランジ54という)に取り付けられ、ろ過用ポンプ59を用いて、配管内圧を上昇させることにより、膜モジュール51を通過したろ過水が水質計測器3側に送られるように構成されている。このように、内圧型の膜モジュール51をクロスフロー方式で使用することで、下水や排水のような濁質負荷の高い試料水を適切に前処理することができる。なお、内圧型に代えて外圧型を採用してもよい。   As the membrane filtration device 11, a membrane module 51 in which several hundreds of hollow fiber membranes are bundled as a filtration membrane is used. The membrane module 51 is disposed in a raw water tank 52 filled with sample water from the screen 12, and one end of the membrane module 51 is attached to a flange of the raw water tank 52 (hereinafter referred to as a water tank flange 54). By using 59, the pipe internal pressure is increased, so that the filtered water that has passed through the membrane module 51 is sent to the water quality measuring instrument 3 side. In this way, by using the internal pressure type membrane module 51 in a cross-flow manner, sample water with a high turbidity load such as sewage and drainage can be appropriately pretreated. An external pressure type may be adopted instead of the internal pressure type.

なお、膜モジュール51は、上記の構成に限定されるものではなく、精密ろ過膜等をろ材として使用するものであれば、ろ過膜の材料および形状、ろ過方式等について各種採用できる。例えば、ろ過膜の材料は、セラミック等の無機系や、ポリアクリルニトリル、酢酸セルロース等の有機系でも良く、また形状は、チューブ状、中空糸状、平膜状、スパイラル状のいずれでも良く、ろ過方式は、クロスフロー方式または全量ろ過方式でも良い。膜モジュール51としては、粒径0.2μm以上の濁質をろ過して除去することができるものが好ましい。   The membrane module 51 is not limited to the above-described configuration, and various materials can be used for the material and shape of the filtration membrane, the filtration method, and the like as long as a microfiltration membrane or the like is used as a filter medium. For example, the material of the filtration membrane may be inorganic such as ceramic, or organic such as polyacrylonitrile or cellulose acetate, and the shape may be any of tube, hollow fiber, flat membrane, or spiral. The method may be a cross flow method or a total filtration method. The membrane module 51 is preferably one that can remove turbidity having a particle size of 0.2 μm or more by filtration.

膜モジュール51を通過したろ過水は、ろ過水配管55を介して、ろ過水槽56に貯留されるように構成されている。ろ過水配管55には、ろ過水配管55の圧力を測定する圧力計57と、ろ過水をろ過水槽56に送るろ過用ポンプ59が設けられている。また、ろ過水槽56には、ろ過水槽56内のろ過水を排出するためのオーバーフロー配管が設けられている。   The filtered water that has passed through the membrane module 51 is configured to be stored in the filtered water tank 56 via the filtered water pipe 55. The filtrate pipe 55 is provided with a pressure gauge 57 that measures the pressure of the filtrate pipe 55 and a filtration pump 59 that sends the filtrate to the filtrate tank 56. The filtered water tank 56 is provided with an overflow pipe for discharging the filtered water in the filtered water tank 56.

膜ろ過装置11の保守法としては、原水槽52内の膜モジュール51近傍に散気管53を設置し、エアポンプ61により膜表面を気泡で常時洗浄する方法(以下、「エアスクラビング」という)と、水槽フランジ54側からエアポンプ60を用いて膜内部に空気圧を付与し、膜表面に補足された濁質を逆流洗浄除去する方法(以下、「逆洗」という)とが用いられる。なお、逆洗は、空気圧に代えて水圧を用いてもよい。   As a maintenance method of the membrane filtration device 11, a method in which an air diffusion pipe 53 is installed in the vicinity of the membrane module 51 in the raw water tank 52, and the membrane surface is constantly washed with bubbles by the air pump 61 (hereinafter referred to as “air scrubbing”), A method of applying air pressure to the inside of the membrane using the air pump 60 from the water tank flange 54 side and removing the turbidity trapped on the membrane surface by backwashing (hereinafter referred to as “backwashing”) is used. The backwashing may use water pressure instead of air pressure.

さらに、膜ろ過装置11内での雑菌繁殖を防止するため、水道水を用いて雑菌の繁殖場所となる部位を定期的に洗浄する方法(以下、「ろ過装置水道水洗浄」という)が用いられる。そのため、ろ過水配管55には、ろ過水配管55内に水導水を導入するための水道水配管62が設けられ、ろ過水配管55に適宜設けられた開閉バルブと、水槽フランジ54に設けられた排水配管と、ろ過水槽56のオーバーフロー配管とにより、水槽フランジ54、ろ過水配管55およびろ過水槽56をそれぞれ別々に水道水で洗浄できるように構成されている。水槽フランジ54の排水配管と、ろ過水槽56のオーバーフロー配管とから排出された洗浄排水は、スクリーン排水槽71へと排出される。なお、洗浄に用いる水道水を導入する水道水配管62、63に対し、給水圧が高過ぎる場合は、図示しない調圧弁とニードルバルブ等の流量調整弁を設けても良い。   Furthermore, in order to prevent the propagation of germs in the membrane filtration device 11, a method of periodically washing a site that is a breeding place of germs using tap water (hereinafter referred to as "filter device tap water washing") is used. . Therefore, the filtered water pipe 55 is provided with a tap water pipe 62 for introducing the water guide water into the filtered water pipe 55, and an open / close valve provided in the filtered water pipe 55 and a water tank flange 54. The drainage pipe and the overflow pipe of the filtered water tank 56 are configured so that the water tank flange 54, the filtered water pipe 55 and the filtered water tank 56 can be separately washed with tap water. The cleaning waste water discharged from the drain pipe of the water tank flange 54 and the overflow pipe of the filtered water tank 56 is discharged to the screen drain tank 71. In addition, when supply water pressure is too high with respect to the tap water piping 62 and 63 which introduces the tap water used for washing | cleaning, you may provide flow regulating valves, such as a pressure regulating valve and a needle valve which are not shown in figure.

(3.水質計測器)
水質計測器3は、バイオセンサ13と、pH計14と、着色度計15とを組み合せることにより構成される。バイオセンサ13とpH計14を組み合せて連続監視を行うことにより、バイオセンサ13の異常警報出力時に異常原因が酸・アルカリ廃液によるものか、シアン等の有害物質によるものかを判別することができる。また、着色度計15を組み合せて連続監視を行うことにより、上記の両者では検出困難な染色剤や6価クロムといった着色成分の混入を検出することができる。なお、監視対象である水源により、水質計測器3をバイオセンサ13単体のみにしてもよい。
(3. Water quality measuring instrument)
The water quality measuring device 3 is configured by combining a biosensor 13, a pH meter 14, and a coloring degree meter 15. By performing continuous monitoring by combining the biosensor 13 and the pH meter 14, it is possible to determine whether the cause of the abnormality is due to acid / alkali waste liquid or a harmful substance such as cyan when the abnormality alarm is output from the biosensor 13. . Further, by performing continuous monitoring by combining the colorimeter 15, it is possible to detect the mixing of coloring components such as a staining agent and hexavalent chromium that are difficult to detect with both of them. Note that the water quality measuring device 3 may be a single biosensor 13 depending on the water source to be monitored.

pH計14および着色度計15をバイオセンサ13と組合せる場合、自動洗浄や自動校正機能を持ったオンライン型でも、ラボ用の簡易型でも良いが、安価にシステムを構築するには後者の方が好ましい。その場合、pH計14のガラス電極を膜ろ過装置11のろ過水槽56内に設置し、着色度計15にはろ過水槽56からチューブポンプを用いて試料水を通水するように構成する。この構成によれば、膜ろ過装置水道水洗浄時に、pH計14のガラス電極および着色度計15の測定セルを同時に水道水で洗浄することができる。また、バイオセンサ13も、ろ過水槽56からチューブポンプを用いて試料水を通水するように構成されている。   When the pH meter 14 and the color meter 15 are combined with the biosensor 13, it may be an on-line type with automatic cleaning and automatic calibration functions, or a simple type for a laboratory. Is preferred. In that case, the glass electrode of the pH meter 14 is installed in the filtered water tank 56 of the membrane filtration device 11, and the color meter 15 is configured to pass sample water from the filtered water tank 56 using a tube pump. According to this structure, the glass electrode of the pH meter 14 and the measurement cell of the color degree meter 15 can be simultaneously washed with tap water when the membrane filtration device tap water is washed. The biosensor 13 is also configured to pass sample water from the filtered water tank 56 using a tube pump.

バイオセンサ13は、図2に示すように、生体材料としては有害物質に極めて弱い微生物である硝化細菌を生きたまま固定化して高分子多孔膜で封じ込めた微生物膜21と、検出器として溶存酸素電極22とを組合せた呼吸活性検知型バイオセンサである。微生物膜21は、フローセル24内部の試料流路25を流れる試料水と接触するように構成されている。   As shown in FIG. 2, the biosensor 13 includes a microbial membrane 21 in which a nitrifying bacterium, which is a microorganism that is extremely weak against harmful substances as a biological material, is alive and is sealed in a polymer porous membrane, and dissolved oxygen as a detector. It is a respiratory activity detection type biosensor in combination with an electrode 22. The microbial membrane 21 is configured to come into contact with the sample water flowing through the sample channel 25 inside the flow cell 24.

溶存酸素電極22は、図3に示すように、微生物膜21と平行に接して配置された酸素透過膜81と、酸素透過膜81に接して配置された錨形状のカソード電極82と、カソード電極82の軸部分の側方を囲む絶縁体84と、絶縁体84の外周部に配置されたアノード電極と、絶縁体84の外周部に充填された内部液85とから構成されたガルバニ電池である。   As shown in FIG. 3, the dissolved oxygen electrode 22 includes an oxygen permeable membrane 81 arranged in contact with the microorganism membrane 21, a bowl-shaped cathode electrode 82 arranged in contact with the oxygen permeable membrane 81, and a cathode electrode The galvanic cell is composed of an insulator 84 that surrounds the side of the shaft portion of 82, an anode electrode disposed on the outer peripheral portion of the insulator 84, and an internal liquid 85 filled in the outer peripheral portion of the insulator 84. .

また、バイオセンサ13は、図4に示すように、恒温槽26内に設置されているとともに、バイオセンサ13の前段に熱交換器27が設置されているので、バイオセンサ13での測定温度を一定に保たれている。また、バイオセンサ13に各種液体や気体を別々または混合して送るように開閉バルブを備えた送風送液機構29が設置されている。   In addition, as shown in FIG. 4, the biosensor 13 is installed in the thermostatic chamber 26, and the heat exchanger 27 is installed in the previous stage of the biosensor 13, so that the temperature measured by the biosensor 13 is set. It is kept constant. Further, an air blowing / feeding mechanism 29 having an open / close valve is installed to send various liquids and gases separately or mixed to the biosensor 13.

バイオセンサ13の試料流路25には、通常、膜ろ過装置11のろ過水槽56からの試料水と、基質および必須栄養素を含んだ緩衝溶液(以下、「フィード液」という)との混合液が酸素飽和状態で送風送液機構29によって供給される。バイオセンサでは、図5に示すように、試料流路25を流れる混合液中の基質88が、微生物膜21中の硝化細菌87により硝化され、このとき混合液中の酸素89が消費される。微生物膜21を通過した酸素89の量は、溶存酸素電極22で測定される(この時のセンサ出力を「測定値」という)。   In the sample flow path 25 of the biosensor 13, a mixed solution of the sample water from the filtered water tank 56 of the membrane filtration device 11 and a buffer solution (hereinafter referred to as “feed solution”) containing a substrate and essential nutrients is usually provided. Supplied by the air blowing mechanism 29 in an oxygen saturated state. In the biosensor, as shown in FIG. 5, the substrate 88 in the mixed solution flowing through the sample flow path 25 is nitrified by the nitrifying bacteria 87 in the microorganism film 21, and oxygen 89 in the mixed solution is consumed at this time. The amount of oxygen 89 that has passed through the microbial membrane 21 is measured by the dissolved oxygen electrode 22 (the sensor output at this time is referred to as “measured value”).

このとき、混合液中に有害物質が混入していなければ、混合液中の酸素は微生物膜21でほぼ全て消費されるので、図6に示すように、酸素消費率はほぼ100%となり、溶存酸素電極22のセンサ出力は非常に低い値となる。一方、混合液中に有害物質が混入していると、硝化細菌87の活性が阻害され、酸素呼吸量が減少することから、酸素消費率は低下し、溶存酸素電極22が酸素を検出してセンサ出力が増加する。これにより試料水中に有害物質が混入しているか否かを検知することができる。   At this time, if no harmful substances are mixed in the mixed solution, almost all the oxygen in the mixed solution is consumed by the microbial membrane 21, so that the oxygen consumption rate is almost 100% as shown in FIG. The sensor output of the oxygen electrode 22 has a very low value. On the other hand, if harmful substances are mixed in the mixed solution, the activity of nitrifying bacteria 87 is inhibited and the oxygen respiration rate is reduced, so that the oxygen consumption rate is reduced and the dissolved oxygen electrode 22 detects oxygen. Sensor output increases. This makes it possible to detect whether or not harmful substances are mixed in the sample water.

また、バイオセンサ13の試料流路25には、校正のために、1日1回程度などの定期的に、純水と、基質は含まずに必須栄養素を含んだ緩衝溶液(以下、「校正液」という)との混合液が酸素飽和状態で送風送液機構29によって供給される。バイオセンサでは、混合液中に基質が含まれないので、硝化細菌は酸素をほとんど消費せず、よって、図6に示すように、酸素消費率はほぼ0%となり、溶存酸素電極のセンサ出力が大きく増加する(この時の値を「スパン校正値」という)。ここで、酸素消費率は、以下の式1により求める。
酸素消費率(%)={1−(測定中の任意のセンサ出力)/(スパン校正値)}×100・・・式1
In addition, the sample channel 25 of the biosensor 13 is periodically calibrated once a day for calibration, for example, pure water and a buffer solution that does not contain a substrate but contains essential nutrients (hereinafter referred to as “calibration”). The liquid mixture is supplied by the blowing liquid feeding mechanism 29 in an oxygen saturated state. In the biosensor, since the substrate is not contained in the mixed solution, the nitrifying bacteria consume almost no oxygen. Therefore, as shown in FIG. 6, the oxygen consumption rate is almost 0%, and the sensor output of the dissolved oxygen electrode is low. Increases greatly (this value is called “span calibration value”). Here, the oxygen consumption rate is obtained by the following formula 1.
Oxygen consumption rate (%) = {1- (arbitrary sensor output during measurement) / (span calibration value)} × 100 (1)

呼吸阻害率は、以下の式2で求める。呼吸阻害率が所定の監視閾値(例えば10%)を超えた場合に、試料水中に有害物質が検知された旨の警報を出す。
呼吸阻害率(%)={1−(有害物質混入時の酸素消費率)/(有害物質混入直前の酸素消費率)}×100・・・式2
The respiratory inhibition rate is obtained by the following formula 2. When the respiratory inhibition rate exceeds a predetermined monitoring threshold (for example, 10%), an alarm is given that a harmful substance has been detected in the sample water.
Respiration inhibition rate (%) = {1− (oxygen consumption rate when contaminated with harmful substances) / (oxygen consumption rate immediately before mixing of harmful substances)} × 100 (2)

さらに、送風送液機構29内の試料流路およびバイオセンサ13の試料流路25には、異常時に、水道水が給水圧によって供給され、これにより前記試料水路を水道水で洗浄すること(以下、「バイオセンサ水道水洗浄」という)ができるので、滞留する雑菌や、微生物膜21の表面に付着した析出物、生物性の汚れが物理的に除去され、これらに起因するセンサ出力の低下を防止することができる。   Furthermore, tap water is supplied to the sample flow path in the air blowing mechanism 29 and the sample flow path 25 of the biosensor 13 by the water supply pressure in the event of an abnormality, thereby washing the sample water path with tap water (hereinafter referred to as the tap water). , “Biosensor tap water cleaning”), the accumulated germs, the deposits attached to the surface of the microbial membrane 21 and biological dirt are physically removed, and the sensor output is reduced due to these. Can be prevented.

なお、ろ過水槽56とバイオセンサ13との間の試料水配管を洗浄するために、定期的に、この試料水配管内には、酸洗浄水が送風送液機構29によって供給され、酸洗浄が行われる。これにより配管内に硬度成分が付着するのを防止することができる。なお、酸洗浄水がバイオセンサ13の試料流路25内に流れないように、酸洗浄水の供給時には、開閉バルブ(図示省略)を切替えて酸洗浄水をバイパス流路28へと流すようにする。これによりバイオセンサ13の微生物が酸洗浄水に接触するのを避けることができる。   In addition, in order to wash | clean the sample water piping between the filtration water tank 56 and the biosensor 13, acid washing water is regularly supplied into this sample water piping by the ventilation liquid feeding mechanism 29, and acid washing is carried out. Done. Thereby, it can prevent that a hardness component adheres in piping. In order to prevent the acid cleaning water from flowing into the sample flow path 25 of the biosensor 13, when the acid cleaning water is supplied, the open / close valve (not shown) is switched so that the acid cleaning water flows to the bypass flow path 28. To do. Thereby, it is possible to avoid the microorganisms of the biosensor 13 from coming into contact with the acid cleaning water.

(4.運転制御装置)
運転制御装置4は、図7に示すように、バイオセンサのセンサ出力等の上記の各構成要素からの各種信号を読み込むアナログデジタル信号変換器46と、これらの信号に基づいて、予め設定された演算処理を行う中央演算処理装置47と、この処理結果に基づいて、上記の各構成要素に対して各種信号を発信するデジタルアナログ信号変換器48とから主に構成されている。運転制御装置4には、信号を発信する時間を設定するためのタイマー31〜42が設けられている。また、中央演算処理装置47は、受信した信号に基づいて各構成要素に命令の信号を発信するか否かの上限値または下限値AL1〜AL3を設定できるように構成されている。
(4. Operation control device)
As shown in FIG. 7, the operation control device 4 is set in advance based on analog-to-digital signal converters 46 that read various signals from the above-described components such as sensor outputs of biosensors, and these signals. A central processing unit 47 that performs arithmetic processing, and a digital-analog signal converter 48 that transmits various signals to the above-described components based on the processing results are mainly configured. The operation control device 4 is provided with timers 31 to 42 for setting a time for transmitting a signal. Further, the central processing unit 47 is configured to set an upper limit value or lower limit values AL1 to AL3 as to whether or not to send a command signal to each component based on the received signal.

運転制御装置4のタイマー31には、スクリーン12におけるスクリーン裏面ブラシ洗浄の運転間隔時間T1が設定される。この時間T1を設定すれば、スクリーン裏面ブラシ洗浄は間欠運転となり、設定しなければ常時運転となる。   In the timer 31 of the operation control device 4, an operation interval time T <b> 1 for cleaning the screen back surface brush on the screen 12 is set. If this time T1 is set, the screen back surface brush cleaning is intermittent operation, and if it is not set, it is always operated.

運転制御装置4のタイマー32には、膜ろ過装置11の逆洗時間T2が、タイマー33には膜ろ過装置11の逆洗間隔時間T3が、タイマー34には膜ろ過装置水道水洗浄時間T4が、タイマー35には膜ろ過装置水道水洗浄間隔時間T5が設定される。なお、この定期的な膜ろ過装置水道水洗浄時には、ろ過水槽56からバイオセンサ13への試料水の供給を停止するように制御する。   The timer 32 of the operation control device 4 has the backwash time T2 of the membrane filtration device 11, the timer 33 has the backwash interval time T3 of the membrane filtration device 11, and the timer 34 has the membrane filtration device tap water washing time T4. The timer 35 is set with a membrane filtration device tap water washing interval time T5. In addition, at the time of this periodic membrane filtration apparatus tap water washing, it controls so that supply of sample water from filtration water tank 56 to biosensor 13 may be stopped.

ろ過水配管55内の吸引圧を測定する圧力計57は、測定した吸引圧の値を運転制御装置4に発信するように構成されている。運転制御装置4には、保守閾値AL1が設定されており、受信した値がAL1以上となった場合、膜ろ過装置11に逆洗信号を発信する。逆洗信号を受信した膜ろ過装置11では逆洗が行われる。なお、逆洗信号が発信されると、逆洗間隔時間T3のタイマー33はリセットされる。   The pressure gauge 57 that measures the suction pressure in the filtrate water pipe 55 is configured to transmit the value of the measured suction pressure to the operation control device 4. A maintenance threshold AL1 is set in the operation control device 4, and when the received value becomes AL1 or more, a backwash signal is transmitted to the membrane filtration device 11. The membrane filtration device 11 that has received the backwash signal performs backwashing. When the backwash signal is transmitted, the timer 33 of the backwash interval time T3 is reset.

運転制御装置4のタイマー36には、バイオセンサ13の校正時間T6が、タイマー37にはバイオセンサ13の校正間隔時間T7が、タイマー38にはバイオセンサ13の酸洗浄時間T8が、タイマー39にはバイオセンサ13の酸洗浄間隔時間T9が、タイマー40にはバイオセンサ水道水洗浄時間T10が、タイマー41にはバイオセンサ水道水洗浄間隔時間T11が、タイマー42には校正完了後のバイオセンサ13の測定待ち時間T12が設定される。   The timer 36 of the operation control device 4 has a calibration time T6 of the biosensor 13, the timer 37 has a calibration interval time T7 of the biosensor 13, and the timer 38 has an acid cleaning time T8 of the biosensor 13. Is the acid cleaning interval time T9 of the biosensor 13, the timer 40 is the biosensor tap water cleaning time T10, the timer 41 is the biosensor tap water cleaning interval time T11, and the timer 42 is the biosensor 13 after calibration is completed. The measurement waiting time T12 is set.

運転制御装置4からは、定期的にバイオセンサ13の校正を行うために、校正間隔時間T7毎に、校正時間T6の間、採水装置1、前処理装置2、水質計測器3に定期校正信号が発信される。採水装置1は、この定期校正信号を受信している間、運転を停止する。前処理装置2は、定期校正信号を受信している間、スクリーン12において、スクリーン表面水道水洗浄を行うとともに、膜ろ過装置水道水洗浄時間T4のタイマー34はリセットされ、膜ろ過装置水道水洗浄を繰り返し行う。膜ろ過装置水道水洗浄は、水槽フランジ54、ろ過水配管55、ろ過水槽56の順に洗浄するが、この定期的なバイオセンサ13の校正時における膜ろ過装置水道水洗浄時間(校正時間T6)を、上記の定期的な膜ろ過装置水道水洗浄時における水道水洗浄時間T4の10倍以上に設定することが好ましい。   In order to periodically calibrate the biosensor 13, the operation control device 4 periodically calibrates the water sampling device 1, the pretreatment device 2, and the water quality measuring device 3 during the calibration time T6 at every calibration interval time T7. A signal is emitted. The water sampling apparatus 1 stops operation while receiving this periodic calibration signal. While receiving the periodic calibration signal, the pretreatment device 2 performs screen surface tap water cleaning on the screen 12, and resets the timer 34 of the membrane filtration device tap water cleaning time T4, so that the membrane filtration device tap water cleaning is performed. Repeat. Membrane filtration device tap water cleaning is performed in the order of the water tank flange 54, the filtrate water pipe 55, and the filtration water tank 56. The membrane filter device tap water cleaning time (calibration time T6) at the time of periodic calibration of the biosensor 13 is used. It is preferable to set it to 10 times or more of the tap water cleaning time T4 at the time of the above periodic membrane filtration device tap water cleaning.

水質計測器3は、定期校正信号を受信している間、校正が行われる。バイオセンサ13には、純水と校正液の混合液が供給され、図8のフローチャートに示すように、その測定値、すなわちスパン校正値が運転制御装置4に送信される。運転制御装置4には、スパン校正異常閾値AL2が設定されており、校正終了時点のスパン校正値がAL2未満の場合、運転制御装置4は、水質計測器3にバイオセンサ水道水洗浄を開始する信号を発信し、送風送液機構29内のチューブポンプを停止して、送風送液機構29およびバイオセンサ13の試料流路の洗浄を行うとともに、採水装置1および前処理装置2には、採水装置1の運転中止および膜ろ過装置水道水洗浄を維持するように信号を発信する。そして、バイオセンサ水道水洗浄時間T10経過後、水質計測器3にバイオセンサ水道水洗浄を終了する信号を発信した後、再び、採水装置1、前処理装置2、水質計測器3に定期校正信号を発信し、再度校正を行う。スパン校正値がAL2以上の場合、測定を開始し、水質監視に戻る。   The water quality measuring instrument 3 is calibrated while receiving the periodic calibration signal. The biosensor 13 is supplied with a mixture of pure water and calibration liquid, and the measured value, that is, the span calibration value is transmitted to the operation control device 4 as shown in the flowchart of FIG. When the span calibration abnormality threshold AL2 is set in the operation control device 4 and the span calibration value at the end of calibration is less than AL2, the operation control device 4 starts the biosensor tap water washing in the water quality measuring instrument 3. A signal is transmitted, the tube pump in the blast liquid feeding mechanism 29 is stopped, the sample flow paths of the blast liquid feeding mechanism 29 and the biosensor 13 are cleaned, and the water sampling device 1 and the pretreatment device 2 are A signal is transmitted so as to maintain the operation stop of the water sampling device 1 and the membrane filtration device tap water cleaning. After the biosensor tap water cleaning time T10 has elapsed, a signal for ending the biosensor tap water cleaning is transmitted to the water quality measuring instrument 3, and then periodically calibrated to the water sampling apparatus 1, the pretreatment apparatus 2, and the water quality measuring instrument 3 again. Send a signal and calibrate again. If the span calibration value is greater than AL2, start measurement and return to water quality monitoring.

なお、運転制御装置4には、上記異常時のバイオセンサ水道水洗浄の繰り返し回数の上限値AL3が設定されている。スパン校正値がAL2未満であっても、上記洗浄の繰り返し回数がAL3に到達した場合は、測定を開始し、水質監視に戻る。   In the operation control device 4, an upper limit value AL3 of the number of repetitions of the biosensor tap water cleaning at the time of the abnormality is set. Even if the span calibration value is less than AL2, if the number of repetitions of the cleaning reaches AL3, the measurement is started and the process returns to water quality monitoring.

また、スパン校正値がAL2以上で、測定を開始する際、運転制御装置4から水質計測器3に測定中断信号を発信するとともに、測定待ち時間T12のタイマー42が起動する。そして、T12の経過後に、運転制御装置4から水質計測器3に測定開始信号を発信する。校正中は膜ろ過装置水道水洗浄が行われ、ろ過水槽56内が水道水で満たされているので、これが試料水に置き換わるまでの間、すなわちT12の間、バイオセンサ13での測定を中断する。   Further, when the span calibration value is AL2 or more and measurement is started, a measurement interruption signal is transmitted from the operation control device 4 to the water quality measuring device 3, and a timer 42 with a measurement waiting time T12 is started. And a measurement start signal is transmitted to the water quality measuring device 3 from the operation control apparatus 4 after progress of T12. During calibration, the membrane filtration device tap water is washed, and the inside of the filtered water tank 56 is filled with tap water, so that the measurement with the biosensor 13 is interrupted until it is replaced with sample water, that is, during T12. .

水質監視が行われている間、有害物質が試料水中に混入して、バイオセンサ13で硝化細菌の呼吸活性が監視閾値以下に低下した場合、バイオセンサ13から運転制御装置4へ警報信号を発信する。このようにして、水質監視システムの自動保守および自動洗浄を行いながら、水質監視システムの運転を行う。   While water quality monitoring is being performed, if a harmful substance is mixed into the sample water and the respiratory activity of nitrifying bacteria falls below the monitoring threshold by the biosensor 13, an alarm signal is transmitted from the biosensor 13 to the operation control device 4. To do. In this way, the water quality monitoring system is operated while performing automatic maintenance and automatic cleaning of the water quality monitoring system.

なお、上記の実施の形態では、バイオセンサ13に繁殖した雑菌を除去するために水道水を用いたが、バイオセンサ13の表面に水道水では除去が困難な析出物や生物性の汚れが付着した場合、水道水に代えて、圧縮空気や加圧水などを用いることができる。   In the above embodiment, tap water is used to remove germs that have propagated on the biosensor 13, but deposits and biological stains that are difficult to remove with tap water adhere to the surface of the biosensor 13. In this case, compressed air or pressurized water can be used instead of tap water.

圧縮空気を用いる場合は、図9に示すように、送風送液機構29内の試料流路に空気を供給する配管に、切替バルブ93を設けて、通常運転時の系統と洗浄時の系統との2系統にし、洗浄時の系統に、空気タンク91とその出口にタンクバルブ94を配置する。このような構成によれば、通常運転時には、タンクバルブ94を閉じておき、洗浄時には、エアポンプにより空気タンク91の内圧を上昇させた後、タンクバルブ94を開くことで、圧縮空気をバイオセンサ13の試料流路25に流し、析出物や生物性の汚れ等の付着物を除去することができる。   When using compressed air, as shown in FIG. 9, a switching valve 93 is provided in a pipe for supplying air to the sample flow path in the air blowing / feeding mechanism 29, and a system for normal operation and a system for cleaning are provided. The air tank 91 and the tank valve 94 are arranged at the outlet of the system at the time of cleaning. According to such a configuration, during normal operation, the tank valve 94 is closed, and during cleaning, the internal pressure of the air tank 91 is increased by the air pump, and then the tank valve 94 is opened, whereby compressed air is supplied to the biosensor 13. It is possible to remove the deposits and deposits such as biological dirt.

加圧水を用いる場合は、図10に示すように、上記の空気タンク91に代えて、水タンク92を設置する。水タンクには水道水が供給される。このような構成によれば、通常運転時には、タンクバルブ94を閉じておき、洗浄時には、エアポンプにより水タンク92の内圧を上昇させた後、タンクバルブ94を開くことで、加圧水をバイオセンサ13の試料流路25に流し、析出物や生物性の汚れ等の付着物を除去することができる。   When using pressurized water, a water tank 92 is installed in place of the air tank 91 as shown in FIG. Tap water is supplied to the water tank. According to such a configuration, during normal operation, the tank valve 94 is closed, and during cleaning, the internal pressure of the water tank 92 is increased by an air pump, and then the tank valve 94 is opened, so that pressurized water is supplied to the biosensor 13. The sample can be passed through the sample channel 25 to remove deposits and deposits such as biological dirt.

また、上記の実施の形態では、前処理装置を用いたが、水質監視対象の水が上水道などの前処理を必要としないものである場合は、前処理装置を設置しなくてもよい。このような構成の水質監視システムであっても、長期間連続運転している間に、バイオセンサの微生物膜の表面に付着した析出物や生物性の汚れを、スパン校正の際に、水道水、加圧水または圧縮空気で除去することができるので、センサ出力の低下を防止できるとともに、微生物の寿命低下を防止でき、よって、微生物膜の交換頻度を少なくし、費用を低減することができる。   In the above embodiment, the pretreatment device is used. However, when the water whose water quality is to be monitored does not require pretreatment such as water supply, the pretreatment device need not be installed. Even with a water quality monitoring system with such a configuration, during continuous operation for a long period of time, deposits and biological dirt adhered to the surface of the biosensor's microbial membrane can be removed during tap calibration. Since it can be removed with pressurized water or compressed air, the sensor output can be prevented from being lowered and the life of the microorganism can be prevented from being lowered. Therefore, the replacement frequency of the microorganism membrane can be reduced, and the cost can be reduced.

(実施例1)
特に言及しない限り図1に示した構成と同様の水質監視システムを、下水処理場の沈砂池に設置して、以下の条件で自動保守および自動洗浄しながら連続運転して、水質監視試験を行った。
(Example 1)
Unless otherwise stated, a water quality monitoring system similar to the configuration shown in Fig. 1 is installed in a sand basin at a sewage treatment plant, and is continuously operated with automatic maintenance and automatic cleaning under the following conditions to conduct a water quality monitoring test. It was.

採水装置1として水中ポンプを使用し、流量約50L/分に調整してスクリーン12に試料水を導水した。スクリーン12のろ過面スリット幅を0.5mm、スクリーン表面水道水洗浄時の流量を約20L/分とした。膜ろ過装置11では中空糸膜を数百本程度束ねた内圧型の膜モジュール51をクロスフロー方式で使用し、原水槽52内への通水流量を約5L/分とした。散気管53によるエアスクラビングは常時行った。逆洗時には空気圧を付与した。膜ろ過装置水道水洗浄時の流量を約4L/分とした。水質計測器3としてはバイオセンサ13のみを使用した。なお、バイオセンサ13の水道水洗浄時の流量は約3L/分とした。   A submersible pump was used as the water sampling device 1 and the flow rate was adjusted to about 50 L / min, and sample water was introduced to the screen 12. The filtration surface slit width of the screen 12 was 0.5 mm, and the flow rate at the time of cleaning the screen surface tap water was about 20 L / min. In the membrane filtration device 11, an internal pressure type membrane module 51 in which several hundreds of hollow fiber membranes were bundled was used in a cross flow method, and the flow rate of water into the raw water tank 52 was set to about 5 L / min. Air scrubbing by the air diffuser 53 was always performed. Air pressure was applied during backwashing. The flow rate at the time of membrane water washing with tap water was about 4 L / min. As the water quality measuring instrument 3, only the biosensor 13 was used. The flow rate when the biosensor 13 was washed with tap water was about 3 L / min.

運転制御装置4の各タイマーの設定値は、T1:3時間、T2:2分、T3:28分、T4:3分、T5:6時間、T6:45分、T7:1日、T8:15分、T9:1日、T10:1分、T11:7日、T12:10分とした。また、運転制御装置4の各制御値は、AL1:−50kPa、AL2:1.5mV、AL3:5回とした。   The set values of the timers of the operation control device 4 are: T1: 3 hours, T2: 2 minutes, T3: 28 minutes, T4: 3 minutes, T5: 6 hours, T6: 45 minutes, T7: 1 day, T8: 15 Minutes, T9: 1 day, T10: 1 minute, T11: 7 days, T12: 10 minutes. Moreover, each control value of the operation control apparatus 4 was AL1: -50 kPa, AL2: 1.5 mV, AL3: 5 times.

中空糸膜の内部あるいは表面の目詰まりが進行すると、ろ過運転時の負圧が大きくなることから、ろ過運転時における圧力計57の測定値(以下、「吸引圧」という)を中空糸膜のろ過性能の指標とすることができる。逆洗を行っても吸引圧がAL1以上となった場合に、膜ろ過装置11は運転継続不能と判定することとした。   When the clogging of the inside or the surface of the hollow fiber membrane proceeds, the negative pressure during the filtration operation increases, so the measured value of the pressure gauge 57 during the filtration operation (hereinafter referred to as “suction pressure”) It can be used as an index of filtration performance. Even when backwashing was performed, when the suction pressure became AL1 or higher, the membrane filtration device 11 was determined to be unable to continue operation.

また、バイオセンサ13内に雑菌や硬度成分が付着したりすると、微生物膜21への酸素拡散が阻害され、スパン校正値が小さくなることから、スパン校正値をバイオセンサ13内の汚れ度合の指標とすることができる。スパン校正値が異常値の場合のバイオセンサ水道水洗浄の繰り返し回数がAL3に到達した場合に、バイオセンサ13は運転継続不能と判定することとした。   Further, if bacteria or hardness components adhere to the biosensor 13, oxygen diffusion to the microorganism film 21 is inhibited and the span calibration value becomes small. Therefore, the span calibration value is used as an index of the degree of contamination in the biosensor 13. It can be. The biosensor 13 is determined to be unable to continue operation when the number of repetitions of biosensor tap water cleaning when the span calibration value is an abnormal value reaches AL3.

図11および図12に、実施例1の水質監視試験の結果を示す。図11は、膜ろ過装置11のろ過性能の指標である吸引圧の推移を示すグラフである。図12は、バイオセンサ13内の汚れ度合の指標であるスパン校正値の推移を示すグラフである。   11 and 12 show the results of the water quality monitoring test of Example 1. FIG. FIG. 11 is a graph showing the transition of the suction pressure, which is an index of the filtration performance of the membrane filtration device 11. FIG. 12 is a graph showing the transition of the span calibration value that is an index of the degree of contamination in the biosensor 13.

図11に示すように、吸引圧は、運転開始時の約4kPaから漸増したが、30日間経過後も−10kPa以下であり、ろ過性能として全く問題のないレベルを維持した。また、中空糸膜の外観を観察すると、中空糸膜表面の汚泥堆積量、水槽フランジ54内および中空糸膜の取付部端面の雑菌付着量ともに軽微であり、中空糸膜の再使用が可能であることが分かった。   As shown in FIG. 11, the suction pressure gradually increased from about 4 kPa at the start of operation, but it was −10 kPa or less after 30 days, and maintained a level with no problem as filtration performance. Further, when the appearance of the hollow fiber membrane is observed, the amount of sludge accumulated on the surface of the hollow fiber membrane, the amount of bacteria adhering to the inside of the water tank flange 54 and the end surface of the mounting portion of the hollow fiber membrane, and the hollow fiber membrane can be reused I found out.

なお、中空糸膜表面の洗浄法である、エアスクラビング、逆洗、水道水洗浄について、上記の条件で洗浄効果の比較試験を行ったところ、最も効果が高いのは、水道水洗浄であることが分かった。このことから、逆洗間隔時間T3は上記設定値よりも長くすることができ、逆洗による中空糸膜内部への雑菌逆流リスクを軽減できる。すなわち、逆洗時には水槽フランジ54内に付着した雑菌を逆洗圧によって膜内に押し込むリスクがあるため、膜表面洗浄を目的とする逆洗の頻度は低下させ、原水槽52内への水道水導水によって膜表面洗浄を補完することが好ましい。   In addition, for air scrubbing, backwashing, and tap water cleaning, which are cleaning methods for the surface of the hollow fiber membrane, a cleaning test was performed under the above conditions, and the most effective was tap water cleaning. I understood. From this, the backwashing interval time T3 can be made longer than the set value, and the risk of backflow of germs into the hollow fiber membrane due to backwashing can be reduced. That is, at the time of backwashing, there is a risk that the germs adhering in the water tank flange 54 will be pushed into the membrane by backwashing pressure, so the frequency of backwashing for the purpose of washing the membrane surface is reduced and the tap water into the raw water tank 52 is reduced. It is preferable to supplement the membrane surface cleaning with water.

図12に示すように、スパン校正値は常時2mV以上であり、バイオセンサ水道水洗浄を行うことなく、安定した測定を継続することができた。また、ろ過水配管55およびろ過水槽56の外観を観察すると、ともに雑菌付着は軽微であった。また、膜ろ過装置水道水洗浄の時にバイオセンサ13の測定を中断したことから、水道水と、試料水である下水との水質差に起因する誤警報を発することはなかった。   As shown in FIG. 12, the span calibration value was always 2 mV or more, and stable measurement could be continued without performing biosensor tap water cleaning. Moreover, when the external appearance of the filtered water piping 55 and the filtered water tank 56 was observed, both bacteria adhesion was slight. Moreover, since the measurement of the biosensor 13 was interrupted when the membrane filtration device tap water was washed, no false alarm was generated due to a difference in water quality between tap water and sewage as sample water.

このように、実施例1では、水質監視システムを、簡易な保守作業で、且つ少ない保守頻度および保守費用で、30日間以上、長期間安定して継続的に運転することができた。   As described above, in Example 1, the water quality monitoring system could be stably and continuously operated for a long period of 30 days or more with simple maintenance work and with low maintenance frequency and maintenance cost.

(実施例2)
実施例1の運転条件のうち、バイオセンサ校正時に膜ろ過装置水道水洗浄を行わないように設定を変更した点を除き、実施例1と同様の運転条件で水質監視試験を行った。その結果を図13および図14に示す。図13は、吸引圧の推移を示すグラフであり、図14は、スパン校正値の推移を示すグラフである。
(Example 2)
Among the operating conditions of Example 1, a water quality monitoring test was performed under the same operating conditions as in Example 1 except that the setting was changed so that the membrane filtration device tap water was not washed during biosensor calibration. The results are shown in FIG. 13 and FIG. FIG. 13 is a graph showing the transition of the suction pressure, and FIG. 14 is a graph showing the transition of the span calibration value.

図13に示すように、吸引圧は、運転開始時の約5kPaから漸増し、30日間経過後に約−40kPaとまでなり、実施例1と比較して大幅に吸引圧が上昇した。膜ろ過装置11の保守を行わずに、そのまま運転を継続したところ、40日後には逆洗を行っても吸引圧は回復せず、運転継続不能となった。この時点で、中空糸膜の外観を観察すると、中空糸膜表面の汚泥堆積量は実施例1と同様に軽微であったが、水槽フランジ54内および中空糸膜取付部端面の雑菌付着量が顕著であり、雑菌による中空糸膜内部の目詰まりのため、簡便な保守のみでは再使用できないことが分かった。   As shown in FIG. 13, the suction pressure gradually increased from about 5 kPa at the start of operation and reached about −40 kPa after 30 days, and the suction pressure was significantly increased as compared with Example 1. When the operation was continued without maintenance of the membrane filtration device 11, the suction pressure did not recover even after 40 days of backwashing, and the operation could not be continued. At this point, when the appearance of the hollow fiber membrane was observed, the amount of sludge deposited on the surface of the hollow fiber membrane was as small as in Example 1, but the amount of germs in the water tank flange 54 and the end surface of the hollow fiber membrane attachment portion was small. It was prominent, and it was found that the inside of the hollow fiber membrane was clogged with various bacteria, and it could not be reused by simple maintenance alone.

なお、この中空糸膜を再使用する場合、中空糸膜内部の薬液洗浄が必要と考えられるが、薬液洗浄後の膜内部の薬液除去が不十分な場合、再稼動後にバイオセンサ13内へ中空糸膜内部に残留した薬液が流入し、微生物膜21にダメージを与え、誤警報を発する恐れがある。そのため、中空糸膜再使用のための保守労力が飛躍的に増大するものと考えられる。   When the hollow fiber membrane is reused, it is considered necessary to clean the inside of the hollow fiber membrane. However, if the removal of the inside of the membrane after the chemical cleaning is insufficient, the hollow fiber membrane is hollowed into the biosensor 13 after restarting. There is a possibility that the chemical solution remaining inside the yarn film flows in, damages the microbial film 21 and generates a false alarm. Therefore, it is considered that the maintenance labor for reusing the hollow fiber membrane is drastically increased.

図14に示すように、スパン校正値は、運転開始時の約3mVから漸減し、約2週間経過後から、バイオセンサ水道水洗浄が定期校正時に必ず1〜3回起動する状態となった。図15に、バイオセンサ水道水洗浄の起動時のバイオセンサ13の校正波形の一例を示す。バイオセンサ水道水洗浄を行うことにより、バイオセンサ13内に付着した雑菌や析出物が剥離・排出され、スパン校正値がAL2以上となったことから、40日後も測定を継続することができた。この結果から、スパン校正異常時にバイオセンサを洗浄する効果が高いことが分かった。   As shown in FIG. 14, the span calibration value gradually decreased from about 3 mV at the start of operation, and after about 2 weeks, the biosensor tap water cleaning was surely started 1 to 3 times during regular calibration. FIG. 15 shows an example of a calibration waveform of the biosensor 13 at the start of biosensor tap water cleaning. By washing the biosensor tap water, the bacteria and deposits attached to the biosensor 13 were peeled and discharged, and the span calibration value was AL2 or more, so the measurement could be continued after 40 days. . From this result, it was found that the effect of cleaning the biosensor when the span calibration is abnormal is high.

また、この時点でのろ過水配管55およびろ過水槽56の外観を観察すると、ともに雑菌付着が顕著であった。このことから、実施例1では、膜ろ過装置水道水洗浄のろ過水配管55およびろ過水槽56の洗浄効果が特に高く、膜ろ過装置11からバイオセンサ23へ雑菌がほとんど流入しなかったことから、上記のような結果が得られたことが分かった。   Moreover, when the external appearance of the filtered water piping 55 and the filtered water tank 56 at this time was observed, both bacteria adhesion was remarkable. From this, in Example 1, the washing effect of the filtration water pipe 55 and the filtration water tank 56 of the membrane filtration device tap water washing is particularly high, and almost no germs flowed from the membrane filtration device 11 to the biosensor 23. It was found that the above results were obtained.

本発明に係る水質監視システムの一実施の形態の概略的な構成を示す模式図である。It is a mimetic diagram showing a schematic structure of one embodiment of a water quality monitoring system concerning the present invention. 図1中に示すバイオセンサの内部構造を示す模式図である。It is a schematic diagram which shows the internal structure of the biosensor shown in FIG. 図2中に示す微生物膜と溶存酸素電極の構成を示す模式図である。It is a schematic diagram which shows the structure of the microbial membrane and dissolved oxygen electrode which are shown in FIG. 図1中に示すバイオセンサの周辺構成の一例を示す模式図である。It is a schematic diagram which shows an example of the periphery structure of the biosensor shown in FIG. バイオセンサが有害物質を検出する機構を説明する模式図である。It is a schematic diagram explaining the mechanism in which a biosensor detects a harmful substance. バイオセンサにおける酸素消費率を示すグラフである。It is a graph which shows the oxygen consumption rate in a biosensor. 図1中の運転制御装置の構成を示す模式図である。It is a schematic diagram which shows the structure of the operation control apparatus in FIG. バイオセンサの洗浄アルゴリズムを示すフロー図である。It is a flowchart which shows the washing | cleaning algorithm of a biosensor. 図1中に示すバイオセンサの周辺構成の別の例を示す模式図である。It is a schematic diagram which shows another example of the periphery structure of the biosensor shown in FIG. 図1中に示すバイオセンサの周辺構成の別の例を示す模式図である。It is a schematic diagram which shows another example of the periphery structure of the biosensor shown in FIG. 実施例1における吸引圧の推移を示すグラフである。3 is a graph showing a change in suction pressure in Example 1. 実施例1におけるスパン校正値の推移を示すグラフである。4 is a graph showing a transition of span calibration values in Example 1. 実施例2における吸引圧の推移を示すグラフである。6 is a graph showing changes in suction pressure in Example 2. 実施例2におけるスパン校正値の推移を示すグラフである。10 is a graph showing a transition of span calibration values in Example 2. バイオセンサを水道水で洗浄した際の校正波形を示すグラフである。It is a graph which shows the calibration waveform at the time of wash | cleaning a biosensor with tap water.

符号の説明Explanation of symbols

1 採水装置
2 前処理装置
3 水質計測器
4 運転制御装置
11 膜ろ過装置
12 スクリーン
13 バイオセンサ
14 pH計
15 着色度計
21 微生物膜
22 溶存酸素電極
24 フローセル
25 試料流路
26 恒温槽
27 熱交換器
28 バイパス流路
29 送風送液機構
31〜42 タイマー
46 アナログデジタル信号変換器
47 中央演算処理装置
48 デジタルアナログ信号変換器
51 膜モジュール
52 原水槽
53 散気管
54 水槽フランジ
55 ろ過水配管
56 ろ過水槽
57 圧力計
58 給水ポンプ
59 ろ過用ポンプ
60 逆洗用エアポンプ
61 エアスクラビング用エアポンプ
62、63 水道水配管
71 スクリーン排水槽
72 スクリーンろ過水槽
81 酸素透過膜
82 カソード電極
83 アノード電極
84 カソード絶縁体
85 内部液
87 硝化細菌
88 基質
89 酸素
91 空気タンク
92 水タンク
93 切替バルブ
94 タンクバルブ
DESCRIPTION OF SYMBOLS 1 Water sampling apparatus 2 Pretreatment apparatus 3 Water quality measuring instrument 4 Operation control apparatus 11 Membrane filtration apparatus 12 Screen 13 Biosensor 14 pH meter 15 Colorimeter 21 Microbial membrane 22 Dissolved oxygen electrode 24 Flow cell 25 Sample flow path 26 Constant temperature bath 27 Heat Exchanger 28 Bypass channel 29 Blowing and feeding mechanism 31-42 Timer 46 Analog-digital signal converter 47 Central processing unit 48 Digital-analog signal converter 51 Membrane module 52 Raw water tank 53 Aeration pipe 54 Water tank flange 55 Filtration water pipe 56 Filtration Water tank 57 Pressure gauge 58 Water supply pump 59 Filtration pump 60 Backwash air pump 61 Air scrubbing air pump 62, 63 Tap water piping 71 Screen drainage tank 72 Screen filtration water tank 81 Oxygen permeable membrane 82 Cathode electrode 83 Anode electrode 84 Cathode insulation 85 internal solution 87 nitrifying bacteria 88 substrate 89 oxygen 91 air reservoir 92 water tank 93 changeover valve 94 Tank Valve

Claims (8)

監視対象となる水源から試料水を連続的に採取する採水装置と、この採水装置で採取した試料水中の濁質を連続的に除去する前処理装置と、この前処理装置で前処理された試料水中の有害物質を連続的に検出する水質計測器と、この水質計測器の定期的な校正の間、前記採水装置の運転を停止するとともに、前記水質計測器への試料水の通水を停止し、前記前処理装置または前記水質計測器を洗浄するように制御する運転制御装置とを備えた水質監視システム。   A water collection device that continuously collects sample water from the water source to be monitored, a pretreatment device that continuously removes turbidity in the sample water collected by this water collection device, and a pretreatment device that is pretreated by this pretreatment device During the periodical calibration of the water quality measuring instrument that continuously detects harmful substances in the sample water and the water quality measuring instrument, the operation of the water sampling device is stopped and the sample water is passed to the water quality measuring instrument. A water quality monitoring system comprising: an operation control device that controls to stop water and wash the pretreatment device or the water quality measuring instrument. 前記前処理装置が、試料水中の汚濁を膜でろ過する膜分離手段と、この膜分離手段と前記水質計測器との間の試料水が流れる部分に水を流して洗浄を行う第1の洗浄手段とを備えたものであり、前記運転制御装置が、前記水質計測器の定期的な校正の間、前記第1の洗浄手段を運転するように制御する請求項1に記載の水質監視システム。   A first cleaning in which the pretreatment device performs cleaning by flowing water through a portion of the sample water flowing between the membrane separation unit and the water quality measuring device between the membrane separation unit that filters the contamination in the sample water with a membrane. The water quality monitoring system according to claim 1, wherein the operation control device controls the first cleaning means to operate during the periodic calibration of the water quality measuring instrument. 前記水質計測器が、バイオセンサと、このバイオセンサ内の試料水が流れる部分に水または空気を流して洗浄を行う第2の洗浄手段とを備えたものであり、前記運転制御装置が、前記バイオセンサの定期的な校正で異常と判断した場合に、前記第2の洗浄手段を運転するように制御する請求項1または2に記載の水質監視システム。   The water quality measuring instrument includes a biosensor and a second cleaning unit that performs cleaning by flowing water or air through a portion in which the sample water flows in the biosensor, and the operation control device includes: 3. The water quality monitoring system according to claim 1, wherein when the biosensor is determined to be abnormal by periodic calibration, the second cleaning unit is controlled to operate. 監視対象となる水源から試料水を連続的に採取する採水装置と、この採水装置で採取した試料水中の有害物質を連続的に検出するバイオセンサであって、微生物を固定した膜と溶存酸素を測定する溶存酸素電極とを備えたバイオセンサと、このバイオセンサ内の試料水が流れる部分に水または空気を流して洗浄を行う洗浄手段と、このバイオセンサを定期的に校正する際、センサ出力の低下により異常と判断した場合に、前記洗浄手段を運転するように制御する運転制御装置とを備えた水質監視システム。   A water sampling device that continuously collects sample water from the water source to be monitored, and a biosensor that continuously detects harmful substances in the sample water collected by this water sampling device, dissolved in a membrane with immobilized microorganisms When a biosensor provided with a dissolved oxygen electrode for measuring oxygen, a cleaning means for cleaning by flowing water or air in a portion where the sample water flows in the biosensor, and periodically calibrating the biosensor, A water quality monitoring system comprising: an operation control device that controls to operate the cleaning means when it is determined to be abnormal due to a decrease in sensor output. 監視対象となる水源から採水装置にて試料水を連続的に採取し、この採取した試料水中の濁質を前処理装置で連続的に除去し、この前処理された試料水中の有害物質を水質計測器で連続的に検出する水質監視工程と、前記水質計測器の定期的な校正の間、前記採水装置の採水運転を停止し、前記水質計測器への試料水の通水を停止し、前記前処理装置を洗浄する校正工程とを含む水質監視方法。   Sample water is continuously collected from the water source to be monitored by the water sampling device, turbidity in the collected sample water is continuously removed by the pretreatment device, and harmful substances in the pretreated sample water are removed. During the water quality monitoring process, which is continuously detected by the water quality measuring instrument, and during the periodic calibration of the water quality measuring instrument, the sampling operation of the water sampling device is stopped, and the sample water is passed through the water quality measuring instrument. A water quality monitoring method including a calibration step of stopping and cleaning the pretreatment device. 前記前処理装置が、試料水中の汚濁を膜でろ過する膜分離手段を備えたものであって、前記校正工程が、前記膜分離手段と前記水質計測器との間の試料水が流れる部分に水を流して洗浄を行う第1の洗浄を行うことを含む請求項5に記載の水質監視方法。   The pretreatment apparatus is provided with a membrane separation means for filtering the contamination in the sample water with a membrane, and the calibration step is performed at a portion where the sample water flows between the membrane separation means and the water quality measuring instrument. The water quality monitoring method according to claim 5, comprising performing a first cleaning in which water is passed to perform cleaning. 前記水質計測器がバイオセンサを備えたものであって、前記校正工程が、前記バイオセンサの校正において異常と判断した場合、前記バイオセンサ内の試料水が流れる部分に水または空気を流して洗浄を行う第2の洗浄を行うことを含む請求項5または6に記載の水質監視方法。   When the water quality measuring instrument is equipped with a biosensor, and the calibration step determines that there is an abnormality in the calibration of the biosensor, the sample is washed with water or air flowing through the portion where the sample water flows in the biosensor. The water quality monitoring method according to claim 5, further comprising performing a second cleaning. 監視対象となる水源から採水装置にて試料水を連続的に採取し、この採取した試料水中の有害物質を、微生物を固定した膜と溶存酸素を測定する溶存酸素電極とを備えたバイオセンサで連続的に検出する水質監視工程と、前記バイオセンサを定期的に校正する際、センサ出力の低下により異常と判断した場合に、このバイオセンサ内の試料水が流れる部分に水または空気を流して洗浄する校正工程とを含む水質監視方法。   A biosensor comprising a sample water sampled continuously from a water source to be monitored and a harmful substance in the sample water sample, a membrane fixed with microorganisms and a dissolved oxygen electrode for measuring dissolved oxygen When water quality is monitored continuously in the process and the biosensor is calibrated periodically, if it is determined that there is an abnormality due to a decrease in sensor output, water or air is allowed to flow through the portion of the biosensor where sample water flows. Water quality monitoring method including calibration process for cleaning.
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JP2025178972A (en) * 2024-05-27 2025-12-09 栗田工業株式会社 Wastewater quality measurement system, wastewater treatment equipment, and wastewater quality measurement method
JP7803365B2 (en) 2024-05-27 2026-01-21 栗田工業株式会社 Wastewater quality measurement system, wastewater treatment equipment, and wastewater quality measurement method
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