JPH04371218A - Liquid supply system for membrane separation equipment - Google Patents
Liquid supply system for membrane separation equipmentInfo
- Publication number
- JPH04371218A JPH04371218A JP3147332A JP14733291A JPH04371218A JP H04371218 A JPH04371218 A JP H04371218A JP 3147332 A JP3147332 A JP 3147332A JP 14733291 A JP14733291 A JP 14733291A JP H04371218 A JPH04371218 A JP H04371218A
- Authority
- JP
- Japan
- Prior art keywords
- raw water
- membrane
- torque meter
- membrane separation
- separation equipment
- 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.)
- Granted
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 47
- 238000000926 separation method Methods 0.000 title claims abstract description 37
- 239000007788 liquid Substances 0.000 title claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 31
- 238000001514 detection method Methods 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Sludge (AREA)
Abstract
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 fluid supply device for a membrane separation device, and more particularly to a fluid supply device for a membrane separation device suitable for use in a secondary treatment system or advanced treatment system of 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。[Prior Art] As is well known, membrane separation equipment supplies liquid under pressure to one side of a separation membrane and extracts permeated water from the other side. When there are many SS components in liquid (raw water) such as sludge, clogging of the separation membrane and its raw water flow path (hereinafter referred to as separation membrane clogging) 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。[Problems to be Solved by the Invention] Particularly, in the tubular type membrane separation apparatus, when the separation membrane becomes clogged, it is not possible to take measures such as opening the frame and cleaning it, and the separation membrane must be completely replaced. It is also expected that clogging of separation membranes can be prevented in membrane separation devices other than tubular types, such as flat plate types and hollow fiber types.
【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、膜分離装置に液を供給するポンプと、該膜分
離装置に供給される液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。[Means for Solving the Problems] A liquid supply device for a membrane separator according to the present invention includes: a pump that supplies liquid to the membrane separator; a torque meter that measures the viscosity of the liquid supplied to the membrane separator; The pump includes a control device that stops the pump when the detected value of the torque meter exceeds a predetermined value.
【0005】[0005]
【作用】本発明者らが種々研究を重ねたところ、原水中
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。[Function] The present inventors have conducted various studies and found that as the SS concentration in raw water increases, the viscosity (detected by a torque meter) gradually increases, and in particular, when the SS concentration in raw water increases, the viscosity (value detected by a torque meter) increases. There is a critical value of SS of about 2 to 4%.
It was found that the torque meter detection value increases rapidly when the concentration is exceeded. This SS concentration of approximately 2 to 4% is also the SS concentration that, if exceeded, tends to cause clogging of the membrane separation device, and if the operation is continued, clogging of the separation membrane will occur.
【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。[0006] Therefore, the present invention prevents the separation membrane of the membrane separator from clogging by stopping the liquid supply to the membrane separator when the viscosity value detected by the torque meter exceeds a predetermined value. This is how it was done.
【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 the membrane separation device is used for biological treatment of wastewater.
【0008】特に、膜分離装置に供給する原水の粘度を
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 raw water supplied to the membrane separation device is measured, and if the measured value exceeds a set value, the pump is stopped, the membrane operation is stopped, and 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。In biological treatment, membrane separation equipment is used for secondary treatment systems containing a large amount of activated sludge and for advanced treatment systems consisting of flocculated sludge.
It is used in systems containing a large amount of S, and torque meters may be installed in both systems to measure it.Since clogging is particularly severe in advanced processing systems, it is preferably used in this 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、原水槽の液の一部を抜き出し
、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 separator is operated, the raw water becomes highly concentrated and the SS concentration increases due to fluctuations in the amount and quality of raw water, fluctuations in FLUX, etc. In the present invention, a part of the liquid in the raw water tank is extracted, the torque value is intermittently measured, and when the torque value is measured at 3% or more (
It is also possible to measure 3% or more a certain number of times. ) Stop the circulation pump and move on to cleaning. Because the amount of liquid in the raw water tank increases during cleaning and the membrane concentrate is not returned,
The concentration in the raw water tank is 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。Embodiment FIG. 1 is a system diagram of a water treatment apparatus incorporating a liquid supply device for 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(図示せず)は、原水槽内に貯留される。[0012] Raw water (not shown) obtained by adding an appropriate flocculant to the secondary treated water of biological treatment is stored in a 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。Raw water in the raw water tank 1 is supplied to a tubular membrane separation device 4 via a liquid supply pump 2 and piping 3. Permeated water is taken out of the system through piping 11, and concentrated water is returned to raw water tank 1 through piping 5. A pipe 6 is branched from the pipe 2 to introduce a portion of the supplied liquid to a torque meter 7.
【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 was measured by the torque meter 7 is transferred to the pipe 8
It is returned to raw water tank 1. The detected value of the torque meter 7 is the converter 9
The signal is input to the control device 10 via the . 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 detection value, and as shown in the figure, when the SS concentration exceeds 3%, the torque meter detection value increases rapidly. In this embodiment, a value (-4V) corresponding to this sudden rise of the torque meter detection value is set as a threshold value, and when the torque meter detection value exceeds this threshold value, the liquid supply pump 2 is stopped and cleaning is started. 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。[0016] When the liquid is introduced into the torque meter 7 and measurement is started, the torque meter detection value has a characteristic that it reaches a peak value immediately after the rotation of the torque meter starts, and thereafter becomes a constant value that slightly decreases. . Therefore, the torque meter operates intermittently at regular intervals. In FIG. 2, the peak value immediately after the start of this measurement is employed as the torque meter detection 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 device of this embodiment, when the SS concentration reaches a high value that is likely to cause blockage in the membrane separation device, the liquid supply pump 2 is automatically stopped, so that blockage of the membrane separation device 4 can be prevented. 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。[0018] The threshold value adopted in the above embodiment is merely an example, and it goes without saying that it may be appropriately selected depending on 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 for a membrane separator of the present invention, clogging of the separation membrane of the membrane separator can be prevented. Therefore, it becomes 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 equipped with a liquid supply device for 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 torque meter detection values.
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 1 Raw water tank 2 Liquid supply pump 4 Membrane separation device 7 Torque meter 10 Control device
Claims (1)
該膜分離装置に供給される液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。[Claim 1] A pump that supplies a liquid to a membrane separation device;
A supply of a membrane separation device comprising a torque meter that measures the viscosity of a liquid supplied to the membrane separation device, and a control device that stops the pump when the detected value of the torque meter exceeds a predetermined value. liquid equipment.
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 true JPH04371218A (en) | 1992-12-24 |
JP3132044B2 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) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10286563A (en) * | 1997-04-16 | 1998-10-27 | Nkk Corp | Membrane separating process |
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 |
FR2903617A1 (en) * | 2006-07-17 | 2008-01-18 | 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
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH10286563A (en) * | 1997-04-16 | 1998-10-27 | Nkk Corp | Membrane separating process |
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 |
FR2903617A1 (en) * | 2006-07-17 | 2008-01-18 | Vallee De L Aigues Sarl Soc In | METHOD FOR CONTROLLING A TANGENTIAL FILTRATION DEVICE AND CORRESPONDING DEVICE |
WO2008009848A2 (en) | 2006-07-17 | 2008-01-24 | Societe Industrielle De La Vallee De L'aigues S.I.V.A. | Tangential filtration device |
WO2008009848A3 (en) * | 2006-07-17 | 2008-04-17 | Vallee De L Aigues S I V A Soc | Tangential filtration device |
US8240482B2 (en) | 2006-07-17 | 2012-08-14 | Societe Industrielle De La Vallee De L'aigues S.I.V.A. | Tangential filtration device |
EP3354329A1 (en) * | 2017-01-25 | 2018-08-01 | Sartorius Stedim Biotech GmbH | Filtration system incorporating viscometer |
WO2018138159A1 (en) * | 2017-01-25 | 2018-08-02 | Sartorius Stedim Biotech Gmbh | Filtration system incorporating viscometer |
Also Published As
Publication number | Publication date |
---|---|
JP3132044B2 (en) | 2001-02-05 |
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