JPH0442046A - Pressure-sending method for sludge - Google Patents

Pressure-sending method for sludge

Info

Publication number
JPH0442046A
JPH0442046A JP14945390A JP14945390A JPH0442046A JP H0442046 A JPH0442046 A JP H0442046A JP 14945390 A JP14945390 A JP 14945390A JP 14945390 A JP14945390 A JP 14945390A JP H0442046 A JPH0442046 A JP H0442046A
Authority
JP
Japan
Prior art keywords
sludge
pump
water
electrode
pressure
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
JP14945390A
Other languages
Japanese (ja)
Inventor
Yuya Yamahata
山畑 祐哉
Noboru Takemura
昇 竹村
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding Co 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP14945390A priority Critical patent/JPH0442046A/en
Publication of JPH0442046A publication Critical patent/JPH0442046A/en
Pending legal-status Critical Current

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  • Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)

Abstract

PURPOSE:To make it possible to stabilize the operation of a sludge pressure- sending pump by measuring an electrolytic current value, and feeding water so that the current value is in a specified range. CONSTITUTION:At least a pair of a cathode and an anode are provided at rotary terminals of a rotary electrode 6 in parallel at an interval of 1 mm or less. The rotary electrode 6 is provided at the side of the inlet port of a sludge pressure-sending pump 3. A specified voltage is applied on the electrode 6, and an electrolytic current is measured. The value is inputted into an operator 7. The operator 7 receives the value and computes the water feeding amount so that the moisture content of dehydrated sludge 10 becomes constant. Then, a water-supply adjusting value 8 adjusts the opening degree based on the signal. Water is supplied into the sludge 10 through the tip part of a water feeding pipe 11. Then, the sludge 10 is sent into the pump 3 by the rotation of a screw 2. The, the pump 3 inputs the sludge 10 into an incinerator through a pressure- sending line 5. In this way, the eletrolytic current is continuously measured by using the electrode 6, and the water is supplied so that the current value is in the specified range. Thus, the moisture content of the sludge 10 is kept in the specified range, and the sludge can be supplied into the pump 3.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は汚泥の圧送方法に関し、さらに詳しくは汚泥の
含水率を簡単な操作で一定に保持しつつ焼却炉等へ安定
供給することができる汚泥の圧送方法に関する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method for pumping sludge, and more specifically, it is possible to stably supply sludge to an incinerator, etc. while keeping the moisture content of sludge constant with simple operations. This article relates to a method for pumping sludge.

〔従来の技術] 従来、脱水汚泥を処理する方法の1つとして、焼却炉で
燃焼する方法が知られている。焼却炉で燃焼する脱水汚
泥は、汚泥圧送ポンプにより圧送して供給されるが、脱
水汚泥の水分含有率が低い場合には、管内圧力損失が増
加してポンプがオーバーロードになるという問題があっ
た。これを避けるため、通常、ポンプ出口の汚泥管内の
圧力を検出したり、ポンプモータの電流値を測定するポ
ンプ保護回路が設置したりして対処してきた。しかし、
−旦ポンプがオーバーロードになりポンプが停止すると
、ポンプを解体した後、復帰させるという大きな手間が
必要であった。また汚泥を圧送して焼却炉で燃焼させる
際にも汚泥の水分含有率に差があると焼却炉での安定し
た燃焼ができないという問題があった。
[Prior Art] Conventionally, a method of burning dehydrated sludge in an incinerator has been known as one of the methods of treating dehydrated sludge. The dehydrated sludge that is burned in the incinerator is pumped and supplied by a sludge pressure pump, but if the moisture content of the dehydrated sludge is low, there is a problem that the pressure loss in the pipes increases and the pump becomes overloaded. Ta. To avoid this, conventional measures include installing a pump protection circuit that detects the pressure inside the sludge pipe at the pump outlet or measures the current value of the pump motor. but,
-When the pump becomes overloaded and stops, it is necessary to disassemble the pump and restore it, which is a huge effort. Furthermore, when sludge is pumped and burned in an incinerator, there is a problem that stable combustion in the incinerator cannot be achieved if there is a difference in the water content of the sludge.

また従来、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たが、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
場合には追従できなかった。
Conventionally, automatic moisture meters that use far ultraviolet light have been used to measure the moisture content of dehydrated sludge;
The sampled sludge is dried and measured using the gravimetric drying method, which requires a long response time and requires sampling, making continuous measurement impossible and unable to follow sudden changes in sludge properties.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明の目的は、前記した従来技術の問題を解決し、汚
泥中の含水率を迅速に測定してこれを一定範囲に保持し
、安定した状態で汚泥圧送ポンプに供給することができ
る方法を提供することにある。
The purpose of the present invention is to solve the problems of the prior art described above, and to provide a method that can quickly measure the water content in sludge, maintain it within a certain range, and supply it to a sludge pressure pump in a stable state. It is about providing.

〔課題を解決するための手段〕[Means to solve the problem]

上記目的を達成するため、本発明者は、先に出願した回
転電極(特願平2−98376号)を汚泥圧送に適用す
ることにより、ポンプのオーバーロードなどを生じるこ
となく、汚泥を安定して圧送できることを見出し、゛本
発明に到達した。
In order to achieve the above object, the present inventor has stabilized the sludge without overloading the pump by applying the previously filed rotating electrode (Japanese Patent Application No. 2-98376) to sludge pumping. It was discovered that the present invention can be carried out under pressure.

本発明は、ホッパに貯溜された汚泥を汚泥圧送ポンプに
より圧送するに際し、該汚泥圧送ポンプの入口側の汚泥
中に、少なくとも1対の陰極および陽極が1m+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汚泥圧送ポンプの
前流側の汚泥中に水を供給することを特徴とする汚泥の
圧送方法に関する。
In the present invention, when sludge stored in a hopper is pumped by a sludge pump, at least one pair of a cathode and an anode are provided in the sludge on the inlet side of the sludge pump in parallel at a rotating terminal with an interval of 1 m or less. Install the rotated electrode,
Sludge pumping characterized by applying a constant voltage to the rotating electrode to measure an electrolytic current, and supplying water into the sludge on the upstream side of the sludge pump so that the measured value falls within a certain range. Regarding the method.

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lam以下、好ましくは0.75m〜0.
1m、より好ましくは0.5111111〜0.3 m
程度の間隔で平行に回転端子に設けられたものである。
In the rotating electrode used in the present invention, at least one pair of a cathode and an anode has a length of less than lam, preferably from 0.75 m to 0.3 m.
1 m, more preferably 0.5111111-0.3 m
They are provided on the rotating terminals in parallel at a certain interval.

陰極と陽極を1−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(、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、この電流値から水分量を算出すること
が可能である。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となる。なお、電解電流値
から水分濃度を算出する際には、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。
By arranging the cathode and anode parallel to each other at a spacing of 1-1 or less on the rotating terminal, there is no need to install a fixed electrode in the sample, and the sample is not limited to a sample where a diffusion tank can be easily obtained. Since it is possible to generate a stable electrolytic current proportional to the amount of electrolysis, it is possible to calculate the amount of water from this current value.Also, by using such a rotating electrode, it is possible to prevent sludge from adhering to the electrode surface. Therefore, continuous current measurement is possible.In addition, when calculating the water concentration from the electrolytic current value, it is preferable to perform temperature correction in order to improve measurement accuracy.

以下、本発明を図面により説明する。Hereinafter, the present invention will be explained with reference to the drawings.

〔実施例〕〔Example〕

第1図は、本発明の一実施例を示す脱水汚泥の供給装置
の構成図、第2図は、第1図で用いた回転電極の斜視図
である。
FIG. 1 is a block diagram of a dewatered sludge supply device showing one embodiment of the present invention, and FIG. 2 is a perspective view of a rotating electrode used in FIG. 1.

第2図において、回転電極6は、■間取下の間隔で平行
に設けられた1対の陰極12および陽極13と、該陰極
12および陽極工3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。
In FIG. 2, the rotating electrode 6 consists of a pair of cathodes 12 and anodes 13 that are provided in parallel with an interval of ① floor plan, and the cathodes 12 and anodes 3 are fixed, and only their tips are fixed. an insulating portion 16 that is exposed and insulated from other components;
It consists of a current collecting brush 14 and a power feeding ring 15 that connect the cathode 12 and anode 13 to a power source and a measuring section, 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、7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5■程度である。
A noble metal such as platinum is used as the material constituting the cathode and the anode, and copper, SUS, etc. can also be used for the cathode. The exposed position of the cathode 12 and anode 13 is the rotating electrode 6
Although the electrodes are provided at the bottom, they may also 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, ceramic, and 7x 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.

第1図において、脱水汚泥の供給装置は、脱水機(図示
せず)等で脱水された脱水汚泥10をホッパ1に搬送す
る搬送コンベア9と、該ホッパ1の下部に設けられた、
汚泥を送り出すためのスクリュー3と、該スクリュー3
で送り出された汚泥10を圧送するための汚泥圧送ポン
プ3と、該圧送された汚泥を焼却炉(図示せず)に輸送
する圧送ライン5と、上記汚泥圧送ポンプ3の入口側の
脱水汚泥中に設けられた回転電極6と、該回転電極6で
測定した電流値から脱水汚泥の含水率を一定に維持する
ために必要な水分量を算出する演算器7と、該演算器7
からの信号により水の供給量を調節する水供給調節弁8
と、水を上記スクリュー2の前流側に供給する水供給管
11とからなる。
In FIG. 1, the dehydrated sludge supply device includes a conveyor 9 that conveys dehydrated sludge 10 dehydrated by a dehydrator (not shown) or the like to a hopper 1, and a conveyor 9 provided at the bottom of the hopper 1.
A screw 3 for sending out sludge, and the screw 3
a sludge pump 3 for pumping the sludge 10 sent out, a pumping line 5 for transporting the pumped sludge to an incinerator (not shown), and a dehydrated sludge on the inlet side of the sludge pump 3. a rotating electrode 6 provided in the rotary electrode 6; a computing unit 7 that calculates the amount of water required to maintain the water content of dehydrated sludge constant from the current value measured by the rotating electrode 6; and the computing unit 7.
Water supply control valve 8 that adjusts the amount of water supplied by a signal from
and a water supply pipe 11 that supplies water to the upstream side of the screw 2.

このような構成において、搬送コンベア9で搬送された
脱水汚泥10は、ホッパ1に貯溜され、スクリュー2の
回転により汚泥圧送ポンプ3に送りこまれる。この際、
汚泥圧送ポンプ3の入口側に設置された回転型FiiA
6により定電圧電解電流が測定されて演算器7に入力さ
れる。演算器7では入力された電流値から脱水汚泥の含
水率が一定となるように水供給量が算出され、その信号
により水供給調節弁8の開度が調節され、水供給管11
の先端部(ノズルまたは孔あき管等)からスクリュー2
の前流側の脱水汚泥中に水が供給される。
In such a configuration, the dewatered sludge 10 transported by the transport conveyor 9 is stored in the hopper 1 and fed into the sludge pump 3 by rotation of the screw 2. On this occasion,
Rotary FiiA installed on the inlet side of the sludge pump 3
6 measures the constant voltage electrolytic current and inputs it to the calculator 7. The arithmetic unit 7 calculates the water supply amount from the input current value so that the water content of the dehydrated sludge is constant, and the opening degree of the water supply control valve 8 is adjusted based on the signal, and the water supply pipe 11 is
Screw 2 from the tip (nozzle or perforated pipe, etc.)
Water is supplied into the dewatered sludge on the upstream side of the sludge.

一方、汚泥圧送ポンプ3で圧送された脱水汚泥は圧送ラ
イン5を経て焼却炉に投入され燃焼される。
On the other hand, the dehydrated sludge pumped by the sludge pump 3 is fed into the incinerator via the pumping line 5 and burned.

汚泥圧送ポンプ3で圧送するのに好適な脱水汚泥の含水
率は、高分子添加剤が添加された下水汚泥では、通常、
78%〜90%の範囲である。
The moisture content of dehydrated sludge suitable for pumping with the sludge pump 3 is usually as follows for sewage sludge to which a polymer additive has been added.
It is in the range of 78% to 90%.

このように、上記した特定の回転電極を用いて試料中の
電解電流値を連続して測定し、該電流値が一定範囲とな
るように水を供給することにより、含水率が一定である
脱水汚泥を汚泥圧送ポンプに供給することが可能となる
In this way, by continuously measuring the electrolytic current value in the sample using the above-mentioned specific rotating electrode and supplying water so that the current value is within a certain range, dehydration with a constant water content can be achieved. It becomes possible to supply sludge to the sludge pump.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、陰極と陽極が1IIIIfi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ること
により、汚泥中の水分の電解電流値を迅速にほとんどリ
アルタイムで測定することができ、該電流値が一定範囲
となるように水の供給量を算出して脱水汚泥に水を供給
し、汚泥中の含水率を一定範囲に保持して圧送ポンプに
供給することができる。そしてこれにより安定した汚泥
圧送ポンプの運転が可能となり、また圧送された汚泥を
焼却炉で燃焼させる際にも安定した燃焼が可能となる。
According to the present invention, by using a rotating electrode in which a cathode and an anode are provided in a rotating terminal in parallel with an interval of 1IIIfi or less, the electrolytic current value of water in sludge can be rapidly measured almost in real time, Water can be supplied to the dehydrated sludge by calculating the amount of water supplied so that the current value is within a certain range, and the sludge can be supplied to the pressure pump while maintaining the water content in the sludge within a certain range. This enables stable operation of the sludge pump, and also enables stable combustion of the pumped sludge in the incinerator.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の一実施例を示す脱水汚泥の供給装置
の構成図、第2図は、第1図で用いた回転電極の斜視図
である。 ■・・・ホッパ、2・・・スクリュー、3・・・汚泥圧
送ポンプ、4・・・モータ、5・・・圧送ライン、6・
・・回転電極、7・・・演算器、8・・・水供給調節弁
、9・・・搬送コンベア、lO・・・脱水汚泥、11・
・・水供給管、12・・・陰極、13・・・陽極、14
・・・給電ブラシ、15・・・集電リンク、16・・・
絶縁部。
FIG. 1 is a block diagram of a dewatered sludge supply device showing one embodiment of the present invention, and FIG. 2 is a perspective view of a rotating electrode used in FIG. 1. ■... Hopper, 2... Screw, 3... Sludge pressure pump, 4... Motor, 5... Force feeding line, 6...
...Rotating electrode, 7...Arithmetic unit, 8...Water supply control valve, 9...Transport conveyor, lO...Dehydrated sludge, 11.
...Water supply pipe, 12...Cathode, 13...Anode, 14
...Power supply brush, 15...Current collection link, 16...
Insulation section.

Claims (1)

【特許請求の範囲】[Claims] (1)ホッパに貯溜された汚泥を汚泥圧送ポンプにより
圧送するに際し、該汚泥圧送ポンプの入口側の汚泥中に
、少なくとも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汚泥圧送ポンプの前流
側の汚泥中に水を供給することを特徴とする汚泥の圧送
方法。
(1) When the sludge stored in the hopper is pumped by the sludge pump, at least one pair of cathode and anode are provided in the rotating terminal in parallel with an interval of 1 mm or less in the sludge on the inlet side of the sludge pump. A rotating electrode is installed, a constant voltage is applied to the rotating electrode, an electrolytic current is measured, and water is supplied into the sludge on the upstream side of the sludge pump so that the measured value is within a certain range. A sludge pumping method characterized by:
JP14945390A 1990-06-07 1990-06-07 Pressure-sending method for sludge Pending JPH0442046A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14945390A JPH0442046A (en) 1990-06-07 1990-06-07 Pressure-sending method for sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14945390A JPH0442046A (en) 1990-06-07 1990-06-07 Pressure-sending method for sludge

Publications (1)

Publication Number Publication Date
JPH0442046A true JPH0442046A (en) 1992-02-12

Family

ID=15475455

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14945390A Pending JPH0442046A (en) 1990-06-07 1990-06-07 Pressure-sending method for sludge

Country Status (1)

Country Link
JP (1) JPH0442046A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07311140A (en) * 1994-05-17 1995-11-28 Ngk Insulators Ltd Method for measuring water content of pumped sludge, and disposal of sludge by incineration utilizing said method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07311140A (en) * 1994-05-17 1995-11-28 Ngk Insulators Ltd Method for measuring water content of pumped sludge, and disposal of sludge by incineration utilizing said method

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