JP2002162338A - Measuring device for suspension water quality - Google Patents

Measuring device for suspension water quality

Info

Publication number
JP2002162338A
JP2002162338A JP2000359705A JP2000359705A JP2002162338A JP 2002162338 A JP2002162338 A JP 2002162338A JP 2000359705 A JP2000359705 A JP 2000359705A JP 2000359705 A JP2000359705 A JP 2000359705A JP 2002162338 A JP2002162338 A JP 2002162338A
Authority
JP
Japan
Prior art keywords
water
suspension
measuring device
activated sludge
water quality
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.)
Pending
Application number
JP2000359705A
Other languages
Japanese (ja)
Inventor
Shigeki Sawada
繁樹 澤田
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 JP2000359705A priority Critical patent/JP2002162338A/en
Publication of JP2002162338A publication Critical patent/JP2002162338A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Investigating Or Analysing Materials By Optical Means (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Activated Sludge Processes (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a measuring device for water quality which can monitor microscopic particle in a suspension by separating. Especially it is useful for operation control of activated sludge process device which carries out solid-liquid separation by filter. SOLUTION: This invention is related to a measuring device for water quality of suspension which features to have the way of water intake to pull out a part of suspension, the way of solid-liquid separation which separates water and concentrated water containing high concentration suspension matter from suspension pulled out by said way of water intake, and the way of muddy ingredient detection which measures the concentration of muddy ingredient in said supernatant water.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、懸濁水の水質測定
装置に関する。さらに詳しくは、本発明は、懸濁水中に
含まれる微細粒子のみを分離してモニターすることがで
き、特にろ過により固液分離を行う活性汚泥処理装置の
運転管理に有用な懸濁水の水質測定装置に関する。
The present invention relates to an apparatus for measuring the quality of suspended water. More specifically, the present invention is capable of separating and monitoring only fine particles contained in suspension water, and in particular, water quality measurement of suspension water useful for operation control of an activated sludge treatment apparatus that performs solid-liquid separation by filtration. Related to the device.

【0002】[0002]

【従来の技術】下水や有機廃水を処理する活性汚泥装置
において、沈澱槽に代わって膜やろ布、不織布を用いて
固液分離する方法は、重力沈降によらないので、汚泥の
沈降性にかかわらず固液分離することができるという利
点を有している。従って、バルキングなどにより沈降性
が悪化した活性汚泥も固液分離し、高濃度に濃縮するこ
とができる。しかし、これらのろ過による固液分離に
は、未分解有機物や微生物の代謝生産物がろ過面を汚染
させ、固液分離速度を低下させるという問題がある。こ
のために、これらの有機成分の濃度を低く維持するよう
に運転管理する必要がある。これらの管理指針として
は、直接的にはろ液の有機成分濃度として、TOC計、
COD計、紫外部吸光度計などを用いることによりモニ
ターし、管理されている。また、活性汚泥混合液の粘度
を計測することにより、活性汚泥混合液中の有機成分濃
度を間接的に推定することができる。一方、これらのろ
過による固液分離においては、微生物の代謝生産物だけ
でなく、微細な活性汚泥成分によっても、ろ過面が汚染
されることが、本発明者らの研究により明らかとなっ
た。微細な活性汚泥粒子は、ろ過面において微生物代謝
生産物とゲル状の強固な層を形成し、ろ過抵抗を増大さ
せるものと想定される。しかしながら、沈澱槽を有しな
い固液分離装置においては、活性汚泥中の微細汚泥粒子
だけを分離してモニターする手段がなかった。本発明者
は、ろ過抵抗を増大させる微細汚泥粒子について、活性
汚泥を沈降分離させて生じる上澄み層の濁度と相関の強
いことを明らかにし、本発明に至った。
2. Description of the Related Art In an activated sludge apparatus for treating sewage and organic wastewater, the method of solid-liquid separation using a membrane, a filter cloth, or a nonwoven fabric instead of a settling tank is not based on gravity sedimentation. And has the advantage that solid-liquid separation can be performed. Therefore, activated sludge whose sedimentation property has deteriorated due to bulking or the like can be separated into solid and liquid and concentrated to a high concentration. However, the solid-liquid separation by these filtrations has a problem that undecomposed organic substances and metabolites of microorganisms contaminate the filtration surface and reduce the solid-liquid separation speed. For this reason, it is necessary to control the operation so as to keep the concentration of these organic components low. As these management guidelines, TOC meter,
It is monitored and managed by using a COD meter, an ultraviolet absorbance meter, or the like. In addition, by measuring the viscosity of the activated sludge mixture, the concentration of the organic component in the activated sludge mixture can be indirectly estimated. On the other hand, in the solid-liquid separation by filtration, the present inventors have found that the filtration surface is contaminated by not only metabolites of microorganisms but also fine activated sludge components. It is assumed that the fine activated sludge particles form a strong gel-like layer with the microbial metabolite on the filtration surface, and increase the filtration resistance. However, in the solid-liquid separation device having no settling tank, there is no means for separating and monitoring only the fine sludge particles in the activated sludge. The present inventors have clarified that fine sludge particles that increase filtration resistance have a strong correlation with the turbidity of a supernatant layer generated by settling and separating activated sludge, and have reached the present invention.

【0003】[0003]

【発明が解決しようとする課題】本発明は、懸濁水中に
含まれる微細粒子のみを分離してモニターすることがで
き、特にろ過により固液分離を行う活性汚泥処理装置の
運転管理に有用な懸濁水の水質測定装置を提供すること
を目的としてなされたものである。
SUMMARY OF THE INVENTION The present invention can separate and monitor only fine particles contained in suspension water, and is particularly useful for operation control of an activated sludge treatment apparatus for performing solid-liquid separation by filtration. The purpose of the present invention is to provide an apparatus for measuring the quality of suspended water.

【0004】[0004]

【課題を解決するための手段】本発明者は、上記の課題
を解決すべく鋭意研究を重ねた結果、懸濁水の一部を抜
き取る取水手段と、抜き取られた懸濁水の上澄みを分離
する固液分離手段と、上澄み中に含まれる濁質成分濃度
を測定する手段を備えた装置により、懸濁水中に含まれ
る微細粒子のみを分離して濁質成分濃度を容易かつ正確
に測定し得ることを見いだし、この知見に基づいて本発
明を完成するに至った。すなわち、本発明は、(1)懸
濁水の水質測定装置であって、懸濁水の一部を抜き取る
取水手段と、該取水手段によって抜き取られた懸濁水を
上澄みと懸濁物質を高濃度に含有する濃縮水とに分離す
る固液分離手段と、該上澄み中に含まれる濁質成分濃度
を測定する濁質成分検知手段とを備えてなることを特徴
とする懸濁水の水質測定装置、(2)懸濁水が、精密ろ
過膜、限外ろ過膜、又は、目開きの粗いろ布、若しく
は、不織布からなるろ過体の表層にダイナミックろ過層
を形成して汚水中の懸濁粒子を捕捉し、ろ過水を取り出
すダイナミックろ過体の少なくとも一つからなるろ過手
段の被処理水である第1項記載の懸濁水の水質測定装
置、(3)懸濁水が、活性汚泥混合液である第1項又は
第2項記載の懸濁水の水質測定装置、及び、(4)濁質
成分検知手段が、表面散乱光式濁度検出器である第1項
〜第3項のいずれかに記載の懸濁水の水質測定装置、を
提供するものである。さらに、本発明の好ましい態様と
して、(5)取水手段が、懸濁水中に取水口が設置され
た取水管及び移送ポンプである第1項記載の懸濁水の水
質測定装置、及び、(6)固液分離手段が、沈降分離カ
ラムである第1項記載の懸濁水の水質測定装置、を挙げ
ることができる。
The inventor of the present invention has conducted intensive studies to solve the above-mentioned problems. As a result, the present inventor has found that a water intake means for extracting a part of the suspension water and a solid solution for separating the supernatant of the extracted suspension water. By means of a device provided with a liquid separating means and a means for measuring the concentration of a turbid component contained in the supernatant, it is possible to easily and accurately measure the turbid component concentration by separating only fine particles contained in the suspension water. And completed the present invention on the basis of this finding. That is, the present invention relates to (1) a water quality measuring device for a suspension water, wherein a water intake means for extracting a part of the suspension water, and the suspension water extracted by the water intake means containing a supernatant and a high concentration of suspended substances. (2) a water quality measuring device for a suspended water, comprising: a solid-liquid separating means for separating into a concentrated water to be separated; and a turbid component detecting means for measuring a turbid component concentration contained in the supernatant. ) Suspended water forms a microfiltration membrane, an ultrafiltration membrane, or a coarse filter cloth, or a dynamic filtration layer on the surface of a filter made of non-woven fabric to capture suspended particles in sewage, 3. The water quality measuring device for suspended water according to claim 1, which is the water to be treated by a filtration means comprising at least one of a dynamic filtration body for extracting filtered water, (3) the suspended liquid, wherein the suspended water is an activated sludge mixed solution or The water quality measuring device for suspended water according to Item 2, and ( ) Turbid component detecting means, there is provided a water quality measuring device, aqueous suspension as claimed in any one of items 1 to 3, wherein the surface light scattering type turbidity detector. Further, as a preferred embodiment of the present invention, (5) the water quality measuring device for suspended water according to item 1, wherein the water intake means is an intake pipe and a transfer pump provided with an intake port in the suspension water, and (6). Item 2. The apparatus for measuring water quality of suspended water according to item 1, wherein the solid-liquid separation means is a sedimentation separation column.

【0005】[0005]

【発明の実施の形態】本発明の懸濁水の水質測定装置
は、懸濁水の一部を抜き取る取水手段と、該取水手段に
よって抜き取られた懸濁水を上澄みと懸濁物質を高濃度
に含有する濃縮水とに分離する固液分離手段と、該上澄
み中に含まれる濁質成分濃度を測定する濁質成分検知手
段とを備えてなる装置である。本発明装置により、懸濁
水中に含まれる微細粒子のみを分離してモニターするこ
とができる。本発明装置は、精密ろ過膜、限外ろ過膜、
又は、目開きの粗いろ布、若しくは、不織布からなるろ
過体の表層にダイナミックろ過層を形成して汚水中の懸
濁粒子を捕捉し、ろ過水を取り出すダイナミックろ過体
の少なくとも一つからなるろ過手段の被処理水に適用す
ることができる。本発明装置を用いることにより、活性
汚泥混合液中に含まれ、ろ過面において微生物代謝生産
物とゲル状の強固な層を形成し、ろ過抵抗を増大させる
と想定される微細な活性汚泥粒子の濃度を測定し、活性
汚泥処理装置の運転管理に有効に活用することができ
る。本発明装置において、懸濁水の一部を抜き取る取水
手段に特に制限はなく、例えば、懸濁水中に取水口が設
置された取水管と移送ポンプの組み合わせ、懸濁水槽か
ら溢流する懸濁水を導く導水管、懸濁水槽の壁面又は底
面に取水口が設けられた水頭により懸濁水を取水する取
水管などを挙げることができる。これらの中で、懸濁水
中に取水口が設置された取水管と移送ポンプの組み合わ
せは、取水の開始と停止をポンプの運転と停止により容
易に制御することができ、常に一定の条件で取水するこ
とができるので、特に好適に用いることができる。
BEST MODE FOR CARRYING OUT THE INVENTION The water quality measuring apparatus of the present invention comprises a water intake means for extracting a part of the suspension water, and the suspension water extracted by the water intake means containing a supernatant and a high concentration of suspended substances. The apparatus comprises a solid-liquid separation means for separating into a concentrated water and a turbid component detecting means for measuring the concentration of a turbid component contained in the supernatant. According to the apparatus of the present invention, only fine particles contained in the suspension water can be separated and monitored. The device of the present invention is a microfiltration membrane, an ultrafiltration membrane,
Or, a filtration cloth comprising coarse filtration cloth, or a dynamic filtration layer that forms a dynamic filtration layer on the surface layer of a filtration body made of a non-woven fabric to capture suspended particles in sewage, and removes filtration water. It can be applied to the treated water of the means. By using the apparatus of the present invention, the microbial metabolites contained in the activated sludge mixed solution, form a strong gel-like layer with the microbial metabolites on the filtration surface, it is assumed that the fine activated sludge particles are assumed to increase filtration resistance The concentration can be measured and used effectively for operation management of the activated sludge treatment device. In the apparatus of the present invention, there is no particular limitation on a water intake means for extracting a part of the suspension water, for example, a combination of an intake pipe and a transfer pump provided with an intake port in the suspension water, and the suspension water overflowing from the suspension water tank. Examples include a water guide pipe that guides the water, a water intake pipe that takes in the suspension water through a water head provided with a water intake port on the wall or bottom surface of the suspension water tank, and the like. Among these, the combination of an intake pipe with an intake port in the suspension water and a transfer pump allows the start and stop of intake to be easily controlled by operating and stopping the pump, and always allows intake under constant conditions. Therefore, it can be particularly preferably used.

【0006】本発明装置において、取水手段によって抜
き取られた懸濁水を上澄みと懸濁物質を高濃度に含有す
る濃縮水とに分離する固液分離手段に特に制限はなく、
例えば、沈降分離カラム、遠心分離機、膜分離装置など
を挙げることができる。これらの中で、沈降分離カラム
は、構造が簡単で維持管理が容易であり、懸濁水槽に直
結して用いることができ、常に一定の条件で固液分離す
ることができるので、特に好適に用いることができる。
沈降分離カラムの大きさと形状に特に制限はないが、移
送ポンプで活性汚泥混合液を移送して沈降分離カラムに
導入するときに、汚泥の沈降が生じないようにポンプ流
量から沈降分離カラムの大きさと形状を設定することが
好ましい。本発明装置において、上澄み中に含まれる濁
質成分濃度を測定する濁質成分検知手段に特に制限はな
く、例えば、表面散乱光式濁度検出器、視覚濁度測定用
器具、透過光濁度計、散乱光濁度計、積分球濁度計など
を挙げることができる。また、レーザー光を用いて、上
澄み中の微粒子による反射光や遮断光の強さを検出する
ことによっても、濁りの強度を検出することができる。
これらの中で、表面散乱光式濁度検出器は、非接触式で
連続測定が可能であり、汚れに対して耐性を有し、標準
液を調製する必要もないので、特に好適に用いることが
できる。
In the apparatus of the present invention, there is no particular limitation on the solid-liquid separation means for separating the suspended water extracted by the water intake means into a supernatant and a concentrated water containing a high concentration of suspended substances.
For example, a sedimentation separation column, a centrifuge, a membrane separation device and the like can be mentioned. Among these, the sedimentation separation column is particularly preferable because it has a simple structure and is easy to maintain and can be used by directly connecting to a suspension water tank, and can always perform solid-liquid separation under constant conditions. Can be used.
There is no particular limitation on the size and shape of the sedimentation separation column.However, when the activated sludge mixture is transferred by the transfer pump and introduced into the sedimentation separation column, the size of the sedimentation separation column is determined from the pump flow rate so that sludge does not settle. It is preferable to set the shape and shape. In the apparatus of the present invention, there is no particular limitation on the turbid component detecting means for measuring the turbid component concentration contained in the supernatant. For example, a surface scattered light turbidity detector, a visual turbidity measuring instrument, a transmitted light turbidity Meter, scattered light turbidity meter, integrating sphere turbidity meter and the like. Also, the intensity of turbidity can be detected by detecting the intensity of light reflected or blocked by fine particles in the supernatant using laser light.
Among these, the surface scattered light type turbidity detector is particularly preferably used because it can perform continuous measurement in a non-contact type, has resistance to dirt, and does not require the preparation of a standard solution. Can be.

【0007】図1は、本発明の懸濁水の水質測定装置の
一態様の説明図であり、図2は、その部分拡大図であ
る。本態様の装置は、活性汚泥曝気槽1、活性汚泥混合
液中に設置された取水口2、取水管3、移送ポンプ4、
バルブ5及び沈降分離カラム6を備えている。活性汚泥
曝気槽内には、散気管7及びろ過ユニット8が設けら
れ、活性汚泥曝気槽の外側にろ過水排出トラフ9が設け
られている。ろ過ユニットとろ過水排出トラフは、ろ過
水排出サイホン管10により結ばれている。原水が活性
汚泥曝気槽に供給され、曝気空気が散気管から放出され
て、曝気槽内の活性汚泥混合液中で有機物の酸化分解が
進行する。ろ過水排出サイホン管は、減圧配管11を通
じて減圧にすることにより、ろ過水で満たされる。活性
汚泥曝気槽の液面は、ろ過水排出トラフの水面より高く
保持され、両液面間の水頭差により活性汚泥混合液がろ
過ユニットでろ過されて、ろ過水がろ過水排出トラフに
流出する。ろ過ユニットが精密ろ過膜又は限外ろ過膜で
ある場合は、散気管を図1に示すようにろ過ユニットの
ほぼ直下に設置し、ろ過ユニットの膜面部の活性汚泥混
合液の流れを上向流のクロスフロー流れとすることが好
ましい。ろ過ユニットが、目開きの粗いろ布又は不織布
からなるろ過体の表層にダイナミックろ過層を形成して
活性汚泥混合液中の懸濁汚泥粒子を捕捉し、ろ過水を取
り出すダイナミックろ過体である場合は、散気管をろ過
ユニットの存在しない側の曝気槽の底部に設置し、ろ過
ユニットの膜面部の活性汚泥混合液の流れを下向流のク
ロスフロー流れとすることが好ましい。必要に応じて、
活性汚泥曝気槽内のろ過ユニット側とろ過ユニットが存
在しない側の間に仕切り板を設けることができる。
FIG. 1 is an explanatory view of one embodiment of the apparatus for measuring the quality of suspended water according to the present invention, and FIG. 2 is a partially enlarged view thereof. The apparatus of this embodiment includes an activated sludge aeration tank 1, an intake port 2 installed in an activated sludge mixture, an intake pipe 3, a transfer pump 4,
A valve 5 and a sedimentation separation column 6 are provided. A diffuser pipe 7 and a filtration unit 8 are provided in the activated sludge aeration tank, and a filtered water discharge trough 9 is provided outside the activated sludge aeration tank. The filtration unit and the filtered water discharge trough are connected by a filtered water discharge siphon tube 10. Raw water is supplied to the activated sludge aeration tank, aerated air is released from the air diffuser, and oxidative decomposition of organic substances proceeds in the activated sludge mixture in the aeration tank. The filtered water discharge siphon pipe is filled with filtered water by reducing the pressure through the pressure reducing pipe 11. The liquid level of the activated sludge aeration tank is kept higher than the water level of the filtered water discharge trough, and the activated sludge mixture is filtered by the filtration unit due to the head difference between the two liquid levels, and the filtered water flows out to the filtered water discharge trough. . When the filtration unit is a microfiltration membrane or an ultrafiltration membrane, an air diffuser is installed almost immediately below the filtration unit as shown in FIG. 1, and the flow of the activated sludge mixture on the membrane surface of the filtration unit is directed upward. It is preferable that the cross-flow flow is as follows. In the case where the filtration unit is a dynamic filtration body that forms a dynamic filtration layer on the surface layer of a filtration body made of a coarsely-clothed filter cloth or a nonwoven fabric, captures suspended sludge particles in the activated sludge mixture, and takes out filtered water. Preferably, a diffuser is installed at the bottom of the aeration tank on the side where the filtration unit is not present, and the flow of the activated sludge mixture on the membrane surface of the filtration unit is a downward cross flow. If necessary,
A partition plate can be provided between the filtration unit side and the side where no filtration unit is present in the activated sludge aeration tank.

【0008】図1に示す態様の本発明装置においては、
活性汚泥混合液が取水口2から取水管3を通じて移送ポ
ンプ4により抜き取られ、沈降分離カラム6底部の導入
口12から沈降分離カラムに送り込まれる。沈降分離カ
ラムの上部は、カラムの周囲から活性汚泥混合液が溢流
トラフ13に均等に溢流し、溢流トラフから排出され
る。沈降分離カラムの最上部には、活性汚泥混合液の液
面が形成され、光照射部14と受光部15とからなる表
面散乱光式濁度検出器により、液面の濁度が検出され
る。測定にあたっては、活性汚泥混合液を沈降分離カラ
ムに移送し、カラム上部より溢流させる。次いで、移送
ポンプ4を停止し、バルブ5を閉じて、活性汚泥混合液
の移送を停止し、一定時間静置する。この静置時間は、
5分から30分程度が好適である。一定時間停止したの
ち、再度活性汚泥混合液を沈降分離カラムに移送する。
図3は、この工程における濁度検出曲線の一例である。
沈降分離カラムへ活性汚泥混合液を一定流量で移送し続
けると、液面の濁度検出強度は一定値を保つ。次いで、
活性汚泥混合液の移送を停止し、静置工程に移ると、液
面の濁度検出強度は多少変動する。この濁度検出強度の
変動は、移送停止による液面の乱れによるものと想定さ
れる。沈降分離カラムへの活性汚泥混合液の移送を再開
すると、液面の濁度検出強度は下がり始め、濁度検出強
度最小点を経由したのち、最初の濁度検出強度の一定値
に復帰する。このような濁度検出曲線から、最小濁度検
出強度を求めることにより、上澄み中に含まれる濁質成
分濃度を測定することができる。沈降分離後の沈降分離
カラム内の液を押し出し溢流させる手段として、活性汚
泥混合液でなく清水を用いた場合には、濁度検出強度は
明瞭な最小値を示さず、上澄み濁度を測定することが困
難となる。なお、沈降分離カラムの清掃用として、清水
給水手段やスクレーパーやブラシなどの補助手段を設け
ることもできる。本発明装置を用いることにより、懸濁
水中に含まれる微細粒子のみを分離してモニターするこ
とができ、ろ過により固液分離を行う活性汚泥処理装置
の運転管理に活用することができる。
[0008] In the apparatus of the present invention shown in FIG.
The activated sludge mixture is withdrawn from the water inlet 2 through the water intake pipe 3 by the transfer pump 4 and sent into the sedimentation column through the inlet 12 at the bottom of the sedimentation column 6. At the upper part of the sedimentation separation column, the activated sludge mixture liquid uniformly overflows the overflow trough 13 from around the column, and is discharged from the overflow trough. The liquid level of the activated sludge mixture is formed at the uppermost part of the settling separation column, and the turbidity of the liquid level is detected by the surface scattered light type turbidity detector including the light irradiation unit 14 and the light receiving unit 15. . In the measurement, the activated sludge mixture is transferred to a sedimentation separation column and overflowed from the upper part of the column. Next, the transfer pump 4 is stopped, the valve 5 is closed, the transfer of the activated sludge mixture is stopped, and the mixture is allowed to stand for a certain period of time. This standing time is
About 5 to 30 minutes is preferable. After stopping for a certain period of time, the activated sludge mixture is again transferred to the sedimentation column.
FIG. 3 is an example of a turbidity detection curve in this step.
When the activated sludge mixture is continuously transferred to the settling separation column at a constant flow rate, the turbidity detection intensity on the liquid surface maintains a constant value. Then
When the transfer of the activated sludge mixture is stopped and the process proceeds to the standing step, the turbidity detection intensity on the liquid surface slightly changes. It is assumed that the fluctuation of the turbidity detection intensity is caused by disturbance of the liquid level due to the stop of the transfer. When the transfer of the activated sludge mixture to the sedimentation separation column is resumed, the turbidity detection intensity on the liquid surface starts to decrease, and after returning to the minimum turbidity detection intensity point, the turbidity detection intensity returns to the initial constant value of the turbidity detection intensity. By obtaining the minimum turbidity detection intensity from such a turbidity detection curve, the concentration of the turbid component contained in the supernatant can be measured. If fresh water is used instead of the activated sludge mixture as a means to push out and overflow the liquid in the sedimentation separation column after sedimentation separation, the turbidity detection intensity does not show a clear minimum value, and the supernatant turbidity is measured. It will be difficult to do. In addition, auxiliary means such as fresh water supply means and a scraper or a brush may be provided for cleaning the sedimentation separation column. By using the apparatus of the present invention, only the fine particles contained in the suspension water can be separated and monitored, and can be utilized for operation management of an activated sludge treatment apparatus that performs solid-liquid separation by filtration.

【0009】[0009]

【実施例】以下に、実施例を挙げて本発明をさらに詳細
に説明するが、本発明はこれらの実施例によりなんら限
定されるものではない。 実施例1 図1に示す装置により、活性汚泥混合液の上澄みの濁度
検出強度を測定した。活性汚泥曝気槽は実効容量1m
3で、側面面積400mm×400mmのろ過モジュールを
有するろ過ユニット5個が配置されている。原水とし
て、BOD180mg/L、SS130mg/Lの下水を用
い、曝気槽の滞留時間を6時間とした。沈降分離カラム
は、底部が円錐形状で、活性汚泥混合液導入口が設けら
れた、内径100mm、高さ500mmの円筒状で、活性汚
泥混合液はカラムの最上部より溢流し、最上部に形成さ
れる液面の濁度を測定する表面散乱光式濁度検出器[電
気化学計器(株)、TUF−5]が設けられている。活性
汚泥曝気槽内に設置された取水口から、移送ポンプによ
り、活性汚泥混合液を50mL/minの速度で沈降分離カ
ラムに送り込んだ。この移送工程において、液面の濁度
検出強度は2,100mg/Lであった。次いで、移送ポ
ンプを停止し、バルブを閉めて、20分間静置を保っ
た。静置工程中、液面の濁度検出強度は多少変動した
が、ほぼ2,000mg/Lであった。ふたたびバルブを
開き、移送ポンプを運転して活性汚泥混合液を50mL/
minの速度で沈降分離カラムに送り込むと、濁度検出強
度は急速に下がり、移送再開11分後に30mg/Lの濁
度検出強度最小点に達した。その後、濁度検出強度は徐
々に上昇し、移送再開46分後に2,100mg/Lに戻
った。図3は、得られた濁度検出曲線である。なお、本
図において、横軸の時間は、静置工程開始時を0として
示す。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the present invention. Example 1 The turbidity detection intensity of the supernatant of the activated sludge mixture was measured by the apparatus shown in FIG. Activated sludge aeration tank is 1m effective capacity
In 3 , three filtration units having a filtration module with a side area of 400 mm × 400 mm are arranged. Sewage of BOD 180 mg / L and SS 130 mg / L was used as raw water, and the residence time in the aeration tank was set to 6 hours. The sedimentation separation column has a conical bottom and is provided with an activated sludge mixture inlet, and has a cylindrical shape with an inner diameter of 100 mm and a height of 500 mm. A surface scattered light type turbidity detector [Electrochemical Instrument Co., Ltd., TUF-5] for measuring the turbidity of the liquid surface to be prepared is provided. The activated sludge mixture was fed into the settling separation column at a rate of 50 mL / min by a transfer pump from an intake port installed in the activated sludge aeration tank. In this transfer step, the turbidity detection intensity of the liquid surface was 2,100 mg / L. Next, the transfer pump was stopped, the valve was closed, and the container was kept still for 20 minutes. During the standing step, the detection intensity of turbidity on the liquid surface slightly changed, but was approximately 2,000 mg / L. Open the valve again and operate the transfer pump to bring the activated sludge mixture to 50 mL /
When sent to the sedimentation separation column at the speed of min, the turbidity detection intensity decreased rapidly, and reached the minimum turbidity detection intensity of 30 mg / L 11 minutes after resumption of the transfer. Thereafter, the turbidity detection intensity gradually increased and returned to 2,100 mg / L 46 minutes after the transfer was resumed. FIG. 3 shows the obtained turbidity detection curve. In the figure, the time on the horizontal axis indicates 0 at the start of the standing process.

【0010】[0010]

【発明の効果】本発明の懸濁水の水質測定装置によれ
ば、簡便かつ正確に懸濁水中に含まれる微細粒子のみを
分離してモニターすることができ、ろ過により固液分離
を行う活性汚泥処理装置の運転管理に特に有用である。
According to the apparatus for measuring the quality of suspended water of the present invention, it is possible to simply and accurately separate and monitor only fine particles contained in suspended water, and to perform activated sludge which performs solid-liquid separation by filtration. It is particularly useful for the operation management of the processing apparatus.

【図面の簡単な説明】[Brief description of the drawings]

【図1】図1は、本発明の懸濁水の水質測定装置の一態
様の説明図である。
FIG. 1 is an explanatory diagram of one embodiment of a water quality measuring device for suspended water of the present invention.

【図2】図2は、図1の部分拡大図である。FIG. 2 is a partially enlarged view of FIG. 1;

【図3】図3は、濁度検出曲線の一例である。FIG. 3 is an example of a turbidity detection curve.

【符号の説明】[Explanation of symbols]

1 活性汚泥曝気槽 2 取水口 3 取水管 4 移送ポンプ 5 バルブ 6 沈降分離カラム 7 散気管 8 ろ過ユニット 9 ろ過水排出トラフ 10 ろ過水排出サイホン管 11 減圧配管 12 導入口 13 溢流トラフ 14 光照射部 15 受光部 DESCRIPTION OF SYMBOLS 1 Activated sludge aeration tank 2 Intake port 3 Intake pipe 4 Transfer pump 5 Valve 6 Sedimentation separation column 7 Diffusion pipe 8 Filtration unit 9 Filtration water discharge trough 10 Filtration water discharge siphon pipe 11 Decompression pipe 12 Inlet 13 Overflow trough 14 Light irradiation Unit 15 Light receiving unit

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/44 C02F 3/12 ZABP 3/12 ZAB G01N 21/49 Z G01N 21/49 21/59 Z 21/59 33/18 A 33/18 B01D 29/04 510E 510F 530A ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/44 C02F 3/12 ZABP 3/12 ZAB G01N 21/49 Z G01N 21/49 21/59 Z 21 / 59 33/18 A 33/18 B01D 29/04 510E 510F 530A

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】懸濁水の水質測定装置であって、懸濁水の
一部を抜き取る取水手段と、該取水手段によって抜き取
られた懸濁水を上澄みと懸濁物質を高濃度に含有する濃
縮水とに分離する固液分離手段と、該上澄み中に含まれ
る濁質成分濃度を測定する濁質成分検知手段とを備えて
なることを特徴とする懸濁水の水質測定装置。
1. A water quality measuring device for a suspension water, comprising: a water intake means for extracting a part of the suspension water; a supernatant water and a concentrated water containing a suspended substance in a high concentration; 1. A water quality measuring device for a suspended water, comprising: a solid-liquid separating means for separating the suspension; and a turbid component detecting means for measuring a turbid component concentration contained in the supernatant.
【請求項2】懸濁水が、精密ろ過膜、限外ろ過膜、又
は、目開きの粗いろ布、若しくは、不織布からなるろ過
体の表層にダイナミックろ過層を形成して汚水中の懸濁
粒子を捕捉し、ろ過水を取り出すダイナミックろ過体の
少なくとも一つからなるろ過手段の被処理水である請求
項1記載の懸濁水の水質測定装置。
2. A method for producing suspended particles in sewage by forming a dynamic filtration layer on the surface of a filter made of a microfiltration membrane, an ultrafiltration membrane, a filter cloth having coarse openings, or a nonwoven fabric. The suspension water quality measuring device according to claim 1, wherein the water quality of the suspended water is at least one of a dynamic filtration body that captures and removes filtered water.
【請求項3】懸濁水が、活性汚泥混合液である請求項1
又は請求項2記載の懸濁水の水質測定装置。
3. The suspension according to claim 1, wherein the suspension is an activated sludge mixture.
Or the water quality measuring device of the suspension water according to claim 2.
【請求項4】濁質成分検知手段が、表面散乱光式濁度検
出器である請求項1〜3のいずれかに記載の懸濁水の水
質測定装置。
4. The water quality measuring device according to claim 1, wherein the turbid component detecting means is a surface scattered light type turbidity detector.
JP2000359705A 2000-11-27 2000-11-27 Measuring device for suspension water quality Pending JP2002162338A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000359705A JP2002162338A (en) 2000-11-27 2000-11-27 Measuring device for suspension water quality

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000359705A JP2002162338A (en) 2000-11-27 2000-11-27 Measuring device for suspension water quality

Publications (1)

Publication Number Publication Date
JP2002162338A true JP2002162338A (en) 2002-06-07

Family

ID=18831433

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000359705A Pending JP2002162338A (en) 2000-11-27 2000-11-27 Measuring device for suspension water quality

Country Status (1)

Country Link
JP (1) JP2002162338A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007125465A (en) * 2005-11-01 2007-05-24 Mitsubishi Rayon Co Ltd Method for estimating degree of contamination of separating membrane used for membrane separation/activated sludge device
CN113230701A (en) * 2021-04-25 2021-08-10 中煤(天津)地下工程智能研究院有限公司 Transparent monitoring devices of unpowered multilayer position thickener
KR102404178B1 (en) * 2021-09-06 2022-05-31 주식회사 유앤유 Sytem for Continuous Monitoring Dissolved Organic Matter

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007125465A (en) * 2005-11-01 2007-05-24 Mitsubishi Rayon Co Ltd Method for estimating degree of contamination of separating membrane used for membrane separation/activated sludge device
CN113230701A (en) * 2021-04-25 2021-08-10 中煤(天津)地下工程智能研究院有限公司 Transparent monitoring devices of unpowered multilayer position thickener
KR102404178B1 (en) * 2021-09-06 2022-05-31 주식회사 유앤유 Sytem for Continuous Monitoring Dissolved Organic Matter

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