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JPH0660890B2 - Suspended substance aggregation state determination device - Google Patents
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JPH0660890B2 - Suspended substance aggregation state determination device - Google Patents

Suspended substance aggregation state determination device

Info

Publication number
JPH0660890B2
JPH0660890B2 JP60091770A JP9177085A JPH0660890B2 JP H0660890 B2 JPH0660890 B2 JP H0660890B2 JP 60091770 A JP60091770 A JP 60091770A JP 9177085 A JP9177085 A JP 9177085A JP H0660890 B2 JPH0660890 B2 JP H0660890B2
Authority
JP
Japan
Prior art keywords
circuit
signal
ultrasonic
suspended substance
sludge
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 - Lifetime
Application number
JP60091770A
Other languages
Japanese (ja)
Other versions
JPS61250552A (en
Inventor
研二 馬場
潤市 石井
昭二 渡辺
舜介 野北
幹雄 依田
雄二 山沢
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP60091770A priority Critical patent/JPH0660890B2/en
Publication of JPS61250552A publication Critical patent/JPS61250552A/en
Publication of JPH0660890B2 publication Critical patent/JPH0660890B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Investigating Or Analyzing Materials By The Use Of Ultrasonic Waves (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は懸濁液における懸濁物質の凝集状態を判別する
懸濁物質の凝集状態判別装置に関する。
Description: FIELD OF THE INVENTION The present invention relates to an apparatus for determining the state of aggregation of suspended substances for determining the state of aggregation of suspended substances in a suspension.

〔発明の背景〕[Background of the Invention]

廃水の活性汚泥プロセスや浄水処理プロセスにおいては
懸濁質フロツクの凝集性又は沈降性の良否が処理水質と
密接な関係がある。このため、懸濁質フロツクの凝集性
又は沈降性の測定はプロセスの運転管理上きわめて重要
なことである。これらを測定する手法としては懸濁液中
の懸濁質フロツクを沈降せしめて、凝集懸濁質フロツク
と分離液との境界を光学的に検出し、この境界位置の経
時変化から、懸濁質フロツクの凝集性又は沈降性を計測
する方法あるいは懸濁液を細管中に導き、細管内におけ
る凝集塊と非凝集塊、特に、非凝集塊の光学的濁度を検
出し、この検出値に基づいて懸濁液中懸濁物質の凝集性
を判別する方法などが知られている。しかし、いずれの
方法においても、境界検出値あるいは非凝集塊の濁度検
出値は光の透過度度又は散乱度などを用いて懸濁液の濁
度を検出し、この濁度から凝集性を判別するものであつ
て、直接的に懸濁物質の凝集状態を計測するものではな
く正確さに欠けるのを免れない。
In the activated sludge process and the purified water treatment process of wastewater, the quality of the flocculation or sedimentation of the suspension flocs is closely related to the treated water quality. For this reason, the measurement of the flocculating property or sedimentation property of the suspension flocs is very important for the operational control of the process. The method for measuring these is to settle the suspended matter flocs in the suspension, and to optically detect the boundary between the flocculated suspended matter flocs and the separated liquid. A method for measuring flocculation or sedimentation of flocs or a suspension is introduced into a thin tube, and the optical turbidity of the agglomerated and non-aggregated agglomerates, especially non-aggregated agglomerates, is detected in the capillary and based on the detected value. There is known a method for discriminating the cohesiveness of a suspended substance in a suspension. However, in any of the methods, the boundary detection value or the turbidity detection value of the non-aggregated lump is determined by detecting the turbidity of the suspension by using the light transmittance or the scattering degree, and the cohesiveness is determined from the turbidity. This is a method for making a distinction, and is not a method for directly measuring the agglomeration state of suspended solids, and it is unavoidable that it lacks accuracy.

また、これらの方法では、光学的計測手段を用いるた
め、検出部壁面の汚れなどの理由で誤差を生じる。さら
に、凝集塊が沈降するまで、または凝集沈降反応が充分
進行するまでの時間を要する。このため、活性汚泥プロ
セスや浄水処理プロセスの状態を判定して凝集剤注入制
御に速やかに反映されることができなかつた。
Further, in these methods, since an optical measuring means is used, an error occurs due to a stain on the wall surface of the detecting portion. Furthermore, it takes time for the aggregate to settle or for the aggregation-sedimentation reaction to proceed sufficiently. For this reason, it was not possible to judge the state of the activated sludge process or the water purification process and promptly reflect it in the coagulant injection control.

一方、汚泥処理プロセスでは、直接脱水方式の場合には
濃縮汚泥が、嫌気性消化方式の場合には消化汚泥が、各
々脱水される。脱水処理では汚泥に無機凝集剤又は有機
高分子凝集剤が注入された後に撹拌により凝集汚泥塊が
形成され、脱水機での脱水処理を効果的に行わせてい
る。無機凝集剤としては塩化第2鉄、硫酸第一鉄、消石
灰などが用いられる。また、有機高分子凝集剤として
は、ポリアクリルアミド、ポリビニルピリジン塩酸塩、
ポリアクリル酸ナトリウム、水溶性アニリン樹脂塩酸塩
及びポリエチレンイミンなどがある。
On the other hand, in the sludge treatment process, the concentrated sludge is dehydrated in the case of the direct dehydration system and the digested sludge is dehydrated in the case of the anaerobic digestion system. In the dehydration treatment, after the inorganic coagulant or the organic polymer coagulant is injected into the sludge, the aggregated sludge mass is formed by stirring, and the dehydration treatment in the dehydrator is effectively performed. As the inorganic coagulant, ferric chloride, ferrous sulfate, slaked lime, etc. are used. Further, as the organic polymer coagulant, polyacrylamide, polyvinyl pyridine hydrochloride,
Examples include sodium polyacrylate, water-soluble aniline resin hydrochloride and polyethyleneimine.

これら凝集剤の注入は汚泥の液流量又は固形物流量に比
例して注入している。ところが実際には、必要な凝集剤
量は、処理固形物流量に必ずしも比例せず、また汚泥性
状変化などの要因によつて所定の凝集効果が得られな
い。このため、注入凝集剤量の過不足が生じる。凝集剤
注入量が適正量よりも少なければ凝集せず、一方、必要
以上に凝集剤を注入すると高価な凝集剤を無駄に浪費し
て不経済であるだけでなく、凝集剤の過剰注入のため凝
集塊の再分散現象が起こる。このため、脱水汚泥の含水
率が低下せず、脱水汚泥量が増加すると共に脱水時間も
長くなる。
The coagulant is injected in proportion to the liquid flow rate of sludge or the solid flow rate. However, in reality, the required amount of coagulant is not always proportional to the flow rate of treated solid matter, and a predetermined coagulation effect cannot be obtained due to factors such as changes in sludge properties. Therefore, the amount of the injected coagulant is excessive or insufficient. If the coagulant injection amount is less than the proper amount, coagulation does not occur. On the other hand, if the coagulant is injected more than necessary, not only is it expensive to waste the expensive coagulant, it is also uneconomical. The phenomenon of redispersion of aggregates occurs. Therefore, the water content of the dehydrated sludge does not decrease, the amount of dehydrated sludge increases, and the dehydration time also increases.

近年、凝集効果の直接判別法として毛細管吸引時間CS
T(Capillary Suction Time )を測定する方法が提
案されている。CSTとは紙の上に円筒を密着載置
し、円筒上部から汚泥を入れて、この汚泥から所定量の
水分が紙上に吸収される時間で定義される。したがつ
て、CSTの測定は汚泥をサンプリングして円筒に供給
する操作を必要とし、オンラインで凝集効果を判定でき
ない。
In recent years, the capillary suction time CS has been used as a direct determination method for the aggregation effect.
A method for measuring T (Cpillary Suction Time) has been proposed. The CST is defined as the time in which a cylinder is placed in close contact with paper, sludge is put in from the top of the cylinder, and a predetermined amount of water is absorbed from the sludge onto the paper. Therefore, the CST measurement requires an operation of sampling sludge and supplying it to the cylinder, and the coagulation effect cannot be determined online.

一方、懸濁物質の粒径を超音波を用いて計測する方法が
例えば特公昭48−6388号公報で知られている。し
かし、粒径と凝集状態とは必ずしも一致せず、粒径を測
つただけでは正確に凝集状態を測定できない。
On the other hand, a method of measuring the particle size of a suspended substance using ultrasonic waves is known in, for example, Japanese Patent Publication No. 48-6388. However, the particle size and the agglomerated state do not always match, and the agglomerated state cannot be accurately measured only by measuring the particle size.

〔発明の目的〕[Object of the Invention]

本発明の目的は、懸濁液中の懸濁質粒子の凝集状態をオ
ンラインで正確に計測できる懸濁物質の凝集状態判別装
置を提供することにある。
An object of the present invention is to provide an apparatus for determining an agglomeration state of a suspended substance, which can accurately measure the agglomeration state of suspended particles in a suspension online.

〔発明の概要〕[Outline of Invention]

本発明の特徴とするところは、パルス発振回路で発生し
たパルス信号を受けて超音波を発生し懸濁液中を伝播さ
せて懸濁物質より反射する反射波を受信し電気信号に変
換する超音波送受信手段と、該超音波送受信手段で受信
した信号を取り込んで懸濁物質の凝集状態を判別する凝
集状態判別回路と、前記パルス発振回路及び前記凝集状
態判別回路に一定周期で0.1〜5KHzの周波数信号
を加えるタイミング設定回路とを備え、 前記凝集状態判別回路には、前記周波数信号を基にして
制御信号を出力するタイミング制御回路と、前記周波数
信号が該タイミング制御回路に入力されてから超音波の
送信波の影響を除くための時間遅れをとってオン制御信
号を出力し一定時間だけオンして前記超音波送受信手段
で受信した受信信号を取り込むアナログスイッチと、該
アナログスイッチをオンすることにより取り込まれた超
音波受信信号を積分し前記タイミング制御回路から出力
されたリセット信号により一定周期ごとにリセットされ
る積分回路と、該積分回路がリセットされる直前の積分
信号の大きさをホールドするサンプルホールド回路と、
該サンプルホールド回路でホールドされたホールド信号
の単位時間当たりの平均値を演算して凝集判別信号とし
て出力する平均値回路とを具備したことにある。超音波
の信号レベルは、反射波量である。
The feature of the present invention is that it receives a pulse signal generated by a pulse oscillating circuit, generates ultrasonic waves, propagates in a suspension, receives a reflected wave reflected from a suspended substance, and converts it into an electric signal. An ultrasonic wave transmitting / receiving means, an agglomeration state judging circuit for taking in a signal received by the ultrasonic wave transmitting / receiving means and judging an agglomeration state of a suspended substance, and a pulse oscillation circuit and an agglomeration state judging circuit for 0.1 to 0.1 times in a constant cycle. A timing setting circuit for applying a frequency signal of 5 KHz, wherein the aggregation state determination circuit outputs a control signal based on the frequency signal, and the frequency signal is input to the timing control circuit. From the above, an ON control signal is output with a time delay to remove the influence of the ultrasonic transmission wave, and the reception signal received by the ultrasonic transmission / reception means is captured by turning on for a certain period of time. The analog switch, an integration circuit that integrates the ultrasonic reception signal captured by turning on the analog switch and is reset at regular intervals by a reset signal output from the timing control circuit, and the integration circuit is reset. A sample and hold circuit that holds the magnitude of the integrated signal immediately before
And an average value circuit for calculating an average value of the hold signals held by the sample hold circuit per unit time and outputting it as an aggregation determination signal. The signal level of ultrasonic waves is the amount of reflected waves.

〔発明の実施例〕Example of Invention

第1図に本発明の一実施例を示す。 FIG. 1 shows an embodiment of the present invention.

第1図において、混和槽10には懸濁物質12を含む懸
濁液11が入つている。混和槽10の側壁に超音波送受
波子20が取付けられている。超音波送受波子20は第
3図に示すようにフランジ101とOリング102,1
03を介し、混和槽10に取付けたフランジ106で固
定されている。超音波送受波子20はパルス発振回路3
2からパルス信号を加えられる。超音波送受波子20は
パルス信号を加えられると超音波を発生し懸濁液中を伝
播させ、懸濁物質12および対向する側壁からの反射波
を受信する。パルス発振回路32はタイミング設定回路
31の発生する周波数信号に同期してパルス信号を発生
する。タイミング設定回路31は0.1〜5KHzの周
波数信号(タイミング信号)Sを発生する。タイミン
グ信号Sは凝集状態判別回路40にも加えられる。超
音波送受波子20の受信信号は増幅器33で増幅された
後に検波回路34に入力される。検波回路34で検波さ
れた受信々号(ビデオ信号)S01は凝集状態判別回路4
0に加えられる。
In FIG. 1, a mixing tank 10 contains a suspension 11 containing a suspended substance 12. An ultrasonic wave transmitter / receiver 20 is attached to the side wall of the mixing tank 10. As shown in FIG. 3, the ultrasonic wave transmitter / receiver 20 has a flange 101 and O-rings 102, 1
It is fixed by the flange 106 attached to the mixing tank 10 via 03. The ultrasonic wave transmitter / receiver 20 is a pulse oscillation circuit 3
The pulse signal is applied from 2. The ultrasonic wave transmitter / receiver 20 generates ultrasonic waves when a pulse signal is applied, propagates in the suspension, and receives the reflected waves from the suspended substance 12 and the opposing side wall. The pulse oscillator circuit 32 generates a pulse signal in synchronization with the frequency signal generated by the timing setting circuit 31. The timing setting circuit 31 generates a frequency signal (timing signal) S T of 0.1 to 5 KHz. The timing signal S T is also applied to the aggregation state determination circuit 40. The reception signal of the ultrasonic wave transmitter / receiver 20 is input to the detection circuit 34 after being amplified by the amplifier 33. The received signal (video signal) S 01 detected by the detection circuit 34 is the aggregation state determination circuit 4
Added to 0.

第2図に凝集状態判別回路40の詳細構成図を示す。FIG. 2 shows a detailed configuration diagram of the aggregation state determination circuit 40.

第2図において、タイミング制御回路401はタイミン
グ信号Sを基にして各種制御信号ST1〜ST4を出力す
る。アナログスイツチ402はオン制御信号ST1により
一定時間Tだけオンし受信々号S01を取り込み信号S
02として出力する。積分回路403は受信々号S02を積
分し、リセツト信号ST2により一定周期毎にリセツトさ
れる。サンプルホールド回路404は積分回路403が
リセツトされる直前の積分信号S03の大きさをホールド
する。平均値回路405は単位時間当りのホールド信号
04の平均値を求め、この平均値を凝集判別信号S05
して表示装置406に加える。
In FIG. 2, the timing control circuit 401 outputs various control signals S T1 to S T4 based on the timing signal S T. The analog switch 402 is turned on for a certain period of time T 1 by the ON control signal S T1 and receives the received signal S 01, and the signal S
Output as 02 . The integrating circuit 403 integrates the received signal S 02 and resets it at a constant cycle by the reset signal S T2 . The sample hold circuit 404 holds the magnitude of the integrated signal S 03 immediately before the reset of the integrating circuit 403. The average value circuit 405 calculates the average value of the hold signal S 04 per unit time and adds this average value to the display device 406 as the aggregation determination signal S 05 .

次に、その動作を第4図,第5図に示す波形図を参照し
て説明する。
Next, the operation will be described with reference to the waveform charts shown in FIGS.

タイミング設定回路31は一定周期でタイミング信号S
を発生する。パルス発振回路32はタイミング信号S
に周期してパルス信号を発生し超音波送受波子20に
加える。超音波送受波子20はパルス信号を加えられる
と懸濁液11中に超音波を送出する。懸濁液11を伝播
した超音波のうち、懸濁物質12に当つた超音波は一部
が透過すると共に1部が吸収され、残りが反射する。懸
濁物質12から反射した超音波は超音波送受波子20に
受信され電気信号に変換される。受信々号は増幅器33
で増幅され検波回路34に入力される。検波回路34は
第4図に示す如きビデオ信号(受信々号)S01を出力す
る。受信々号S01はアナログスイツチ402に入力され
る。タイミング制御回路401はタイミング信号S
入力してからΔt時間後に一定時間Tだけオン制御信
号ST1を出力する。アナログスイツチ402は時間T
だけオンする。アナログスイツチ402をオンするのを
タイミング信号Sから時間Δtだけ遅れさせたのは送
信波(漏れ込波)の影響を除くためである。また、時間
は混和槽10の対向側壁面からの反射波を積分回路
403に入力しないようにして決定される。具体的に
は、混合槽10の内径をL、懸濁液中の音速をvとする
と、超音波が超音波送受波子20から対向側壁面まで伝
播する時間tは次式で表わされる。
The timing setting circuit 31 outputs the timing signal S at a constant cycle.
Generate T. The pulse oscillation circuit 32 uses the timing signal S
A pulse signal is generated in a cycle of T and applied to the ultrasonic wave transmitter / receiver 20. The ultrasonic wave transmitter / receiver 20 transmits an ultrasonic wave into the suspension 11 when a pulse signal is applied. Among the ultrasonic waves propagated through the suspension 11, a part of the ultrasonic waves hitting the suspended substance 12 are transmitted, part of the ultrasonic waves is absorbed, and the other is reflected. The ultrasonic wave reflected from the suspended substance 12 is received by the ultrasonic wave transmitter / receiver 20 and converted into an electric signal. Received signal is amplifier 33
It is amplified by and input to the detection circuit 34. The detection circuit 34 outputs a video signal (received signal) S 01 as shown in FIG. The received signal S 01 is input to the analog switch 402. The timing control circuit 401 outputs the ON control signal S T1 for a certain time T 1 after Δt time from the input of the timing signal S T. The analog switch 402 takes time T 1
Just turn it on. The reason why the analog switch 402 is turned on is delayed from the timing signal S T by the time Δt is to eliminate the influence of the transmission wave (leak wave). Further, the time T 1 is determined so that the reflected wave from the opposing side wall surface of the mixing tank 10 is not input to the integrating circuit 403. Specifically, assuming that the inner diameter of the mixing tank 10 is L and the sound velocity in the suspension is v, the time t 1 for the ultrasonic wave to propagate from the ultrasonic wave transmitter / receiver 20 to the opposing side wall surface is represented by the following equation.

=L/v ……(1) 対向側壁面から反射した超音波が超音波送受波子20に
到達して受信されるまでの時間tは次式のようにな
る。
t 1 = L / v (1) The time t 2 until the ultrasonic wave reflected from the opposed side wall surface reaches the ultrasonic wave transmitter / receiver 20 and is received is as follows.

=2L/v ……(2) したがつて、時間Tの最長時間tmax は次式で制限さ
れる。
t 2 = 2L / v (2) Therefore, the maximum time t max of the time T 1 is limited by the following equation.

max <2L/v ……(3) アナログスイツチ402から得られる受信々号S02は第
4図に示すようになる。積分回路403は受信々号S02
を積分した積分信号S03を出力する。タイミング制御回
路401はオン制御信号ST1の立下り時に同期してサン
プルホールド回路404にホールド指令信号ST3を与え
る。サンプルホールド回路404はホールド指令信号S
T3を与えられた時点の積分信号S03の値を取込みホール
ドする。タイミング制御回路401はサンプルホールド
を行うのに要する時間後にリセツト信号ST2を積分回路
403に与えてリセツトさせる。このような動作はタイ
ミング設定回路31がタイミング信号Sを発生する毎
に繰返し行われる。この動作が所定回数行われると、タ
イミング制御回路401は平均値回路405に演算開始
指令信号ST4を与える。平均値回路405は信号ST4
与えられると第5図に示すように信号ST4の一周期間に
おけるホールド値S04、つまり受信信号S02の大きさの
平均値S05を求める。第5図はタイミング信号Sの3
周期を平均値演算の一周期にしている例を示している。
実用に際してはタイミング信号Sの10周期以上を平
均値演算の一周期とするのが望ましい。平均値S05は凝
集判別信号として表示装置406に入力される。凝集判
別信号S05の大きさ、つまり懸濁物質12からの反射波
レベルが小さいと凝集が良好に行われていると判別し、
信号S05のレベルが大きいと凝集が充分でないと判別す
る。
t max <2 L / v (3) The reception signal S 02 obtained from the analog switch 402 is as shown in FIG. The integrating circuit 403 receives the received signal S 02.
An integrated signal S 03 obtained by integrating is output. The timing control circuit 401 gives a hold command signal S T3 to the sample hold circuit 404 in synchronization with the fall of the ON control signal S T1 . The sample hold circuit 404 holds the hold command signal S
The value of the integrated signal S 03 at the time when T3 is given is taken in and held. The timing control circuit 401 gives a reset signal S T2 to the integrator circuit 403 for resetting after a time required for performing the sample hold. Such an operation is repeated every time the timing setting circuit 31 generates the timing signal S T. When this operation is performed a predetermined number of times, the timing control circuit 401 gives the average value circuit 405 a calculation start command signal S T4 . When the average value circuit 405 is supplied with the signal S T4 , it calculates the hold value S 04 during one cycle of the signal S T4 , that is, the average value S 05 of the magnitude of the received signal S 02 , as shown in FIG. FIG. 5 shows 3 of the timing signal S T.
An example is shown in which the cycle is one cycle of the average value calculation.
In practical use, it is desirable to set 10 cycles or more of the timing signal S T as one cycle of the average value calculation. The average value S 05 is input to the display device 406 as an aggregation determination signal. If the magnitude of the aggregation determination signal S 05 , that is, the level of the reflected wave from the suspended substance 12 is small, it is determined that the aggregation is performed well,
If the level of the signal S 05 is large, it is determined that the aggregation is not sufficient.

本発明は以上のように、懸濁物質からの反射波の積分
値、換言すると反射波量によつて凝集状態を判別してい
る。懸濁物質からの反射波量によつて凝集状態を判別で
きる理由を実験結果に基づき説明する。
As described above, the present invention determines the aggregation state based on the integrated value of the reflected wave from the suspended substance, in other words, the reflected wave amount. The reason why the aggregation state can be determined by the amount of reflected waves from the suspended substance will be explained based on the experimental results.

都市下水処理場の汚泥脱水工程において、凝集剤注入前
の汚泥を採取し、汚泥懸濁固形物量に対する凝集剤注入
量の割合、すなわち凝集剤注入率を変化させて本発明と
CSTによる凝集効果判別値を測定した。
In the sludge dewatering process of an urban sewage treatment plant, the sludge before injecting the coagulant is collected and the ratio of the coagulant injection amount to the sludge suspended solids amount, that is, the coagulant injection rate is changed to determine the coagulation effect according to the present invention and CST. The value was measured.

第6図に凝集剤注入率に対するCSTの変化を示す。凝
集剤注入率の増加に伴つてCSTは減少し、注入率が約
0.6%のとき最小値になつている。注入率が0.6%
のとき脱水性が最も良いことを示している。
FIG. 6 shows the change in CST with respect to the coagulant injection rate. The CST decreases as the coagulant injection rate increases, and reaches the minimum value when the injection rate is about 0.6%. Injection rate is 0.6%
It shows that the dehydration is the best.

一方、本発明は超音波送受波子20の振動数は0.5M
Hz、時間Tを60μs、タイミング信号Sの周波
数を1KHz、平均値演算の一周期の時間を0.1秒に
して実験した。この実験におけるビデオ信号S01と積分
信号S03との薬注率に対する変化は第8図(a)〜(f)のよ
うになつた。第8図(a)〜(f)における薬注率は各々0,
0.121,0.220,0.382,0.578,0.839%である。
On the other hand, in the present invention, the ultrasonic transducer 20 has a frequency of 0.5M.
The experiment was conducted by setting the frequency Hz, the time T 1 to 60 μs, the frequency of the timing signal S T to 1 KHz, and the period of one cycle of the average value calculation to 0.1 seconds. The changes in the video signal S 01 and the integrated signal S 03 with respect to the drug injection rate in this experiment are as shown in FIGS. 8 (a) to (f). The drug injection rate in FIGS. 8 (a) to (f) is 0,
It is 0.121, 0.220, 0.382, 0.578, 0.839%.

本発明の実験結果による凝集剤注入率に対する凝集効果
判別値の変化を第7図に示す。
FIG. 7 shows the change in the aggregation effect determination value with respect to the coagulant injection rate according to the experimental results of the present invention.

第6図と第7図を比較して明らかなように、本発明によ
る凝集効果判別値はCSTの対数値と同じパターンにな
つている。したがつて、懸濁物質からの反射量の大きさ
によつて凝集効果の良否を判別できることがわかる。
As is clear from comparison between FIG. 6 and FIG. 7, the aggregation effect determination value according to the present invention has the same pattern as the logarithmic value of CST. Therefore, it can be seen that the quality of the aggregation effect can be determined based on the magnitude of the amount of reflection from the suspended substance.

このように、本発明は懸濁物質の反射波量によつて凝集
状態を判別している。この現象は定かでないが、本発明
者達は次の理由であると考えている。
As described above, the present invention discriminates the aggregation state based on the reflected wave amount of the suspended substance. Although this phenomenon is not clear, the present inventors consider it as the following reason.

汚泥凝集の模式図を第9図に示す。凝集前の汚泥の微小
粒子61は懸濁液中でコロイド状で分散しており、表面
付着水62や間隙水63を多量に有する。凝集剤64が
注入されると、この凝集剤64は微小汚泥粒子61の表
面から付着水を分離させて粒子61相互を結びつけ、凝
集塊すなわちフロツク65を形成する。同時に、汚泥粒
子61間からは間隙水63が除去される。このため、フ
ロツク65外の水分が増加して汚泥から水分が抜けやす
くなる。このように、汚泥の凝集では、単に汚泥粒子の
粒径が増加するだけでなく、汚泥粒子そのものの性質
(密度や音響特性)が変化する。また、汚泥フロツクは
撹拌で容易に壊れ易いことから、凝集剤64が粒子61
相互を結びつける力は弱い。このことは、汚泥フロツク
65の構造が柔構造であることを意味する。したがつ
て、汚泥フロツク65に当つた超音波はその波長が汚泥
フロツク65に近いところで、共振現象をおこし、超音
波エネルギーを吸収するものと考えられる。
A schematic diagram of sludge aggregation is shown in FIG. The fine particles 61 of sludge before aggregation are dispersed in a suspension in a colloidal form, and have a large amount of surface-adhered water 62 and pore water 63. When the coagulant 64 is injected, the coagulant 64 separates the adhered water from the surface of the fine sludge particles 61 and binds the particles 61 to each other to form a coagulated mass or a block 65. At the same time, the pore water 63 is removed from between the sludge particles 61. For this reason, the water content outside the block 65 increases, and the water content easily escapes from the sludge. Thus, in the sludge agglomeration, not only the particle size of the sludge particles increases, but also the properties (density and acoustic characteristics) of the sludge particles themselves change. In addition, since the sludge flocks are easily broken by stirring, the coagulant 64 becomes particles 61
The power to connect each other is weak. This means that the structure of the sludge block 65 is a flexible structure. Therefore, it is considered that the ultrasonic wave hitting the sludge flocks 65 causes a resonance phenomenon and absorbs ultrasonic energy when the wavelength thereof is close to the sludge flocks 65.

この推論の妥当性を検証するために次の実験を実施し
た。汚泥粒子61にあたる超音波は第10図のように、
反射、吸収及び透過する。超音波の吸収量は直接に測定
できないので、反射量と透過量とを同時に測定すること
で、吸収量を測定した。その結果、表1に示す。
The following experiment was conducted to verify the validity of this inference. The ultrasonic waves that hit the sludge particles 61 are as shown in FIG.
Reflects, absorbs and transmits. Since the absorption amount of ultrasonic waves cannot be directly measured, the absorption amount was measured by simultaneously measuring the reflection amount and the transmission amount. The results are shown in Table 1.

表1に示すように、凝集後の反射量と透過量とは凝集前
に比べて減少した。このことから、汚泥フロツク65の
超音波吸収量が増加したことが判る。また、凝集後の汚
泥フロツク65の粒径分布を測定したところ第11図の
ようになり、粒径が2ないし3mmのフロツクが多数を占
めた。周波数が0.5MHzのときの波長は2.97mm
であり、フロツク粒径とほぼ同じである。このことは、
汚泥粒子はフロツクになると超音波を吸収するという推
論と一致する。
As shown in Table 1, the amount of reflection and the amount of transmission after aggregation were smaller than those before aggregation. From this, it can be seen that the amount of ultrasonic waves absorbed by the sludge block 65 increased. When the particle size distribution of the sludge flocs 65 after coagulation was measured, the result was as shown in FIG. 11, and the majority of the flocs having particle sizes of 2 to 3 mm. When the frequency is 0.5MHz, the wavelength is 2.97mm
And is almost the same as the floc particle size. This is
This is consistent with the inference that sludge particles absorb ultrasonic waves when they become flocked.

〔発明の効果〕〔The invention's effect〕

以上説明したように、本発明によれば懸濁液中における
懸濁物質粒子の凝集性をオンラインで計測できるので、
懸濁物質の凝集状態又は効果を管理するプロセスのモニ
ターあるいは制御に利用でき、プロセスの処理性能を向
上させることができる。
As described above, according to the present invention, the aggregating property of suspended substance particles in a suspension can be measured online,
It can be used for monitoring or controlling the process for controlling the agglomeration state or effect of suspended matter, and can improve the process performance of the process.

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

第1図は本発明の一実施例を示す構成図、第2図は凝集
状態判別回路の詳細構成図、第3図は超音波送受波子の
取付構成図、第4図,第5図は動作説明用の波形図、第
6図,第7図は実験結果の特性図、第8図は実験で得ら
れた信号波形図、第9図は凝集の模式図、第10図は超
音波の吸収度合の説明用模式図、第11図はフロツクの
粒径分布測定特性図である。 10……混和槽、20……超音波送受波子、30……超
音波送受信器、40……凝集効果判別回路、401……
タイミング制御回路、402……アナログスイツチ、4
03……積分回路、404……サンプルホールド回路、
405……平均値回路、406……表示装置。
FIG. 1 is a configuration diagram showing an embodiment of the present invention, FIG. 2 is a detailed configuration diagram of an agglomeration state determination circuit, FIG. 3 is an attachment configuration diagram of ultrasonic transducers, and FIGS. 4 and 5 are operations. Waveforms for explanation, FIGS. 6 and 7 are characteristic diagrams of experimental results, FIG. 8 is a signal waveform diagram obtained in the experiment, FIG. 9 is a schematic diagram of aggregation, and FIG. 10 is absorption of ultrasonic waves. Fig. 11 is a schematic diagram for explaining the degree, and Fig. 11 is a characteristic diagram for measuring the particle size distribution of flock. 10 ... Mixing tank, 20 ... Ultrasonic transmitter / receiver, 30 ... Ultrasonic transceiver, 40 ... Aggregation effect discrimination circuit, 401 ...
Timing control circuit, 402 ... Analog switch, 4
03 ... integrator circuit, 404 ... sample hold circuit,
405 ... Average value circuit, 406 ... Display device.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 野北 舜介 茨城県日立市久慈町4026番地 株式会社日 立製作所日立研究所内 (72)発明者 依田 幹雄 茨城県日立市大みか町5丁目2番1号 株 式会社日立製作所大みか工場内 (72)発明者 山沢 雄二 東京都千代田区神田駿河台4丁目6番地 株式会社日立製作所内 (56)参考文献 特開 昭49−74995(JP,A) 特開 昭52−148193(JP,A) ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Shunsuke Nokita 4026 Kujimachi, Hitachi City, Ibaraki Prefecture Hitachi Research Laboratory, Hitachi Co., Ltd. (72) Inventor Mikio Yoda 5-2-1 Omikacho, Hitachi City, Ibaraki Prefecture Incorporated company Hitachi Ltd. Omika factory (72) Inventor Yuji Yamazawa 4-6 Kanda Surugadai, Chiyoda-ku, Tokyo Inside Hitachi Ltd. (56) Reference JP 49-74995 (JP, A) JP 52 -148193 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】パルス発振回路で発生したパルス信号を受
けて超音波を発生し懸濁液中を伝播させて懸濁物質より
反射する反射波を受信し電気信号に変換する超音波送受
信手段と、該超音波送受信手段で受信した信号を取り込
んで懸濁物質の凝集状態を判別する凝集状態判別回路
と、前記パルス発振回路及び前記凝集状態判別回路に一
定周期で0.1〜5KHzの周波数信号を加えるタイミ
ング設定回路とを備え、 前記凝集状態判別回路には、前記周波数信号を基にして
制御信号を出力するタイミング制御回路と、前記周波数
信号が該タイミング制御回路に入力されてから超音波の
送信波の影響を除くための時間遅れをとってオン制御信
号を出力し一定時間だけオンして前記超音波送受信手段
で受信した受信信号を取り込むアナログスイッチと、該
アナログスイッチをオンすることにより取り込まれた超
音波受信信号を積分し前記タイミング制御回路から出力
されたリセット信号により一定周期ごとにリセットされ
る積分回路と、該積分回路がリセットされる直前の積分
信号の大きさをホールドするサンプルホールド回路と、
該サンプルホールド回路でホールドされたホールド信号
の単位時間当たりの平均値を演算して凝集判別信号とし
て出力する平均値回路とを具備したことを特徴とする懸
濁物質の凝集状態判別装置。
1. An ultrasonic wave transmitting / receiving means for receiving a pulse signal generated by a pulse oscillating circuit, generating ultrasonic waves, propagating in a suspension, receiving a reflected wave reflected from a suspended substance, and converting the reflected wave into an electric signal. An agglomeration state determination circuit that takes in a signal received by the ultrasonic transmission / reception means and determines the agglomeration state of a suspended substance, and a frequency signal of 0.1 to 5 KHz at a constant cycle in the pulse oscillation circuit and the agglomeration state determination circuit And a timing setting circuit that applies a timing control circuit that outputs a control signal based on the frequency signal, and an ultrasonic wave after the frequency signal is input to the timing control circuit. An analog switch that outputs an ON control signal with a time delay for removing the influence of a transmission wave, turns on for a certain period of time, and captures a reception signal received by the ultrasonic transmission / reception means. , An integrating circuit which integrates the ultrasonic reception signal taken in by turning on the analog switch and is reset at regular intervals by a reset signal output from the timing control circuit, and an integrating circuit immediately before the integrating circuit is reset. A sample and hold circuit that holds the magnitude of the integrated signal,
An average value circuit for calculating an average value of the hold signals held by the sample and hold circuit per unit time and outputting the average value as an aggregation determination signal.
JP60091770A 1985-04-26 1985-04-26 Suspended substance aggregation state determination device Expired - Lifetime JPH0660890B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60091770A JPH0660890B2 (en) 1985-04-26 1985-04-26 Suspended substance aggregation state determination device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60091770A JPH0660890B2 (en) 1985-04-26 1985-04-26 Suspended substance aggregation state determination device

Publications (2)

Publication Number Publication Date
JPS61250552A JPS61250552A (en) 1986-11-07
JPH0660890B2 true JPH0660890B2 (en) 1994-08-10

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ID=14035805

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH0660890B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2533699B2 (en) * 1991-06-25 1996-09-11 株式会社日立製作所 Acoustic leak detector
JP4822611B2 (en) * 2001-05-18 2011-11-24 西松建設株式会社 Muddy water treatment apparatus and muddy water treatment method
JP5577958B2 (en) * 2010-08-30 2014-08-27 大同特殊鋼株式会社 Method for measuring concentration of non-dissolved liquid by ultrasound
CN103728370A (en) * 2013-08-12 2014-04-16 太仓派欧技术咨询服务有限公司 Detection device for quantitatively measuring suspension property of glass cotton pulp
JP7182497B2 (en) * 2019-03-12 2022-12-02 株式会社日立製作所 Sludge treatment system

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4974995A (en) * 1972-11-18 1974-07-19
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Also Published As

Publication number Publication date
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