JPS5875061A - Measuring apparatus for concentration of floating matter of activated sludge - Google Patents
Measuring apparatus for concentration of floating matter of activated sludgeInfo
- Publication number
- JPS5875061A JPS5875061A JP17307781A JP17307781A JPS5875061A JP S5875061 A JPS5875061 A JP S5875061A JP 17307781 A JP17307781 A JP 17307781A JP 17307781 A JP17307781 A JP 17307781A JP S5875061 A JPS5875061 A JP S5875061A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- concentration
- circuit
- measurement
- ultrasonic waves
- 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.)
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Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/18—Water
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Medicinal Chemistry (AREA)
- Physics & Mathematics (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Investigating Or Analyzing Materials By The Use Of Ultrasonic Waves (AREA)
Abstract
Description
【発明の詳細な説明】
l)発明技術分針
本発明は、下水処理場の活性汚泥処理の管理指標を求め
る活性汚泥浮遊物濃度測定装置、に係り、特に直接ML
88濃度を測定することなしに簡易的にMLSSを求め
る装置に関する。DETAILED DESCRIPTION OF THE INVENTION l) Inventive technology minute hand The present invention relates to an activated sludge suspended matter concentration measuring device for determining a management index for activated sludge treatment in a sewage treatment plant, and particularly relates to a direct ML
This invention relates to a device for simply determining MLSS without measuring 88 concentration.
2)従来技術 “
下水処理場において活性汚泥処理の効率を高めるためC
:、制御指標として、処理槽(ばつ気槽)内の水温、P
H,溶存酸素などの他に、活性汚泥処理物(以下、これ
をML88と相称する)の濃度および沈降汚泥容it(
以T1これを8■と相称する)を測定している。また、
最近は活性汚泥の管理指標として、8V/ML88の比
をとってモールマン指標と呼ぶ汚泥容量゛指標(以下、
これを8VIと相称する)を重要視しその測定を行なっ
ている。2) Conventional technology “C
: As a control index, water temperature in the treatment tank (aeration tank), P
In addition to H, dissolved oxygen, etc., the concentration of the activated sludge treated product (hereinafter referred to as ML88) and the settled sludge volume it (
Hereinafter T1 (hereinafter referred to as 8■) is measured. Also,
Recently, as a management index for activated sludge, the ratio of 8V/ML88 is taken and the sludge capacity index (hereinafter referred to as Moleman index) is used.
This is commonly referred to as 8VI) and is being measured.
従って、この種装置は、ML88濃度とSVを自動的に
測定し、さらにsV/MLSSを演算してSVI値を自
動的(二算出している。Therefore, this type of device automatically measures the ML88 concentration and SV, and further calculates the SVI value by calculating sV/MLSS.
以下、第1図を参照して従来装置の一連の動作を工程別
に分けて説明する。Hereinafter, a series of operations of the conventional apparatus will be explained step by step with reference to FIG.
■ サンプリング工程・・・先ず、弁1.2および三方
弁3を開いてエアポンプ4を動作させ、8 Veill
定w 5 オヨi:J:Ml、8811定セル6 O内
部を減圧してばっ気!II7の中の汚泥液8を配管9を
通して吸引し、MLS88111定セル6およびSv測
定管5の中に採取する。この採取量を所定の容量(IJ
)とするためにレベル計10が一般けられており、 S
v測定管5の所定レベルまで汚泥液を採取したら弁1、
および三方弁3を閉じ、ヱアボ・ンプ4を停止し、大気
開放弁11を開いて8v測定管5の中を大気圧の状態に
設定する。■ Sampling process...First, open valve 1.2 and three-way valve 3, operate air pump 4,
Constant w 5 Oyo i: J: Ml, 8811 constant cell 6 O Reduce the pressure inside and vent! Sludge liquid 8 in II 7 is sucked through pipe 9 and collected into MLS88111 constant cell 6 and Sv measuring tube 5. This sampled amount is set to a predetermined capacity (IJ
), the level meter 10 is generally truncated, and S
v When the sludge liquid has been collected to a predetermined level in the measuring pipe 5, the valve 1
Then, the three-way valve 3 is closed, the abo pump 4 is stopped, and the atmosphere release valve 11 is opened to set the inside of the 8V measuring tube 5 to atmospheric pressure.
■ ML88測定工程・・・次に、空気導入弁13を開
けてgt、ss@1定セル6に空気を吹込み採取した汚
泥液を攪拌する。これは、汚泥液採取終了と同時に汚泥
浮遊物が沈降するので、MLSS測゛定にあたって汚泥
液の攪拌を行なって汚泥浮遊物の均一分解を図り測定誤
差の生じないようシニしたものである。(2) ML88 measurement process...Next, the air introduction valve 13 is opened and air is blown into the gt, ss@1 constant cell 6 to stir the collected sludge liquid. This is because the sludge suspension settles as soon as the sludge liquid collection is completed, so the sludge liquid is stirred in the MLSS measurement to ensure uniform decomposition of the sludge suspension and to avoid measurement errors.
汚泥液の攪拌會終了したならば、空気導入弁13および
弁2を閉じてMLSM一度の測定に入る。MLS89度
の測定は、ガラス等の透明体のMLSS測定セル6をは
さんで投光器14および受光器15を配置し、 所定の
タイミングでこれらの機器14 、15を動作させてM
L88測定回路16でMLSS濃度を測定している。When the stirring of the sludge liquid is completed, the air introduction valve 13 and the valve 2 are closed to begin one MLSM measurement. To measure MLS of 89 degrees, a light emitter 14 and a light receiver 15 are placed across an MLSS measurement cell 6 made of a transparent material such as glass, and these devices 14 and 15 are operated at a predetermined timing.
The L88 measurement circuit 16 measures the MLSS concentration.
即ち、投光器14の光が測定セル6の中の汚泥液を透過
して受光器15で受光するが、 この透過受光量が汚泥
浮遊物濃度と一定の関係にあるので、その受光量をもっ
てMLS 8濃度を測定できる。そして、ここで測定し
たMLSS濃度値はML8S値データホールド回路17
にホールドされる。That is, the light from the projector 14 passes through the sludge in the measurement cell 6 and is received by the light receiver 15. Since the amount of transmitted light has a certain relationship with the sludge suspended solids concentration, the amount of light received is used as the MLS 8. Concentration can be measured. The MLSS concentration value measured here is the ML8S value data hold circuit 17.
is held.
■ SV測定行程・・次(−1同じく透明体のS V
ill定管5の中の汚泥液を所定時間(例えば30゛分
間)静置させると、汚泥沈殿部21と上澄液部22′と
に分かれ境界面23が形成される。この境界面23の位
置はサーボ機構24に接続したs v @1定用投光器
25および受光器26で構成する光゛峨スイッチによっ
て 検出され、後続のボテンVヨメータ27より位置信
号を発生す名。従って、この位置信号をSVI
測定回路28で8v値として測定し出力する。■ SV measurement process...Next (-1 SV of the same transparent body
When the sludge liquid in the ill fixed tube 5 is allowed to stand still for a predetermined period of time (for example, 30 minutes), it is divided into a sludge settling portion 21 and a supernatant liquid portion 22', and a boundary surface 23 is formed. The position of this boundary surface 23 is detected by an optical intensity switch consisting of an SV@1 regular emitter 25 and a light receiver 26 connected to a servo mechanism 24, and a position signal is generated from a subsequent button V yometer 27. Therefore, this position signal is measured and output as an 8V value by the SVI measurement circuit 28.
■ SvI値算比算出1以−Fのようにして測定したS
V値とMLS8値は8V1値演算回路30 に入り、こ
こで8V1MLSSの演算を行なってSVI値を求め出
力する。■ SvI value calculation ratio calculation 1 - S measured as in F
The V value and the MLS8 value enter an 8V1 value calculation circuit 30, where an 8V1MLSS calculation is performed to determine and output the SVI value.
■ 排出・洗浄工程・・・以上のような測定動作が終了
した。ならば、弁1,2および三方弁31を開いてエア
ポンプ4を動作させ、Sv測定管5の−E部より空気を
入れて加圧し、Sv測定管5およびML88測定セル6
の中(二汚泥液を配管9を通して排出する。■ Discharge/cleaning process...The above measurement operations have been completed. If so, open the valves 1 and 2 and the three-way valve 31, operate the air pump 4, pressurize the air from the -E section of the Sv measurement tube 5, and then open the Sv measurement tube 5 and the ML88 measurement cell 6.
(The sludge liquid is discharged through pipe 9.
次に、汚泥′液の排出が終了したならば、弁lを閉じて
洗浄水弁32を開いて清水を導入しSV測定管5および
ML88測定セル6の中シー清水をためる。そして、空
気導入弁13を開いて空気を導入し、パブ嗅、ングして
測定管5、測定セル6を洗浄する。洗浄後、前記排出行
程と、同様の動作で洗浄水を排出する。Next, when the discharge of the sludge liquid is completed, the valve 1 is closed and the wash water valve 32 is opened to introduce fresh water and collect the fresh water in the SV measuring tube 5 and the ML88 measuring cell 6. Then, the air introduction valve 13 is opened to introduce air, and the measurement tube 5 and measurement cell 6 are cleaned by sniffing. After cleaning, the cleaning water is discharged by an operation similar to the discharge process described above.
3)従来技術の問題点
以上第1図により汚泥容曽指JIA測定装置の従来例を
説明してきたが、かなり複雑で高価な装置である。3) Problems with the Prior Art The conventional example of the sludge volume JIA measuring device has been described above with reference to FIG. 1, but it is a fairly complicated and expensive device.
すなわち、(1) ML88測定部とSV測定部の二つ
の測定部が必要である。(2)電気回路的にみてもML
S S測定回路、ML8S値データホールF回路、8■
測測定M、SVI (、= 8V(*)/MLSSWb
))演算回路が必要であるり(3) MLS8 、8V
とも光学的測定法を用いて、いるため1回の測定終了毎
にSV測定管内およびM L S S測定セ゛ル内に洗
浄水を導゛入し、さらに空気に゛よりバブリングして洗
浄を行なわなければならない。That is, (1) two measurement units, an ML88 measurement unit and an SV measurement unit, are required. (2) ML from an electrical circuit perspective
S S measurement circuit, ML8S value data hole F circuit, 8■
Measurement measurement M, SVI (, = 8V (*) / MLSSWb
)) Requires an arithmetic circuit (3) MLS8, 8V
Since both methods use an optical measurement method, cleaning water must be introduced into the SV measurement tube and the MLSS measurement cell after each measurement, and further cleaning must be carried out by bubbling air. Must be.
したがって、もつと構造が簡単で簡易的にsvt 、
svおよびML588を求められる装置が要望されると
ころである。Therefore, the structure is simple and it is easy to use svt,
A device that can obtain sv and ML588 is desired.
4)発明の目的及び構成
本発明は、上記要望1:対処して成されたもので、s
V #I定管内で所定時間経過後のSVおよび沈殿部分
の汚泥濃度を測定し、SV値・と汚泥濃を値の乗算によ
りMLSSを求めるようにしたもので、従来(二くらべ
構造が簡単で安価な装置を提供することを目的としてい
る。4) Object and structure of the invention The present invention has been accomplished in response to the above request 1.
V #I Measures the SV and the sludge concentration in the settling part after a predetermined period of time in a fixed pipe, and calculates the MLSS by multiplying the SV value and the sludge concentration. The aim is to provide inexpensive equipment.
5)発明の実施例 本発明の一実施例について第2図を参照して説明する。5) Examples of the invention An embodiment of the present invention will be described with reference to FIG.
なお、第2図において2乃至5゜7乃至11 、21乃
至23 、31.32は従来例の@1図と同じであるの
で、その詳細な説明は省略する。Note that in FIG. 2, 2 to 5 degrees, 7 to 11 degrees, 21 to 23 degrees, and 31.32 are the same as in FIG. @1 of the conventional example, so a detailed explanation thereof will be omitted.
40は、測定管5の側壁(二上下方向に配列されて取り
付けられた複数個の超音波送信子で、41は上下方向4
;長い超音波受信子(複数個のものを組み合せたもので
よい)で、超音波送信子40と対向して測定管5の側壁
に取り付けられている。42は、超音波受信子41から
の受信信号を増幅する増幅器、43は受信信号がある一
定値以上レベルであったかどうかを判定するためのレベ
ル判定回路、44は発振回路45t−制御し、またレベ
ル判定回路43からの4IT号を受けて何番目の超音波
送信子からの超音波が一定値以上の強度で受4tlされ
たかの信号を変換回路46に送るための制御回路である
。40 is a plurality of ultrasonic transmitters arranged and attached in the vertical direction (2) on the side wall of the measuring tube 5;
; A long ultrasonic receiver (a combination of a plurality of ultrasonic receivers may be used) is attached to the side wall of the measuring tube 5, facing the ultrasonic transmitter 40. 42 is an amplifier for amplifying the received signal from the ultrasonic receiver 41; 43 is a level determination circuit for determining whether the received signal is at a certain level or higher; 44 is an oscillation circuit 45t for controlling and level This is a control circuit that receives the 4IT signal from the determination circuit 43 and sends to the conversion circuit 46 a signal indicating from which ultrasonic transmitter the ultrasonic wave was received with an intensity equal to or higher than a certain value.
47は、増−器42からの信号を受けてその信号の大き
さC;より汚泥濃度(9%)を決定するための汚泥濃度
測定回路、 48は、汚泥けて100/i)を演算する
逆数演算回路である。47 is a sludge concentration measuring circuit for receiving a signal from the multiplier 42 and determining the sludge concentration (9%) based on the magnitude C of the signal; 48 is a circuit for calculating sludge concentration (100/i); This is a reciprocal calculation circuit.
また、49は、変換回路46で得られたSv゛値と汚泥
濃度測定回路47で得られた濃度D(%)を乗算するた
めの乗算回路である。Further, 49 is a multiplication circuit for multiplying the Sv′ value obtained by the conversion circuit 46 and the concentration D (%) obtained by the sludge concentration measurement circuit 47.
Sv■の定義は、 である。The definition of Sv■ is It is.
8V測定管(−採取された汚泥液の所定線(11)中に
分散し゛〔いる汚泥浮遊物は、Sv測測定所定時間(3
0分)経過後には測定管下部にtk、殿する、すなわち
沈殿部分(−濃縮されており、そのam度はlOO/5
v(aIb)テアル。The sludge floating matter dispersed in the predetermined line (11) of the 8V measuring tube (-) of the sampled sludge liquid is measured for the predetermined Sv measurement time (3
After 0 minutes), tk precipitates at the bottom of the measuring tube, i.e., the precipitate part (- is concentrated, and its am degree is lOO/5
v(aIb) Theal.
したがって、沈殿部分の汚泥濃度D(%)はとなる。よ
って、
また、
5vS)Xl)($l=ML8S(%)−=・(4)こ
の(3)式が示すように沈殿部分の汚泥ati)を測定
し、さらに100/I)を演算すればSVIが求められ
る。Therefore, the sludge concentration D (%) in the settling part is as follows. Therefore, 5vS) SVI is required.
また、(4)式が示すようC二Svおよび沈殿部分の汚
泥濃度りを測定し、8VxDを演算することによりML
8Bを求めることもできる。In addition, as shown in equation (4), the ML
You can also find 8B.
以上述べたように従来はSvおよびML88をホ11定
して5VI5求めていたが、本発明の装置においては沈
殿部分の汚泥11fおよびSvを測定して8VIおよび
1viL88を求めるのが特徴である。As described above, conventionally, 5VI5 was determined by determining Sv and ML88, but the apparatus of the present invention is characterized in that 8VI and 1viL88 are determined by measuring sludge 11f and Sv in the sedimentation part.
次に、一連の動作を工程別に職を追って説明する。Next, the series of operations will be explained step by step.
■サンプリング工程
先ず弁2および三方弁3を開いてエアポンプ4を動作さ
せ測定管5の内部を減圧してばつ気槽7の中の汚泥液8
を配管9を通して吸引し、Sv測測定5の中に採取する
。この採取篭を所定の容1t(1/)とするためレベル
計10が設けられており、8v測定管5の所定レベルま
で汚泥液を採取したら弁2および三方弁3を閉じ、エア
ポンプ4を停止し、大気開放弁11を開いてS■測定管
5の中を大気圧の状態にする。■ Sampling process First, open the valve 2 and the three-way valve 3, operate the air pump 4, reduce the pressure inside the measuring tube 5, and sludge liquid 8 in the aeration tank 7.
is sucked through the pipe 9 and collected in the Sv measurement 5. A level meter 10 is provided to make this collection basket have a predetermined volume of 1 t (1/), and when the sludge liquid is collected to the predetermined level of the 8V measuring tube 5, the valve 2 and the three-way valve 3 are closed, and the air pump 4 is stopped. Then, open the atmospheric release valve 11 to bring the inside of the S① measuring tube 5 to atmospheric pressure.
0測芝工程
(イ)8 V m 定
S■測定管5の中の汚泥液を所定時間
(30分間)静置すると、汚泥沈殿部21 とF澄液
部22とに分かれ境界面23が形成さnる。制御回路4
4 G二より発振回路45を制(社)して、超音波送信
子40の下側のものから順次超音波を発射させ、この超
音波を超音波受信子41で受信し、受信される超音波強
度がある一定値以上であるかどうかをレベル判定回路4
3で判定し、判定信号を制御回路44に送る。0 Grass measurement process (A) 8 V m Constant S ■ When the sludge liquid in the measuring tube 5 is allowed to stand still for a predetermined time (30 minutes), it is divided into a sludge settling part 21 and an F clear liquid part 22, and a boundary surface 23 is formed. Sanru. Control circuit 4
4 Control the oscillation circuit 45 from G2 to sequentially emit ultrasonic waves from the lower side of the ultrasonic transmitter 40, receive the ultrasonic waves with the ultrasonic receiver 41, and transmit the received ultrasonic waves. A level judgment circuit 4 determines whether the sound wave intensity is above a certain value.
3 and sends a determination signal to the control circuit 44.
汚泥沈殿21が存在する高さまでの位置にある超音波送
信子から発射された超音波は汚泥による減衰を受けるた
め、受信強度はレベル判定回路43で設定されるある−
定値以下である。そして、沈殿境界面23よりも上側(
:位置する超音波送信子か、ら発射された超音波は汚泥
減衰を受けないため、受信強度はレベル判定回路43で
設定されるある一定値以上となる。このように、何番目
の光源から発射された超音波がある一定値以上の強度で
受信されたかを検出することにより汚泥沈殿の高さを測
定し、変換回路46を通してSV値を求めることができ
る。Since the ultrasonic waves emitted from the ultrasonic transmitter located at the height of the sludge sediment 21 are attenuated by the sludge, the reception intensity is set by the level determination circuit 43.
It is below the fixed value. And above the precipitation boundary surface 23 (
: Since the ultrasonic waves emitted from the located ultrasonic transmitter are not subject to sludge attenuation, the reception intensity is equal to or higher than a certain value set by the level determination circuit 43. In this way, the height of sludge precipitation can be measured by detecting which number of light sources the ultrasonic waves emitted from are received with an intensity above a certain value, and the SV value can be determined through the conversion circuit 46. .
(ロ)沈殿汚泥濃度測定
(1)の8v測定において汚泥沈殿の高さが測定された
ので、制御回路44により発振回路45を制御して沈殿
視界面23より下に位置する超音波送信子の一つから超
音波を発射し、超音波受信子41で受信される超音波強
度から汚泥llIl測度回路47により沈殿汚泥の濃度
を測定する。(b) Since the height of sludge sedimentation was measured in the 8V measurement of sedimentation sludge concentration measurement (1), the control circuit 44 controls the oscillation circuit 45 to transmit the ultrasonic transmitter located below the sedimentation viewing surface 23. An ultrasonic wave is emitted from one, and the concentration of the settled sludge is measured from the intensity of the ultrasonic wave received by the ultrasonic receiver 41 by the sludge measurement circuit 47.
■SVI値算出
以上のように測定した沈殿部21の汚泥濃度り一)は逆
数演算回路48人力され、100/l)= svi値を
求め出力される。(2) Calculation of SVI value The sludge concentration in the sedimentation section 21 measured as described above is inputted to the reciprocal calculation circuit 48, and 100/l)=svi value is determined and output.
■MLS8算出
変換回路46からのS V <@値と汚泥濃度測定回路
47からの沈殿汚泥績f D (*)は乗算回路49−
二人力され(SV)xt) =MLSS(罰を求め出力
される。■SV<@ value from MLS8 calculation conversion circuit 46 and settled sludge result f D from sludge concentration measurement circuit 47 (*) is multiplication circuit 49-
Two people are forced (SV) xt) = MLSS (punishment is sought and output.
■排出工程
以上の動作か終了したら弁2および三方弁31を開いて
ヱアボンプ4を動作させSv測定管5の上部より空気入
れて加圧し、Sv測測定管の中の汚泥液を配管9を通し
て排出する。■When the discharge process and above operations are completed, open the valve 2 and the three-way valve 31, operate the air pump 4, pump air from the upper part of the Sv measuring pipe 5, pressurize it, and discharge the sludge liquid in the Sv measuring pipe through the pipe 9. do.
なお、超廿波式測定法は光学式測定法はど汚れのえいき
ようを受けないので1回の測牢科了毎に洗゛浄水を導入
して、SV測定管内洗浄する必要はない。したがって、
洗浄水弁32を開いて洗浄水導入する洗浄動作はある期
間毎に行うようはすればよい。In addition, since the ultra-high wave measurement method is not affected by the effects of dirt like the optical measurement method, there is no need to introduce clean water to clean the inside of the SV measurement pipe after each measurement. therefore,
The cleaning operation of opening the cleaning water valve 32 and introducing cleaning water may be performed every certain period.
また、この実施例C二おいては、SV値を決定した超音
波送信子からの超音波の・強度をもって汚泥強度を求め
ているため、沈殿の濃度分布が高さ方向に一様でなかっ
た場合には、測定誤差を生ずる。それを解決する手段に
ついて第3図を用いて説明する。In addition, in this Example C2, the sludge strength was determined based on the intensity of the ultrasonic waves from the ultrasonic transmitter that determined the SV value, so the concentration distribution of the sediment was not uniform in the height direction. In some cases, measurement errors occur. A means for solving this problem will be explained using FIG. 3.
沈殿汚泥濃度測定にあたっては、沈殿境界面23より下
に位置する超音波送信子のすべてから順次超音波を発射
し、それぞれC:ついて超音波受信子で受信される超音
波強度から各高さ位置の沈殿汚泥一度りを測定し、さら
に平均化回路50によりDの平均値りを求めるものであ
る。このようCユ平均濃度を求めること(−より、界面
の濃度分布の影響を除去することができ′る。To measure the settled sludge concentration, ultrasonic waves are sequentially emitted from all the ultrasonic transmitters located below the settling boundary surface 23, and the ultrasonic intensity received by the ultrasonic receivers is measured at each height position. The settled sludge of D is measured once, and the average value of D is determined by an averaging circuit 50. By determining the average concentration of C in this way, the influence of the concentration distribution at the interface can be removed.
6)発明の効果
従来の装置はMLS8測定セル部と8v測定管部の二つ
の測定部が必要で、またMLBS値゛ データホールド
回路も必要であり、したがって装置が複雑で高価であっ
た。6) Effects of the Invention The conventional device required two measurement sections, an MLS8 measurement cell section and an 8V measurement tube section, and also required an MLBS value data hold circuit, making the device complicated and expensive.
これに対して、′本発明1:よれば8v測定管′flカ
必要11jり(tテ、しかも8V、SVI、Ml、88
の三つの測定項目の値を求めることができる装置の構成
が簡単で安価な活性汚泥浮遊物−l測度装置を提供する
ことができる。On the other hand, according to the present invention 1, an 8V measuring tube is required, and 8V, SVI, Ml, 88
It is possible to provide an activated sludge suspended solids-l measuring device which has a simple configuration and is inexpensive, which can determine the values of the three measurement items.
第1図は従来の測定装置を示す構成図、1J42図は本
発明の一実施例を示す構成図、第3図は本発明の他の実
施例を示す回路構成図である。
40・・・超音波送信子 45・・・発振回路41・・
・超音波受信子 46・・・変換回路42・・・増幅器
47・・・汚泥濃度測定回路43・・・レベル
判定回路 48・・・逆数変換回路44・・・制御回路
49・・・乗算回路代理人 弁理士 則近雁佑
(ほか1名)第2図
第3図FIG. 1 is a block diagram showing a conventional measuring device, FIG. 1J42 is a block diagram showing one embodiment of the present invention, and FIG. 3 is a circuit diagram showing another embodiment of the present invention. 40... Ultrasonic transmitter 45... Oscillation circuit 41...
- Ultrasonic receiver 46... Conversion circuit 42... Amplifier 47... Sludge concentration measurement circuit 43... Level judgment circuit 48... Reciprocal conversion circuit 44... Control circuit 49... Multiplier circuit Agent Patent Attorney Gansuke Norichika
(1 other person) Figure 2 Figure 3
Claims (1)
、所定時間(例えば30分間)静置した後(二形成され
る汚泥沈殿部の容量(SV)および汚泥濃度(D)を測
定し、この汚泥容量(8v)と汚泥濃度(L))とを乗
算することにより活性汚泥浮遊物(Ml、88 )11
1度を求めるようにしたことを特徴とする活性汚泥浮遊
物濃度測定装置。Collect the sludge liquid with a predetermined content (for example, 11) in the measurement pipe, and after allowing it to stand for a predetermined period of time (for example, 30 minutes), measure the volume (SV) and sludge concentration (D) of the sludge settling part formed, By multiplying this sludge volume (8V) and sludge concentration (L), activated sludge suspended matter (Ml, 88)11
An activated sludge suspended matter concentration measuring device characterized in that it measures 1 degree.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17307781A JPS5875061A (en) | 1981-10-30 | 1981-10-30 | Measuring apparatus for concentration of floating matter of activated sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17307781A JPS5875061A (en) | 1981-10-30 | 1981-10-30 | Measuring apparatus for concentration of floating matter of activated sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5875061A true JPS5875061A (en) | 1983-05-06 |
Family
ID=15953775
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17307781A Pending JPS5875061A (en) | 1981-10-30 | 1981-10-30 | Measuring apparatus for concentration of floating matter of activated sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5875061A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115452670A (en) * | 2022-11-11 | 2022-12-09 | 清华大学 | Method and device for measuring sediment content in flowing water body |
-
1981
- 1981-10-30 JP JP17307781A patent/JPS5875061A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115452670A (en) * | 2022-11-11 | 2022-12-09 | 清华大学 | Method and device for measuring sediment content in flowing water body |
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