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JPH08126803A - Control of sedimentation tank - Google Patents

Control of sedimentation tank

Info

Publication number
JPH08126803A
JPH08126803A JP26671394A JP26671394A JPH08126803A JP H08126803 A JPH08126803 A JP H08126803A JP 26671394 A JP26671394 A JP 26671394A JP 26671394 A JP26671394 A JP 26671394A JP H08126803 A JPH08126803 A JP H08126803A
Authority
JP
Japan
Prior art keywords
concentration
precipitate
settling tank
sedimentation tank
supernatant water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP26671394A
Other languages
Japanese (ja)
Inventor
Yukihiro Tsuge
幸宏 柘植
Masayuki Makita
正行 槙田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works 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 Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP26671394A priority Critical patent/JPH08126803A/en
Publication of JPH08126803A publication Critical patent/JPH08126803A/en
Pending legal-status Critical Current

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Investigating Or Analysing Materials By Optical Means (AREA)

Abstract

PURPOSE: To provide a control method of a sedimentation tank enabling to keep a level of a separation boundary constant by easily detecting concentration of treated waste water, keeping concentration of impurities in the treated waste water constant, detecting the separation boundary formed between the precipitate and the supernatant water by a sensor and discharging the precipitate from the bottom surface. CONSTITUTION: In this sedimentation tank for separating the precipitate 5 and the supernatant water 14 from the process waste water, the control method of the sedimentation tank provided with a concentration sensor 4 under a liquid surface comprises detecting the concentration of impurities floating in the supernatant water by a concentration sensor 4 and informing abnormality of the concentration of the treated waste water discharged from the sedimentation tank.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、積層板やプリント配線
板を製造する工程で発生した工程廃液を沈殿物と上澄水
とに分離する沈殿槽に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a settling tank for separating a process waste liquid generated in a process of manufacturing a laminated board or a printed wiring board into a precipitate and a supernatant water.

【0002】[0002]

【従来の技術】積層板やプリント配線板を製造するに
は、様々な工程で多量の水やアルカリ性溶液や酸性溶液
が使用される。一度使用した上記の水やアルカリ性溶液
や酸性溶液等には、アルミニウム、銅、半田等が含ま
れ、工程廃液として扱われる。この工程廃液は、上記の
ような不純物が含まれるためそのまま排水として放流す
ることはできないので、液体部分と固体部分とに分離す
る必要があった。
2. Description of the Related Art A large amount of water, an alkaline solution or an acidic solution is used in various steps for manufacturing a laminated board or a printed wiring board. The above-mentioned water, alkaline solution, acidic solution, etc. used once contains aluminum, copper, solder, etc. and is treated as a process waste liquid. Since this process waste liquid cannot be discharged as waste water as it is because it contains the above impurities, it has been necessary to separate it into a liquid portion and a solid portion.

【0003】上記分離方法としては、図3に示すような
沈殿槽がある。この沈殿槽13aは、槽の上部取込口1
0から工程廃液を沈殿槽13aに取り込み、攪拌機7a
で攪拌しながら凝集剤を注入し、混合することにより、
液中に存在する不純物を凝集する。攪拌翼7で攪拌され
た廃液中の不純物は凝集が促進されて沈殿物5となり、
沈殿分離した沈殿物5は、仕切り板15に囲まれて凝集
するため沈殿槽13aの下層に蓄積され、上澄水14と
の分離界面6を形成する。
As a separation method, there is a precipitation tank as shown in FIG. This settling tank 13a has an upper intake port 1 of the tank.
The process waste liquid is taken into the settling tank 13a from 0, and the agitator 7a
By injecting the coagulant while stirring and mixing,
Impurities existing in the liquid are aggregated. Impurities in the waste liquid stirred by the stirring blade 7 are promoted to form a precipitate 5,
The sediment 5 separated by sedimentation is accumulated in the lower part of the sedimentation tank 13a because it is surrounded by the partition plate 15 and aggregates to form a separation interface 6 with the supernatant water 14.

【0004】さらに、工程廃液を取り込んでいくと上澄
水14の液面12が上昇し、上澄水14が処理排水とし
て処理水流出部11より排出される。このとき、上澄水
14の液面12が上昇するのと同様に、分離界面6も上
昇してゆく。この分離界面6が上昇していく速度は、工
程廃液を取り込む量で略確定されるので、定期的に沈殿
物5を槽底からポンプ8により貯槽9へ排出している。
Further, as the process waste liquid is taken in, the liquid level 12 of the supernatant water 14 rises, and the supernatant water 14 is discharged from the treated water outlet 11 as treated waste water. At this time, the separation interface 6 also rises in the same manner as the liquid surface 12 of the supernatant water 14 rises. Since the speed at which the separation interface 6 rises is substantially determined by the amount of the process waste liquid taken in, the precipitate 5 is periodically discharged from the bottom of the tank to the storage tank 9 by the pump 8.

【0005】しかしながら、工程廃液の不純物濃度が高
かったり、凝集剤による凝集が悪かったりすると、沈殿
物5が凝集して沈殿槽の下層に蓄積せず、上澄水14中
に不純物が多量に含んだ状態になり、不純物を多量に含
んだ処理排水として処理水流出部11より排出されると
いう問題がある。
However, if the concentration of impurities in the process effluent is high or if the coagulation by the coagulant is poor, the precipitate 5 does not accumulate and does not accumulate in the lower layer of the sedimentation tank, and the supernatant water 14 contains a large amount of impurities. There is a problem that the treated water is discharged from the treated water outflow portion 11 as treated waste water containing a large amount of impurities.

【0006】[0006]

【発明が解決しようとする課題】本発明は上記の事情に
鑑みてなされたものであり、その目的とするところは、
処理排水の濃度を容易に検出して処理排水の不純物濃度
を一定に保ち、沈殿物と上澄水とで形成される分離界面
をセンサにより検出して沈殿物を底面より排出すること
により、分離界面のレベルを一定に保つことができる沈
殿槽の制御方法を提供することにある。
The present invention has been made in view of the above circumstances, and its object is to:
The concentration of the treated effluent can be easily detected to keep the impurity concentration of the treated effluent constant, and the separation interface formed by the precipitate and the supernatant water is detected by the sensor, and the precipitate is discharged from the bottom surface to separate the separation interface. The object of the present invention is to provide a method for controlling a settling tank, which can keep the level of the constant.

【0007】[0007]

【課題を解決するための手段】本発明の請求項1に係る
沈殿槽の制御方法は、工程廃液を沈殿物と上澄水とに分
離する沈殿槽において、液面下に濃度センサを備え、こ
の濃度センサにより上澄水内に浮遊している不純物の濃
度を検出し、上記沈殿槽から排出される処理排水の濃度
異常を知らせることを特徴とする。
According to a first aspect of the present invention, there is provided a method for controlling a settling tank, wherein a settling tank for separating a process waste liquid into a precipitate and a supernatant water is provided with a concentration sensor below the liquid surface. It is characterized in that the concentration sensor detects the concentration of impurities floating in the supernatant water and notifies the concentration abnormality of the treated wastewater discharged from the settling tank.

【0008】また、本発明の請求項2に係る沈殿槽の制
御方法は、上記沈殿槽の液面下に光学式センサを備え、
この光学式センサにより沈殿物と上澄水との分離界面を
検出し、上限を検出すると沈殿物を底面より排出し、下
限を検出すると排出を停止することを特徴とする。
The method of controlling a settling tank according to claim 2 of the present invention comprises an optical sensor below the liquid surface of the settling tank,
The optical sensor detects the separation interface between the precipitate and the supernatant water, and when the upper limit is detected, the precipitate is discharged from the bottom surface, and when the lower limit is detected, the discharge is stopped.

【0009】[0009]

【作用】本発明に係る沈殿槽の制御方法は、工程廃液を
沈殿物と上澄水とに分離する沈殿槽において、液面下に
濃度センサを備え、この濃度センサにより上澄水内に浮
遊している不純物の濃度を検出するので、上記沈殿槽か
ら排出される処理排水の濃度異常を警報として発令し、
不純物が含まれた処理排水の流出を知らせることができ
る。
The method for controlling a settling tank according to the present invention is a settling tank for separating a process waste liquid into a precipitate and supernatant water, and a concentration sensor is provided below the liquid surface, and the concentration sensor floats in the supernatant water. Since it detects the concentration of impurities present, it issues an alarm as a concentration abnormality of the treated wastewater discharged from the settling tank,
The outflow of treated wastewater containing impurities can be notified.

【0010】また、上記沈殿槽の液面下に光学式センサ
を備え、この光学式センサにより沈殿物と上澄水との分
離界面の上限と下限を検出して、沈殿物を槽底より排出
するので、沈殿槽の下層に蓄積した沈殿物の量を一定に
保ち、高濃度の沈殿物を貯槽へ排出することができる。
Further, an optical sensor is provided below the liquid surface of the settling tank, and the upper and lower limits of the separation interface between the precipitate and the supernatant water are detected by this optical sensor, and the precipitate is discharged from the bottom of the tank. Therefore, the amount of the sediment accumulated in the lower layer of the sedimentation tank can be kept constant, and the highly concentrated sediment can be discharged to the storage tank.

【0011】以下、本発明を添付した図面に沿って詳細
に説明する。
Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.

【0012】[0012]

【実施例】図1は本発明の沈殿槽の制御方法を使用した
一実施例に係る沈殿槽の断面図である。図2は本発明の
沈殿槽の制御方法に使用される濃度センサの説明図であ
る。
FIG. 1 is a sectional view of a settling tank according to an embodiment using the method for controlling a settling tank according to the present invention. FIG. 2 is an explanatory diagram of a concentration sensor used in the method of controlling the settling tank of the present invention.

【0013】図1に示す如く、本発明に係る沈殿槽の制
御方法を使用した沈殿槽の一実施例は、沈殿槽13と、
この沈殿槽13の上部側面に形成された取込口10と、
攪拌機7aと、仕切り板15と、ポンプ8とから構成さ
れ、液面下に位置するように、濃度センサ4と、光学式
センサ3とが配置されている。
As shown in FIG. 1, an embodiment of a settling tank using the method for controlling a settling tank according to the present invention is as follows:
An intake port 10 formed on the upper side surface of the settling tank 13,
It is composed of an agitator 7a, a partition plate 15, and a pump 8, and a concentration sensor 4 and an optical sensor 3 are arranged so as to be located below the liquid surface.

【0014】上記攪拌機7aは、取り込んだ工程廃液を
攪拌するための攪拌翼7を備えている。また、濃度セン
サ4は投受光式のレーザーセンサが使用され、アンプ2
に接続されて制御装置へと信号が送られる。この濃度セ
ンサ4は、図2に示すように投光部4aと受光部4bと
アンプ2とから構成され、投光部4aより一定の光20
が受光部4bへと照射されるが、投光部4aと受光部4
bとの間に不純物21が存在すると遮光されるため、受
光部4bの受光量が変動し、この値をアンプ2により演
算し濃度を求めるものである。
The stirrer 7a is provided with a stirring blade 7 for stirring the taken-in process waste liquid. Further, as the concentration sensor 4, a light emitting and receiving type laser sensor is used, and the amplifier 2
Is connected to and a signal is sent to the control device. As shown in FIG. 2, the density sensor 4 is composed of a light projecting section 4a, a light receiving section 4b and an amplifier 2, and a constant light 20 is emitted from the light projecting section 4a.
Is emitted to the light receiving portion 4b, but the light emitting portion 4a and the light receiving portion 4b
When the impurity 21 exists between the light receiving element 4b and b, the light receiving amount of the light receiving portion 4b fluctuates, and this value is calculated by the amplifier 2 to obtain the density.

【0015】上記光学式センサ3は、分離界面6を検出
するもので、この分離界面6のレベルを制御するため
に、上限レベル6aと下限レベル6bに配置されてい
る。この光学式センサ3は特に限定されないが、反射式
の光学式センサが好ましく、さらに、容易にレベルが調
整が可能で、耐水性が良いファイバ式のものが好まし
い。
The optical sensor 3 detects the separation interface 6, and is arranged at the upper limit level 6a and the lower limit level 6b in order to control the level of the separation interface 6. The optical sensor 3 is not particularly limited, but a reflection type optical sensor is preferable, and a fiber type sensor whose level can be easily adjusted and which has good water resistance is preferable.

【0016】以下に、上記沈殿槽の使用例を図を参照し
説明する。まず、槽の上部取込口10から工程廃液を仕
切り板15の内側の沈殿槽13に取り込む。そして、攪
拌機7aで攪拌しながら凝集剤を注入し、攪拌すること
により、液中に存在する不純物を凝集する。攪拌翼7で
攪拌された廃液中の不純物は凝集が促進されて沈殿物5
となり下層に蓄積され、上澄水14との分離界面6を形
成する。
An example of using the above settling tank will be described below with reference to the drawings. First, the process waste liquid is taken into the settling tank 13 inside the partition plate 15 from the upper inlet 10 of the tank. Then, the aggregating agent is injected while stirring with the stirrer 7a, and by stirring, the impurities existing in the liquid are aggregated. Impurities in the waste liquid stirred by the stirring blade 7 are promoted to coagulate, and precipitates 5
Next, it accumulates in the lower layer and forms a separation interface 6 with the supernatant water 14.

【0017】上記上澄水14の液面12付近に設置され
た濃度センサ4は、上澄水14の液面12付近の不純物
濃度を測定し、アンプ2により測定した値を用いて濃度
を算出し、濃度が高ければ工程廃液の取り込みを停止し
て液面12が上昇するのを防ぎ、濃度異常の警報を発令
する。また、濃度が低ければ、さらに、工程廃液を取り
込み上澄水14の液面12が上昇させて、処理水流出部
11より処理排水として排出する。
The concentration sensor 4 installed near the liquid surface 12 of the supernatant water 14 measures the impurity concentration near the liquid surface 12 of the supernatant water 14 and calculates the concentration using the value measured by the amplifier 2. If the concentration is high, the intake of the process waste liquid is stopped to prevent the liquid surface 12 from rising, and an alarm of abnormal concentration is issued. Further, if the concentration is low, the process waste liquid is further taken in, the liquid surface 12 of the supernatant water 14 is raised, and is discharged from the treated water outflow portion 11 as treated waste water.

【0018】また、不純物の沈殿が進むにつれて、沈殿
物5の分離界面6が上昇する。この分離界面6のレベル
を光学式センサ3により検知し、上限レベル6aになる
と、光学式センサ3に接続されたアンプ1により沈殿槽
13の槽底に設置されたポンプ8を運転し、沈殿物5を
貯槽9へ排出する。
Further, as the precipitation of impurities progresses, the separation interface 6 of the precipitate 5 rises. The level of the separation interface 6 is detected by the optical sensor 3, and when the upper limit level 6a is reached, the amplifier 1 connected to the optical sensor 3 operates the pump 8 installed at the bottom of the settling tank 13 to settle the precipitate. 5 is discharged to the storage tank 9.

【0019】沈殿物5を貯槽9へ排出することにより分
離界面6のレベルが低下し、この分離界面6が下限レベ
ル6bより低下するとアンプ1によりポンプ8を停止し
て沈殿物の排出を止める。
By discharging the precipitate 5 to the storage tank 9, the level of the separation interface 6 decreases, and when the separation interface 6 becomes lower than the lower limit level 6b, the pump 8 is stopped by the amplifier 1 to stop the discharge of the precipitate.

【0020】このように、ポンプ8の運転停止を繰り返
すことにより、沈殿物5と上澄水14との分離界面6を
望ましいレベルに調整することができる。
As described above, the separation interface 6 between the precipitate 5 and the supernatant water 14 can be adjusted to a desired level by repeatedly stopping the operation of the pump 8.

【0021】[0021]

【発明の効果】以上、述べたように、本発明の沈殿槽の
制御方法によると、沈殿槽の液面下の上澄水の濃度を測
定することにより、処理排水の濃度を一定に保ち、不純
物が高濃度に含有する処理排水の流出を防ぐことができ
る。また、凝集した不純物の分離界面を検知し、この分
離界面のレベルを望ましい位置に制御できるので、凝集
分離を自動連続処理を行うことができる。
As described above, according to the method for controlling a settling tank of the present invention, by measuring the concentration of supernatant water below the liquid surface of the settling tank, the concentration of treated wastewater is kept constant and impurities It is possible to prevent the outflow of the treated wastewater containing a high concentration of. Moreover, since the separation interface of the aggregated impurities can be detected and the level of this separation interface can be controlled to a desired position, the aggregation separation can be automatically performed continuously.

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

【図1】本発明に係る一実施例の沈殿槽の断面図であ
る。
FIG. 1 is a sectional view of a settling tank according to an embodiment of the present invention.

【図2】本発明に使用される濃度センサを説明する説明
図である。
FIG. 2 is an explanatory diagram illustrating a concentration sensor used in the present invention.

【図3】従来の沈殿槽の断面図である。FIG. 3 is a sectional view of a conventional settling tank.

【符号の説明】[Explanation of symbols]

1 アンプ 2 アンプ 3 光学式センサ 4 濃度センサ 5 沈殿物 6 分離界面 7 攪拌翼 8 ポンプ 10 取込口 11 処理水流出部 12 液面 13 沈殿槽 14 上澄水 1 Amplifier 2 Amplifier 3 Optical Sensor 4 Concentration Sensor 5 Precipitate 6 Separation Interface 7 Stirring Blade 8 Pump 10 Intake Port 11 Treated Water Outflow Portion 12 Liquid Level 13 Precipitation Tank 14 Clear Water

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 工程廃液を沈殿物と上澄水とに分離する
沈殿槽において、液面下に濃度センサを備え、この濃度
センサにより上澄水内に浮遊している不純物の濃度を検
出し、上記沈殿槽から排出される処理排水の濃度異常を
知らせることを特徴とする沈殿槽の制御方法。
1. A settling tank for separating a process waste liquid into a precipitate and a supernatant water, a concentration sensor is provided below the liquid surface, and the concentration sensor detects the concentration of impurities floating in the supernatant water. A method for controlling a sedimentation tank, which comprises notifying an abnormal concentration of treated wastewater discharged from the sedimentation tank.
【請求項2】 上記沈殿槽の液面下に光学式センサを備
え、この光学式センサにより沈殿物と上澄水との分離界
面を検出し、上限を検出すると沈殿物を底面より排出
し、下限を検出すると排出を停止することを特徴とする
請求項1記載の沈殿槽の制御方法。
2. An optical sensor is provided below the liquid surface of the settling tank, the optical sensor detects the separating interface between the precipitate and the supernatant water, and when the upper limit is detected, the precipitate is discharged from the bottom surface, and the lower limit is set. The method for controlling a settling tank according to claim 1, wherein the discharging is stopped when the above is detected.
JP26671394A 1994-10-31 1994-10-31 Control of sedimentation tank Pending JPH08126803A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26671394A JPH08126803A (en) 1994-10-31 1994-10-31 Control of sedimentation tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26671394A JPH08126803A (en) 1994-10-31 1994-10-31 Control of sedimentation tank

Publications (1)

Publication Number Publication Date
JPH08126803A true JPH08126803A (en) 1996-05-21

Family

ID=17434652

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26671394A Pending JPH08126803A (en) 1994-10-31 1994-10-31 Control of sedimentation tank

Country Status (1)

Country Link
JP (1) JPH08126803A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001239297A (en) * 2000-03-02 2001-09-04 Chuyu Shoji Kk System for recovering/recycling cleaning water and its operating method
JP2019171308A (en) * 2018-03-29 2019-10-10 株式会社日立製作所 Turbid material separation unit, turbid material separation method, and turbid material separation system
CN114287317A (en) * 2021-12-26 2022-04-08 郭瑶 Environment-friendly blasting rivers utilize device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001239297A (en) * 2000-03-02 2001-09-04 Chuyu Shoji Kk System for recovering/recycling cleaning water and its operating method
JP2019171308A (en) * 2018-03-29 2019-10-10 株式会社日立製作所 Turbid material separation unit, turbid material separation method, and turbid material separation system
CN114287317A (en) * 2021-12-26 2022-04-08 郭瑶 Environment-friendly blasting rivers utilize device
CN114287317B (en) * 2021-12-26 2024-07-02 南京呗茵特互联网科技有限公司 Environment-friendly blasting water flow utilization device

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