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JP4016352B2 - Membrane filtration device - Google Patents

Membrane filtration device Download PDF

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JP4016352B2
JP4016352B2 JP2005192407A JP2005192407A JP4016352B2 JP 4016352 B2 JP4016352 B2 JP 4016352B2 JP 2005192407 A JP2005192407 A JP 2005192407A JP 2005192407 A JP2005192407 A JP 2005192407A JP 4016352 B2 JP4016352 B2 JP 4016352B2
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membrane
filtration
flow rate
turbidity
water quality
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JP2007007567A (en
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剛 武本
昭二 渡辺
晃治 ▲陰▼山
伊智朗 圓佛
直樹 原
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Hitachi Ltd
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Description

本発明は、原水に含まれる濁質や病原性原虫などの分離除去のために設置される膜ろ過処理装置に関する。   The present invention relates to a membrane filtration treatment apparatus installed for separating and removing turbidity and pathogenic protozoa contained in raw water.

膜ろ過処理装置は、河川などの表流水に代表される原水を浄化する浄水施設等に設置される。膜ろ過処理装置は、原水に含まれる濁質や病原性原虫等(以下、濁質と適宜総称する)を分離除去するろ過膜を有する。   The membrane filtration apparatus is installed in a water purification facility that purifies raw water represented by surface water such as rivers. The membrane filtration apparatus has a filtration membrane that separates and removes turbidity, pathogenic protozoa and the like (hereinafter collectively referred to as turbidity) contained in raw water.

このような膜ろ過処理装置においては、ろ過、逆洗、薬品洗浄などの処理が繰り返されるため、ろ過膜に破断が生じることがある。ろ過膜の破断が生じると、ろ過膜の破断部分から未処理の原水が漏れるため、ろ過水に濁質が混入する。   In such a membrane filtration processing apparatus, filtration, backwashing, chemical washing, and the like are repeated, so that the filtration membrane may break. When the filtration membrane breaks, untreated raw water leaks from the broken portion of the filtration membrane, so that turbidity is mixed into the filtered water.

ろ過水に濁質が混入するのを防ぐため、ろ過水の濁度を計測器で測定し、測定した濁度の大きさに基づき、ろ過膜の破断を検出することが行われる(例えば、特許文献1参照)。   In order to prevent turbidity from being mixed into the filtered water, the turbidity of the filtered water is measured with a measuring instrument, and the breakage of the filtration membrane is detected based on the measured turbidity (for example, patents). Reference 1).

特開平10−128086号公報JP-A-10-128086

ところで、濁度が比較的小さい原水(例えば、伏流水、地下水)をろ過する場合や、ろ過膜の正常部分に対する破断部分の割合が小さい場合は、ろ過膜に破談が生じた際のろ過水の濁度も比較的小さい。しかし、濁度を計測する機器類は、検出感度に一定の制限があるのが一般的であるから、特許文献1のような方式では、ろ過水の濁度を計測器で測定できない場合がある。その結果、ろ過膜に破断が生じているときでも、その破断を検出できないおそれがある。   By the way, when raw water with relatively low turbidity (for example, underground water, groundwater) is filtered, or when the ratio of the broken part to the normal part of the filter membrane is small, the filtered water when the filter membrane is broken Turbidity is also relatively small. However, since instruments that measure turbidity generally have a certain limit in detection sensitivity, the turbidity of filtered water may not be measured with a measuring instrument in the method as in Patent Document 1. . As a result, even when a rupture occurs in the filtration membrane, the rupture may not be detected.

本発明の課題は、ろ過膜の破断を的確に検出するのにより好適な膜ろ過処理装置を実現することにある。   An object of the present invention is to realize a membrane filtration apparatus that is more suitable for accurately detecting the breakage of a filtration membrane.

上記課題を解決するために、本発明の膜ろ過処理装置は、原水に含まれる濁質を分離除去するろ過膜を有する膜ろ過手段と、膜ろ過手段のろ過水の濁度を計測する水質計測手段と、水質計測手段の計測値に基づきろ過膜の破断を検出する膜破断検出手段と、膜破断検出手段からの指令に基づいてろ過膜を通過する原水の流量を調整するろ過流量変更手段とを備え、その膜破断検出手段は、ろ過流量変更手段に通過流量を減少させる指令を出力してろ過膜を通過する原水の流量を減少させ、通過流量の減少後に水質計測手段から取り込んだ計測値に基づいて、ろ過膜の破断を検出することを特徴とする。 In order to solve the above problems, the membrane filtration apparatus of the present invention includes a membrane filtration means having a filtration membrane for separating and removing turbidity contained in raw water, and a water quality measurement for measuring the turbidity of filtrate water of the membrane filtration means. Means, a membrane rupture detection means for detecting the rupture of the filtration membrane based on the measurement value of the water quality measurement means, and a filtration flow rate changing means for adjusting the flow rate of the raw water passing through the filtration membrane based on a command from the membrane rupture detection means, The membrane breakage detecting means outputs a command to reduce the passage flow rate to the filtration flow rate changing means to reduce the flow rate of the raw water passing through the filtration membrane, and the measured value taken from the water quality measurement means after the reduction of the passage flow rate Based on the above, it is characterized by detecting the breakage of the filtration membrane.

すなわち、破断が生じたろ過膜に対する通過流量を減少させると、ろ過膜の正常部分を通過する水量は、ろ過膜に対する水圧の低下に起因して減るのに対し、破断部分を通過する水量は、正常部分よりも減少幅が小さい。ここで破断部分を通過する原水は、未処理であるため、濁質を比較的多く含む。したがって、通過流量の減少後のろ過水の濁度は、減少前よりも増加することになる。   That is, when the flow rate through the filtration membrane with the breakage is reduced, the amount of water passing through the normal portion of the filtration membrane is reduced due to a decrease in the water pressure with respect to the filtration membrane, whereas the amount of water passing through the breakage portion is The decrease is smaller than the normal part. Here, the raw water that passes through the broken portion is untreated, and therefore contains a relatively large amount of turbidity. Therefore, the turbidity of the filtered water after the reduction of the passage flow rate increases more than before the reduction.

このような知見に基づき、ろ過膜の破断を検出するに際し、通過流量を減少させることにより、ろ過水の濁度を増加させることができる。その結果、例えば原水の濁度が比較的小さい場合でも、濁度計測器の検出感度にかかわらず、ろ過水の濁度を的確に検出できるため、ろ過膜の破断を検出する精度が向上する。よって、破断が生じた際の処置を施すのが的確になるから、安心かつ安全な浄水を常時供給するのが容易になる。なお、ここでの濁度とは、単位体積あたりの濁質の割合である。   Based on such knowledge, the turbidity of filtered water can be increased by decreasing the passing flow rate when detecting the breakage of the filtration membrane. As a result, for example, even when the turbidity of the raw water is relatively small, the turbidity of the filtered water can be accurately detected regardless of the detection sensitivity of the turbidity measuring instrument, so that the accuracy of detecting the breakage of the filtration membrane is improved. Therefore, since it becomes appropriate to take measures when the breakage occurs, it is easy to always supply safe and safe purified water. In addition, turbidity here is the ratio of the turbidity per unit volume.

この場合において、膜破断検出手段は、ろ過流量変更手段に通過流量を減少させる指令を出力して通過流量を減少させる前の水質計測手段の計測値を第一の計測値として取得し、通過流量を減少させた後の水質計測手段の計測値を第二の計測値として取得し、第二の計測値が第一の計測値よりも大きいときにろ過膜に破断が生じたものと判定できる。これにより、膜破断の有無を判定するに際し、通過流量の減少前後における濁度の差分の大きさを基準とするため、原水の濁度自体には左右されず、ろ過膜の漏れを的確に検出できる。 In this case, the membrane breakage detection means outputs a command to reduce the passage flow rate to the filtration flow rate change means, acquires the measurement value of the water quality measurement means before reducing the passage flow rate as the first measurement value, and passes the flow rate. The measured value of the water quality measuring means after the decrease is obtained as the second measured value, and it can be determined that the filter membrane has been broken when the second measured value is larger than the first measured value. As a result, when judging the presence or absence of membrane rupture, the turbidity difference before and after the decrease in the flow rate of the flow is used as a reference, so it is not affected by the turbidity of the raw water itself, and the leakage of the filtration membrane is accurately detected. it can.

また、膜破断検出手段は、ろ過流量変更手段に通過流量を減少させる指令を出力して通過流量を減少させた後の水質計測手段の計測値を取得し、取得した計測値が設定値よりも大きいときにろ過膜に破断が生じたものと判定できる。これにより、膜破断の有無を判定するに際し、閾値である設定値を基準にするため、膜破断検出処理を簡単にすることができる。 Further, the membrane breakage detecting means outputs a command to reduce the passage flow rate to the filtration flow rate changing means to obtain the measurement value of the water quality measurement means after reducing the passage flow rate, and the obtained measurement value is less than the set value. When it is large, it can be determined that the filter membrane is broken. Thereby, when determining the presence or absence of a film rupture, since the set value which is a threshold is used as a reference, the film rupture detection process can be simplified.

また、膜破断検出手段は、ろ過膜に破断がないものと判定したときろ過流量変更手段に通過流量を元の量に戻す指令を出力できる。これにより、膜ろ過処理の運転を継続できるので、膜破断検出処理に伴う運転停止時間を短縮できる。 The membrane breakage detecting means can output a command for returning the passage flow rate to the original amount to the filtration flow rate changing means when it is determined that the filtration membrane is not broken. Thereby, since the operation | movement of a membrane filtration process can be continued, the operation stop time accompanying a membrane fracture | rupture detection process can be shortened.

また、膜ろ過手段の上流側の原水の濁度を計測する被処理水質計測手段を設け、膜破断検出手段は、被処理水質計測手段の計測値が設定値以下の際、ろ過流量変更手段に通過流量を減少させる指令を出力して通過流量を減少させることができる。これにより、膜破断検出処理を開始すべき場合を自動検出できるため、装置の使い勝手が向上する。 Also, a treated water quality measuring means for measuring the turbidity of the raw water upstream of the membrane filtering means is provided, and the membrane breakage detecting means is used as a filtration flow rate changing means when the measured value of the treated water quality measuring means is less than a set value. A command for reducing the passage flow rate can be output to reduce the passage flow rate. Thereby, since the case where a film | membrane break detection process should be started can be detected automatically, the usability of an apparatus improves.

また、膜ろ過手段及びろ過流量変更手段は、複数設けられるものとし、水質計測手段は、各膜ろ過手段から流出する処理水の合流後の濁度を計測し、膜破断検出手段は、複数のろ過流量変更手段のうち、一のろ過流量変更手段に通過流量を減少させる指令を出力して一の膜ろ過手段の通過通量を減少させることができる。これにより、複数の膜ろ過手段の個々について順番に膜破断の有無を検出できるから、膜破断が生じた膜ろ過手段を特定することができるので、膜破断に対する処置を施すのが容易になる。 Also, a plurality of membrane filtration means and filtration flow rate changing means are provided, the water quality measurement means measures the turbidity after merging of treated water flowing out from each membrane filtration means, and the membrane breakage detection means includes a plurality of membrane breakage detection means . Of the filtration flow rate changing means, a command for decreasing the passage flow rate can be output to one filtration flow rate changing means to reduce the passage amount of one membrane filtration means. Thereby, since the presence or absence of the membrane rupture can be detected in order for each of the plurality of membrane filtration means, it is possible to specify the membrane filtration means in which the membrane rupture has occurred.

また、膜破断検出手段は、複数の膜ろ過手段のうち、一の膜ろ過手段の通過流量を減少させつつ、他のろ過流量変更手段に通過流量を増加させる指令を出力して他の膜ろ過手段の通過流量を増加させることができる。これにより、通過流量を減らすことに起因する処理水量の減少を補填できるため、所望の処理水量を確保できる。 In addition, the membrane breakage detection means outputs a command to increase the passage flow rate to the other filtration flow rate change means while reducing the passage flow rate of one membrane filtration means among the plurality of membrane filtration means. The passage flow rate of the means can be increased. Thereby, since reduction of the amount of treated water resulting from reducing a passage flow rate can be compensated, the desired amount of treated water can be secured.

また、本発明の膜ろ過処理方法は、原水に含まれる濁質をろ過膜で分離除去するろ過工程と、ろ過膜を通過したろ過水の濁度を計測する水質計測工程と、水質計測工程の計測値に基づきろ過膜の破断を検出する膜破断検出工程とを備え、その膜破断検出工程は、ろ過膜を通過する原水の流量を減少させ、通過流量の減少後に水質計測手段から取り込んだ計測値に基づいて、ろ過膜の破断を検出することを特徴とする。   The membrane filtration method of the present invention includes a filtration step of separating and removing turbidity contained in raw water with a filtration membrane, a water quality measurement step of measuring the turbidity of filtered water that has passed through the filtration membrane, and a water quality measurement step. A membrane rupture detection step that detects the rupture of the filtration membrane based on the measured value. The membrane rupture detection step reduces the flow rate of the raw water that passes through the filtration membrane, and takes the measurement taken from the water quality measuring means after the passage flow rate is reduced. Based on the value, the filter membrane is detected to be broken.

本発明によれば、ろ過膜の破断を的確に検出するのにより好適な膜ろ過処理装置を実現できる。例えば、原水の濁度が比較的小さい場合でも、ろ過水の濁度を的確に検出できるため、ろ過膜の破断を検出する精度が向上する。   ADVANTAGE OF THE INVENTION According to this invention, the more suitable membrane filtration processing apparatus is realizable by detecting the fracture | rupture of a filtration membrane exactly. For example, even when the turbidity of the raw water is relatively small, the turbidity of the filtered water can be accurately detected, so that the accuracy of detecting the breakage of the filtration membrane is improved.

(第1の実施形態)
本発明を適用した膜ろ過処理装置の第一の実施形態について説明する。本実施形態の膜ろ過処理装置は、ろ過膜の破断を検出するに際し、ろ過膜の通過流量を一時的に減少させると、ろ過膜に破断が生じている場合は、ろ過水の濁度が向上するという知見に基づき実現されている。より具体的には、本実施形態の膜ろ過処理装置は、ろ過膜を通過する原水の流量を減少させ、その通過流量の減少後のろ過水の濁度に基づき、ろ過膜の破断を検出する。
(First embodiment)
A first embodiment of a membrane filtration apparatus to which the present invention is applied will be described. When the membrane filtration treatment device of the present embodiment detects the breakage of the filtration membrane, when the flow rate through the filtration membrane is temporarily reduced, the turbidity of the filtered water is improved if the filtration membrane is broken. It is realized based on the knowledge that More specifically, the membrane filtration apparatus of this embodiment reduces the flow rate of raw water that passes through the filtration membrane, and detects the breakage of the filtration membrane based on the turbidity of the filtrate water after the reduction of the flow rate. .

以下に、第一ないし第四の実施例により本実施形態の膜ろ過処理装置を説明する。ただし、各実施例で説明した構成部や変形例等を組み合わせ、あるいは置き換えるなど、必要に応じて変更することができる。   Below, the membrane filtration apparatus of this embodiment is demonstrated by the 1st thru | or 4th Example. However, it can be changed as necessary, for example, by combining or replacing the components and modifications described in each embodiment.

(実施例1−1)
図1は、本発明を適用した第一の実施形態の膜ろ過処理装置の第一の実施例を示す図である。本実施例の膜ろ過処理装置は、膜ろ過処理装置は、河川などの表流水に代表される原水を浄化する浄化施設等に設置される。このような膜ろ過処理装置は、図1に示すように、原水に含まれる濁質を分離除去するろ過膜を有する膜ろ過手段1と、ろ過膜を通過する原水の流量を調整するろ過流量変更手段2と、膜ろ過手段1のろ過水の濁度を計測する水質計測手段(以下、処理水質計測手段3)と、処理水質計測手段3の計測値に基づきろ過膜の破断を検出する膜破断検出手段としての制御手段4などを備えている。
(Example 1-1)
FIG. 1 is a diagram showing a first example of a membrane filtration apparatus according to the first embodiment to which the present invention is applied. The membrane filtration processing apparatus of this embodiment is installed in a purification facility or the like that purifies raw water represented by surface water such as rivers. As shown in FIG. 1, such a membrane filtration apparatus has a membrane filtration means 1 having a filtration membrane for separating and removing turbidity contained in raw water, and a filtration flow rate change for adjusting the flow rate of raw water passing through the filtration membrane. Means 2, a water quality measuring means (hereinafter, treated water quality measuring means 3) for measuring the turbidity of the filtered water of the membrane filtration means 1, and a membrane breakage for detecting the breakage of the filtration membrane based on the measured values of the treated water quality measuring means 3. The control means 4 etc. as a detection means are provided.

そして、本実施例の膜ろ過処理装置に適用する制御手段4は、ろ過膜を通過する原水の流量(以下、通過流量と適宜称する)をろ過流量変更手段2に減少させ、通過流量の減少後に処理水質計測手段3から取り込んだ計測値に基づいて、ろ過膜の破断を検出する機能を有している。   And the control means 4 applied to the membrane filtration processing apparatus of a present Example reduces the flow volume of raw | natural water (henceforth a passage flow rate suitably) which passes a filtration membrane to the filtration flow volume change means 2, and after the passage flow volume decreases, Based on the measured value taken from the treated water quality measuring means 3, it has a function of detecting breakage of the filtration membrane.

より詳細に、本実施例の膜ろ過処理装置について説明する。膜ろ過手段1は、原水中の濁質や微粒子などを除去するろ過膜が実装されている。ろ過膜は、数千本の中空糸膜が組み込まれて構成されたモジュール単位で加工されている。このようなろ過膜は、膜の孔径よりも大きな微粒子をほぼ除去でき、しかも維持管理が容易であるから、浄水施設に導入するのに好ましい。   In more detail, the membrane filtration apparatus of a present Example is demonstrated. The membrane filtration means 1 is mounted with a filtration membrane that removes turbidity, fine particles and the like in the raw water. The filtration membrane is processed in units of modules configured by incorporating thousands of hollow fiber membranes. Such a filtration membrane is preferable for introduction into a water purification facility because it can substantially remove fine particles larger than the pore size of the membrane and is easy to maintain.

ろ過流量変更手段2は、膜ろ過手段1の上流側に直列に配設されている。ただし、ろ過流量変更手段2については、膜ろ過手段1の下流側に配設してもよい。このようなろ過流量変更手段2は、膜ろ過手段1のろ過流束を変更するポンプ等を有している。また、処理水質計測手段3は、膜ろ過手段1の下流側に配設されている。なお、本実施例の処理水質計測手段3として、高感度濁度計を採用している。   The filtration flow rate changing means 2 is arranged in series upstream of the membrane filtration means 1. However, the filtration flow rate changing means 2 may be arranged on the downstream side of the membrane filtration means 1. Such filtration flow rate changing means 2 has a pump or the like that changes the filtration flux of the membrane filtration means 1. Further, the treated water quality measuring means 3 is disposed on the downstream side of the membrane filtration means 1. In addition, the highly sensitive turbidimeter is employ | adopted as the treated water quality measurement means 3 of a present Example.

制御手段4は、処理水質計測手段3から計測信号を取り込む機能と、ろ過流量変更手段2に通過流量の変更指令を出力する機能と、膜ろ過手段1のろ過膜に破断が生じているか否かを判定する機能を有する。   The control means 4 has a function of taking a measurement signal from the treated water quality measuring means 3, a function of outputting a flow rate change command to the filtration flow rate changing means 2, and whether or not the filtration membrane of the membrane filtration means 1 is broken. It has the function to judge.

このように構成される膜ろ過処理装置の基本動作について説明する。まず、原水(例えば、表流水、伏流水、地下水)が膜ろ過手段1に供給される。供給された原水は、ろ過膜を通過するに際し、原水中の濁質等が分離除去される。膜ろ過手段1から流出するろ過水は、後段の水処理設備に供給される。   The basic operation of the membrane filtration apparatus configured as described above will be described. First, raw water (for example, surface water, underground water, groundwater) is supplied to the membrane filtration means 1. When the supplied raw water passes through the filtration membrane, turbidity in the raw water is separated and removed. The filtered water flowing out from the membrane filtration means 1 is supplied to a subsequent water treatment facility.

ここで、ろ過膜の破断を検出する動作について説明する。制御手段4は、膜ろ過処理装置が基本動作をしている際、処理水質計測手段3から濁度の計測値Aを第一の計測値として取り込む。   Here, the operation for detecting the breakage of the filtration membrane will be described. The control means 4 takes in the measured value A of turbidity from the treated water quality measuring means 3 as the first measured value when the membrane filtration apparatus is performing a basic operation.

次に、ろ過膜の破断を検出するに際し、制御手段4は、膜ろ過手段1の通過流量を減少させる指令をろ過流量変更手段2に出力する。ろ過流量変更手段2は、制御手段4の減少指令に応じ、通過流量を減少する。その後、制御手段4は、処理水質計測手段3から濁度の計測値Bを第二の計測値として取り込む。なお、通過流量を減少させた時から計測値Bを取得するまでの時間については、通過流量の減少後の水質を計測値Bに反映できるように設定すればよい。例えば、ろ過流量変更手段2から処理水質計測手段3までの配管長や通過流量などに基づいて、計測値Bの取得時間を決めればよい。   Next, when detecting the breakage of the filtration membrane, the control means 4 outputs a command for reducing the passage flow rate of the membrane filtration means 1 to the filtration flow rate changing means 2. The filtration flow rate changing means 2 reduces the passage flow rate in response to a decrease command from the control means 4. Then, the control means 4 takes in the turbidity measurement value B from the treated water quality measurement means 3 as the second measurement value. In addition, what is necessary is just to set so that the water quality after the reduction | decrease of a passage flow rate can be reflected in the measurement value B about the time from the time of reducing a passage flow amount until acquiring measurement value B. For example, the acquisition time of the measured value B may be determined based on the pipe length from the filtration flow rate changing unit 2 to the treated water quality measuring unit 3 or the passing flow rate.

次に、制御手段4は、計測値Aと計測値Bを比較し、比較結果に基づきろ過膜の破断を検出する。より具体的には、制御手段4は、計測値Bが計測値Aよりも大きい場合、ろ過膜の破断部分から原水が漏れているものと解釈し、ろ過膜に破断が生じているものと判定する。その場合、制御手段4は、通過流量をゼロにする指令をろ過流量変更手段2に出力する。ろ過流量変更手段2は、制御手段4の指令に応じ、通過流量をゼロにする。なお、制御手段4は、計測値Bが計測値A以下の場合、ろ過膜に破断がないものと判定し、その通過流量を元に戻す指令をろ過流量変更手段2に出力する。   Next, the control means 4 compares the measurement value A with the measurement value B, and detects the breakage of the filtration membrane based on the comparison result. More specifically, when the measured value B is larger than the measured value A, the control means 4 interprets that raw water is leaking from the ruptured portion of the filtration membrane, and determines that the rupture has occurred in the filtration membrane. To do. In that case, the control means 4 outputs a command to make the passage flow rate zero to the filtration flow rate changing means 2. The filtration flow rate changing means 2 makes the passage flow rate zero according to the command of the control means 4. When the measurement value B is equal to or less than the measurement value A, the control unit 4 determines that the filtration membrane is not broken, and outputs a command to restore the passage flow rate to the filtration flow rate changing unit 2.

要するに、本実施例の制御手段4は、ろ過膜の破断を検出するに際し、ろ過膜を通過する原水の流量を一時的に減少させ、減少前後のろ過水の濁度のそれぞれ(例えば、計測値Aと計測値B)を取得し、計測値Bが計測値Aよりも大きいとき、ろ過膜に破断が生じたものと判定する。   In short, when detecting the breakage of the filtration membrane, the control means 4 of the present embodiment temporarily decreases the flow rate of the raw water passing through the filtration membrane, and each of the turbidity of the filtrate water before and after the decrease (for example, measured value) A and measured value B) are acquired, and when measured value B is larger than measured value A, it is determined that the filter membrane has been broken.

すなわち、破断が生じたろ過膜の通過流量を減少させると、ろ過膜の正常部分を通過する水量は、ろ過膜に対する水圧の低下に起因して減るのに対し、破断部分を通過する水量は、正常部分よりも減少幅が小さい。ここで破断部分を通過する原水は、未処理であるため、濁質を比較的多く含む。したがって、通過流量の減少後のろ過水の単位体積あたりの濁度は、減少前よりも増加することになる。   That is, when the passage flow rate of the filtration membrane in which breakage occurs is reduced, the amount of water passing through the normal portion of the filtration membrane decreases due to a decrease in water pressure on the filtration membrane, whereas the amount of water passing through the breakage portion is The decrease is smaller than the normal part. Here, the raw water that passes through the broken portion is untreated, and therefore contains a relatively large amount of turbidity. Therefore, the turbidity per unit volume of filtered water after the reduction of the passage flow rate will increase more than before the reduction.

このような知見に基づいた本実施例によれば、ろ過膜の破断を検出するに際し、通過流量を減少させることにより、ろ過水の濁度を増加させることができる。その結果、例えば原水の濁度が比較的小さい場合でも、濁度計測器の検出感度にかかわらず、ろ過水の濁度を的確に検出できるため、ろ過膜の破断を検出する精度が向上する。よって、破断が生じたろ過膜に処置を施すのが的確になるから、安心かつ安全な浄水の供給が容易になる。なお、ここでの濁度とは、単位体積あたりの濁質の割合である。   According to the present embodiment based on such knowledge, the turbidity of filtered water can be increased by decreasing the passing flow rate when detecting the breakage of the filtration membrane. As a result, for example, even when the turbidity of the raw water is relatively small, the turbidity of the filtered water can be accurately detected regardless of the detection sensitivity of the turbidity measuring instrument, so that the accuracy of detecting the breakage of the filtration membrane is improved. Therefore, since it becomes appropriate to perform a treatment on the filter membrane in which breakage has occurred, it is easy to supply safe and safe purified water. In addition, turbidity here is the ratio of the turbidity per unit volume.

また、本実施例によれば、膜破断の有無を判定するに際し、通過流量の減少前後における濁度の差分の大きさを基準とするため、原水の濁度自体には左右されず、ろ過膜の漏れを的確に検出できる。   In addition, according to the present embodiment, when determining the presence or absence of membrane breakage, since it is based on the magnitude of the difference in turbidity before and after the reduction of the passage flow rate, it is not affected by the turbidity of the raw water itself, and the filtration membrane Can be accurately detected.

ここで通過流量とろ過水の濁度との関係について図2を参照して補足する。図2は、通過流量に対するろ過水の濁度の変化を計測した一例である。図2の縦軸は、ろ過水の濁度(ろ液濁度)を示し、横軸は、通過流量に対応するろ過流束を示している。なお、図2の計測値を取得するに際し、ろ過膜の中空糸膜を所定量だけ切断する度に、濁度が同じ原水をろ過膜に通過させた。   Here, the relationship between the passage flow rate and the turbidity of the filtered water will be supplemented with reference to FIG. FIG. 2 is an example of measuring the change in turbidity of filtered water relative to the passing flow rate. The vertical axis in FIG. 2 indicates the turbidity of filtrate (filtrate turbidity), and the horizontal axis indicates the filtration flux corresponding to the passing flow rate. In addition, when acquiring the measured value of FIG. 2, every time the hollow fiber membrane of the filtration membrane was cut | disconnected by predetermined amount, the raw | natural water with the same turbidity was allowed to pass through a filtration membrane.

図2に示すように、ろ過流束を増大させるにつれて、ろ過水の濁度が徐々に低減している。換言すると、ろ過流束を減少させると、ろ過水の濁度が徐々に増加する。このような計測結果によって得た知見に基づき、本実施例の膜ろ過処理装置が実現されている。すなわち、本実施例の膜ろ過処理装置は、ろ過流束つまり通過流量を減少させることにより、処理水質計測手段3の濁度計測による膜破断検出感度を向上できる。   As shown in FIG. 2, the turbidity of the filtrate is gradually reduced as the filtration flux is increased. In other words, when the filtration flux is decreased, the turbidity of the filtered water gradually increases. Based on the knowledge obtained from such measurement results, the membrane filtration apparatus of the present embodiment is realized. That is, the membrane filtration processing apparatus of the present embodiment can improve the membrane breakage detection sensitivity by the turbidity measurement of the treated water quality measuring means 3 by reducing the filtration flux, that is, the passing flow rate.

上述のとおり、本実施例の膜ろ過処理装置を説明したが、これに限られるものではない。例えば、処理水質計測手段3の計測値にばらつきがある場合、制御手段4は、処理水質計測手段3から例えば計測値Aを複数取得し、取得した計測値Aの平均値を第一の計測値として取得できる。計測値Bについても、複数の計測値Bの平均値を第二の計測値として取得できる。また、制御手段4は、処理水質計測手段3による計測値のばらつきを考慮した設定値を保持し、計測値Bと計測値Aの偏差(計測値B−計測値A)がその設定値を超えた場合に、ろ過膜に破断が生じていると判定できる。これにより、例えば経年劣化に起因して計測値がドリフトするなど、処理水質計測手段3の計測値がばらつく場合でも、その計測値に内包する誤差を低減できる。   As described above, the membrane filtration apparatus of the present embodiment has been described, but the present invention is not limited to this. For example, when the measured values of the treated water quality measuring means 3 vary, the control means 4 obtains, for example, a plurality of measured values A from the treated water quality measuring means 3, and sets the average value of the obtained measured values A as the first measured value. Can be obtained as Regarding the measurement value B, the average value of the plurality of measurement values B can be acquired as the second measurement value. Moreover, the control means 4 holds the set value in consideration of the variation in the measurement value by the treated water quality measurement means 3, and the deviation between the measurement value B and the measurement value A (measurement value B-measurement value A) exceeds the set value. In this case, it can be determined that the filter membrane is broken. Thereby, even when the measured value of the treated water quality measuring means 3 varies, for example, the measured value drifts due to aging deterioration, the error included in the measured value can be reduced.

また、制御手段4は、計測値Aと計測値Bを比較することに代えて、予め設定した上限値Hと計測値Bを比較する。そして、制御手段4は、計測値Bが上限値Hを超えた場合、ろ過膜の破断部分から原水が漏れていると解釈し、ろ過膜の破断を検出できる。これにより、膜破断の有無を判定するに際し、閾値である設定値を基準にするため、膜破断検出処理を簡単にすることができる。   Further, the control means 4 compares the preset upper limit value H with the measured value B instead of comparing the measured value A with the measured value B. And the control means 4 can interpret that the raw | natural water has leaked from the fracture | rupture part of a filtration membrane, when the measured value B exceeds the upper limit H, and can detect the fracture | rupture of a filtration membrane. Thereby, when determining the presence or absence of a film rupture, since the set value which is a threshold is used as a reference, the film rupture detection process can be simplified.

また、制御手段4は、ろ過膜に破断がないものと判定した際、通過流量を元に戻すことから、膜ろ過処理の運転を継続できるので、膜破断検出処理に伴う運転停止時間を短縮できる。また、制御手段4は、通過流量を元に戻すことに代えて、通過流量を元の量よりも増大させることができる。これにより、膜ろ過手段1を一時的に停止したことに起因する処理水総量の減少を補填できるため、所定の処理水量を確保できる。   In addition, when the control means 4 determines that there is no breakage in the filtration membrane, the flow rate is restored, so that the operation of the membrane filtration process can be continued, so that the operation stop time associated with the membrane breakage detection process can be shortened. . Further, the control means 4 can increase the passing flow rate more than the original amount instead of returning the passing flow rate to the original. Thereby, since the reduction | decrease of the total amount of treated water resulting from having stopped the membrane filtration means 1 temporarily can be compensated, a predetermined treated water amount can be ensured.

また、膜ろ過手段1の下流側に貯留槽を設け、ろ過膜の破断が検出された場合、膜ろ過手段1から流出するろ過水を貯留槽に一時的に溜めることができる。これにより、ろ過膜の破断に起因してろ過水の濁度が上昇した場合、後段の水処理設備にそのろ過水を供給することを防止できる。また、ろ過水を貯留槽に溜めることに代えて、濁度を低下させるための消毒剤の添加量を増加してもよい。   Further, when a storage tank is provided on the downstream side of the membrane filtration means 1 and a breakage of the filtration membrane is detected, the filtrate water flowing out from the membrane filtration means 1 can be temporarily stored in the storage tank. Thereby, when the turbidity of filtrate water rises resulting from the fracture | rupture of a filtration membrane, it can prevent supplying the filtrate water to a water treatment installation of a back | latter stage. Moreover, it replaces with storing filtered water in a storage tank, and you may increase the addition amount of the disinfectant for reducing turbidity.

また、制御手段4は、ろ過水の濁度についての設定値Sを保持し、計測手段3の計測値がその設定値S以上である場合に、ろ過膜の破断検出処理を開始できる。ここでの設定値Sについては、上限値Hが設定される場合、上限値Hよりも小さい値に設定される。また、制御手段4は、ろ過膜の破断検出処理を所定時刻、所定間隔で開始できる。   Moreover, the control means 4 can hold | maintain the setting value S about the turbidity of filtered water, and when the measured value of the measurement means 3 is more than the setting value S, it can start the fracture | rupture detection process of a filtration membrane. The set value S here is set to a value smaller than the upper limit value H when the upper limit value H is set. Moreover, the control means 4 can start the filtration membrane breakage detection process at a predetermined time and a predetermined interval.

なお、従前の破断検出法として、逆洗時に加圧気体を充填し、その圧力を流量の変化に基づいてろ過膜の破断を検出する方法がある(例えば、特開2000−93765号公報)。しかし、この方法では、検出処理が逆洗時ごとに実行されるため、ろ過膜に破断が生じた場合でも、その破断が次の逆洗時まで検出されないというタイムラグが生じる。この点、本実施例によれば、設定値Sに基づいた開始処理により、ろ過膜の破断をオンラインで検出できる。また、開始時刻又は開始間隔を自在に設定できるため、ろ過膜の破断を必要に応じて臨機応変に検出できる。   As a conventional rupture detection method, there is a method of filling a pressurized gas at the time of backwashing and detecting the rupture of the filtration membrane based on a change in the flow rate of the pressure (for example, Japanese Patent Laid-Open No. 2000-93765). However, in this method, since the detection process is executed every time the backwashing is performed, even if a rupture occurs in the filtration membrane, there occurs a time lag that the rupture is not detected until the next backwashing. In this regard, according to the present embodiment, the rupture of the filtration membrane can be detected online by the start process based on the set value S. Moreover, since the start time or the start interval can be set freely, it is possible to detect the breakage of the filtration membrane as needed.

また、本実施例の膜ろ過処理装置を用いた膜破断検出方法は、原水に含まれる濁質をろ過膜で分離除去するろ過工程と、ろ過膜を通過したろ過水の濁度を計測する水質計測工程と、水質計測工程の計測値に基づきろ過膜の破断を検出する膜破断検出工程とを備える。そして、その膜破断検出工程は、ろ過膜を通過する原水の流量を減少させ、通過流量の減少後に水質計測手段から取り込んだ計測値に基づいて、ろ過膜の破断を検出することを特徴とする。   In addition, the membrane breakage detection method using the membrane filtration apparatus of the present embodiment includes a filtration step for separating and removing turbidity contained in raw water with a filtration membrane, and a water quality for measuring the turbidity of filtered water that has passed through the filtration membrane. A measurement step, and a membrane breakage detection step for detecting breakage of the filtration membrane based on the measurement value of the water quality measurement step. And the membrane breakage detection step reduces the flow rate of the raw water passing through the filtration membrane, and detects the breakage of the filtration membrane based on the measured value taken from the water quality measuring means after the passage flow rate is reduced. .

以上、本実施例によれば、膜ろ過手段1から流出するろ過水の濁度を増加させ、処理水質計測手段3による膜破断検出の感度を向上し、より安心・安全な浄水を供給する膜ろ過処理装置の運転方法を提供できる。   As described above, according to the present embodiment, the turbidity of the filtrate flowing out from the membrane filtration means 1 is increased, the sensitivity of the membrane breakage detection by the treated water quality measurement means 3 is improved, and a membrane that supplies safer and safer purified water. A method for operating the filtration apparatus can be provided.

(実施例1−2)
図3は、本発明を適用した第一の実施形態の膜ろ過処理装置の第二の実施例を示す図である。本実施例の膜ろ過処理装置は、膜ろ過手段1の上流側に設置した被処理水質計測手段5の計測値に基づき、膜破断検出処理を開始する点で、実施例1−1と異なる。ここでの被処理水質計測手段5は、膜ろ過手段1に供給される原水の濁度を計測する濁度計であり、計測値を制御手段4に送信する。
(Example 1-2)
FIG. 3 is a diagram showing a second example of the membrane filtration apparatus of the first embodiment to which the present invention is applied. The membrane filtration processing apparatus of the present embodiment is different from the embodiment 1-1 in that the membrane breakage detection process is started based on the measurement value of the treated water quality measurement means 5 installed on the upstream side of the membrane filtration means 1. The treated water quality measuring means 5 here is a turbidimeter that measures the turbidity of the raw water supplied to the membrane filtration means 1, and transmits the measured value to the control means 4.

本実施例の膜破断検出処理について説明する。まず、制御手段4は、膜ろ過処理装置が基本動作をしている際、処理水質計測手段3から濁度の計測値Aを所定間隔で取り込む。次に、制御手段4は、予め設定した下限値Lと計測値Aを比較するそして、制御手段4は、計測値Aが下限値L以下の場合、処理対象の原水は濁度が比較的小さなものであると解釈し、膜破断検出処理を開始する。膜破断検出処理の内容については、実施例1−1と同様である。   The film break detection process of the present embodiment will be described. First, the control means 4 takes the measured value A of turbidity from the treated water quality measuring means 3 at a predetermined interval when the membrane filtration apparatus is performing a basic operation. Next, the control means 4 compares the preset lower limit L with the measured value A. When the measured value A is less than or equal to the lower limit L, the control means 4 has relatively low turbidity in the raw water to be treated. The film break detection process is started. The contents of the film break detection process are the same as those in Example 1-1.

なお、計測値Aが下限値Lを下回ることが長時間に渡る場合は、制御手段4は、予め設定した頻度で処理を開始してもよい。換言すると、ろ過流量変更手段2は、制御手段4の指令に応じ、通過流量を間欠的に減少することもできる。   In addition, when it is over a long time that the measured value A falls below the lower limit value L, the control unit 4 may start the process at a preset frequency. In other words, the filtration flow rate changing means 2 can also intermittently reduce the passing flow rate in accordance with the command of the control means 4.

本実施例によれば、実施例1−1で説明した効果に加えて、処理対象の原水濁度が比較的小さい場合を被処理水質計測手段5により自動検出できる。すなわち、膜破断検出処理を開始すべき場合を自動検出できる。その結果、ろ過膜の破断を的確に検出できるとともに、装置の使い勝手が向上する。   According to the present embodiment, in addition to the effects described in Embodiment 1-1, a case where the raw water turbidity to be treated is relatively small can be automatically detected by the treated water quality measuring means 5. That is, it is possible to automatically detect when the film break detection process should be started. As a result, the breakage of the filtration membrane can be accurately detected, and the usability of the apparatus is improved.

(実施例1−3)
図4は、本発明を適用した第一の実施形態の膜ろ過処理装置の第三の実施例を示す図である。本実施例の膜ろ過処理装置は、図1の膜ろ過手段1とろ過流量変更手段2のそれぞれを複数配設した点で、実施例1−1と異なる。なお、本実施例では、膜ろ過手段1とろ過流量変更手段2を3つずつ配設した例を説明するが、数については適宜増やしてよい。
(Example 1-3)
FIG. 4 is a diagram showing a third example of the membrane filtration apparatus of the first embodiment to which the present invention is applied. The membrane filtration processing apparatus of the present embodiment differs from that of Example 1-1 in that a plurality of the membrane filtration means 1 and the filtration flow rate changing means 2 of FIG. In the present embodiment, an example in which three membrane filtration means 1 and three filtration flow rate changing means 2 are arranged will be described, but the number may be increased as appropriate.

図4に示すように、膜ろ過手段1−1〜1−3は、並列に配設されている。また、ろ過流量変更手段2−1〜2−3は、膜ろ過手段1−1〜1−3のそれぞれの上流側に設けられている。例えば、ろ過流量変更手段2−1は、膜ろ過手段1−1の上流側に直列に設けられている。なお、処理水質計測手段3は、膜ろ過手段1−1〜1−3から流出する処理水の合流後の濁度を計測する。   As shown in FIG. 4, the membrane filtration means 1-1 to 1-3 are arranged in parallel. The filtration flow rate changing means 2-1 to 2-3 are provided on the upstream side of the membrane filtration means 1-1 to 1-3. For example, the filtration flow rate changing means 2-1 is provided in series upstream of the membrane filtration means 1-1. The treated water quality measuring means 3 measures the turbidity after joining the treated water flowing out from the membrane filtration means 1-1 to 1-3.

本実施例の膜破断検出処理を開始すると、制御手段4は、処理水質計測手段3から濁度の計測値Aを取り込む。次に、制御手段4は、膜ろ過手段1−1の通過流量を減少させる指令をろ過流量変更手段2−1に出力する。ろ過流量変更手段2−1は、制御手段4の指令に応じ、膜ろ過手段1−1の通過流量を減少する。次に、制御手段4は、処理水質計測手段3から濁度の計測値B1を取り込む。なお、通過流量を減少させた時から計測値Bを取得するまでの時間は、通過流量の減少後の水質を計測値Bに反映できるように設定される。   When the membrane breakage detection process of the present embodiment is started, the control means 4 takes in the measured value A of turbidity from the treated water quality measurement means 3. Next, the control means 4 outputs a command for decreasing the passage flow rate of the membrane filtration means 1-1 to the filtration flow rate changing means 2-1. The filtration flow rate changing means 2-1 decreases the passage flow rate of the membrane filtration means 1-1 according to the command of the control means 4. Next, the control unit 4 takes in the turbidity measurement value B <b> 1 from the treated water quality measurement unit 3. The time from when the passage flow rate is reduced until the measurement value B is acquired is set so that the water quality after the reduction of the passage flow rate can be reflected in the measurement value B.

そして、制御手段4は、計測値Aと計測値B1を比較し、計測値B1が計測値Aよりも大きい場合、膜ろ過手段1−1のろ過膜に破断が生じているものと判定する。その場合、制御手段4は、膜ろ過手段1−1の通過流量をゼロにする指令をろ過流量変更手段2−1に出力する。なお、制御手段4は、計測値B1が計測値A以下の場合、膜ろ過手段1−1のろ過膜に破断がないものと判定し、その通過流量を元に戻す指令をろ過流量変更手段2−1に出力する。膜ろ過手段1−1のろ過膜の破断を検出する例を代表的に説明したが、膜ろ過手段1−2、1−3の場合も同様である。   And the control means 4 compares the measured value A and measured value B1, and when measured value B1 is larger than measured value A, it determines with the fracture | rupture having arisen in the filtration membrane of the membrane filtration means 1-1. In that case, the control means 4 outputs the instruction | command which makes the passage flow rate of the membrane filtration means 1-1 to zero to the filtration flow rate change means 2-1. When the measurement value B1 is equal to or less than the measurement value A, the control means 4 determines that the filtration membrane of the membrane filtration means 1-1 is not broken, and gives a command to restore the passage flow rate to the filtration flow rate change means 2 Output to -1. Although the example which detects the fracture | rupture of the filtration membrane of the membrane filtration means 1-1 was demonstrated typically, the case of the membrane filtration means 1-2 and 1-3 is also the same.

このような膜破断検出処理を膜ろ過手段1−1〜1−3ごとに順番に実行すると、ろ過膜に破断が生じた膜ろ過手段(例えば、膜ろ過手段1−1)を的確に特定できる。これにより、複数の膜ろ過手段1−1〜1−3が配設された場合でも、実施例1−1で説明した効果に加えて、停止すべき膜ろ過手段(例えば、膜ろ過手段1−1)を的確に特定できるため、安心かつ安全な浄水の供給が容易になる。   When such membrane breakage detection processing is executed in order for each of the membrane filtration means 1-1 to 1-3, the membrane filtration means (for example, the membrane filtration means 1-1) in which the filtration membrane is broken can be accurately identified. . Thereby, even when a plurality of membrane filtration means 1-1 to 1-3 are provided, in addition to the effect described in the embodiment 1-1, the membrane filtration means to be stopped (for example, the membrane filtration means 1- 1) can be specified accurately, so it is easy to supply clean and safe water.

また、制御手段4は、複数の膜ろ過手段1−1〜1−3のうち、ろ過膜に破断が生じた例えば膜ろ過手段1−1を特定すると、他の膜ろ過手段1−2、1−3の通過流量を増加させる指令を過流量変更手段2−2、2−3に出力する。これにより、膜ろ過手段1−1を停止することに起因するろ過水の減少を補填できるため、所定の処理水量を確保できる。また、予備の膜ろ過手段を設け、例えば膜ろ過手段1−1が停止したとき、その予備の膜ろ過手段を一時的に稼動させてもよい。   Moreover, if the control means 4 specifies the membrane filtration means 1-1 in which the filtration membrane broke among the plurality of membrane filtration means 1-1 to 1-3, for example, the other membrane filtration means 1-2, 1 -3 is output to the overflow rate changing means 2-2 and 2-3. Thereby, since the reduction | decrease of the filtrate water resulting from stopping the membrane filtration means 1-1 can be compensated, predetermined | prescribed amount of treated water is securable. Further, a spare membrane filtration means may be provided, and for example, when the membrane filtration means 1-1 is stopped, the spare membrane filtration means may be temporarily operated.

(実施例1−4)
図5は、本発明を適用した第一の実施形態の膜ろ過処理装置の第四の実施例を示す図である。本実施例の膜ろ過処理装置は、膜ろ過手段1−1〜1−3の上流側に設置した被処理水質計測手段5の計測値に基づき膜破断検出処理を開始する点で、実施例1−3と異なる。ここでの被処理水質計測手段5は、膜ろ過手段1−1〜1−3に分岐して供給される原水の濁度を計測する濁度計であり、計測値を制御手段4に送信する。
(Example 1-4)
FIG. 5 is a diagram showing a fourth example of the membrane filtration apparatus of the first embodiment to which the present invention is applied. The membrane filtration treatment apparatus of the present embodiment is the first embodiment in that the membrane breakage detection process is started based on the measurement value of the treated water quality measurement means 5 installed on the upstream side of the membrane filtration means 1-1 to 1-3. -3. The treated water quality measuring means 5 here is a turbidimeter that measures the turbidity of the raw water that is branched and supplied to the membrane filtration means 1-1 to 1-3, and transmits the measured value to the control means 4. .

すなわち、図5に示すように、本実施例の膜ろ過処理装置は、実施例1−3の膜ろ過処理装置に、実施例1−2の被処理水質計測手段5を配設し、被処理水質計測手段5を制御する機能を制御手段4に実装したものである。したがって、本実施例によれば、実施例1−3で説明した効果に加えて、処理対象の原水濁度が比較的小さい場合を被処理水質計測手段5により自動検出できる。換言すると、膜破断検出処理を開始すべき場合を自動検出できる。その結果、ろ過膜の破断を的確に検出できるとともに、装置の使い勝手が向上する。   That is, as shown in FIG. 5, the membrane filtration treatment apparatus of the present example is provided with the treated water quality measuring means 5 of Example 1-2 in the membrane filtration treatment apparatus of Example 1-3, A function for controlling the water quality measuring means 5 is implemented in the control means 4. Therefore, according to the present embodiment, in addition to the effects described in Embodiment 1-3, a case where the raw water turbidity to be treated is relatively small can be automatically detected by the treated water quality measuring means 5. In other words, it is possible to automatically detect when the film break detection process should be started. As a result, the breakage of the filtration membrane can be accurately detected, and the usability of the apparatus is improved.

参考例
本発明を適用した膜ろ過処理装置の参考例について説明する。本参考例の膜ろ過処理装置は、ろ過膜の破断を検出するに際し、原水に濁質源を添加する点で、第一の実施形態と異なる。より具体的には、本参考例の膜ろ過処理装置は、膜ろ過手段の上流側の原水に濁質源を添加させ、濁質源の添加後に取り込んだろ過水の濁度に基づいて、ろ過膜の破断を検出する。
( Reference example )
A reference example of a membrane filtration apparatus to which the present invention is applied will be described. The membrane filtration apparatus of the present reference example differs from the first embodiment in that a turbidity source is added to raw water when detecting the breakage of the filtration membrane. More specifically, the membrane filtration treatment apparatus of this reference example adds a turbidity source to the raw water upstream of the membrane filtration means, and performs filtration based on the turbidity of filtrated water taken after the addition of the turbidity source. Detect film breaks.

以下に、第一ないし第四の実施例により本参考例の膜ろ過処理装置を説明する。ただし、各実施例又は第一の実施形態で説明した構成部や変形例等を組み合わせ、あるいは置き換えるなど、必要に応じて変更することができる。なお、第一の実施形態と相違する点を中心に説明し、相互に対応する箇所については適宜省略する。 Below, the membrane filtration apparatus of this reference example is demonstrated by the 1st thru | or 4th Example. However, it can be changed as necessary, for example, by combining or replacing the constituent parts and modifications described in each example or the first embodiment. Note that differences from the first embodiment will be mainly described, and portions corresponding to each other will be omitted as appropriate.

(実施例2−1)
図6は、本発明を適用した参考例の膜ろ過処理装置の第一の実施例を示す図である。図6に示すように、濁質源添加手段6は、その添加口が膜ろ過手段1の上流側の配管に接続している。このような濁質源添加手段6は、制御手段4の指令に応じ、膜ろ過手段1に供給する原水に濁質源を添加する。ここでの濁質源は、次亜塩素酸カルシウム、あるいは1mm以下の気泡など、水に溶解する性質を有し、所定時間で溶解により消滅する物質を用いるのがよい。
(Example 2-1)
FIG. 6 is a diagram showing a first embodiment of a membrane filtration apparatus of a reference example to which the present invention is applied. As shown in FIG. 6, the turbidity source addition means 6 has an addition port connected to a pipe on the upstream side of the membrane filtration means 1. Such a turbidity source addition means 6 adds a turbidity source to the raw water supplied to the membrane filtration means 1 in accordance with a command from the control means 4. As the turbidity source, it is preferable to use a substance that has a property of dissolving in water, such as calcium hypochlorite or bubbles of 1 mm or less, and disappears by dissolution in a predetermined time.

本実施例の膜破断検出処理について説明する。制御手段4は、膜ろ過処理装置が基本動作をしている際、処理水質計測手段3から濁度の計測値Aを取り込む。   The film break detection process of the present embodiment will be described. The control means 4 takes in the measured value A of turbidity from the treated water quality measuring means 3 when the membrane filtration apparatus is performing a basic operation.

次に、ろ過膜の破断を検出するに際し、制御手段4は、濁質源の添加指令を濁質源添加手段6に出力する。濁質源添加手段6は、制御手段4の指令に応じ、処理対象の原水に濁質源を所定量だけ添加する。ここでの添加量は、濁質源の溶解速度や、添加位置から処理水質計測手段3の計測位置までの流下時間を考慮して決めればよい。なお、流下時間は、ろ過膜に破断が生じている際に予め計測した時間である。   Next, when detecting the breakage of the filtration membrane, the control means 4 outputs a turbidity source addition command to the turbidity source addition means 6. The turbidity source addition means 6 adds a predetermined amount of the turbidity source to the raw water to be treated in accordance with the command from the control means 4. The amount added here may be determined in consideration of the dissolution rate of the turbidity source and the flow time from the addition position to the measurement position of the treated water quality measuring means 3. The flow-down time is a time measured in advance when the filter membrane is broken.

濁質源が添加された後、制御手段4は、処理水質計測手段3から濁度の計測値Bを取り込む。なお、濁質源を添加した時から計測値Bを取得するまでの時間については、濁質源による水質の濁度を計測値Bに反映できるように設定すればよい。例えば、濁質源の添加位置から処理水質計測手段3の計測位置までの配管長さや、通過流量などに基づいて、計測値Bの取得時間を決めればよい。   After the turbidity source is added, the control means 4 takes in the measured value B of turbidity from the treated water quality measurement means 3. In addition, what is necessary is just to set so that the turbidity of the water quality by a turbidity source can be reflected in the measured value B about the time from the time of adding a turbidity source until acquisition of the measured value B. For example, the acquisition time of the measurement value B may be determined based on the length of the pipe from the addition position of the turbidity source to the measurement position of the treated water quality measurement means 3, the passing flow rate, and the like.

次に、制御手段4は、計測値Aと計測値Bを比較し、比較結果に基づきろ過膜の破断を検出する。より具体的には、制御手段4は、計測値Bが計測値Aよりも大きい場合、ろ過膜の破断部分から濁質源が漏れているものと解釈し、ろ過膜に破断が生じているものと判定する。判定後の処理は、実施例1−1と同様である。また、ろ過水に含まれる濁質源は、処理水質計測手段3の計測位置の下流側で消滅する。なお、制御手段4は、計測値Bが計測値A以下の場合、ろ過膜に破断がないものと判定する。   Next, the control means 4 compares the measurement value A with the measurement value B, and detects the breakage of the filtration membrane based on the comparison result. More specifically, when the measured value B is larger than the measured value A, the control means 4 interprets that the turbidity source is leaking from the broken portion of the filtration membrane, and the filtration membrane is broken. Is determined. The processing after the determination is the same as that of Example 1-1. Further, the turbidity source contained in the filtered water disappears on the downstream side of the measurement position of the treated water quality measuring means 3. Note that when the measurement value B is equal to or less than the measurement value A, the control unit 4 determines that the filtration membrane is not broken.

本実施例の濁質源として採用した次亜塩素酸カルシウムは、殺菌作用やろ過膜の洗浄作用を奏する。また、1mm以下の気泡は、溶解または圧力刺激で圧壊するとOHラジカルを発生するため、発生したOHラジカルにより殺菌作用やろ過膜の洗浄作用を奏する。したがって、本実施例によれば、ろ過膜の破断を的確に検出できる効果に加えて、浄水の消毒効果や、ろ過膜の洗浄効果も発揮できる。   Calcium hypochlorite employed as a turbidity source in this example has a bactericidal action and a filter membrane cleaning action. In addition, since bubbles of 1 mm or less generate OH radicals when dissolved or crushed by pressure stimulation, the generated OH radicals exert a bactericidal action and a filter membrane cleaning action. Therefore, according to the present Example, in addition to the effect which can detect the fracture | rupture of a filtration membrane exactly, the disinfection effect of purified water and the cleaning effect of a filtration membrane can also be exhibited.

なお、従前の破断検出法として、ろ過水の濁度を計測するに際し、カオリンや珪素土などの濁質を原水に添加する方法がある(例えば、特開平6−320157号公報)。しかし、この方法では、衛生上無害ではあるがカオリンや珪素土が処理水に混入するため、好ましいものとは言えない。この点、本実施例によれば、次亜鉛素酸カルシウム等の濁質源は、所定時間経過後に消滅するため、後段における処理水の浄化度が向上する。   As a conventional method for detecting breakage, there is a method of adding turbidity such as kaolin or silicon earth to raw water when measuring the turbidity of filtered water (for example, JP-A-6-320157). However, although this method is harmless for hygiene, it is not preferable because kaolin and silicon earth are mixed into the treated water. In this respect, according to the present embodiment, the turbidity source such as calcium hypozinc acid disappears after the elapse of a predetermined time, so that the degree of purification of the treated water in the subsequent stage is improved.

また、本実施例の膜ろ過処理装置を用いた膜破断検出方法は、原水に含まれる濁質をろ過膜で分離除去するろ過工程と、ろ過膜を通過したろ過水の濁度を計測する水質計測工程と、水質計測工程の計測値に基づきろ過膜の破断を検出する膜破断検出工程とを備えている。そして、その膜破断検出工程は、膜ろ過手段の上流側の原水に濁質源を添加させ、濁質源の添加後に水質計測手段から取り込んだ計測値に基づいて、ろ過膜の破断を検出する。   In addition, the membrane breakage detection method using the membrane filtration apparatus of the present embodiment includes a filtration step for separating and removing turbidity contained in raw water with a filtration membrane, and a water quality for measuring the turbidity of filtered water that has passed through the filtration membrane. A measurement step and a membrane breakage detection step of detecting a breakage of the filtration membrane based on the measurement value of the water quality measurement step are provided. Then, the membrane breakage detection step adds a turbidity source to the raw water upstream of the membrane filtration means, and detects the breakage of the filtration membrane based on the measured value taken from the water quality measurement means after the addition of the turbidity source. .

(実施例2−2)
図7は、本発明を適用した参考例の膜ろ過処理装置の第二の実施例を示す図である。本実施例の膜ろ過処理装置は、膜ろ過手段1の上流側に設置した被処理水質計測手段5の計測値に基づき、膜破断検出処理を開始する点で、実施例2−1と異なる。ここでの被処理水質計測手段5は、膜ろ過手段1に供給される原水の濁度を計測する濁度計であり、計測値を制御手段4に送信する。
(Example 2-2)
FIG. 7 is a diagram showing a second embodiment of the membrane filtration apparatus of the reference example to which the present invention is applied. The membrane filtration apparatus of the present embodiment is different from the embodiment 2-1 in that the membrane breakage detection process is started based on the measurement value of the water quality measurement means 5 to be treated installed on the upstream side of the membrane filtration means 1. The treated water quality measuring means 5 here is a turbidimeter that measures the turbidity of the raw water supplied to the membrane filtration means 1, and transmits the measured value to the control means 4.

すなわち、図7に示すように、本実施例の膜ろ過処理装置は、図6の膜ろ過処理装置に、図3の被処理水質計測手段5を配設し、被処理水質計測手段5を制御する機能を制御手段4に実装したものである。したがって、本実施例によれば、実施例2−1で説明した効果に加えて、処理対象の原水濁度が比較的小さい場合を被処理水質計測手段5により自動検出できる。換言すると、膜破断検出処理を開始すべき場合を自動検出できる。その結果、ろ過膜の破断を的確に検出できるとともに、装置の使い勝手が向上する。   That is, as shown in FIG. 7, the membrane filtration apparatus of the present embodiment has the treated water quality measuring means 5 of FIG. 3 disposed in the membrane filtration treatment apparatus of FIG. This function is implemented in the control means 4. Therefore, according to the present embodiment, in addition to the effects described in Embodiment 2-1, when the raw water turbidity to be treated is relatively small, the treated water quality measuring means 5 can automatically detect. In other words, it is possible to automatically detect when the film break detection process should be started. As a result, the breakage of the filtration membrane can be accurately detected, and the usability of the apparatus is improved.

(実施例2−3)
図8は、本発明を適用した参考例の膜ろ過処理装置の第三の実施例を示す図である。本実施例の膜ろ過処理装置は、図6の膜ろ過手段1とろ過流量変更手段2のそれぞれを複数配設した点で、実施例2−1と異なる。なお、本実施例では、膜ろ過手段1とろ過流量変更手段2を3つずつ配設した例を説明するが、数については適宜増やしてよい。
(Example 2-3)
FIG. 8 is a diagram showing a third embodiment of the membrane filtration apparatus of the reference example to which the present invention is applied. The membrane filtration processing apparatus of the present embodiment is different from that of Example 2-1 in that a plurality of the membrane filtration means 1 and the filtration flow rate changing means 2 of FIG. In the present embodiment, an example in which three membrane filtration means 1 and three filtration flow rate changing means 2 are arranged will be described, but the number may be increased as appropriate.

図8に示すように、膜ろ過手段1−1〜1−3は、並列に配設されている。また、ろ過流量変更手段2−1〜2−3は、膜ろ過手段1−1〜1−3のそれぞれの上流側に設けられている。例えば、ろ過流量変更手段2−1は、膜ろ過手段1−1の上流側に直列に設けられている。なお、処理水質計測手段3は、膜ろ過手段1−1〜1−3から流出する処理水の合流後の濁度を計測する。   As shown in FIG. 8, the membrane filtration means 1-1 to 1-3 are arranged in parallel. The filtration flow rate changing means 2-1 to 2-3 are provided on the upstream side of the membrane filtration means 1-1 to 1-3. For example, the filtration flow rate changing means 2-1 is provided in series upstream of the membrane filtration means 1-1. The treated water quality measuring means 3 measures the turbidity after joining the treated water flowing out from the membrane filtration means 1-1 to 1-3.

本実施例の膜ろ過処理装置に適用する制御手段4は、膜ろ過処理装置が基本動作をしている際、処理水質計測手段3から濁度の計測値Aを第一の計測値として取り込む。次に、ろ過膜の破断を検出するに際し、制御手段4は、濁質源の添加指令を濁質源添加手段6に出力する。濁質源添加手段6は、制御手段4の指令に応じ、膜ろ過手段1−1に供給する原水に濁質源を所定量だけ添加する。次に、制御手段4は、処理水質計測手段3から濁度の計測値B1を取り込む。なお、濁質源を添加した時から計測値B1を取得するまでの時間については、濁質源添加後の水質を計測値B1に反映できるように設定すればよい。   The control means 4 applied to the membrane filtration processing apparatus of this embodiment takes in the measured value A of turbidity from the treated water quality measuring means 3 as the first measurement value when the membrane filtration processing apparatus is performing a basic operation. Next, when detecting the breakage of the filtration membrane, the control means 4 outputs a turbidity source addition command to the turbidity source addition means 6. The turbidity source addition means 6 adds a predetermined amount of the turbidity source to the raw water supplied to the membrane filtration means 1-1 according to the command of the control means 4. Next, the control unit 4 takes in the turbidity measurement value B <b> 1 from the treated water quality measurement unit 3. In addition, what is necessary is just to set so that the water quality after addition of a turbidity source can be reflected in measurement value B1 about the time from the time of adding a turbidity source until acquisition of measured value B1.

そして、制御手段4は、計測値Aと計測値B1を比較し、計測値B1が計測値Aよりも大きい場合、膜ろ過手段1−1のろ過膜に破断が生じているものと判定する。なお、制御手段4は、計測値Bが計測値A以下の場合、膜ろ過手段1−1のろ過膜に破断がないものと判定する。判定後の処理は、第一の実施形態と同様である。膜ろ過手段1−1のろ過膜の破断を検出する例を代表的に説明したが、膜ろ過手段1−2、1−3の場合も同様である。   And the control means 4 compares the measured value A and measured value B1, and when measured value B1 is larger than measured value A, it determines with the fracture | rupture having arisen in the filtration membrane of the membrane filtration means 1-1. When the measurement value B is equal to or less than the measurement value A, the control unit 4 determines that the filtration membrane of the membrane filtration unit 1-1 is not broken. Processing after the determination is the same as in the first embodiment. Although the example which detects the fracture | rupture of the filtration membrane of the membrane filtration means 1-1 was demonstrated typically, the case of the membrane filtration means 1-2 and 1-3 is also the same.

このような膜破断検出処理を膜ろ過手段1−1〜1−3ごとに順番に実行すると、ろ過膜に破断が生じた膜ろ過手段(例えば、膜ろ過手段1−1)を特定できる。したがって、本実施例によれば、実施例2−1で説明した効果に加えて、複数の膜ろ過手段1−1〜1−3が配設された場合でも、停止すべき膜ろ過手段(例えば、膜ろ過手段1−1)を的確に特定できるため、安心かつ安全な浄水の供給が容易になる。   When such a membrane breakage detection process is executed in order for each of the membrane filtration means 1-1 to 1-3, the membrane filtration means (for example, the membrane filtration means 1-1) in which the filtration membrane is broken can be specified. Therefore, according to the present embodiment, in addition to the effects described in the embodiment 2-1, even when the plurality of membrane filtration means 1-1 to 1-3 are disposed, the membrane filtration means to be stopped (for example, Since the membrane filtration means 1-1) can be accurately specified, safe and safe water supply can be facilitated.

(実施例2−4)
図9は、本発明を適用した参考例の膜ろ過処理装置の第四の実施例を示す図である。本実施例の膜ろ過処理装置は、膜ろ過手段1−1〜1−3の上流側に設置した被処理水質計測手段5の計測値に基づき膜破断検出処理を開始する点で、実施例2−3と異なる。ここでの被処理水質計測手段5は、膜ろ過手段1−1〜1−3に分岐して供給される原水の濁度を計測する濁度計であり、計測値を制御手段4に送信する。
(Example 2-4)
FIG. 9 is a diagram showing a fourth embodiment of the membrane filtration apparatus of the reference example to which the present invention is applied. The membrane filtration treatment apparatus of the present embodiment is the second embodiment in that the membrane breakage detection process is started based on the measurement value of the treated water quality measurement means 5 installed on the upstream side of the membrane filtration means 1-1 to 1-3. -3. The treated water quality measuring means 5 here is a turbidimeter that measures the turbidity of the raw water that is branched and supplied to the membrane filtration means 1-1 to 1-3, and transmits the measured value to the control means 4. .

すなわち、図9に示すように、本実施例の膜ろ過処理装置は、図8の膜ろ過処理装置に、図5の被処理水質計測手段5を配設し、被処理水質計測手段5を制御する機能を制御手段4に実装したものである。したがって、本実施例によれば、実施例2−3で説明した効果に加えて、処理対象の原水濁度が比較的小さい場合を被処理水質計測手段5により自動検出できる。換言すると、膜破断検出処理を開始すべき場合を自動検出できる。その結果、ろ過膜の破断を的確に検出できるとともに、装置の使い勝手が向上する。   That is, as shown in FIG. 9, the membrane filtration apparatus of the present embodiment is provided with the treated water quality measuring means 5 of FIG. 5 in the membrane filtration treatment apparatus of FIG. 8, and controls the treated water quality measuring means 5. This function is implemented in the control means 4. Therefore, according to the present embodiment, in addition to the effects described in Embodiment 2-3, a case where the raw water turbidity to be treated is relatively small can be automatically detected by the treated water quality measuring means 5. In other words, it is possible to automatically detect when the film break detection process should be started. As a result, the breakage of the filtration membrane can be accurately detected, and the usability of the apparatus is improved.

以上、第一の実施形態及び参考例によれば、ろ過膜を通過する原水の流量を減少することにより、あるいは、ろ過水を通過する原水に濁質源を添加することにより、膜ろ過手段1のろ過膜に破断が生じた際のろ過水の濁度を増加させることができる。したがって、処理水質計測手段3の濁度計測に基づいた膜破断検出感度が向上する。その結果、ろ過膜の破断を的確に検出できるため、膜破断に対する処置も的確に実施できるので、安心かつ安全な浄水の供給が容易になる。 As described above, according to the first embodiment and the reference example , the membrane filtration means 1 can be obtained by reducing the flow rate of the raw water passing through the filtration membrane or by adding a turbidity source to the raw water passing through the filtrate. It is possible to increase the turbidity of filtered water when the filter membrane breaks. Therefore, the membrane breakage detection sensitivity based on the turbidity measurement of the treated water quality measuring means 3 is improved. As a result, since the rupture of the filtration membrane can be accurately detected, the treatment for the rupture of the membrane can be accurately performed, so that safe and safe supply of purified water is facilitated.

本発明を適用した第一の実施形態の膜ろ過処理装置の第一の実施例を示す図である。It is a figure which shows the 1st Example of the membrane filtration processing apparatus of 1st embodiment to which this invention is applied. 図2は、図1の膜ろ過手段のろ過膜を通過する原水量に対するろ過水の濁度の変化を計測した一例である。FIG. 2 is an example in which the change in the turbidity of filtered water relative to the amount of raw water passing through the filtration membrane of the membrane filtration means in FIG. 1 is measured. 本発明を適用した第一の実施形態の膜ろ過処理装置の第二の実施例を示す図である。It is a figure which shows the 2nd Example of the membrane filtration processing apparatus of 1st embodiment to which this invention is applied. 本発明を適用した第一の実施形態の膜ろ過処理装置の第三の実施例を示す図である。It is a figure which shows the 3rd Example of the membrane filtration processing apparatus of 1st embodiment to which this invention is applied. 本発明を適用した第一の実施形態の膜ろ過処理装置の第四の実施例を示す図である。It is a figure which shows the 4th Example of the membrane filtration processing apparatus of 1st embodiment to which this invention is applied. 本発明を適用した参考例の膜ろ過処理装置の第一の実施例を示す図である。It is a figure which shows the 1st Example of the membrane filtration processing apparatus of the reference example to which this invention is applied. 本発明を適用した参考例の膜ろ過処理装置の第二の実施例を示す図である。It is a figure which shows the 2nd Example of the membrane filtration processing apparatus of the reference example to which this invention is applied. 本発明を適用した参考例の膜ろ過処理装置の第三の実施例を示す図である。It is a figure which shows the 3rd Example of the membrane filtration processing apparatus of the reference example to which this invention is applied. 本発明を適用した参考例の膜ろ過処理装置の第四の実施例を示す図である。It is a figure which shows the 4th Example of the membrane filtration processing apparatus of the reference example to which this invention is applied.

符号の説明Explanation of symbols

1 膜ろ過手段
2 ろ過流量変更手段
3 処理水質計測手段
4 制御手段
5 被処理水質計測手段
6 濁質源添加手段
1 membrane filtration means 2 filtration flow rate changing means 3 treated water quality measuring means 4 control means 5 treated water quality measuring means 6 turbidity source adding means

Claims (7)

原水に含まれる濁質を分離除去するろ過膜を有する膜ろ過手段と、該膜ろ過手段のろ過水の濁度を計測する水質計測手段と、該水質計測手段の計測値に基づき前記ろ過膜の破断を検出する膜破断検出手段と、該膜破断検出手段からの指令に基づいて前記ろ過膜を通過する原水の流量を調整するろ過流量変更手段とを備え、
前記膜破断検出手段は、前記ろ過流量変更手段に通過流量を減少させる指令を出力して前記ろ過膜を通過する原水の流量を減少させ、前記通過流量の減少後に前記水質計測手段から取り込んだ計測値に基づいて、前記ろ過膜の破断を検出することを特徴とする膜ろ過処理装置。
Membrane filtration means having a filtration membrane for separating and removing turbidity contained in raw water, water quality measurement means for measuring the turbidity of filtrate water of the membrane filtration means, and based on the measured value of the water quality measurement means, A membrane rupture detecting means for detecting a rupture, and a filtration flow rate changing means for adjusting the flow rate of the raw water passing through the filtration membrane based on a command from the membrane rupture detection means ,
The membrane breakage detecting means outputs a command to reduce the passage flow rate to the filtration flow rate changing means to reduce the flow rate of the raw water passing through the filtration membrane, and the measurement taken from the water quality measurement means after the reduction of the passage flow rate A membrane filtration apparatus for detecting breakage of the filtration membrane based on a value.
前記膜破断検出手段は、前記ろ過流量変更手段に通過流量を減少させる指令を出力して前記通過流量を減少させる前の前記水質計測手段の計測値を第一の計測値として取得し、前記通過流量を減少させた後の前記水質計測手段の計測値を第二の計測値として取得し、前記第二の計測値が前記第一の計測値よりも大きいときに前記ろ過膜に破断が生じたものと判定する請求項1に記載の膜ろ過処理装置。 The membrane breakage detection means outputs a command to reduce the passage flow rate to the filtration flow rate change means, obtains the measurement value of the water quality measurement means before reducing the passage flow rate as a first measurement value, and passes the passage The measurement value of the water quality measuring means after reducing the flow rate is acquired as a second measurement value, and the filter membrane breaks when the second measurement value is larger than the first measurement value. The membrane filtration processing apparatus of Claim 1 determined to be a thing. 前記膜破断検出手段は、前記ろ過流量変更手段に通過流量を減少させる指令を出力して前記通過流量を減少させた後の前記水質計測手段の計測値を取得し、取得した計測値が設定値よりも大きいときに前記ろ過膜に破断が生じたものと判定する請求項1に記載の膜ろ過処理装置。 The membrane breakage detecting means outputs a command to reduce the passage flow rate to the filtration flow rate changing means to obtain a measurement value of the water quality measurement means after reducing the passage flow rate, and the obtained measurement value is a set value. The membrane filtration processing apparatus according to claim 1, wherein it is determined that a breakage has occurred in the filtration membrane when larger than. 前記膜破断検出手段は、前記ろ過膜に破断がないものと判定したとき前記ろ過流量変更手段に前記通過流量を元の量に戻す指令を出力する請求項1乃至3のいずれか1項に記載の膜ろ過処理装置。 The film breaking detecting means, according to any one of claims 1 to 3 outputs a command to return the amount of based on the flow rate through the filtration flow changing means when it is determined that there is no break in the filtration membrane Membrane filtration equipment. 前記膜ろ過手段の上流側の原水の濁度を計測する被処理水質計測手段を設け、前記膜破断検出手段は、前記被処理水質計測手段の計測値が設定値以下の際、前記ろ過流量変更手段に通過流量を減少させる指令を出力して前記通過流量を減少させる請求項1乃至4のいずれか1項に記載の膜ろ過処理装置。 A treated water quality measuring means for measuring the turbidity of raw water upstream of the membrane filtration means is provided, and the membrane breakage detecting means is configured to change the filtration flow rate when the measured value of the treated water quality measuring means is equal to or less than a set value. The membrane filtration processing apparatus according to any one of claims 1 to 4 , wherein a command for decreasing the passage flow rate is output to the means to reduce the passage flow rate . 前記膜ろ過手段及び前記ろ過流量変更手段は、複数設けられるものとし、前記水質計測手段は、前記各膜ろ過手段から流出する処理水の合流後の濁度を計測し、
前記膜破断検出手段は、前記複数のろ過流量変更手段のうち、一の前記ろ過流量変更手段に通過流量を減少させる指令を出力して一の前記膜ろ過手段の通過流量を減少させる請求項1乃至5のいずれか1項に記載の膜ろ過処理装置。
A plurality of the membrane filtration means and the filtration flow rate changing means are provided, and the water quality measurement means measures the turbidity after merging of treated water flowing out from each of the membrane filtration means,
The membrane breakage detecting means outputs a command to reduce the passage flow rate to one of the filtration flow rate changing means among the plurality of filtration flow rate changing means to reduce the passage flow rate of the one membrane filtration means. The membrane filtration processing apparatus of any one of thru | or 5.
前記膜破断検出手段は、前記一の膜ろ過手段の通過流量を減少させつつ、他の前記ろ過流量変更手段に通過流量を増加させる指令を出力して他の前記膜ろ過手段の前記通過流量を増加させる請求項6に記載の膜ろ過処理装置。 The membrane breakage detection means outputs a command to increase the passage flow rate to the other filtration flow rate change means while reducing the passage flow rate of the one membrane filtration means, and determines the passage flow rate of the other membrane filtration means. The membrane filtration processing apparatus according to claim 6 to be increased.
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