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JP3300764B2 - Suspension coagulation test method and coagulant injection amount determination method - Google Patents
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JP3300764B2 - Suspension coagulation test method and coagulant injection amount determination method - Google Patents

Suspension coagulation test method and coagulant injection amount determination method

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Publication number
JP3300764B2
JP3300764B2 JP26679691A JP26679691A JP3300764B2 JP 3300764 B2 JP3300764 B2 JP 3300764B2 JP 26679691 A JP26679691 A JP 26679691A JP 26679691 A JP26679691 A JP 26679691A JP 3300764 B2 JP3300764 B2 JP 3300764B2
Authority
JP
Japan
Prior art keywords
light intensity
transmitted light
injection amount
agglutination
coagulant
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 - Fee Related
Application number
JP26679691A
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Japanese (ja)
Other versions
JPH07171307A (en
Inventor
文雄 中村
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Individual
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Individual
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Priority to JP26679691A priority Critical patent/JP3300764B2/en
Publication of JPH07171307A publication Critical patent/JPH07171307A/en
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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

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】この発明は、一本の凝集反応
装置の延長上に設置した1組または複数の透過光強度測
定装置により連続的に測定された透過光強度変化から、
凝集反応の良否の判定と最適凝集剤注入量を決定する凝
集試験方法であるので、反応槽内における各種の粒子の
成長過程の検知、検出、解析に有効であり、特に、浄
水、下水、産業用廃水等における凝集沈殿処理分野に有
効である。
BACKGROUND OF THE INVENTION The present invention relates to a method for measuring a change in transmitted light intensity continuously measured by one or a plurality of transmitted light intensity measuring devices installed on an extension of one agglutination reaction device.
This agglutination test method determines the quality of the agglutination reaction and determines the optimal amount of coagulant to be injected.It is effective for detecting, detecting, and analyzing the growth process of various particles in the reaction tank. It is effective in the field of coagulation and sedimentation treatment for industrial wastewater.

【0002】[0002]

【従来の技術】従来、懸濁液の凝集試験は、主としてジ
ャーテスト法により実施されており、その結果に基づい
て最適凝集剤注入量が決定されてきた。しかしながら、
ジャーテスト法はバッチ方式で実施されるものであり、
時間、労力、経験を必要とする欠点があり、したがっ
て、水質の時間変動に即応しない欠点がある。この対応
策として、実験式法およびフィードバック法があるが、
これらは基本的には、数個の水質項目と関連づけた凝集
剤注入量決定方法であり、水質の変動に対する対応性と
信頼性に欠ける欠点がある。他に、ファジー法やPDA
法等があるが、未だ検討段階にあるものであり、実用性
に乏しい。
2. Description of the Related Art Conventionally, a coagulation test of a suspension is mainly performed by a jar test method, and an optimum coagulant injection amount has been determined based on the results. However,
The jar test method is performed in a batch method,
It has the disadvantage of requiring time, effort, and experience, and therefore has the disadvantage of not responding to water quality fluctuations over time. There are empirical formula and feedback method as a countermeasure for this.
These are basically methods for determining the coagulant injection amount associated with several water quality items, and have a drawback in that they lack responsiveness and reliability to fluctuations in water quality. In addition, the fuzzy method and PDA
Although there is a law, it is still in the stage of examination and is not practical.

【0003】[0003]

【発明が解決しようとする課題】凝集沈殿処理における
最適凝集剤注入量は、水温、水中の各種共存イオンの種
類とその濃度、懸濁物の質および量、撹拌条件などの多
様な因子の変動により時々刻々変化するものであり、し
たがって、各時点における条件に即応した最適凝集剤注
入量を決定する必要がある。しかしながら、前述のよう
に、従来の凝集試験方法(ジャーテスト法)に基づく最
適凝集剤注入量決定方法は時間、労力、経験を必要と
し、水質の時間変動に対する即応性と信頼性にかける欠
点がある。
The optimum coagulant injection amount in the coagulation and sedimentation process depends on various factors such as water temperature, types and concentrations of various coexisting ions in water, quality and amount of suspension, and stirring conditions. Therefore, it is necessary to determine the optimal coagulant injection amount corresponding to the conditions at each time point. However, as described above, the method for determining the optimal coagulant injection amount based on the conventional coagulation test method (jar test method) requires time, effort, and experience, and has a drawback in terms of responsiveness and reliability to time fluctuation of water quality. is there.

【0004】そこで、一本の凝集反応装置の延長上に設
置した1組または複数の透過光強度測定装置により連続
的に測定された透過光強度変化から、凝集反応の良否の
判定と最適凝集剤注入量を連続的に推定する方法を確立
し、それに基づいて、水質の時間変動への即応性を持
ち、短時間に、しかも、労力と経験を必要とせずに、自
動的に最適凝集剤注入量を決定し得る方法を確立せんと
するものである。
[0004] Therefore, from the change in transmitted light intensity continuously measured by one or a plurality of transmitted light intensity measuring devices installed on the extension of one agglutination reaction device, it is determined whether or not the agglutination reaction is good and the optimum aggregating agent is used. Established a method for continuously estimating the amount of injection, and based on this method, was able to respond quickly to changes in water quality, and in a short time, without the need for labor and experience, to automatically optimize the coagulant injection The aim is to establish a method by which the amount can be determined.

【0005】[0005]

【課題を解決するための手段】前記の問題点を解決する
ための本発明の手段は (a)濃度の異なる凝集剤と懸濁液との混和液を連続的
に作成するか、または凝集剤濃度変化装置により連続的
に濃度を変化させた凝集剤を懸濁液に注入する第1の段
階と (b)光源部と受光部とから成る1組または複数の透過
光強度測定装置とを具備する一本の凝集反応装置中に、
凝集剤濃度の異なる所定量の混和液を所定の速度で連続
的にポンプ送水し、混合・撹拌し、凝集反応を進行させ
る第2の段階と (c)第2の段階の過程で、連続的に透過光強度を測定
する第3の段階と (d)第3の段階で、連続的に測定された透過光強度変
化から、平均透過光強度およびその振幅を求め、これよ
り凝集・フロック形成速度(以下凝集速度と記す)、フ
ロック径、フロック数を算出する第4の段階と (e)第4の段階で連続的に算出された凝集速度、フロ
ック径、フロック数、およびそれらの最大値または最小
値に基づき、凝集反応の良否の判定と最適凝集剤注入量
を決定する第5の段階とを具備することを特徴とする懸
濁液の凝集試験方法および凝集剤注入量決定方法であ
る。
Means for Solving the Problems] whether the means of the present invention to solve the problems of creating a mixed solution of coagulant and suspensions of different (a) concentrations continuous manner, or aggregation A first step of injecting a coagulant whose concentration has been continuously changed by an agent concentration changing device into a suspension; and (b) one or a plurality of transmitted light intensity measuring devices including a light source unit and a light receiving unit. In one agglutination reactor equipped,
A second step of continuously pumping a predetermined amount of the mixed liquid having a different coagulant concentration at a predetermined speed, mixing and stirring, and allowing the coagulation reaction to proceed; and (c) a continuous step in the second step. And (d) in the third step, the average transmitted light intensity and its amplitude are obtained from the continuously measured changes in transmitted light intensity, and the aggregation / floc formation speed is calculated from this. (Hereinafter referred to as a flocculation rate), a floc diameter, a floc number and a fourth step of calculating the floc number; and (e) a flocculation rate, a floc diameter, a floc number continuously calculated in the fourth step, and their maximum values or A method for testing the agglutination of a suspension and a method for determining an amount of an aggregating agent to be injected, comprising: a step of judging the quality of the agglutination reaction based on a minimum value and a fifth step of determining an optimal amount of an aggregating agent to be injected.

【0006】撹拌機および光源部と受光部とから成る透
過光強度測定装置とを具備する凝集反応槽中において、
所定の撹拌速度で撹拌し凝集反応を進行させると、凝集
の進行にともない透過光強度(または電圧)の連続的な
変化が起こる。この透過光強度は次式にしたがって変化
する。
In an agglutination reaction tank provided with a stirrer and a transmitted light intensity measuring device comprising a light source unit and a light receiving unit,
When the agglutination reaction proceeds with stirring at a predetermined stirring speed, a continuous change in transmitted light intensity (or voltage) occurs as the agglutination proceeds. This transmitted light intensity changes according to the following equation.

【0007】[0007]

【数1】 I=Iexp(−KNπr) ・・・(1) I ;透過光強度 I;光源強度 K ;定数 N ;粒子数 r ;粒子半径 すなわち、凝集反応の進行にともない透過光強度が増大
することになる。したがって、透過光強度は凝集の良否
および凝集剤注入量の適否を反映することになり、透過
光強度変化に基づいて最適凝集剤注入量を決定すること
が可能となる。本発明の懸濁液の凝集試験方法および凝
集剤注入量決定方法は、一本の凝集反応装置の延長上に
設置した1組または複数の透過光強度測定装置により連
続的に測定された透過光強度変化から、短時間に、しか
も労力と経験を必要とせずに自動的に最適凝集剤注入量
を決定する方法を提供する作用を持つとともに、凝集速
度、フロック径、フロック数を計測・算出する作用を持
つ。
I = I 0 exp (−KNπr 2 ) (1) I: transmitted light intensity I 0 ; light source intensity K: constant N: number of particles r: particle radius, ie, transmission as the agglutination reaction proceeds The light intensity will increase. Therefore, the transmitted light intensity reflects the quality of the aggregation and the suitability of the coagulant injection amount, and the optimum coagulant injection amount can be determined based on the transmitted light intensity change. The agglutination test method and the method for determining the amount of coagulant injection of the suspension of the present invention are based on the method of transmitting transmitted light continuously measured by one or more transmitted light intensity measuring devices installed on an extension of one agglutination reaction device. It has the function of automatically determining the optimal coagulant injection amount in a short time and without the need for labor and experience from the change in strength, and measures and calculates the coagulation speed, floc diameter and floc number. Has an action.

【0008】[0008]

【発明の実施の形態】次に本発明について添付図面を参
照しつつ具体的に説明するが、本発明はこれら図面およ
び実施例に限定されるものではない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, the present invention will be described in detail with reference to the accompanying drawings, but the present invention is not limited to these drawings and embodiments.

【0009】図1は、本発明の最適凝集剤注入量決定方
法の装置概要図である。
FIG. 1 is a schematic diagram of an apparatus for determining the optimum coagulant injection amount according to the present invention.

【0010】図2−aは、混和液作成装置において濃度
の異なる混和液が一定時間間隔で連続的に作成される様
子を示しており、図2−bは、一本の凝集反応管に、濃
度の異なる混和液の所定量が一定流速で順次連続的に送
水され、混合・撹拌される過程で、凝集剤濃度に応じた
凝集反応が進行している様子を示す。
FIG. 2A shows a state in which mixed liquids having different concentrations are continuously prepared in the mixed liquid preparation apparatus at a constant time interval. FIG. This shows a state in which a predetermined amount of the mixed liquid having different concentrations is sequentially and continuously supplied at a constant flow rate, and aggregating reaction is progressing according to the aggregating agent concentration in the process of mixing and stirring.

【0011】図3は、図1の試験装置によって本発明の
実施例を実行したときの透過光強度の時間変化を示す図
である。
FIG. 3 is a diagram showing a change over time in transmitted light intensity when the embodiment of the present invention is executed by the test apparatus of FIG.

【0012】図4は、透過光強度測定装置を具備する凝
集反応槽中において、一定の凝集剤注入量で凝集反応を
進行させたときに得られる透過光強度(または電圧)経
時変化を数種の注入量について重ね書きしたものであ
る。
FIG. 4 shows several changes in transmitted light intensity (or voltage) over time obtained when the agglutination reaction is advanced at a fixed coagulant injection amount in an agglutination reaction tank equipped with a transmitted light intensity measuring device. Is overwritten with respect to the injection amount.

【0013】図5は、一本の凝集反応管に具備した複数
の透過光強度測定装置から得られる所定距離(時間)毎
の透過光強度変化に基づき、凝集剤注入量と透過光強度
変化との関係に作図しなおしたものである。
FIG. 5 shows the amount of coagulant injection and the change in transmitted light intensity based on the change in transmitted light intensity for each predetermined distance (time) obtained from a plurality of transmitted light intensity measuring devices provided in one agglutination reaction tube. It is redrawn to show the relationship.

【0014】図6は、連続的に測定された透過光強度変
化から求められた特定の凝集剤注入量における透過光強
度変化と、単位時間当たりの平均凝集反応速度分布、お
よびこれに基づき算出した透過光強度変化を示す。
FIG. 6 shows a change in transmitted light intensity at a specific coagulant injection amount determined from a continuously measured change in transmitted light intensity, an average agglutination reaction rate distribution per unit time, and a calculation based on this. 5 shows a change in transmitted light intensity.

【0015】図7は、凝集剤濃度変化装置により連続的
に凝集剤濃度を変化させた混和液を凝集反応装置に送水
し、これを1組の透過光強度測定装置を具備する凝集反
応槽によって本発明の実施例を実行したときの透過光強
度および凝集剤濃度の時間変化を示す。
FIG. 7 shows a mixed solution in which the concentration of the coagulant is continuously changed by the coagulant concentration changing device, which is fed to the coagulation reaction device, and is fed to the coagulation reaction tank having a set of transmitted light intensity measuring devices. 5 shows the temporal changes in transmitted light intensity and flocculant concentration when an embodiment of the present invention is performed.

【0016】まず、図1の測定装置について説明する。
装置は基本的には、 (a)懸濁液と凝集剤との混和液を連続的に作成し送水
する複数の混和液作成部分 (b)1組または複数の透過光強度測定装置を具備した
凝集反応装置部分 (c)制御・解析部分の3部分から成る。
First, the measuring device shown in FIG. 1 will be described.
The apparatus basically includes (a) a plurality of mixed liquid preparation portions for continuously preparing and sending a mixed liquid of a suspension and a flocculant, and (b) one or more transmitted light intensity measuring devices. Agglutination reaction device part (c) Consisting of three parts: control and analysis part.

【0017】混和液作成部分では、開閉弁(2)と第1
の水位計(3)を介して所定量の懸濁液が水槽(A)に
導入され、さらに、開閉弁(4)を介して所定量の凝集
剤が水槽(A)に導入され撹拌子(5)によって急速撹
拌される。一定時間後に開閉弁(7)を開いて定量ポン
プ(9)により凝集反応装置に送水される。
In the mixture preparation section, the on-off valve (2) and the first
A predetermined amount of the suspension is introduced into the water tank (A) through the water level meter (3), and a predetermined amount of the coagulant is introduced into the water tank (A) through the on-off valve (4). Rapid stirring by 5). After a certain time, the on-off valve (7) is opened, and water is sent to the agglutination reactor by the metering pump (9).

【0018】水槽(A)の水位が第2の水位計(6)に
達するまでの間に水槽(B)に同様のプロセスで給水、
凝集剤注入、撹拌を行ない、凝集剤濃度の異なる混和液
を作成して次の送水の準備を完了する。水槽(A)の水
位が第2の水位計(6)に達した段階で開閉弁(18お
よび7)を開閉して水槽(B)の混和水の送水を開始す
る。この時点で、開閉弁(8)を開いて水槽(A)の水
を排水し、試水で水槽内を洗浄後、再び水槽(A)への
導水、凝集剤注入、撹拌を行ない、次の送水の準備をす
る。
Water is supplied to the water tank (B) by the same process until the water level in the water tank (A) reaches the second water level gauge (6).
The coagulant is injected and stirred to prepare mixed liquids having different coagulant concentrations, and preparation for the next water supply is completed. When the water level in the water tank (A) reaches the second water level gauge (6), the on-off valves (18 and 7) are opened and closed to start feeding the mixed water in the water tank (B). At this time, the on-off valve (8) is opened to drain the water in the water tank (A), and the inside of the water tank is washed with a test sample, and then water is again introduced into the water tank (A), a coagulant is injected, and stirring is performed. Prepare for water supply.

【0019】すなわち、凝集剤濃度を段階的に変化させ
た混和液を半連続的に各水槽で作成し、所定強度で所定
時間の撹拌後、その一定量を一定速度で連続的に凝集反
応装置に送水する装置である。
That is, an admixture in which the concentration of the coagulant is changed stepwise is semi-continuously prepared in each water tank, and after stirring for a predetermined time at a predetermined intensity, a predetermined amount thereof is continuously supplied at a constant speed to the coagulation reaction apparatus. It is a device to send water to.

【0020】なお、上記のような半連続的な混和液作成
方法ではなくて、図1の上部左側に示すような凝集剤濃
度変換装置により、濃度を連続的に変化させた凝集剤を
懸濁液に注入させ、濃度変化が連続的な混和液を作成す
ることも可能である。すなわち、所定量の蒸留水を満た
した希釈水槽(17)に、濃厚凝集剤溶液(16)を定
量ポンプ(14)により連続的に注入し、同時に、ポン
プ(9)により定量的に送水されている懸濁液(15)
に同一速度で注入する方式により、凝集剤濃度が連続的
に変化している混和液を作成することができる。ここ
で、定量ポンプ(14)の吸水送水速度を加減すること
により凝集剤濃度の変化速度を加減する。また、定量ポ
ンプ(14),(9)の凝集剤吸水送水速度および懸濁
液送水速度から、希釈液および混和液中の凝集剤濃度が
算出できる。
It is to be noted that the coagulant whose concentration is continuously changed is suspended by the coagulant concentration converter shown in the upper left part of FIG. It is also possible to inject the mixture into a liquid to create a mixture having a continuous concentration change. That is, the concentrated flocculant solution (16) is continuously injected into the dilution water tank (17) filled with a predetermined amount of distilled water by the quantitative pump (14), and is simultaneously quantitatively sent by the pump (9). Suspension (15)
In this manner, a mixture in which the concentration of the flocculant is continuously changed can be prepared by the method of injecting the mixture at the same speed. Here, the rate of change of the flocculant concentration is adjusted by adjusting the rate of water absorption and delivery of the metering pump (14). Further, the flocculant concentration in the diluent and the admixture can be calculated from the flocculant absorption water supply speed and the suspension water supply speed of the metering pumps (14) and (9).

【0021】なお、図示はしないが、半連続的混和液作
成方法と同じく(図1上部右側)、蒸留水水槽、水位
計、給排水開閉弁等をプロセス制御装置と連動させれ
ば、一連の凝集試験後おなじ希釈液および混和液作成プ
ロセスを反復させることができ、複数の凝集剤濃度変換
装置を用いればスムーズな操作を行ない得る。
Although not shown, as in the semi-continuous mixed liquid preparation method (upper right in FIG. 1), if a distilled water tank, a water level gauge, a water supply / drainage opening / closing valve, etc. are linked with a process control device, a series of coagulation can be achieved. After the test, the same diluent and admixture preparation process can be repeated, and smooth operation can be performed using a plurality of coagulant concentration converters.

【0022】なお、これらのプロセスは制御装置(1
2)によりコントロールされるが、このプロセスをスム
ーズに進行させるために、2個以上の混和液作成水槽、
または凝集剤濃度変換装置を用意することも可能であ
る。
These processes are performed by the control unit (1).
Controlled by 2), in order to make this process proceed smoothly, two or more mixed liquid preparation tanks,
Alternatively, a coagulant concentration converter can be prepared.

【0023】一方、凝集反応管部分は一本の透明な管で
あり、混和水が管内を一定の流速で流れる過程で混合・
撹拌され凝集反応が進行するが、混合・撹拌強度を加減
するため、および管長を短くするために、管内に迂流、
旋回流等をおこさせる隔壁を設けることもできる。管内
流速は所定のG値が得られるように設定する。また、凝
集反応管は所定の勾配および曲率に設定する。
On the other hand, the agglutination reaction tube portion is a single transparent tube, and the mixed water is mixed and mixed in the process of flowing at a constant flow rate in the tube.
The agglutination reaction proceeds while being stirred, but in order to adjust the mixing / stirring intensity and to shorten the length of the tube, a bypass flows into the tube,
A partition for causing a swirling flow or the like may be provided. The flow velocity in the pipe is set so as to obtain a predetermined G value. The agglutination reaction tube is set to a predetermined gradient and curvature.

【0024】さらに、この管の延長上に光源部(10)
と受光部(11)とから成る1組または複数の透過光強
度測定装置が所定間隔で設置される。凝集反応管内の流
速は一定であるので、ポンプから各透過光強度測定装置
までの距離を加減することにより混合・撹拌時間が設定
される。したがって、一つの透過光強度測定装置は、所
定の混合・撹拌時間における凝集剤注入濃度毎の透過光
強度変化を検出・測定することになる。なお、光源部と
受光部との間にレンズを設置し、粒子の粒径に応じた光
強度変化を拡大または縮小することも可能である。
Further, a light source section (10) is provided on the extension of the tube.
One or a plurality of transmitted light intensity measuring devices, each of which includes a light receiving unit (11), are installed at predetermined intervals. Since the flow rate in the agglutination reaction tube is constant, the mixing / stirring time is set by adjusting the distance from the pump to each transmitted light intensity measuring device. Therefore, one transmitted light intensity measuring device detects and measures a transmitted light intensity change for each coagulant injection concentration during a predetermined mixing / stirring time. In addition, it is also possible to arrange a lens between the light source unit and the light receiving unit to enlarge or reduce a change in light intensity according to the particle diameter of the particles.

【0025】演算装置(13)はリード線により受光部
(11)と接続されており、一連の凝集反応実験開始前
から終了時までの各透過光強度測定装置における透過光
量(I)または電圧(V)の時間変化が測定・記録さ
れ、データに基づき各凝集指標が計算される。
The arithmetic unit (13) is connected to the light receiving unit (11) by a lead wire, and transmits the light intensity (I) or voltage (I) in each transmitted light intensity measuring device from before the start to the end of a series of agglutination reaction experiments. The time change of V) is measured and recorded, and each aggregation index is calculated based on the data.

【0026】図2−aは、混和液作成装置において濃度
の異なる混和液が一定時間間隔で連続的に作成される様
子を示しており、図2−bは、一本の凝集反応管に濃度
の異なる混和液の所定量が一定流速で順次連続的に送水
され、混合・撹拌される過程で凝集剤濃度に応じた凝集
反応が進行している様子を示す。
FIG. 2A shows a state in which mixed liquids having different concentrations are continuously prepared at a fixed time interval in the mixed liquid preparation apparatus, and FIG. This shows a state in which a predetermined amount of a different mixed liquid is sequentially and continuously supplied at a constant flow rate, and a coagulation reaction according to a coagulant concentration is progressing in the process of mixing and stirring.

【0027】凝集反応装置には、一定の距離間隔で複数
の透過光強度測定装置(L,L・・・・L)が取
り付けられており、各点(時間;T,T・・T
における透過光量(I)または電圧(V)の時間変化が
測定・記録される。
A plurality of transmitted light intensity measuring devices (L 1 , L 2 ... L n ) are attached to the agglutination reaction device at fixed intervals, and each point (time; T 1 , T 2) ..T n )
The time change of the transmitted light amount (I) or the voltage (V) is measured and recorded.

【0028】図3は、図1の測定装置によって本発明の
実施例を実行したとき、各測定点において測定された透
過光強度の時間変化を示す図である。撹拌・混合開始後
の時間;Tにおいては、時間経過が少ないため凝集反
応の進行が不完全であり、各凝集剤注入量における透過
光強度変化は相対的に小さいにしてもV字形変化を取
り、最適注入量近傍において最大値を取る。凝集反応時
間の長いTにおいてはさらに深いV字形変化を取り、
ここでも最適注入量近傍において最大値を取る。
FIG. 3 is a diagram showing the change over time of the transmitted light intensity measured at each measurement point when the embodiment of the present invention is executed by the measuring apparatus of FIG. Stirring and mixing after the start time; in T 1, is incomplete the progress of the agglutination reaction for a small time, a V-shaped change in the transmitted light intensity changes relatively small in each coagulant injection amount And take the maximum value near the optimal injection volume. Take deeper V-shaped change in the long T 2 of the agglutination reaction time,
Here, the maximum value is obtained near the optimum injection amount.

【0029】図4は、透過光強度測定装置を具備する凝
集反応槽中において、一定の凝集剤注入量(D,D
・・・・D)で凝集反応を進行させたときに得られる
透過光強度(または電圧)経時変化を数種の注入量につ
いて重ね書きしたものである。凝集剤注入量が最適値に
接近するに連れ、凝集反応速度が増大しフロック径(振
幅)も増大するが、過剰注入になると速度およびフロッ
ク径は減少するという経過を辿る。前掲の図3は、図4
に示す時間;T,Tでの各凝集剤注入量毎の透過光
強度(または電圧)変化に相当するものである。
FIG. 4 shows a fixed coagulant injection amount (D 1 , D 2) in a coagulation reaction tank equipped with a transmitted light intensity measuring device.
... Dn) are obtained by overwriting changes in transmitted light intensity (or voltage) over time obtained when the agglutination reaction is advanced in D n ) for several injection amounts. As the coagulant injection amount approaches the optimum value, the coagulation reaction speed increases and the floc diameter (amplitude) also increases, but if the injection is excessive, the speed and the floc diameter decrease. FIG. 3 shown in FIG.
The time corresponds to the change in transmitted light intensity (or voltage) for each coagulant injection amount at T 1 and T 2 .

【0030】図5は、図1の測定装置によって本発明の
実施例を実行したとき、複数の透過光強度測定装置から
得られる所定時間(T,T・・T)毎の透過光強
度変化に基づき、凝集剤注入量と透過光強度変化との関
係に作図しなおしたものである。凝集反応時間に応じた
V字形の透過光強度変化が得られるが、いずれの時間
(T,T・・T)においても平均透過光強度およ
び振幅は最適注入量(De)近傍において最大値を取
る。すなわち、V字形変化の谷に相当する部分で、各反
応時間での最良のフロック形成がなされていることにな
る。したがって、複数の透過光強度測定装置により得ら
れる透過光強度変化から、透過光強度変化から、透過光
強度および振幅が最大値となる注入量を読み取れば、そ
れが最適注入量に相当することになる。
FIG. 5 shows transmitted light at predetermined time intervals (T 1 , T 2 ... T n ) obtained from a plurality of transmitted light intensity measuring devices when the embodiment of the present invention is executed by the measuring device of FIG. Based on the intensity change, the relationship between the coagulant injection amount and the transmitted light intensity change is plotted again. Although a V-shaped transmitted light intensity change according to the agglutination reaction time is obtained, the average transmitted light intensity and amplitude are maximum near the optimum injection amount (De) at any time (T 1 , T 2 ... T n ). Take the value. That is, the best floc formation at each reaction time is performed in the portion corresponding to the valley of the V-shaped change. Therefore, from the transmitted light intensity change obtained by a plurality of transmitted light intensity measuring devices, from the transmitted light intensity change, reading the injection amount at which the transmitted light intensity and the amplitude are maximum values, it is equivalent to the optimal injection amount. Become.

【0031】一方、複数の透過光強度測定装置により得
られる透過光強度変化に基づき、各凝集剤注入量毎の時
間;T,T・・Tでの計測結果を繋ぎ合わせれ
ば、図4に示すと同様の各凝集剤注入量毎の透過光強度
(または電圧)の時間変化が得られる。また、所定の凝
集剤注入量における凝集速度分布および所定時間後の平
均透過光強度、振幅が求まれば、その注入量におけるフ
ロック径、数が計算できる。
On the other hand, based on the transmitted light intensity variations obtained by the plurality of transmission light intensity measuring device, the coagulant injection amount per time;, combined together the measurement results at T 1, T 2 ·· T n , FIG. As shown in FIG. 4, a time-dependent change in transmitted light intensity (or voltage) for each coagulant injection amount can be obtained. Further, if the aggregation speed distribution and the average transmitted light intensity and amplitude after a predetermined time are obtained for a predetermined coagulant injection amount, the floc diameter and the number at the injection amount can be calculated.

【0032】図6は、複数の透過光強度測定装置により
測定された連続的透過光強度変化に基づき、上記の方法
で求めた特定の凝集剤注入量における透過光強度の時間
変化(図6−a)と、これに基づく単位時間当たりの平
均凝集反応速度分布(図6−b)、およびこれらに基づ
き算出・作図した透過光強度の時間変化(図6−c)を
示す図である。すなわち、各凝集剤注入量毎の時間;T
,T・・・・Tの計測結果を繋ぎ合わせることに
より得られる所定の凝集剤注入量における凝集速度分布
等に基づき、所定時間後の平均透過光強度、振幅を算出
することが可能となる。したがって特願平1−1124
64号の方法により、その注入量におけるフロック径、
数が計算できることになる。
FIG. 6 is a graph showing the time change of the transmitted light intensity at the specific coagulant injection amount obtained by the above method based on the continuous transmitted light intensity change measured by a plurality of transmitted light intensity measuring devices (FIG. 6). FIG. 6A is a diagram showing an average agglutination reaction rate distribution per unit time based on the graph (FIG. 6B), and a time change of transmitted light intensity calculated and plotted based on the graph (FIG. 6C). That is, the time for each coagulant injection amount; T
It is possible to calculate the average transmitted light intensity and amplitude after a predetermined time based on a coagulation velocity distribution at a predetermined coagulant injection amount obtained by joining the measurement results of 1 , T 2 ... T n. Becomes Therefore, Japanese Patent Application No. 1-1124
According to the method of No. 64, the floc diameter at the injection amount,
The numbers can be calculated.

【0033】図7は、凝集剤濃度変化装置により連続的
に凝集剤濃度を変化させた混和液を凝集反応装置に送水
し、これを1組の透過光強度測定装置を具備する凝集反
応槽によって本発明の実施例を実行したときの透過光強
度および凝集剤濃度の時間変化を示す。この結果は、図
3と基本的には同じものである。しかしながら、図7−
bに示されるように凝集剤濃度が連続的に変化している
ので、透過光強度の時間変化はよりスムーズなV字形変
化を取り、最適注入量近傍において最大値を取る。
FIG. 7 shows that the mixed solution having the coagulant concentration changed continuously by the coagulant concentration changing device is supplied to the coagulation reaction device, and the water is supplied to the coagulation reaction tank equipped with a set of transmitted light intensity measuring devices. 5 shows the temporal changes in transmitted light intensity and flocculant concentration when an embodiment of the present invention is performed. This result is basically the same as FIG. However, FIG.
Since the concentration of the flocculant continuously changes as shown in FIG. 2B, the time change of the transmitted light intensity takes a smoother V-shaped change, and takes the maximum value near the optimum injection amount.

【0033】[0033]

【発明の効果】本発明の懸濁液の凝集試験方法および凝
集剤注入量決定方法は上述のような作用を持っているの
で、 (a)従前の方法より短時間で凝集反応の良否の判定と
最適凝集剤注入量の決定が可能となる効果を有し、 (b)原水の水質変動に容易に対応し得る効果を有し、 (c)本発明において用いている凝集反応の指標は、自
動的な計測・計算・出力が可能であり、したがって、凝
集反応試験および最適凝集剤注入量の決定の自動化が可
能となる効果を有し、 (d)多数の指標に基づく試験法であることから、判定
および決定精度が向上する効果を有する。
The method of the present invention for testing the agglutination of a suspension and the method for determining the amount of a coagulant to be injected have the above-mentioned effects. (A) Judgment of the agglutination reaction in a shorter time than the conventional method. And (b) have the effect of easily coping with fluctuations in the quality of raw water, and (c) the index of the agglutination reaction used in the present invention is as follows: Automatic measurement, calculation, and output are possible, and thus have the effect of automating the agglutination reaction test and determination of the optimal coagulant injection amount. (D) The test method is based on a number of indices Therefore, there is an effect that the accuracy of determination and determination is improved.

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

【図1】 本発明の最適凝集剤注入量決定方法を実施す
るための試験装置を示す断面図である。
FIG. 1 is a cross-sectional view showing a test apparatus for carrying out a method for determining an optimum coagulant injection amount according to the present invention.

【図2】 aは混和液作成装置において濃度の異なる混
和液が作成される様子を示す図であり、bは濃度の異な
る混和液の所定量が一定流速で一本の凝集反応管に順次
連続的に送水されている様子を示す図である。
FIG. 2A is a view showing a state in which mixed liquids having different concentrations are prepared in the mixed liquid preparation apparatus, and FIG. 2B is a diagram in which a predetermined amount of the mixed liquids having different concentrations is successively transferred to one coagulation reaction tube at a constant flow rate. It is a figure which shows a mode that the water is sent temporarily.

【図3】 図1の試験装置によって本発明の実施例を実
行したときの透過光強度の時間変化を示す図である。
FIG. 3 is a diagram showing a change over time in transmitted light intensity when the embodiment of the present invention is executed by the test apparatus of FIG. 1;

【図4】 透過光強度測定装置を具備する凝集反応槽中
において、一定の凝集剤注入量で凝集反応を進行させた
ときに得られる透過光強度(または電圧)経時変化を数
種の注入量について重ね書きした図である。
FIG. 4 shows the change over time in transmitted light intensity (or voltage) obtained when an agglutination reaction is allowed to proceed with a fixed amount of aggregating agent in an agglutination reaction tank equipped with a transmitted light intensity measuring device. FIG.

【図5】 一本の凝集反応管に具備した複数の透過光強
度測定装置から得られる所定距離(時間)毎の透過光強
度変化に基づき、凝集剤注入量と透過光強度変化との関
係に作図しなおした図である。
FIG. 5 shows the relationship between the amount of coagulant injection and the change in transmitted light intensity based on the change in transmitted light intensity for each predetermined distance (time) obtained from a plurality of transmitted light intensity measurement devices provided in a single agglutination reaction tube. It is a diagram redrawn.

【図6】 連続的に測定された透過光強度変化から求め
られた特定の凝集剤注入量における透過光強度変化と、
単位時間当たりの平均凝集反応速度分布、およびこれに
基づき算出した透過光強度変化を示す図である。
FIG. 6 shows a change in transmitted light intensity at a specific coagulant injection amount obtained from a continuously measured change in transmitted light intensity,
It is a figure which shows the average agglutination-reaction rate distribution per unit time, and the transmitted light intensity change calculated based on this.

【図7】 凝集剤濃度変化装置により連続的に凝集剤濃
度を変化させた混和液を凝集反応装置に送水し、これを
1組の透過光強度測定装置を具備する凝集反応槽によっ
て本発明の実施例を実行したときの透過光強度および凝
集剤濃度の時間変化を示す図である。
FIG. 7 is a flow chart showing an embodiment of the present invention, in which an admixture having a coagulant concentration changed continuously by a coagulant concentration changing device is fed to an agglutination reaction device, and is fed to an agglutination reaction tank equipped with a set of transmitted light intensity measuring devices. It is a figure which shows the time change of the transmitted light intensity and the coagulant density | concentration when an Example is performed.

【符号の説明】[Explanation of symbols]

1 凝集剤貯留容器 2,4,7,8,18 開閉弁 3 第1の水位計 5 撹拌子 6 第2の水位計 9 定量ポンプ 10 光源部 11 受光部 12 制御装置 13 演算装置 14 定量ポンプ 15 懸濁液(原水) 16 濃厚凝集剤溶液 17 希釈水槽 DESCRIPTION OF SYMBOLS 1 Flocculant storage container 2,4,7,8,18 On-off valve 3 First water level gauge 5 Stirrer 6 Second water level meter 9 Metering pump 10 Light source unit 11 Light receiving unit 12 Control device 13 Arithmetic device 14 Metering pump 15 Suspension (raw water) 16 Concentrated flocculant solution 17 Dilution water tank

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 (a)濃度の異なる凝集剤と懸濁液との
混和液を連続的に作成するか、または凝集剤濃度変化装
置により連続的に濃度を変化させた凝集剤を懸濁液に注
入する第1の段階と (b)光源部と受光部とから成る1組または複数の透過
光強度測定装置とを具備する一本の凝集反応装置中に、
凝集剤濃度の異なる所定量の混和液を所定の速度で連続
的にポンプ送水し、混合・撹拌し、凝集反応を進行させ
る第2の段階と (c)第2の段階の過程で、連続的に透過光強度を測定
する第3の段階と (d)第3の段階で、連続的に測定された透過光強度変
化から、平均透過光強度およびその振幅を求め、これよ
り凝集・フロック形成速度(以下凝集速度と記す)、フ
ロック径、フロック数を算出する第4の段階と (e)第4の段階で連続的に算出された凝集速度、フロ
ック径、フロック数、およびそれらの最大値または最小
値に基づき、凝集反応の良否の判定と最適凝集剤注入量
を決定する第5の段階とを具備することを特徴とする懸
濁液の凝集試験方法および凝集剤注入量決定方法。
1. A (a) to create a liquid mixture of different flocculants and suspensions of concentration continuous manner, or flocculant concentration change instrumentation
The flocculant, whose concentration has been continuously changed by
During the first stage and (b) a light source unit and the light receiving portion and a pair or more of the transmitted light intensity measurement device and agglutination reactor one having a consists of entry,
A second step of continuously pumping a predetermined amount of the mixed liquid having a different coagulant concentration at a predetermined speed, mixing and stirring, and allowing the coagulation reaction to proceed; and (c) a continuous step in the second step. And (d) in the third step, the average transmitted light intensity and its amplitude are obtained from the continuously measured changes in transmitted light intensity, and the aggregation / floc formation speed is calculated from this. (Hereinafter referred to as a flocculation rate), a floc diameter, a floc number and a fourth step of calculating the floc number; and (e) a flocculation rate, a floc diameter, a floc number continuously calculated in the fourth step, and their maximum values or A method for testing the agglutination of a suspension and a method for determining an amount of an aggregating agent to be injected, comprising: judging the quality of the agglutination reaction based on the minimum value and a fifth step of determining an optimal amount of an aggregating agent to be injected.
【請求項2】 第の段階において、光源部と受光部と
の間にレンズを設置し、凝集反応装置内を流動する粒子
群を拡大または縮小することにより、粒子の粒径に応じ
た光強度変化を拡大または縮小して凝集反応の良否の判
定と最適凝集剤注入量を決定することを特徴とする請求
項1に記載の懸濁液の凝集試験方法および凝集剤注入量
決定方法。
2. In the third stage, a lens is provided between the light source unit and the light receiving unit, and a group of particles flowing in the agglutination reaction device is enlarged or reduced, so that light corresponding to the particle size of the particles is obtained. The method for testing the agglutination of a suspension and the method for determining the amount of aggregating agent to be injected according to claim 1, wherein the determination of the quality of the agglutination reaction and the optimal amount of the aggregating agent to be injected are determined by expanding or reducing the intensity change.
【請求項3】 第3の段階において、一本の凝集反応装
置の延長上に所定の間隔で設置された1組または複数の
透過光強度測定装置により連続的に測定された透過光強
度変化から、平均透過光強度および振幅の最大値を読み
取り、それに基づき、凝集反応の良否の判定と最適凝集
剤注入量を決定することを特徴とする請求項1に記載の
懸濁液の凝集試験方法および凝集剤注入量決定方法。
3. In the third stage, a change in transmitted light intensity continuously measured by one or a plurality of transmitted light intensity measurement devices installed at predetermined intervals on an extension of one agglutination reaction device is obtained. The method of claim 1, wherein the maximum value of the average transmitted light intensity and the amplitude is read, and based on the read value, the quality of the agglutination reaction is determined and the optimal coagulant injection amount is determined. Coagulant injection amount determination method.
【請求項4】 第3の段階において、複数の透過光強度
測定装置より得られる連続的な透過光強度変化に基づ
き、各凝集剤注入量毎の透過光強度(または電圧)の時
間変化を求め、また、所定の凝集剤注入量における凝集
速度分布および所定時間後の平均透過光強度、振幅を求
めて、その注入量におけるフロック径、フロック数を計
算し、それらに基づき、凝集反応の良否の判定と最適凝
集剤注入量を決定することを特徴とする請求項1に記載
の懸濁液の凝集試験方法および凝集剤注入量決定方法。
4. In a third stage, a time change in transmitted light intensity (or voltage) for each coagulant injection amount is determined based on continuous transmitted light intensity changes obtained from a plurality of transmitted light intensity measuring devices. Further, the aggregation speed distribution at a predetermined coagulant injection amount and the average transmitted light intensity after a predetermined time, the amplitude are obtained, the floc diameter at the injection amount, the floc number is calculated, and based on them, the quality of the coagulation reaction is determined. The method of claim 1, wherein the determination and the optimal coagulant injection amount are determined.
JP26679691A 1991-07-12 1991-07-12 Suspension coagulation test method and coagulant injection amount determination method Expired - Fee Related JP3300764B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26679691A JP3300764B2 (en) 1991-07-12 1991-07-12 Suspension coagulation test method and coagulant injection amount determination method

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JP4950908B2 (en) * 2007-05-18 2012-06-13 メタウォーター株式会社 Method and apparatus for determining coagulant injection rate in water treatment method for coagulation sedimentation treatment
JP5326055B2 (en) * 2011-07-12 2013-10-30 積水アクアシステム株式会社 Precipitation evaluation device and optimum addition amount calculation device
CN103708590A (en) * 2012-09-29 2014-04-09 埃科莱布美国股份有限公司 Water treatment dosing optimizing system, water treatment system, and method of water treatment dosing optimizing system
JP6281534B2 (en) * 2015-07-22 2018-02-21 栗田工業株式会社 Aggregation monitoring apparatus, aggregation monitoring method, and aggregation system
JP7169111B2 (en) * 2018-08-02 2022-11-10 オルガノ株式会社 Aggregation condition evaluation device, aggregation condition evaluation method, aggregation treatment system, and aggregation treatment method

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