JP2785856B2 - Apparatus and method for measuring turbidity of separated liquid in centrifugal dehydrator - Google Patents

Apparatus and method for measuring turbidity of separated liquid in centrifugal dehydrator

Info

Publication number
JP2785856B2
JP2785856B2 JP4239984A JP23998492A JP2785856B2 JP 2785856 B2 JP2785856 B2 JP 2785856B2 JP 4239984 A JP4239984 A JP 4239984A JP 23998492 A JP23998492 A JP 23998492A JP 2785856 B2 JP2785856 B2 JP 2785856B2
Authority
JP
Japan
Prior art keywords
separated liquid
liquid
separated
turbidity
bubbles
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
JP4239984A
Other languages
Japanese (ja)
Other versions
JPH0663451A (en
Inventor
良行 菅原
肇 田原
祐司 甲斐
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.)
NISHIHARA KANKYO EISEI KENKYUSHO KK
Original Assignee
NISHIHARA KANKYO EISEI KENKYUSHO KK
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 NISHIHARA KANKYO EISEI KENKYUSHO KK filed Critical NISHIHARA KANKYO EISEI KENKYUSHO KK
Priority to JP4239984A priority Critical patent/JP2785856B2/en
Publication of JPH0663451A publication Critical patent/JPH0663451A/en
Application granted granted Critical
Publication of JP2785856B2 publication Critical patent/JP2785856B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Centrifugal Separators (AREA)
  • Treatment Of Sludge (AREA)
  • Investigating Or Analysing Materials By Optical Means (AREA)

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、汚泥を固液分離して分
離液と脱水ケーキとに分ける遠心脱水機に関し、その分
離液の濁度を連続的に監視する装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a centrifugal dehydrator for separating sludge into solids and liquids and separating the sludge into a separated liquid and a dewatered cake, and relates to an apparatus for continuously monitoring the turbidity of the separated liquid.

【0002】[0002]

【從来の技術】遠心分離機の分離液には浮遊固定物質
(SS)が含まれるので、後処理のために、SSの濃度
すなわち濁度を測定する必要がある。
2. Description of the Related Art Since the separated liquid of a centrifuge contains suspended solids (SS), it is necessary to measure the concentration of SS, that is, turbidity, for post-treatment.

【0003】通常の光式又は超音波式の濁度計では、測
定液に泡が存在すると、光や音波の散乱により正確な測
定ができない。そこで、遠心脱水機の分離液中の泡の影
響を受けないように、分離液の測定試料を一定量採取
し、これを静置して濁度測定に供していた。また、従
来、遠心脱水機の分離液の濁度を連続的に測定する装置
はなかった。
[0003] In a normal optical or ultrasonic turbidity meter, if bubbles are present in the measurement liquid, accurate measurement cannot be performed due to scattering of light or sound waves. Therefore, a certain amount of a measurement sample of the separated solution was collected and left to stand for measurement of turbidity so as not to be affected by bubbles in the separated solution of the centrifugal dehydrator. Conventionally, there has been no apparatus for continuously measuring the turbidity of a separated liquid from a centrifugal dehydrator.

【0004】[0004]

【発明が解決しようとする課題】遠心脱水機の運転状況
の連続した監視、自動制御の要請に応えるため、遠心脱
水機の分離液の分離液の濁度を連続的に測定する必要が
生じた。
SUMMARY OF THE INVENTION In order to continuously monitor the operation status of the centrifugal dehydrator and to meet the demand for automatic control, it has been necessary to continuously measure the turbidity of the separated liquid of the centrifugal dehydrator. .

【0005】しかし、分離液には凝集剤が入っているた
めに、泡立ちやすい性質がある。従って、遠心脱水機の
分離液中の泡の影響を受けることなく、その分離液の濁
度を連続的測定可能にしなければならないという問題点
があった。
[0005] However, since the separated liquid contains a flocculant, it has a property of easily foaming. Therefore, there is a problem that the turbidity of the separated liquid must be continuously measured without being affected by bubbles in the separated liquid of the centrifugal dehydrator.

【0006】本発明は、上記問題点を解決し、遠心脱水
機の運転状況の監視、自動制御を可能とする遠心脱水機
分離液の濁度測定装置を提供することを目的としてい
る。
An object of the present invention is to solve the above-mentioned problems and to provide an apparatus for measuring the turbidity of a separated liquid of a centrifugal dehydrator, which makes it possible to monitor the operation status of the centrifugal dehydrator and automatically control the same.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するた
め、本発明の遠心脱水機の濁度測定装置は、遠心脱水機
の分離液中の泡に付着している浮遊固形物を該泡から分
離し該分離液中に均質に分布させるために該分離液を攪
拌混合する混合槽と、攪拌混合された該分離液中の該泡
を気液分離により脱泡する泡分離槽と、該泡が脱泡され
た該分離液の濁度を測定する装置とからなる。また、本
発明の濁度測定方法は、遠心脱水機の分離液中の泡に付
着している浮遊固形物を該泡から分離し該分離液中に均
質に分布させるために該分離液を攪拌した後、該分離液
中の該泡を気液分離により脱泡し、脱泡した該分離液の
濁度を連続的に測定することを特徴とする。
In order to achieve the above object, a turbidity measuring apparatus for a centrifugal dehydrator according to the present invention is configured to remove suspended solids adhering to bubbles in a separated liquid of a centrifugal dehydrator from the foam. A mixing tank for stirring and mixing the separated liquid in order to separate and uniformly distribute the separated liquid in the separated liquid; a foam separation tank for defoaming the mixed and separated bubbles in the separated liquid by gas-liquid separation; And a device for measuring the turbidity of the degassed separated liquid. Further, the turbidity measuring method of the present invention is a method of separating a suspended solid adhering to foam in a separated liquid of a centrifugal dehydrator from the foam and stirring the separated liquid to uniformly distribute the separated solid in the separated liquid. After that, the foam in the separated liquid is defoamed by gas-liquid separation, and the turbidity of the defoamed separated liquid is continuously measured.

【0008】[0008]

【作用】遠心分離機の分離液を混合槽に流入し、ミキサ
ー等で攪拌混合する。この攪拌工程により、分離液中の
濁度、泡の分布を均質にするだけでなく、泡に付着して
いた浮遊固形物が泡から分離し、分離液中に均質に分布
する。なお、攪拌は、分離液濁度に応じ配管内攪拌でも
良い。その後、攪拌混合された分離液を泡分離槽に移送
する。泡分離槽に移送された分離液中の泡は、液相から
気相への泡の上昇により泡分離槽の上部流出口から排出
され、泡分離槽の底部に脱泡液が分離される。
The separated liquid from the centrifugal separator flows into the mixing tank and is stirred and mixed by a mixer or the like. By this stirring step, not only the turbidity and the distribution of bubbles in the separated solution are made uniform, but also the suspended solids attached to the bubbles are separated from the bubbles and uniformly distributed in the separated solution. The stirring may be stirring in a pipe depending on the turbidity of the separated liquid. Then, the separated and mixed liquid is transferred to a foam separation tank. The foam in the separated liquid transferred to the foam separation tank is discharged from the upper outlet of the foam separation tank by the rise of the foam from the liquid phase to the gas phase, and the defoamed liquid is separated at the bottom of the foam separation tank.

【0009】泡分離槽の底部に接続される配管系統を介
して泡分離槽の流出口より排出する脱泡分離液を前記配
管系統に取付けた濁度測定装置により測定すると、泡の
影響を受けることなく、連続的に分離液の濁度を測定す
ることができる。
When the defoamed separated liquid discharged from the outlet of the foam separation tank via a piping system connected to the bottom of the foam separation tank is measured by a turbidity measuring device attached to the piping system, the liquid is affected by the bubbles. Without this, the turbidity of the separated liquid can be continuously measured.

【0010】[0010]

【実施例】実施例について、図1に基づいて説明する。An embodiment will be described with reference to FIG.

【0011】図1は、濁度測定装置構成の系統関係を明
示し、図1に示したシステムは、混合槽1と、泡分離槽
3と、分離液及び泡を移送する配管5、6、8、9、1
1、12とからなる。
FIG. 1 clearly shows the system relationship of the configuration of the turbidity measuring device. The system shown in FIG. 1 is composed of a mixing tank 1, a foam separation tank 3, and pipes 5, 6, for transferring separated liquid and foam. 8, 9, 1
1 and 12.

【0012】混合槽1の容量は2lで、ミキサー2の回
転数は5〜200rpmである。ミキサー2の回転数は
分離液の濃度により変更する。
The capacity of the mixing tank 1 is 2 l, and the rotation speed of the mixer 2 is 5 to 200 rpm. The rotation speed of the mixer 2 is changed according to the concentration of the separated liquid.

【0013】泡分離槽3の容量は2lで、寸法は110
mmΦ×250mmHである。濁度計は、光式濃度計S
SD−20型(電気化学計器)を使用し、配管8と配管
9の間に配置した。
The volume of the foam separation tank 3 is 2 liters and the size is 110
mmΦ × 250 mmH. The turbidimeter is an optical densitometer S
Using SD-20 type (electrochemical meter), it was arranged between the pipe 8 and the pipe 9.

【0014】遠心脱水機分離液は、混合槽1に流量15
〜20l/分で投入され、攪拌された。この攪拌により
SSの塊などを分散し、濁度が均質になると共に泡に付
着した汚濁物質が取り去られ、液中に移った。
The centrifugal dehydrator separation liquid is supplied to the mixing tank 1 at a flow rate of 15%.
Charged at 2020 l / min and stirred. By this stirring, the lump of SS and the like were dispersed, the turbidity became homogenous, and the contaminants adhering to the foam were removed and transferred into the liquid.

【0015】攪拌された分離液が、泡分離槽3に移送さ
れた。そこで、泡が液相から気相へ上昇し、上部流出口
10から泡のみがオーバーフローし、下部流出口7から
は脱泡液が流出した。この結果ほぼ完全に泡が分離でき
ることが確認できた。
The stirred separated liquid was transferred to the foam separation tank 3. Then, the bubbles rose from the liquid phase to the gas phase, only the bubbles overflowed from the upper outlet 10, and the defoamed liquid flowed out from the lower outlet 7. As a result, it was confirmed that bubbles could be almost completely separated.

【0016】本発明の特徴の一つである泡分離槽3内の
出口10から出口7方向に分離液が流れる間に泡の上昇
を利用し、泡のみを出口10よりオーバーフローにより
流出させ、出口7より脱泡液を得ることが認められた。
泡分離槽3の上部1/3が泡14で、下部2/3が分離
液13で占められた。出口7より流出した脱泡液は、光
式濃度計SSD−20型(電気化学計器)により計測さ
れた後、泡分離槽3を出口10からオーバーフローした
泡と混合され配管12を介して排出された。
While the separated liquid flows from the outlet 10 in the foam separation tank 3 to the outlet 7 as one of the features of the present invention, the rise of the bubbles is utilized, and only the bubbles are caused to flow out of the outlet 10 by overflow. 7, it was confirmed that a defoamed liquid was obtained.
The upper 1/3 of the foam separation tank 3 was occupied by the foam 14, and the lower 2/3 by the separated liquid 13. The defoamed liquid flowing out from the outlet 7 is measured by an optical densitometer SSD-20 type (electrochemical meter), mixed with the foam overflowing from the outlet 10 through the foam separation tank 3, and discharged through the pipe 12. Was.

【0017】濃度測定の結果を表1に示す。Table 1 shows the results of the density measurement.

【0018】[0018]

【表1】 [Table 1]

【0019】表1に示されるように、混合槽と泡分離槽
を組み合わせた場合にはJIS試験法に一致する測定値
が得られた。これに対し、泡を分離しないで測定した場
合には、JIS試験法に比べて濁度が大きく検出され、
泡分離槽のみを使用した場合にも、測定値とのばらつき
が大きいことがわかる。
As shown in Table 1, when the mixing tank and the foam separation tank were combined, a measured value consistent with the JIS test method was obtained. On the other hand, when the measurement is performed without separating the foam, the turbidity is detected larger than the JIS test method,
It can be seen that even when only the foam separation tank is used, the variation from the measured value is large.

【0020】[0020]

【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。
Since the present invention is configured as described above, it has the following effects.

【0021】遠心脱水機の分離液に泡が含まれていて
も、泡の影響を受けることなく、連続的にその分離液の
濁度を測定できる。従って、遠心脱水機の分離液の濁度
を連続的に測定することにより、分離液の測定をもとに
して遠心脱水機の運転状況の監視や自動制御が可能とな
る。また、濁度に応じた混合槽のミキサーの回転数制御
ができ、更には遠心脱水機の処理流量の最適化を図るこ
とができる。なお、本発明によれば、遠心脱水機の分離
液にかぎらず、泡を含む各種液の濁度測定に使用でき
る。
Even if bubbles are contained in the separated liquid of the centrifugal dehydrator, the turbidity of the separated liquid can be continuously measured without being affected by the bubbles. Therefore, by continuously measuring the turbidity of the separated liquid of the centrifugal dehydrator, it becomes possible to monitor and automatically control the operation state of the centrifugal dehydrator based on the measurement of the separated liquid. In addition, the number of revolutions of the mixer in the mixing tank can be controlled according to the turbidity, and the processing flow rate of the centrifugal dehydrator can be optimized. In addition, according to the present invention, it can be used for measuring the turbidity of not only the separated liquid of the centrifugal dehydrator but also various liquids containing bubbles.

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

【図1】遠心脱水機の分離液濁度測定装置の系統図であ
る。
FIG. 1 is a system diagram of a separation turbidity measuring device of a centrifugal dehydrator.

【符号の説明】[Explanation of symbols]

1 混合槽 2 ミキサー 3 泡分離槽 4 濁度測定器 5 遠心分離液流入配管 6 移送配管 7 分離槽の脱泡液流出口 8、9 脱泡液移送配管 10 分離槽の泡排出口 11 泡排出配管 12 流出配管 13 脱泡液 14 泡 DESCRIPTION OF SYMBOLS 1 Mixing tank 2 Mixer 3 Foam separation tank 4 Turbidity measuring device 5 Centrifugal separation liquid inflow pipe 6 Transfer pipe 7 Separation tank defoaming liquid outlet 8, 9 Defoaming liquid transfer pipe 10 Separation tank foam outlet 11 Foam discharge Piping 12 Outflow piping 13 Defoaming liquid 14 Foam

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 遠心脱水機の分離液中の泡に付着してい
る浮遊固形物を該泡から分離し該分離液中に均質に分布
させるために該分離液を攪拌混合する混合槽と、攪拌混
合された該分離液中の該泡を比重差による気液分離によ
り脱泡する泡分離槽と、該泡が脱泡された該分離液の濁
度を測定する装置とで構成される遠心脱水機分離液の濁
度測定装置。
A mixing tank for stirring and mixing the separated liquid to separate suspended solids attached to bubbles in the separated liquid of the centrifugal dehydrator from the bubbles and to distribute the separated solids homogeneously in the separated liquid; A centrifugal separation tank configured to defoam the bubbles in the stirred and separated liquid by gas-liquid separation based on a difference in specific gravity, and a device for measuring the turbidity of the separated liquid from which the bubbles have been defoamed; Turbidity measurement device for dehydrator separation liquid.
【請求項2】 遠心脱水機の分離液中の泡に付着してい
る浮遊固形物を該泡から分離し該分離液中に均質に分布
させるために該分離液を攪拌した後、該分離液中の該泡
比重差による気液分離により脱泡し、脱泡した該分離
液の濁度を連続的に測定することを特徴とする遠心脱水
機分離液の濁度測定方法。
2. The centrifugal dewatering machine separates suspended solids adhering to bubbles in the separated liquid from the foam and stirs the separated liquid to uniformly distribute the separated solids in the separated liquid. A method for measuring turbidity of a separated liquid in a centrifugal dehydrator, comprising defoaming the foam therein by gas-liquid separation based on a specific gravity difference, and continuously measuring the turbidity of the defoamed separated liquid.
JP4239984A 1992-08-17 1992-08-17 Apparatus and method for measuring turbidity of separated liquid in centrifugal dehydrator Expired - Lifetime JP2785856B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4239984A JP2785856B2 (en) 1992-08-17 1992-08-17 Apparatus and method for measuring turbidity of separated liquid in centrifugal dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4239984A JP2785856B2 (en) 1992-08-17 1992-08-17 Apparatus and method for measuring turbidity of separated liquid in centrifugal dehydrator

Publications (2)

Publication Number Publication Date
JPH0663451A JPH0663451A (en) 1994-03-08
JP2785856B2 true JP2785856B2 (en) 1998-08-13

Family

ID=17052750

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4239984A Expired - Lifetime JP2785856B2 (en) 1992-08-17 1992-08-17 Apparatus and method for measuring turbidity of separated liquid in centrifugal dehydrator

Country Status (1)

Country Link
JP (1) JP2785856B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004167401A (en) * 2002-11-20 2004-06-17 Toshiba Corp Waste water treatment equipment and waste water treatment method
KR102228446B1 (en) * 2019-04-24 2021-03-15 전형곤 Automatic control centrifugal separator by turbidity

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55152445A (en) * 1979-05-17 1980-11-27 Toshiba Corp Device for measuring concentration
JPS6054753A (en) * 1983-09-05 1985-03-29 Hitachi Ltd Turbidity controlling device of centrifugal dehydrator

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5580734U (en) * 1978-11-30 1980-06-03

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55152445A (en) * 1979-05-17 1980-11-27 Toshiba Corp Device for measuring concentration
JPS6054753A (en) * 1983-09-05 1985-03-29 Hitachi Ltd Turbidity controlling device of centrifugal dehydrator

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Publication number Publication date
JPH0663451A (en) 1994-03-08

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