JPH0550100A - Method for incinerating sludge mixed with high molecular flocculant - Google Patents
Method for incinerating sludge mixed with high molecular flocculantInfo
- Publication number
- JPH0550100A JPH0550100A JP21527591A JP21527591A JPH0550100A JP H0550100 A JPH0550100 A JP H0550100A JP 21527591 A JP21527591 A JP 21527591A JP 21527591 A JP21527591 A JP 21527591A JP H0550100 A JPH0550100 A JP H0550100A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- water
- incinerator
- water content
- supplied
- 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.)
- Withdrawn
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は高分子凝集剤添加汚泥の
焼却方法に関し、さらに詳しくは高分子凝集剤を含む汚
泥を焼却炉で安定に燃焼をすることができる高分子凝集
剤添加汚泥の焼却方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for incinerating a polymer flocculant-added sludge, and more particularly to a polymer flocculant-added sludge capable of stably burning sludge containing a polymer flocculant in an incinerator. Regarding incineration method.
【0002】[0002]
【従来の技術】排水処理設備や下水処理施設等から排出
される汚泥の処理方法のひとつとして、多段炉や流動炉
などの焼却炉で汚泥を焼却する方法が知られている。通
常、焼却の前の汚泥に適当な凝集剤が加えられ、脱水機
等で脱水し、含水率約80重量%の脱水汚泥とした後、
焼却炉に供給される。近年、凝集剤として、石灰等の無
機系凝集剤の代わりに高分子凝集剤が用いられており、
これによって得られる脱水汚泥(高分子汚泥)は、固形
分発熱量が高く、また含水率も約75重量%と低いた
め、多段炉においては、含水率の変化によって高分子汚
泥の燃焼が不安定となりやすく、例えば含水率が一定値
以下になると、不完全燃焼により未燃分が多く発生し、
また多段炉の上段で汚泥が自燃状態となるため除熱装置
や冷ガス循環装置の設置が必要であった。また流動炉に
おいても、含水率が低く発熱量の多い汚泥は自燃状態と
なりやすいため、燃焼空気冷却装置や冷却水散水装置な
どの設置が必要であった。2. Description of the Related Art As one of the methods for treating sludge discharged from wastewater treatment facilities, sewage treatment facilities, etc., there is known a method of incinerating sludge in an incinerator such as a multistage furnace or a fluidized furnace. Usually, a suitable flocculant is added to the sludge before incineration, and the sludge is dehydrated with a dehydrator to obtain dehydrated sludge with a water content of about 80% by weight.
Supplied to the incinerator. In recent years, polymer flocculants have been used as flocculants instead of inorganic flocculants such as lime,
The dehydrated sludge (polymer sludge) thus obtained has a high solid content calorific value and a low water content of about 75% by weight. Therefore, in a multi-stage furnace, combustion of the polymer sludge becomes unstable due to changes in water content. If the water content falls below a certain value, a large amount of unburned components will be generated due to incomplete combustion.
Moreover, since sludge becomes a self-combustion state in the upper stage of the multistage furnace, it was necessary to install a heat removal device and a cold gas circulation device. Also in the fluidized reactor, since sludge with a low water content and high calorific value is likely to be in a self-combustion state, it was necessary to install a combustion air cooling device, a cooling water sprinkling device, and the like.
【0003】従来、焼却炉に供給する汚泥の含水率は、
遠紫外線を利用した自動水分計などで水分測定をして調
整を行っていたが、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
測定ができず、汚泥の性状が急変した場合には追従する
ことができなかった。Conventionally, the water content of sludge supplied to an incinerator is
The water content was adjusted by using an automatic moisture meter that uses far-ultraviolet rays, and this adjustment was made by drying the sampled sludge and measuring it by the weight drying method. Since sampling was required, continuous measurement was not possible and it was not possible to follow up when the properties of sludge suddenly changed.
【0004】[0004]
【発明が解決しようとする課題】本発明の目的は、前記
従来技術の問題を解決し、高分子凝集剤添加汚泥を焼却
炉に供給し、安定燃焼させて焼却することができる高分
子凝集剤添加汚泥の焼却方法を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art and to supply a polymer coagulant-added sludge to an incinerator for stable combustion and incineration. It is to provide a method for incinerating added sludge.
【0005】[0005]
【課題を解決するための手段】本発明者らは、上記目的
を達成するため、先に出願した回転電極(特願平2−9
8376号)を汚泥の含水率測定に適用して汚泥の性状
に追従し、かつ連続的な汚泥の含水率調整を行うことに
より、焼却炉における安定した汚泥の焼却をすることが
できることを見出し、本発明に到達した。SUMMARY OF THE INVENTION In order to achieve the above-mentioned object, the inventors of the present invention have proposed a rotating electrode previously applied (Japanese Patent Application No. 2-9).
8376) was applied to the measurement of the water content of sludge to follow the properties of the sludge, and by continuously adjusting the water content of the sludge, it was found that stable sludge incineration in an incinerator can be achieved. The present invention has been reached.
【0006】本発明は、高分子凝集剤添加汚泥を焼却炉
に供給して焼却するに際し、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、上記汚泥中に設置し、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の水分を調整した後、焼却炉に供
給することを特徴とする高分子凝集剤添加汚泥の焼却方
法に関する。According to the present invention, when supplying sludge containing a polymer coagulant to an incinerator for incineration, at least a pair of cathode and anode are provided with rotating electrodes provided in parallel with rotating terminals at intervals of 1 mm or less. It is installed in sludge, a constant voltage is applied to the rotary electrode to measure an electrolysis current, and after adjusting the water content of the sludge so that the measured value falls within a predetermined range, the sludge is supplied to an incinerator. The present invention relates to a method for incinerating sludge containing a polymer flocculant.
【0007】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.
75〜0.1mm、より好ましくは0.5〜0.3mm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
層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。The rotating electrode used in the present invention has at least one pair of cathode and anode of 1 mm or less, preferably 0.
The rotating terminals are provided in parallel at intervals of about 75 to 0.1 mm, more preferably about 0.5 to 0.3 mm. By installing the cathode and anode parallel to the rotary terminal at intervals of 1 mm or less, the fixed electrode is not installed in the sample, and the amount of water in the sample is not restricted by the sample in which the diffusion layer is easily obtained. Since a proportional and stable electrolytic current can be generated, the amount of water can be calculated from this current value. Further, by using such a rotating electrode, it is possible to prevent the adhesion of sludge to the electrode surface,
It enables continuous current measurement. When calculating the water concentration from the electrolysis current value, it is preferable to perform temperature correction in order to improve the measurement accuracy.
【0008】以下、本発明を図面により説明する。The present invention will be described below with reference to the drawings.
【0009】[0009]
【実施例】図1は、本発明の一実施例を示す多段焼却炉
の汚泥供給装置の説明図である。図1において、多段焼
却炉の汚泥供給装置は、汚泥を定量して供給する定量供
給槽5と、該定量供給槽5から排出された汚泥を搬送し
て多段焼却炉1に投入するベルトコンベア3および投入
スクリュー2と、上記ベルトコンベア3上の汚泥に設置
された回転電極6と接続する水分計4と、該水分計4で
測定された信号により汚泥の含水率を一定するための水
量を算出する演算器7と、該演算器7からの信号に基づ
いて散布する水の量を調節する水供給調節弁8とからな
る。EXAMPLE FIG. 1 is an explanatory view of a sludge supply device for a multistage incinerator showing an example of the present invention. In FIG. 1, a sludge supply device for a multi-stage incinerator comprises a constant amount supply tank 5 for supplying a fixed amount of sludge, and a belt conveyor 3 for conveying the sludge discharged from the constant amount supply tank 5 and introducing it into the multi-stage incinerator 1. And a feeding screw 2, a moisture meter 4 connected to the rotary electrode 6 installed in the sludge on the belt conveyor 3, and a signal measured by the moisture meter 4 to calculate the amount of water for keeping the moisture content of the sludge constant. And a water supply control valve 8 that adjusts the amount of water to be sprayed based on a signal from the calculator 7.
【0010】このような構成において、定量供給槽5内
の汚泥は、ベルトコンベア3に一定量に調節されて排出
され、投入スクリュー2に搬送されて該投入スクリュー
2によって多段焼却炉1の頂部から炉に供給され、焼却
される。一方、ベルトコンベア3上の汚泥に挿入された
回転電極6により連続的に汚泥の定電圧電解電流が測定
されて水分計4を経て演算器7に入力され、ここで汚泥
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
9の先端部から定量供給槽5内に水が散布される。In such a construction, the sludge in the fixed amount supply tank 5 is discharged to the belt conveyor 3 after being adjusted to a certain amount, conveyed to the feeding screw 2, and then fed by the feeding screw 2 from the top of the multistage incinerator 1. It is supplied to the furnace and incinerated. On the other hand, the constant voltage electrolysis current of the sludge is continuously measured by the rotary electrode 6 inserted in the sludge on the belt conveyor 3 and is input to the calculator 7 through the moisture meter 4, where the water content of the sludge is constant. The water supply amount is calculated so that the opening degree of the water supply control valve 8 is adjusted by the signal, and water is sprayed from the tip of the water supply pipe 9 into the fixed amount supply tank 5.
【0011】多段炉に供給する汚泥は、通常、78〜8
0重量%に調整される。回転電極6の取りつけ位置は、
ベルトコンベア3に限定されず、例えば定量供給槽5や
投入スクリュー2内の汚泥に設置してもよい。また水の
散布する位置も定量供給槽5に限定されず、例えばベル
トコンベア3や投入スクリュー2でもよい。図2には図
1で用いた回転電極6の斜視図を示した。図2におい
て、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側部に接続する
集電ブラシ14および給電リング15とからなる。The sludge supplied to the multistage furnace is usually 78 to 8
Adjusted to 0% by weight. The mounting position of the rotating electrode 6 is
It is not limited to the belt conveyor 3, and may be installed, for example, in the sludge in the constant amount supply tank 5 or the charging screw 2. The position where the water is sprayed is not limited to the fixed amount supply tank 5, and may be, for example, the belt conveyor 3 or the charging screw 2. FIG. 2 shows a perspective view of the rotary electrode 6 used in FIG. In FIG. 2, the rotating electrode 6 has a pair of cathodes 12 and anodes 13 provided in parallel at intervals of 1 mm or less, and the cathodes 12 and 13 are fixed, and only the tips of these are exposed.
Insulating part 16 which insulates from other components, and the cathode 12
And an anode 13, and a current collecting brush 14 and a power feeding ring 15 for connecting the anode 13 to the power source and the meter side, respectively.
【0012】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、またくし型条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
以下とするのが好ましく、より好ましくは5mm程度であ
る。A noble metal such as platinum is used as the material forming the cathode and the anode, and copper, SUS or the like can be used as the cathode. The exposed positions of the cathode 12 and the anode 13 are provided at the bottom of the rotary electrode 6, but they may be provided at the side or the comb-shaped electrode. Insulation part 16
As the resin, a resin such as an epoxy resin, a vinyl chloride resin, a phenol resin, or ceramics is used. From the viewpoint of measurement accuracy, the length of the electrode is preferably short, 20 to 10 mm.
The thickness is preferably the following, and more preferably about 5 mm.
【0013】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
が一定である汚泥を多段焼却炉に供給することができる
ため、安定した汚泥の燃焼が可能となる。同様の方法を
流動炉に採用しても同様の効果を得ることができる。In this way, the electrolytic current value in the sample is continuously measured using the above-mentioned specific rotating electrode, and water is supplied so that the current value falls within a certain range, whereby the water content becomes constant. Since it is possible to supply the sludge to the multi-stage incinerator, it is possible to stably burn the sludge. The same effect can be obtained even if the same method is adopted in the flow furnace.
【0014】[0014]
【発明の効果】本発明によれば、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る
ことにより、汚泥中の水分の電解電流値を迅速かつ連続
的に測定し、該電流値に基づいて汚泥の含水率を一定に
調節することができるため、焼却炉における汚泥の自燃
状態を防止して安定な汚泥燃焼を行うことができるとと
もに、不完全燃焼による未燃分の発生を少なくすること
ができる。According to the present invention, the electrolytic current value of water in sludge can be measured rapidly and continuously by using the rotary electrode in which the cathode and the anode are parallel to each other at intervals of 1 mm or less on the rotary terminal. However, since the water content of the sludge can be adjusted to a constant value based on the current value, it is possible to prevent the self-combustion state of the sludge in the incinerator and perform stable sludge combustion, as well as unburned due to incomplete combustion. The generation of minutes can be reduced.
【図1】図1は本発明の一実施例を示す多段焼却炉の汚
泥供給装置の説明図である。FIG. 1 is an explanatory view of a sludge supply device for a multistage incinerator showing an embodiment of the present invention.
【図2】図2は図1で用いた回転電極の斜視図である。
1…多段焼却炉、2…投入スクリュー、3…ベルトコン
ベア、4…水分計、5…定量供給槽、6…回転電極、7
…演算器、8…水供給調節弁、9…水供給管、12…陰
極、13…陽極、14…集電ブラシ、15…給電リン
グ、16…絶縁部。FIG. 2 is a perspective view of the rotary electrode used in FIG.
1 ... Multi-stage incinerator, 2 ... Input screw, 3 ... Belt conveyor, 4 ... Moisture meter, 5 ... Fixed amount supply tank, 6 ... Rotating electrode, 7
... arithmetic unit, 8 ... water supply control valve, 9 ... water supply pipe, 12 ... cathode, 13 ... anode, 14 ... collector brush, 15 ... power supply ring, 16 ... insulation part.
Claims (1)
て焼却するに際し、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、上記汚泥中に設置し、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
うに前記汚泥の水分を調整した後、焼却炉に供給するこ
とを特徴とする高分子凝集剤添加汚泥の焼却方法。1. When supplying sludge containing a polymer flocculant to an incinerator for incineration, at least one pair of cathode and anode are provided with rotating electrodes parallel to each other at intervals of 1 mm or less on a rotating terminal, and Is installed in the rotary electrode, a constant voltage is applied to the rotating electrode to measure an electrolytic current, and the water content of the sludge is adjusted so that the measured value falls within a certain range, and then the sludge is supplied to an incinerator. Incineration method of sludge containing molecular coagulant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21527591A JPH0550100A (en) | 1991-08-27 | 1991-08-27 | Method for incinerating sludge mixed with high molecular flocculant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21527591A JPH0550100A (en) | 1991-08-27 | 1991-08-27 | Method for incinerating sludge mixed with high molecular flocculant |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0550100A true JPH0550100A (en) | 1993-03-02 |
Family
ID=16669618
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21527591A Withdrawn JPH0550100A (en) | 1991-08-27 | 1991-08-27 | Method for incinerating sludge mixed with high molecular flocculant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0550100A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013129199A1 (en) * | 2012-02-29 | 2013-09-06 | 三菱マテリアル株式会社 | Sludge treatment facility |
-
1991
- 1991-08-27 JP JP21527591A patent/JPH0550100A/en not_active Withdrawn
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2013129199A1 (en) * | 2012-02-29 | 2013-09-06 | 三菱マテリアル株式会社 | Sludge treatment facility |
JP2013176738A (en) * | 2012-02-29 | 2013-09-09 | Mitsubishi Materials Corp | Sludge treatment facility |
CN104136382A (en) * | 2012-02-29 | 2014-11-05 | 三菱综合材料株式会社 | Sludge treatment facility |
AU2013227605B2 (en) * | 2012-02-29 | 2015-10-08 | Mitsubishi Ube Cement Corporation | Sludge disposal facility |
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Legal Events
Date | Code | Title | Description |
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A300 | Withdrawal of application because of no request for examination |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19981112 |