JPH04371218A - Liquid supply system for membrane separation equipment - Google Patents

Liquid supply system for membrane separation equipment

Info

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
Application number
JP3147332A
Other languages
Japanese (ja)
Other versions
JP3132044B2 (en
Inventor
Sachio Toyoshima
豊島 佐知夫
Takeshi Sato
武 佐藤
Ryoji Oyama
大山 良二
Toshio Shiibashi
椎橋 利雄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP03147332A priority Critical patent/JP3132044B2/en
Publication of JPH04371218A publication Critical patent/JPH04371218A/en
Application granted granted Critical
Publication of JP3132044B2 publication Critical patent/JP3132044B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To prevent clogging of a separation membrane and a raw water passage of membrane separation equipment. CONSTITUTION:Part of raw water introduced to membrane separation equipment 4 is led to a torque meter 7 which detects viscosity. This detected value is input to a controller 10 through a converter 9. When the detected value of the torque meter becomes a prescribed one or more, the controller 10 stops a liquid supply pump 2. Thereby there is a correlation between the detected value of the torque meter and SS concentration in the raw water: when the SS concentration in the raw water exceeds a certain value, the detected value of the torque meter is increased suddenly. Therefore, the raw water of high SS concentration that may cause clogging of the separation membrane of the membrane separation equipment is prevented from flowing into the membrane separation equipment, so that clogging of the separation membrane and the raw water passage is prevented.

Description

【発明の詳細な説明】[Detailed description of the invention]

【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.

【図面の簡単な説明】[Brief explanation of the drawing]

【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.

【符号の説明】[Explanation of symbols]

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)

【特許請求の範囲】[Claims] 【請求項1】  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.
JP03147332A 1991-06-19 1991-06-19 Liquid supply device for membrane separation device Expired - Fee Related JP3132044B2 (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (9)

* Cited by examiner, † Cited by third party
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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