JP3132044B2 - Liquid supply device for membrane separation device - Google Patents
Liquid supply device for membrane separation deviceInfo
- Publication number
- JP3132044B2 JP3132044B2 JP03147332A JP14733291A JP3132044B2 JP 3132044 B2 JP3132044 B2 JP 3132044B2 JP 03147332 A JP03147332 A JP 03147332A JP 14733291 A JP14733291 A JP 14733291A JP 3132044 B2 JP3132044 B2 JP 3132044B2
- Authority
- JP
- Japan
- Prior art keywords
- membrane separation
- separation device
- torque meter
- liquid supply
- membrane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Sludge (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は膜分離装置の給液装置に
係り、特に生物処理の二次処理系あるいは高度処理系に
膜分離装置を用いる場合に好適な膜分離装置の給液装置
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid supply device for a membrane separation device, and more particularly to a liquid supply device for a membrane separation device suitable for use in a secondary or advanced treatment system for biological treatment. .
【0002】[0002]
【従来の技術】膜分離装置は、周知の通り、分離膜の一
方の側に液を加圧供給し、他方の側から透過水を取り出
すものであるが、生物処理のように活性汚泥あるいは凝
集汚泥等、液(原水)中にSS成分が多いと分離膜及び
その原水流路の閉塞(以下、分離膜の閉塞という。)が
起こり易い。2. Description of the Related Art As is well known, a membrane separation apparatus pressurizes and supplies a liquid to one side of a separation membrane and takes out permeated water from the other side. If the SS component in the liquid (raw water) such as sludge is large, blockage of the separation membrane and its raw water flow path (hereinafter, blockage of the separation membrane) is likely to occur.
【0003】[0003]
【発明が解決しようとする課題】特に、チューブラ型膜
分離装置は、分離膜が閉塞した場合に開枠洗浄等の対処
をとることができず、分離膜を全て交換せざるをえな
い。また、チューブラ型以外の平板型、中空糸型などの
膜分離装置においても、分離膜の閉塞を未然に防止でき
ることが期待される。In particular, in the case of the tubular type membrane separation apparatus, when the separation membrane is clogged, it is not possible to take measures such as frame cleaning, and the replacement of the entire separation membrane is inevitable. Further, it is expected that blockage of the separation membrane can be prevented even in a membrane separation device such as a flat plate type and a hollow fiber type other than the tubular type.
【0004】[0004]
【課題を解決するための手段】本発明の膜分離装置の給
液装置は、膜分離装置に生物処理水を供給するポンプ
と、該膜分離装置に供給される生物処理水の粘度を測定
するトルク計と、該トルク計の検出値が所定値以上とな
った場合に前記ポンプを停止させる制御装置とを備えて
なるものである。According to the present invention, there is provided a liquid supply device for a membrane separation device, which comprises a pump for supplying biological treatment water to the membrane separation device and a viscosity of the biological treatment water supplied to the membrane separation device. A torque meter; and a control device for stopping the pump when a detected value of the torque meter becomes equal to or more than a predetermined value.
【0005】[0005]
【作用】本発明者らが種々研究を重ねたところ、生物処
理水中のSS濃度が高くなると粘度(トルク計の検出
値)が次第に高くなること、そして、特に2〜4%程度
にこのトルク計検出値の臨界値があり、この2〜4%程
度のSS濃度を超えるとトルク計検出値が急速に増大す
ることを見出した。この2〜4%程度のSS濃度は、そ
れを超えると膜分離装置に閉塞をもたらし易いSS濃度
でもあり、運転を継続すると分離膜の閉塞を生じる。[Action] The inventors of the present invention we have conducted various research, biological treatment
When the SS concentration in Risui increases viscosity (the detected value of the torque meter) it gradually increases, and, in particular to 2 to 4%, the critical value of the torque meter detection value of the order of 2-4% It was found that when the SS concentration was exceeded, the torque meter detected value rapidly increased. The SS concentration of about 2 to 4% is also an SS concentration that tends to cause blockage in the membrane separation device if it exceeds that, and if the operation is continued, the separation membrane will be blocked.
【0006】そこで、本発明は、トルク計で検出される
粘度値が所定値以上になった場合に、膜分離装置への給
液を停止し、膜分離装置の分離膜の閉塞を未然に防ぐよ
うにしたものである。Therefore, the present invention stops the supply of the liquid to the membrane separation device when the viscosity value detected by the torque meter becomes a predetermined value or more, thereby preventing the separation membrane of the membrane separation device from being blocked. It is like that.
【0007】本発明は、廃水の生物処理に膜分離装置を
使用する際の分離膜の閉塞を防止する。The present invention prevents clogging of a separation membrane when using a membrane separation device for biological treatment of wastewater.
【0008】特に、膜分離装置に供給する生物処理水の
粘度を測定し、測定値が設定値を超えた場合に、ポンプ
を止めて膜の運転を停止して、洗浄に移行する。In particular, the viscosity of the biologically treated water to be supplied to the membrane separation device is measured, and when the measured value exceeds a set value, the pump is stopped to stop the operation of the membrane, and the cleaning is started.
【0009】生物処理では、膜分離装置は活性汚泥を多
く含む二次処理系及び凝集汚泥からなる高度処理系のS
S分を多く含む系に使用されており、両方の系にトルク
計を設け測定しても良く、特に高度処理系において閉塞
が激しいので、この系に好適に使用される。[0009] In biological treatment, the membrane separation device is a secondary treatment system containing a large amount of activated sludge and an advanced treatment system comprising coagulated sludge.
It is used in a system containing a large amount of S, and may be measured by providing a torque meter in both systems. Particularly, the system is preferably used in this system because the clogging is severe in an advanced treatment system.
【0010】膜分離装置を運転すると、原水量及び水質
の変動、FLUXの変動等により、高濃縮されSS濃度
が上昇する。本発明では、原水槽の生物処理水の一部を
抜き出し、トルク値を間欠的に測定し、3%以上を計測
すると(3%以上を一定回数計測した場合でも良い。)
循環ポンプを停止し、洗浄に移行する。洗浄の間に原水
槽内の液量が増加すること、膜濃縮液が返送されないこ
とから、原水槽内は所定値の濃度となる。[0010] When the membrane separation device is operated, the concentration of SS is increased due to high concentration due to fluctuations in the amount of raw water and water quality, fluctuations in FLUX, and the like. In the present invention, a part of the biologically treated water in the raw water tank is extracted, the torque value is intermittently measured, and 3% or more is measured.
Stop the circulating pump and move to washing. Since the amount of liquid in the raw water tank increases during washing and the membrane concentrated liquid is not returned, the concentration in the raw water tank becomes a predetermined value.
【0011】[0011]
【実施例】第1図は実施例に係る膜分離装置の給液装置
を組み込んだ水処理装置の系統図である。FIG. 1 is a system diagram of a water treatment apparatus incorporating a liquid supply device of a membrane separation apparatus according to an embodiment.
【0012】生物処理の二次処理水に適宜の凝集剤が添
加された原水は、原水槽内に貯留される。[0012] Biological treatment of the secondary processing the raw water suitable aggregating agent is added to the water is stored in the raw water tank.
【0013】原水槽1内の原水は、給液ポンプ2及び配
管3を経てチューブラ型膜分離装置4に供給される。透
過水は配管11で系外に取り出され、濃縮水は配管5で
原水槽1に戻される。配管2からは給液の一部をトルク
計7に導入するための配管6が分岐されている。The raw water in the raw water tank 1 is supplied to a tubular type membrane separation device 4 via a liquid supply pump 2 and a pipe 3. The permeated water is taken out of the system by a pipe 11, and the concentrated water is returned to the raw water tank 1 by a pipe 5. From the pipe 2, a pipe 6 for introducing a part of the liquid supply to the torque meter 7 is branched.
【0014】トルク計7で粘度が測定された液は配管8
で原水槽1に戻される。トルク計7の検出値は変換器9
を経て制御装置10に入力される。制御装置10は前記
給液ポンプ2に制御信号を出力している。The liquid whose viscosity is measured by the torque meter 7 is supplied to a pipe 8
Is returned to the raw water tank 1. The detected value of the torque meter 7 is converted by the converter 9
Is input to the control device 10 through The control device 10 outputs a control signal to the liquid supply pump 2.
【0015】第2図はこの原水中のSS濃度とトルク計
検出値との相関図であり、図示の如くSS濃度が3%を
超えるとトルク計検出値が急激に増大している。本実施
例では、トルク計検出値のこの急激な立上り部に相当す
る値(−4V)を閾値として設定し、トルク計検出値が
この閾値を超えると給液ポンプ2を停止し、洗浄に移行
する。FIG. 2 is a correlation diagram between the SS concentration in the raw water and the torque meter detected value. As shown, when the SS concentration exceeds 3%, the torque meter detected value sharply increases. In the present embodiment, a value (-4 V) corresponding to this sharp rising portion of the torque meter detection value is set as a threshold, and when the torque meter detection value exceeds this threshold, the liquid supply pump 2 is stopped, and the operation shifts to cleaning. I do.
【0016】なお、液をトルク計7に導入して計測を開
始すると、トルク計検出値はトルク計の回転開始直後に
ピーク値に到達し、その後はやや低下した一定値になる
という特性がある。従って、トルク計は一定時間毎に間
欠的に運転する。第2図では、この測定開始直後のピー
ク値をトルク計検出値として採用している。When the liquid is introduced into the torque meter 7 and the measurement is started, the detected value of the torque meter reaches a peak value immediately after the start of the rotation of the torque meter, and thereafter becomes a slightly reduced constant value. . Therefore, the torque meter operates intermittently at regular intervals. In FIG. 2, the peak value immediately after the start of the measurement is adopted as the torque meter detected value.
【0017】かかる本実施例装置によると、SS濃度が
膜分離装置に閉塞をもたらしそうな高い値になると、自
動的に給液ポンプ2が停止されるため、膜分離装置4の
閉塞が未然に防止される。According to the apparatus of this embodiment, when the SS concentration becomes high enough to cause blockage in the membrane separation device, the liquid supply pump 2 is automatically stopped. Is prevented.
【0018】なお、上記実施例で採用した閾値は一例に
過ぎず、原水の性状等に応じ適宜選定するのはもちろん
である。It should be noted that the threshold value employed in the above embodiment is merely an example, and it is needless to say that the threshold value is appropriately selected according to the properties of the raw water.
【0019】[0019]
【発明の効果】以上の通り、本発明の膜分離装置の給液
装置によると、膜分離装置の分離膜の閉塞を未然に防止
できる。従って、長期間にわたって安定して膜分離装置
を稼動させることが可能となる。As described above, according to the liquid supply device of the membrane separation device of the present invention, it is possible to prevent the separation membrane of the membrane separation device from being blocked. Therefore, it is possible to operate the membrane separation device stably for a long period of time.
【図1】実施例に係る膜分離装置の給液装置を備えた水
処理装置の系統図である。FIG. 1 is a system diagram of a water treatment device provided with a liquid supply device of a membrane separation device according to an embodiment.
【図2】トルク計検出値の一例を示すグラフである。FIG. 2 is a graph showing an example of a torque meter detection value.
1 原水槽 2 給液ポンプ 4 膜分離装置 7 トルク計 10 制御装置 DESCRIPTION OF SYMBOLS 1 Raw water tank 2 Feed pump 4 Membrane separation device 7 Torque meter 10 Control device
───────────────────────────────────────────────────── フロントページの続き (72)発明者 椎橋 利雄 東京都新宿区西新宿3丁目4番7号 栗 田工業株式会社内 (56)参考文献 特開 昭57−84712(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 61/00 - 65/10 C02F 1/44 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Toshio Shiibashi 3-4-7 Nishi-Shinjuku, Shinjuku-ku, Tokyo Inside Kurita Kogyo Co., Ltd. (56) References JP-A-57-84712 (JP, A) (58) ) Surveyed field (Int.Cl. 7 , DB name) B01D 61/00-65/10 C02F 1/44
Claims (1)
プと、該膜分離装置に供給される生物処理水の粘度を測
定するトルク計と、該トルク計の検出値が所定値以上と
なった場合に前記ポンプを停止させる制御装置とを備え
てなる膜分離装置の給液装置。1. A pump for supplying biological treatment water to a membrane separation device, a torque meter for measuring the viscosity of biological treatment water supplied to the membrane separation device, and a detection value of the torque meter being equal to or more than a predetermined value. And a control device for stopping the pump in the event of a failure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03147332A JP3132044B2 (en) | 1991-06-19 | 1991-06-19 | Liquid supply device for membrane separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03147332A JP3132044B2 (en) | 1991-06-19 | 1991-06-19 | Liquid supply device for membrane separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04371218A JPH04371218A (en) | 1992-12-24 |
| JP3132044B2 true JP3132044B2 (en) | 2001-02-05 |
Family
ID=15427792
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP03147332A Expired - Fee Related JP3132044B2 (en) | 1991-06-19 | 1991-06-19 | Liquid supply device for membrane separation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3132044B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10286563A (en) * | 1997-04-16 | 1998-10-27 | Nkk Corp | Membrane separation method |
| WO2004067146A1 (en) * | 2003-01-27 | 2004-08-12 | Bucher-Guyer Ag | Method and device for cross-flow filtration |
| WO2004069377A1 (en) * | 2003-01-29 | 2004-08-19 | Bucher-Guyer Ag | System for cross-flow filtration and method for the operation thereof |
| FR2903617B1 (en) | 2006-07-17 | 2009-03-20 | Vallee De L Aigues Sarl Soc In | METHOD FOR CONTROLLING A TANGENTIAL FILTRATION DEVICE AND CORRESPONDING DEVICE |
| EP3354329A1 (en) * | 2017-01-25 | 2018-08-01 | Sartorius Stedim Biotech GmbH | Filtration system incorporating viscometer |
-
1991
- 1991-06-19 JP JP03147332A patent/JP3132044B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04371218A (en) | 1992-12-24 |
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