JP2854388B2 - Water control method for dewatered sludge - Google Patents
Water control method for dewatered sludgeInfo
- Publication number
- JP2854388B2 JP2854388B2 JP2149454A JP14945490A JP2854388B2 JP 2854388 B2 JP2854388 B2 JP 2854388B2 JP 2149454 A JP2149454 A JP 2149454A JP 14945490 A JP14945490 A JP 14945490A JP 2854388 B2 JP2854388 B2 JP 2854388B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- dewatered sludge
- dewatered
- dehydrator
- water content
- 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
Links
Landscapes
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明の脱水汚泥の水分制御法に関し、さらに詳しく
は脱水汚泥の含水率を簡単な操作で連続的に一定に制御
することができる脱水汚泥の水分制御法に関する。Description: TECHNICAL FIELD The present invention relates to a method for controlling the moisture content of dewatered sludge of the present invention, and more particularly, to dewatered sludge capable of continuously and constantly controlling the water content of dewatered sludge by a simple operation. Water control method.
従来、汚泥を濃縮、脱水して得られる脱水汚泥の水分
測定には、遠紫外線を利用した自動水分計などが用いら
れている。しかしながら、この計測器は、サンプリング
した汚泥を乾燥させて重量乾燥法で測定するものであ
り、応答時間が長く、またサンプリングが必要であるた
め連続的測定ができず、汚泥性状が急変した場合に追従
できないという問題があった。2. Description of the Related Art Conventionally, an automatic moisture meter using far ultraviolet rays has been used for moisture measurement of dewatered sludge obtained by concentrating and dewatering sludge. However, this measuring instrument measures the sludge by drying the sampled sludge by the gravimetric drying method.The response time is long, and continuous measurement cannot be performed because sampling is required. There was a problem that they could not follow.
本発明の目的は、前記した従来技術の問題を解決し、
脱水汚泥の水分量を連続かつ高精度に測定し、脱水汚泥
の含水率を一定に制御することができる脱水汚泥の水分
制御法を提供することにある。An object of the present invention is to solve the above-mentioned problems of the prior art,
It is an object of the present invention to provide a method for controlling the water content of dewatered sludge that can continuously and highly accurately measure the water content of the dewatered sludge and control the water content of the dewatered sludge to a constant value.
〔課題を解決するための手段〕 本発明者は、先に出願した回転電極(特願平2−9837
6号、特開平3−295460号)を脱水汚泥の水分制御に適
用することにより、上記目的を達成できるとを見出し、
本発明に到達した。[Means for Solving the Problems] The present inventor has proposed a rotating electrode (Japanese Patent Application No. 2-9837) filed earlier.
No. 6, Japanese Unexamined Patent Publication No. 3-295460) found that the above object can be achieved by applying moisture control of dewatered sludge.
The present invention has been reached.
本発明は、汚泥タンクに貯溜された汚泥を薬剤混合槽
に導入して薬剤を注入、混合した後、脱水機により脱水
して脱水汚泥を製造するに際し、該脱水汚泥中に、少な
くも1対の陰極および陽極が1mm以下の間隔で平行に回
転端子に設けられた回転電極を設置し、該回転電極に一
定電圧を印加して電解電流を測定し、この測定値が一定
範囲となるように、前記脱水機の回転数、薬剤混合槽へ
の汚泥供給量または薬剤注入量を調節して脱水汚泥の含
水率を一定に制御することを特徴とする脱水汚泥の水分
制御法に関する。The present invention relates to a method for producing dewatered sludge by introducing sludge stored in a sludge tank into a chemical mixing tank, injecting and mixing a drug, and then dehydrating the dewatered sludge by a dehydrator. A negative electrode and a positive electrode are provided with a rotating electrode provided on a rotating terminal in parallel at an interval of 1 mm or less, a constant voltage is applied to the rotating electrode, and an electrolytic current is measured so that the measured value falls within a certain range. The present invention also relates to a method for controlling the water content of dewatered sludge, wherein the water content of dewatered sludge is controlled to be constant by adjusting the rotation speed of the dehydrator, the amount of sludge supplied to the chemical mixing tank, or the amount of injected chemical.
本発明に用いられる回転電極は、少なくとも1対の陰
極および陽極が1mm以下、好ましくは0.75mm〜0.1mm、よ
り好ましくは0.5mm〜0.3mm程度の間隔で平行に回転端子
に設けられたものである。陰極と陽極を1mm以下の間隔
で平行に回転端子に設けることにより、試料中に固定極
を設置することなく、また拡散槽が得られやすい試料に
制約されることなく、試料中の水分量に比例した安定し
た電解電流を発生させることができるため、この電流値
から試料中の水分量を算出することができる。またこの
ような回転電極を用いることにより、電極表面への汚泥
の付着を防止することができるため、連続した電流測定
が可能である。なお、電解電流値から水分量を算出する
際には、測定精度を向上させるために温度補正をするこ
とが好ましい。The rotating electrode used in the present invention, at least one pair of cathode and anode is 1 mm or less, preferably 0.75 mm to 0.1 mm, more preferably provided on the rotating terminal at intervals of about 0.5 mm to 0.3 mm in parallel. is there. By providing the cathode and anode parallel to the rotating terminal at an interval of 1 mm or less, it is possible to reduce the amount of water in the sample without installing a fixed pole in the sample and without being restricted to a sample in which a diffusion tank is easily obtained. Since a proportionally stable electrolysis current can be generated, the amount of water in the sample can be calculated from the current value. In addition, by using such a rotating electrode, it is possible to prevent sludge from adhering to the electrode surface, so that continuous current measurement is possible. When calculating the water content from the electrolytic current value, it is preferable to perform temperature correction in order to improve measurement accuracy.
第4図は、本発明に用いられる一例の回転電極の斜視
図である。この回転電極6は、1mm以下の間隔で平行に
設けられた1対の陰極12および陽極13と、該陰極12およ
び陽極13を固定し、かつこれらの先端部のみを露出さ
せ、他の構成部分から絶縁する絶縁部16と、上記陰極12
および陽極13をそれぞれ電源および計測部に接続する集
電ブラシ14および給電リング15とからなる。FIG. 4 is a perspective view of an example of a rotating electrode used in the present invention. The rotating electrode 6 is composed of a pair of cathodes 12 and anodes 13 provided in parallel at an interval of 1 mm or less, fixing the cathodes 12 and anodes 13 and exposing only their tips, and other components. An insulating portion 16 for insulating the cathode 12
And a current collecting brush 14 and a power supply ring 15 for connecting the anode 13 to a power supply and a measuring unit, respectively.
陰極および陽極を構成する物質としては白金等の貴金
属が用いられ、陰極には銅、、SUSなどを用いることも
できる。陰極12および陽極13の露出位置は回転電極6の
底部に設けられているが、側部に設けてもよく、またく
し型状の電極としてもよい。絶縁部16には、エポキシ樹
脂、塩化ビニル樹脂、フェノール樹脂等の樹脂類やセラ
ミックスなどが用いられる。電極の長さは、測定精度の
点から短い方が好ましく、20〜10mm以下とすることが好
ましく、より好ましくは5mm程度である。Noble metals such as platinum are used as the materials constituting the cathode and the anode, and copper, SUS, and the like can also be used for the cathode. Although the exposed positions of the cathode 12 and the anode 13 are provided at the bottom of the rotating electrode 6, they may be provided at the sides or may be comb-shaped electrodes. For the insulating portion 16, resins such as epoxy resin, vinyl chloride resin, and phenol resin, ceramics, and the like are used. The length of the electrode is preferably shorter from the viewpoint of measurement accuracy, preferably 20 to 10 mm or less, and more preferably about 5 mm.
本発明においては、汚泥の性状変化(水分量変化)に
より電解電流が変化することを利用したものであり、該
電解電流値を上記回転電極で直接かつ連続的に測定し、
汚泥の性状を瞬時に把握することができるため、この性
状の変化に応じて薬剤混合槽への汚泥供給量、薬剤注入
量または脱水機の回転数を調節することにより、脱水汚
泥の含水率を一定にコントロールすることができる。The present invention utilizes the fact that the electrolysis current changes due to the change in the properties of the sludge (change in the amount of water). The electrolysis current value is measured directly and continuously by the rotating electrode,
Since the properties of the sludge can be grasped instantaneously, the water content of the dehydrated sludge can be adjusted by adjusting the amount of sludge supplied to the chemical mixing tank, the amount of the chemical injected, or the rotation speed of the dehydrator according to the change in the properties. It can be controlled constantly.
以下、本発明を図面により詳しく説明する。 Hereinafter, the present invention will be described in detail with reference to the drawings.
第1図は、本発明の一実施例を示す脱水汚泥の製造装
置の工程図である。この装置は、汚泥9を貯溜する汚泥
タンク1と、該汚泥タンク1から供給された汚泥9に薬
剤を注入して撹拌機8で混合する薬剤混合槽2と、該薬
剤混合槽2で混合された混合液を脱水する脱水機3と、
該脱脂機3で脱水された脱水汚泥10を搬送するベルトコ
ンベア4と、該脱水汚泥10中に設置され、一定電圧での
電解電流を連続的に測定する回転電極5と、該回転電極
5での測定値が一定範囲となるように上記脱水機3の回
転数を制御する演算器6とからなる。FIG. 1 is a process diagram of an apparatus for producing dehydrated sludge showing one embodiment of the present invention. This apparatus comprises a sludge tank 1 for storing sludge 9, a medicine mixing tank 2 for injecting a medicine into sludge 9 supplied from the sludge tank 1 and mixing the mixture with a stirrer 8, and mixing in the medicine mixing tank 2. A dehydrator 3 for dehydrating the mixed liquid,
A belt conveyor 4 for transporting the dewatered sludge 10 dehydrated by the degreasing machine 3, a rotating electrode 5 installed in the dewatered sludge 10 and continuously measuring an electrolytic current at a constant voltage; And a computing unit 6 for controlling the rotation speed of the dehydrator 3 so that the measured value of the dehydrator 3 is within a certain range.
このような構成において、汚泥タンク1に貯溜された
汚泥9は、ポンプ7により薬剤混合槽2に導入され、一
定量の薬剤(高分子凝集剤、無機凝集剤等)が注入され
て撹拌機8により混合された後、脱水機3に導入され、
脱水されて脱水汚泥10となり、ベルトコンベア4で搬送
される。一方、脱水汚泥10中に設置された回転電極5に
一定電圧が印加されて脱水汚泥の電解電流が測定されて
演算機6に入力され、ここで測定値が一定範囲となるよ
うに上記脱水機3の回転数が算出されで脱脂機3に伝達
され、脱水汚泥の含水率が一定となるようにコントロー
ルされる。In such a configuration, the sludge 9 stored in the sludge tank 1 is introduced into the medicine mixing tank 2 by the pump 7, and a certain amount of medicine (polymer coagulant, inorganic coagulant, etc.) is injected into the stirrer 8 And then introduced into the dehydrator 3,
The dewatered sludge 10 is dewatered and conveyed by the belt conveyor 4. On the other hand, a constant voltage is applied to the rotating electrode 5 installed in the dewatered sludge 10, the electrolytic current of the dewatered sludge is measured and input to the calculator 6, and the dehydrator is set so that the measured value is within a certain range. The rotation speed of the dewatered sludge is calculated and transmitted to the degreasing machine 3, and is controlled so that the water content of the dewatered sludge is constant.
第2図は、本発明の他の実施例を示す脱水汚泥の製造
装置の工程図である。第2図で第1図と異なる点は、脱
水機3の回転数の制御の代わりに、薬剤供給調節弁11を
設け、演算器6からの信号に応じて薬剤供給量を調節し
て脱水汚泥の含水率を一定にコントロールするようにし
たことである。FIG. 2 is a process diagram of a dewatered sludge producing apparatus showing another embodiment of the present invention. The difference between FIG. 2 and FIG. 1 is that instead of controlling the rotation speed of the dehydrator 3, a chemical supply control valve 11 is provided, and the chemical supply amount is adjusted according to a signal from the arithmetic unit 6 so that the dewatered sludge is adjusted. Is controlled to be constant.
第3図は、本発明のさらに他の実施例を示す脱水汚泥
の製造装置の工程図である。第3図で第1図と異なる点
は、脱脂機3の回転数の制御の代わりに、ポンプ7によ
り薬剤混合槽2に供給する汚泥の供給量を調節して脱水
汚泥の含水率を一定にコントロールするようにしたこと
である。FIG. 3 is a process diagram of a dewatered sludge producing apparatus showing still another embodiment of the present invention. The difference between FIG. 3 and FIG. 1 is that instead of controlling the number of rotations of the degreasing machine 3, the amount of sludge supplied to the chemical mixing tank 2 by the pump 7 is adjusted to keep the water content of the dewatered sludge constant. It is to control.
第1図、第2図および第3図に示す装置においては、
脱水汚泥をサンプリングする必要がなく、脱水汚泥の性
状を連続的かつ瞬時に把握し、該汚泥性状に応じた運転
条件を設定し、脱水汚泥の含水率を一定にコントロール
することができる。In the device shown in FIGS. 1, 2 and 3,
There is no need to sample the dewatered sludge, and the properties of the dewatered sludge can be grasped continuously and instantaneously, operating conditions can be set according to the properties of the sludge, and the moisture content of the dewatered sludge can be controlled to a constant value.
本発明の脱水汚泥の水分制御法によれば、陰極と陽極
が1mm以下の間隔で平行に回転端子に設けられた回転電
極を用い、汚泥中の電解電流値を高精度で直接かつ連続
的に測定し、該電流値が一定範囲となるように運電条件
を設定することができるため、汚泥の性状が急激に変化
した場合でも、脱水汚泥の含水率を容易に一定に制御す
ることができる。According to the method for controlling the moisture content of dewatered sludge of the present invention, a cathode and an anode use a rotating electrode provided on a rotating terminal in parallel at an interval of 1 mm or less, and the electrolytic current value in the sludge is directly and continuously measured with high precision. It is possible to measure and set the power supply conditions so that the current value falls within a certain range. Therefore, even when the properties of the sludge change rapidly, the moisture content of the dewatered sludge can be easily controlled to be constant. .
【図面の簡単な説明】 第1図は、本発明の一実施例を示す脱水汚泥の製造装置
の工程図、第2図は、本発明の他の実施例を示す脱水汚
泥の製造装置の工程図、第3図は、さらに他の実施例を
示す脱水汚泥の製造装置の工程図、第4図は、本発明に
用いられる一例の回転電極の斜視図である。 1……汚泥タンク、2……薬剤混合槽、3……脱水機、
4……ベルトコンベア、5……回転電極、6……演算
器、7……ポンプ、8……撹拌機、9……汚泥、10……
脱水汚泥、11……薬剤供給調節弁、12……陰極、13……
陽極、14……給電ブラシ、15……集電リンク、16……絶
縁部。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a process diagram of an apparatus for producing dehydrated sludge showing one embodiment of the present invention, and FIG. 2 is a process diagram of an apparatus for producing dehydrated sludge showing another embodiment of the present invention. FIG. 3 is a process diagram of a dewatered sludge producing apparatus showing still another embodiment, and FIG. 4 is a perspective view of an example of a rotating electrode used in the present invention. 1 ... sludge tank, 2 ... chemical mixing tank, 3 ... dehydrator,
4 ... belt conveyor, 5 ... rotating electrode, 6 ... arithmetic unit, 7 ... pump, 8 ... stirrer, 9 ... sludge, 10 ...
Dewatered sludge, 11 ... Chemical supply control valve, 12 ... Cathode, 13 ...
Anode, 14: Power supply brush, 15: Current collecting link, 16: Insulating part.
フロントページの続き (56)参考文献 特開 平3−295460(JP,A) 特開 平3−180747(JP,A) 特開 平4−42046(JP,A) 特開 平3−274448(JP,A) 実開 昭58−163865(JP,U) (58)調査した分野(Int.Cl.6,DB名) G01N 27/30,27/416 G01N 27/00 - 27/24 C02F 11/14Continuation of the front page (56) References JP-A-3-295460 (JP, A) JP-A-3-180747 (JP, A) JP-A-4-42046 (JP, A) JP-A-3-274448 (JP) , A) Real opening 58-163865 (JP, U) (58) Fields investigated (Int. Cl. 6 , DB name) G01N 27 / 30,27 / 416 G01N 27/00-27/24 C02F 11/14
Claims (1)
に導入して薬剤を注入、混合した後、脱水機により脱水
して脱水汚泥を製造するに際し、該脱水汚泥中に、少な
くも1対の陰極および陽極が1mm以下の間隔で平行に回
転端子に設けられた回転電極を設置し、該回転電極に一
定電圧を印加して電解電流を測定し、この測定値が一定
範囲となるように、前記脱水機の回転数、薬剤混合槽へ
の汚泥供給量または薬剤注入量を調節して脱水汚泥の含
水率を一定に制御することを特徴とする脱水汚泥の水分
制御法。A sludge stored in a sludge tank is introduced into a chemical mixing tank to inject and mix a medicine, and then dewatered by a dehydrator to produce dewatered sludge. A pair of cathodes and anodes are provided with a rotating electrode provided at a rotating terminal in parallel at an interval of 1 mm or less, a constant voltage is applied to the rotating electrode, and an electrolytic current is measured, so that the measured value is in a certain range. A method of controlling the water content of the dewatered sludge, wherein the water content of the dewatered sludge is controlled to be constant by adjusting the rotation speed of the dehydrator, the amount of sludge supplied to the chemical mixing tank or the amount of injected chemical.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2149454A JP2854388B2 (en) | 1990-06-07 | 1990-06-07 | Water control method for dewatered sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2149454A JP2854388B2 (en) | 1990-06-07 | 1990-06-07 | Water control method for dewatered sludge |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0442047A JPH0442047A (en) | 1992-02-12 |
JP2854388B2 true JP2854388B2 (en) | 1999-02-03 |
Family
ID=15475479
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2149454A Expired - Fee Related JP2854388B2 (en) | 1990-06-07 | 1990-06-07 | Water control method for dewatered sludge |
Country Status (1)
Country | Link |
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JP (1) | JP2854388B2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4523127B2 (en) * | 2000-07-24 | 2010-08-11 | 三井造船株式会社 | Sludge monitoring system, sludge control system, water treatment system and sludge treatment system |
JP2003181498A (en) * | 2001-12-20 | 2003-07-02 | Nishihara Environment Technology Inc | Dehydration apparatus |
JP2005201753A (en) * | 2004-01-15 | 2005-07-28 | Kett Electric Laboratory | Moisture detecting unit and moisture measuring apparatus |
JP4906918B2 (en) * | 2006-05-01 | 2012-03-28 | エフ ホフマン−ラ ロッシュ アクチェン ゲゼルシャフト | Sample fluid test apparatus and method for analyzing sample fluid |
JP5716049B2 (en) * | 2012-03-02 | 2015-05-13 | 三井造船環境エンジニアリング株式会社 | Sludge treatment system and sludge treatment method |
JP7255198B2 (en) * | 2019-01-24 | 2023-04-11 | 栗田工業株式会社 | ecosystem |
-
1990
- 1990-06-07 JP JP2149454A patent/JP2854388B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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JPH0442047A (en) | 1992-02-12 |
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