JPH0478481A - Method and device for quality control of coal ash - Google Patents

Method and device for quality control of coal ash

Info

Publication number
JPH0478481A
JPH0478481A JP2189848A JP18984890A JPH0478481A JP H0478481 A JPH0478481 A JP H0478481A JP 2189848 A JP2189848 A JP 2189848A JP 18984890 A JP18984890 A JP 18984890A JP H0478481 A JPH0478481 A JP H0478481A
Authority
JP
Japan
Prior art keywords
silo
coal ash
ash
fine powder
coal
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.)
Granted
Application number
JP2189848A
Other languages
Japanese (ja)
Other versions
JPH0563239B2 (en
Inventor
Noboru Kuroda
昇 黒田
Akira Saji
佐治 明
Hayamizu Ito
伊東 速水
Shuhei Tatsumi
巽 修平
Taisuke Shibata
泰典 柴田
Yasushi Takahashi
泰 高橋
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.)
Chubu Electric Power Co Inc
Kawasaki Heavy Industries Ltd
Original Assignee
Chubu Electric Power Co Inc
Kawasaki Heavy Industries 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 Chubu Electric Power Co Inc, Kawasaki Heavy Industries Ltd filed Critical Chubu Electric Power Co Inc
Priority to JP2189848A priority Critical patent/JPH0478481A/en
Publication of JPH0478481A publication Critical patent/JPH0478481A/en
Publication of JPH0563239B2 publication Critical patent/JPH0563239B2/ja
Granted legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PURPOSE:To confirm the suitability of a quality of a coal ash for shipment and to make unmanned control through day and night continuously available by automatically sampling a coal ash generated from the outlet of electrostatic precipitater to the inlet of the coal ash silo and automatically analyzing the ash with the analytical instruments. CONSTITUTION:The coal ash is sampled automatically from the outlets of the electrostatic precipitaters 1, 1a to the inlets of the silos 3, 4, and this coal ash is packed automatically into a capsule and pneumatically transferred to an analysis room 25 and executing automatic analysis by the analytical instruments 17, 18 and whether coal ash in electrostatic precipitaters 1, 1a or relaying tank 2 is sent to the recovery silo 4 or the waste ash silo 3 is judged. From the result of the property analysis analyzed automatically by analytical instruments 17, 18, the quality of the coal ash for shipment is adjusted by adjusting the condition of the classification treatment by the coal ash classifier 7 in the recovery silo 4. Additionally, referring to the analytical result obtained by automatic analysis using analytical instruments 17, 18, the suitability of the quality of the coal ash in a fine powder silo 6 is ascertained before shipment.

Description

【発明の詳細な説明】 〔産業上の利用分野] 本発明は、セメント混和材等として利用されている品質
の優れた石炭灰を、効率よく、かつ、より多く回収する
とともに、品質をきめこまかく管理する方法及び装置、
詳しくは、石炭焚きボイラから発生する石炭灰を自動サ
ンプリングして、分析l!屋まで空気搬送し、分析装置
で自動分析を行うことにより、石炭灰品質の良否の判断
、分級装置のコントロールによる品質の調整、出荷用石
炭灰品質が適正であることの見定めを行う石炭灰品質管
理方法及び装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention efficiently recovers a large amount of high-quality coal ash, which is used as a cement admixture, etc., and also carefully controls the quality. method and apparatus for
For more information, see Automatic sampling and analysis of coal ash generated from coal-fired boilers! Coal ash quality is determined by air transporting it to the warehouse and automatically analyzing it with an analyzer to determine whether the quality of coal ash is good or bad, adjust the quality by controlling the classification device, and determine whether the quality of coal ash for shipping is appropriate. This invention relates to a management method and device.

〔従来の技術〕[Conventional technology]

従来、石炭焚きボイラの電気集塵機で捕集された石炭灰
は、中継タンクを介して、又は介さずに回収用サイロ又
は捨て灰用サイロに空気搬送され、回収用サイロの灰は
分級装置に導かれて粗粉と細粉とに分級され、粗粉は粗
粉サイロに、細粉は細粉サイロに投入される灰処理方法
が一般に行われている。
Conventionally, coal ash collected by an electrostatic precipitator of a coal-fired boiler is air-conveyed to a recovery silo or a waste ash silo with or without a relay tank, and the ash in the recovery silo is led to a classification device. A commonly used ash processing method is to separate the ash into coarse powder and fine powder, with the coarse powder being charged into a coarse powder silo and the fine powder into a fine powder silo.

そして、現在、石炭灰はセメン1混和材用等として約3
0%利用されている。その石炭灰を分析する場合は、電
気集塵機下のデイフユーザフィーダ部に設けたバルブを
手動操作して、少量の石炭灰をサンプリングし、分析建
屋まで車又は徒歩で運び、手動操作にて分析を行い、品
質が適正であれば、電気集塵機の石炭灰を回収用サイロ
に搬送し、回収している。
Currently, coal ash is used as an admixture for cement 1, etc.
0% used. When analyzing the coal ash, manually operate the valve installed in the diffuser feeder section under the electrostatic precipitator to sample a small amount of coal ash, transport it by car or foot to the analysis building, and analyze it manually. If the quality is appropriate, the coal ash from the electrostatic precipitator is transported to a collection silo and collected.

また、出荷用の石炭灰品質については、出荷直前に回収
用サイロ、又は細粉サイロの下部にあるロータリフィー
ダ下より少量をサンプリングし、分析i!屋まで車又は
徒歩で運び、手動操作にて分析を行い、品質が適正であ
るかを見定めている。
Regarding the quality of coal ash for shipping, just before shipping, a small amount is sampled from below the rotary feeder at the bottom of the collection silo or the fine powder silo, and analyzed by i! The products are transported by car or on foot to the store, where they are manually analyzed to determine whether the quality is appropriate.

〔発明が解決しようとする課題] 従来の石炭灰品質管理方法は、石炭灰の利用率が低い場
合1発電所規模が小さい場合、使用石炭種類が少ない場
合、ボイラ負荷変動が少ない場合等の条件が整えば、昼
間のみに人手をかけて対応可能である。しかしながら、
最近の石炭焚きボイラの発電所においては、大型化、多
種類の石炭の使用、1日数回のボイラ負荷変動等により
、品質の優れた石炭灰を効率よく、かつより多く回収す
るには、石炭灰の品質管理を昼夜連続して行う必要があ
り、従来の方法では困難となっている。
[Problems to be solved by the invention] Conventional coal ash quality control methods are difficult to solve under conditions such as when the utilization rate of coal ash is low, when the scale of a single power plant is small, when there are few types of coal used, when there are few boiler load fluctuations, etc. Once this is in place, it will be possible to respond by manpower only during the day. however,
Modern coal-fired boiler power plants have become larger, use more types of coal, and fluctuate the boiler load several times a day. Ash quality control must be carried out continuously day and night, which is difficult with conventional methods.

本発明は、上記の点に鑑みなされたもので、石炭焚きボ
イラから発生する石炭灰を、電気集塵機出口から石炭灰
サイロ入口までの間で自動サンプリングし、カプセルに
入れて分析建屋まで空気搬送し、分析装置で自動分析を
行うことにより、電気集塵機の石炭灰、又は中継タンク
の石炭灰品質の良否の判断、分級装置の調整による品質
の調整を行うとともに、分級装置の細粉出口から細粉号
イロ入口までの間す自動サンプリングし、カプセルに入
れて分析建屋まで空気搬送し、分析装置で自動分析を行
うことにより、出荷用石炭灰品質が適正であることを見
定めることのできる昼夜連続無人運転の可能な石炭灰品
質管理方法を折倒することを目的とするものである。
The present invention was developed in view of the above points, and it automatically samples coal ash generated from a coal-fired boiler between the outlet of an electrostatic precipitator and the entrance of a coal ash silo, puts it in a capsule, and transports it by air to an analysis building. By performing automatic analysis with an analyzer, we can judge whether the quality of coal ash in the electrostatic precipitator or relay tank is good or bad, adjust the quality by adjusting the classification device, and collect fine powder from the fine powder outlet of the classification device. An unmanned system running day and night that can determine whether the quality of coal ash for shipping is appropriate by automatically sampling all the way to the entrance of No. 1, putting it in a capsule, pneumatically transporting it to the analysis building, and automatically analyzing it with an analyzer. The aim is to develop an operational coal ash quality control method.

〔課題を解決するための手段及び作用〕」二記の目的を
達成するために、請求項1の石炭灰品質管理方法は、図
面に示すように、石炭焚きボイラの電気集塵機1.1a
捕隼灰を、中継タンク2を介し7て、又&よ介さずに回
収用サイロ4又は捨て天用号“イロ3に空気搬送し、回
収用クイ口4の灰を分級装置7に導いて粗粉と細粉とに
分級し、粗粉を粗粉サイロ5に、細粉を細粉サイロ乙に
投入する灰処理方法において、 電気集塵機1.1a出口からサイロ3.4人口までの間
で石炭灰を自動サンプリングし、この石炭灰をカプセル
に自動充填して分析建屋25まで空気搬送し、分析装!
+7.18で自動分析を行い、その性状分析結果より、
電気年産Il+、1aの石炭灰又は中継タンク20石炭
灰を回収用サイロ4に送るか、捨て灰用サイロ3に送る
かを判断することを特徴としている。
[Means and operations for solving the problem] In order to achieve the second object, the coal ash quality control method according to claim 1, as shown in the drawing, uses an electrostatic precipitator 1.1a of a coal-fired boiler.
The captured ash is air-transferred to a collection silo 4 or a disposal tank 3 through a relay tank 2 7, and the ash from the collection pipe opening 4 is guided to a classification device 7. In the ash processing method of classifying coarse powder and fine powder and feeding the coarse powder into coarse powder silo 5 and the fine powder into fine powder silo B, the ash between the electrostatic precipitator 1.1a exit and silo 3.4 population is Coal ash is automatically sampled, this coal ash is automatically filled into capsules, and transported by air to analysis building 25, where it is loaded into the analysis equipment!
Automatic analysis was performed at +7.18, and from the property analysis results,
It is characterized in that it is determined whether to send the coal ash of electric annual production Il+, 1a or the relay tank 20 coal ash to the recovery silo 4 or to the waste ash silo 3.

また、請求項2の方法は、石炭焚きボイラの電気集11
機1.1a捕集灰を、中継タンク2を介して、又は介さ
ずに回収用サイロ4又は捨て灰用サイロ3に空気搬送し
、回収用サイロ4の灰を分級装置7に導いて粗粉と細粉
とに分級し、粗粉を粗粉サイロ5に、細粉を細粉サイロ
6に投入する灰処理方法において、 電気集塵機1.1a出「】からサイロ、3.4人「]ま
での間で石炭灰を自動サンプリングし、この石炭灰をカ
プセルに自動充填して分析建屋25まで空気搬送し、分
析装置17.18で自動分析を行い、その性状分析結果
より、回収用サイロ4の石炭灰の分級装置7による分級
操作条件を調整して、出荷用石炭灰の品質を調整するこ
とを特徴としている。
Further, the method according to claim 2 provides an electrical collector 11 of a coal-fired boiler.
Machine 1.1a Collected ash is pneumatically conveyed to a recovery silo 4 or a waste ash silo 3 via a relay tank 2 or not, and the ash in the recovery silo 4 is guided to a classification device 7 to be divided into coarse particles. In the ash processing method, which separates coarse powder into coarse powder silo 5 and fine powder into fine powder silo 6, from electrostatic precipitator 1.1a output "" to silo, 3.4 people "] Coal ash is automatically sampled between the chambers, this coal ash is automatically filled into capsules and transported by air to the analysis building 25, and automatically analyzed using the analyzers 17 and 18. Based on the property analysis results, the It is characterized in that the quality of coal ash for shipping is adjusted by adjusting the classification operation conditions by the coal ash classification device 7.

さらに7、請求項3の方法は、石炭焚きボイラの電気X
、W機1.1a浦集灰を、中継タンク2を介して、又は
介さずに回収用サイロ4又は捨て天用号イロ3に空気搬
送し、回収用サイロ4の灰を分級装置7に導いて粗粉と
細粉とに分級し、粗粉を粗粉サイロ5に、細粉を細粉サ
イロ6に投入する灰処理方法において、 分級装置7の細粉出口から細粉サイロ6人口までの間で
石炭灰を自動サンプリングし、この石炭灰をカプセルに
自動充填して分析建屋25まで空気搬送し、分析装W1
7.18で自動分析を行い、その性状分析結果より、細
粉サイロ乙の石炭灰の出荷までに性状が適正かを見定め
ることを特徴としている。
Furthermore, 7, the method of claim 3 provides an electric
, W machine 1.1a Ura collected ash is pneumatically conveyed to a collection silo 4 or a sacrificial tenyogo Iro 3 through or without a relay tank 2, and the ash in the collection silo 4 is guided to a classification device 7. In the ash processing method, the coarse powder is classified into coarse powder and fine powder, and the coarse powder is charged into the coarse powder silo 5 and the fine powder is charged into the fine powder silo 6. Coal ash is automatically sampled between
7.18, automatic analysis is performed, and based on the property analysis results, it is determined whether the properties of the coal ash in the fine powder silo B are appropriate before shipment.

請求項4の方法は、請求項1.2又は3の方法において
、自動サンプリングした石炭灰を、分析装置17.18
との連係のために一時貯蔵した後、カプセルに自動充填
することを特徴とするものである。
In the method of claim 4, in the method of claim 1.2 or 3, the automatically sampled coal ash is analyzed using an analyzer 17.18.
It is characterized by the automatic filling of capsules after temporary storage for connection with the capsules.

そして、請求項5の石炭灰品質管理装置は、石炭焚きボ
イラの電気集塵機1.1aの下部に、気流輸送管23.
23aを介して回収用サイロ4及び捨て灰用サイロ3を
接続し、この回収用サイロ4の下部に分級装置7を介し
2て粗粉サイロ5及び細粉サイロ6を接続した灰処理装
置において2電気集m機1.1a下部若しくは気流輸送
管23.23a、、及び分級装W7の細粉出口若しくは
細粉サイロ6人口に自動サンプリング装W8.8a、1
1を接続し、該自動サンプリング装置と分析装置I7.
18とをサンプル搬送管26を介して接続したことを特
徴としている。
The coal ash quality control device according to the fifth aspect of the present invention includes an air flow transport pipe 23.
In the ash processing device, a collection silo 4 and a waste ash silo 3 are connected via a ash processing device 23a, and a coarse powder silo 5 and a fine powder silo 6 are connected to the lower part of the recovery silo 4 via a classifier 7. An automatic sampling device W8.8a, 1 is installed at the lower part of the electric collector 1.1a or the air flow transport pipe 23.23a, and at the fine powder outlet of the classifier W7 or the fine powder silo 6 population.
1, and the automatic sampling device and analyzer I7.
18 are connected to each other via a sample transport tube 26.

分析装置17.18は、通常は1.一方が強熱減量測定
装置、他方が粒度分布測定装置である6自動サンプリン
グ装置8.8a、11としては、粉体の輸送管内に1又
は複数の孔を穿設したサンプリングバイブを挿入し、こ
のサンプリングバイブを介して粉体を粉体捕集容器内に
吸引するようにした構造のものが用いられる。
Analyzers 17.18 typically have 1. One is an ignition loss measuring device and the other is a particle size distribution measuring device 6 Automatic sampling device 8.8a, 11 is a sampling vibrator with one or more holes drilled into the powder transport pipe. A structure is used in which powder is sucked into a powder collection container through a sampling vibrator.

カプセルセンディング装置l0110a、13としては
、−時貯蔵装置9.9a、12からの石炭灰を円筒状の
カプセル内に入れた後、カプセルを約25度回転して(
傾斜させて)ねじ込み式の蓋をし、反転させて加圧空気
を用いて石炭灰の入ったカプセルをカプセルレシービン
グ装置16に送るように構成した公知の構造のものが用
いられる。これらの操作は、すべて自動的に行われる。
As the capsule sending device 10110a, 13, after putting the coal ash from the storage device 9.9a, 12 into the cylindrical capsule, the capsule is rotated about 25 degrees (
A known construction is used which is configured to have a screw-on lid (tilted) and be inverted to deliver the capsule containing coal ash to the capsule receiving device 16 using pressurized air. All these operations are performed automatically.

カプセルの材質として、石炭灰の付着が少ない金属が用
いられ、特に黄銅が好適である。
As the material of the capsule, a metal to which less coal ash adheres is used, and brass is particularly suitable.

−時貯蔵装置9.9a、12.28としては、回転円盤
の周方向に底がエアシリンダー等にて開閉する円筒容器
が複数個接続され、円筒容器の底を閉めた状態で回転円
盤の受取位置にて石炭灰を受け、排出時には回転円盤を
回転させて円筒容器を排出位1に持っていき、エアシリ
ンダー等にて底を開けることによって石炭灰を排出する
ように構成した公知の構造のものが用いられる。
- As the time storage devices 9.9a and 12.28, a plurality of cylindrical containers are connected in the circumferential direction of the rotating disk, the bottom of which opens and closes with an air cylinder, etc., and the rotating disk is received with the bottom of the cylindrical container closed. This is a known structure in which the cylindrical container is received at a position, and when it is discharged, a rotating disk is rotated to bring the cylindrical container to the discharge position 1, and the bottom is opened with an air cylinder or the like to discharge the coal ash. things are used.

カプセルレシービング装置i6としては、転換装W、1
4bで蓋が上にされたカプセルを受け、約25度回転し
て(傾斜させて)蓋を外し、反転させて石炭灰を二分割
装219に払い出し、その後、反転させて蓋をし、約2
5度回転させて(傾斜させて)加圧空気を用いてカプセ
ルセンディング装置10.10a、T:5に送るように
構成した公知の構造のものが用いられる。
As the capsule receiving device i6, conversion equipment W, 1
4b receives the capsule with the lid on top, rotates it about 25 degrees (tilts it), removes the lid, inverts it and discharges the coal ash into the two-part compartment 219, then inverts it, closes the lid, and removes the lid. 2
A known structure configured to rotate (tilt) 5 degrees and send pressurized air to the capsule sending device 10.10a, T:5 is used.

転換装置1[+4.14a、14bとしては、XTシリ
ンダー等の駆動装置にてパイプの方向を換え、別のバイ
ブと接続されるように構成した公知の構造のものが用い
られる。
As the conversion device 1[+4.14a, 14b, a known structure in which the direction of the pipe is changed by a drive device such as an XT cylinder and connected to another vibrator is used.

二分割装置19は、カプセルレシービング装置16から
払い出された石炭灰を、自動的に二分割して2台の分析
装置17.18へ供給する装置で、振動式の粉体供給機
に、6fi前後のピッチの溝が16個以上(偶数)開き
、これらの溝が交互に2つのンユートに振り分けられた
二分器(JIS M 8811で公知)を接続し、これ
らのシュートに、分析装置が故障時に作動する分配機を
接続したg置である。
The two-splitting device 19 is a device that automatically splits the coal ash discharged from the capsule receiving device 16 into two and supplies it to the two analyzers 17 and 18. At least 16 (even number) grooves are opened at the front and rear pitches, and a bisection device (known in JIS M 8811) is connected to which these grooves are alternately divided into two chutes, and these chutes are connected to This is a g position with a working distributor connected.

また、分級装置7としては、重力式、慣性力式、遠心力
式等の乾式の風力式のものが用いられる。
Further, as the classification device 7, a dry wind type type, such as a gravity type, an inertial force type, or a centrifugal force type, is used.

なお、通常は、第1図及び第2図に示すように、−時貯
蔵装置9.9a、12は自動サンプリング装W8.8a
、11の下流側に隣接して設けられるが、サンプリング
サイクルが長い場合には、第3図に示すように、−時貯
蔵装置27を分析装置I7.18の直前に設置するよう
に構成する。
Note that normally, as shown in FIGS. 1 and 2, the -time storage devices 9.9a and 12 are automatic sampling devices W8.8a.
, 11, but when the sampling cycle is long, the -time storage device 27 is arranged to be installed immediately before the analyzer I7.18, as shown in FIG.

本発明の方法及び装置により、つぎのような品質管理が
行われる。
The method and apparatus of the present invention perform the following quality control.

(1)  電気隻塵機灰の製品としての可否の判断:気
流輸送管23.23a又は電気集塵at、1aの下部か
ら灰を自動サンプリングした後、自動分析(強熱減量測
定、粒度分布測定)を行い、良質灰であれば、回収用サ
イロ4△、送る。
(1) Determining whether or not electric dust machine ash can be used as a product: After automatically sampling the ash from the lower part of the pneumatic transport pipe 23, 23a or the electrostatic precipitator at, 1a, automatic analysis (ignition loss measurement, particle size distribution measurement ), and if the ash is of good quality, send it to collection silo 4△.

(2)  電気集塵機灰の品質の調整度合の判断:気流
輸送管23.23m又は電気集rtxmr、1aの下部
から自動サンプリングした灰の平均粒径が適正値より外
れておれば、分級装置7の回転数を調整し、適正な平均
粒径とする。
(2) Judging the degree of adjustment of the quality of electrostatic precipitator ash: If the average particle size of the ash automatically sampled from the lower part of the airflow transport pipe 23.23m or the electrostatic precipitator rtxmr, 1a is outside the appropriate value, the classification device 7 Adjust the rotation speed to obtain an appropriate average particle size.

(3)  製品品質の保証精度の向上:分級装置7の細
粉回収ラインから自動サンプリングした後、自動分析を
行い、製品品質の保証精度を向上させる。
(3) Improving the accuracy of product quality assurance: After automatic sampling from the fine powder collection line of the classifier 7, automatic analysis is performed to improve the accuracy of product quality assurance.

したがって、石炭焚きボイラの発電所の大型化、多種類
の石炭の使用、1日数回のボイラ負荷変動等に対応でき
、品質の優れた石炭灰を効率よく、かつ、できる限り多
く回収することのできる石炭灰品質管理方法を擢供する
ことができる。また、本発明の方法では、多数のサンプ
リング及び分析が短時間で可能であるため、石炭灰品質
精度が高く、かつ、ボイラの燃焼状態の監視のハンクア
ソブが可能である。
Therefore, it is possible to cope with the increasing size of coal-fired boiler power plants, the use of multiple types of coal, and the fluctuation of boiler load several times a day, and to efficiently recover as much high-quality coal ash as possible. Coal ash quality control methods can be provided. Furthermore, in the method of the present invention, a large number of samplings and analyzes can be carried out in a short period of time, so that the quality of coal ash is highly accurate and the combustion state of the boiler can be monitored as a hunk.

C実施例〕 以下、図面を参照して本発明の好適な実施例を詳細に説
明する。ただしこの実施例に記載されている構成機器の
形状、その相対配置などは、とくに特定的な記載がない
限りは、本発明の範囲をそれらのみに限定する趣旨のも
のではなく、単なる説明例にすぎない。
C Embodiment] Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings. However, unless there is a specific description, the shapes of the components described in this example, their relative positions, etc. are not intended to limit the scope of the present invention to these, but are merely illustrative examples. Only.

実施例1 第1図は本発明の石炭灰品質管理装置の一実施例を示し
、中継タンク2を設置する場合である。
Embodiment 1 FIG. 1 shows an embodiment of the coal ash quality control apparatus of the present invention, in which a relay tank 2 is installed.

以下、70万に−の石炭火力発電所に、本発明の石炭灰
品質管理方法を通用した例を、第1図に基づいて説明す
る6 一例として、2基の電気集塵Il+、1aがらの気流輸
送管23.23aのA(又はC)の位置から、自動サン
プリング=ZS、8aで、−例として、16室よりなる
電気集塵s1.1aの代表的な2室の石炭灰を、各20
00m+ +サンプリングし、縮分して各2001とし
また後、余剰石炭灰は気流輸送管23.23aに戻し、
分析用石炭灰は一時貯蔵装置9.9aに保管し、分析装
置17 (強熱減量測定装置)、分析装置18(粒度分
布測定装置)の両方が測定可能となれば、−時貯蔵装置
1f9.9aの石炭灰をカプセルセンディング装置10
、IDaを用いてカプセルに入れ、ただちに、カプセル
レシービング装置t+6に空気搬送し、二分割装置19
に石炭灰を移し、分析装置1F17.18で分析を行う
An example in which the coal ash quality control method of the present invention was applied to a 700,000 coal-fired power plant will be explained below based on Figure 1.6 As an example, two electrostatic precipitators Il+ and 1a From position A (or C) of airflow transport pipe 23.23a, automatic sampling = ZS, 8a - As an example, coal ash from two representative chambers of electrostatic precipitator s1.1a consisting of 16 chambers is 20
After sampling 00m+ and reducing it to 2001 each, the excess coal ash is returned to the airflow transport pipe 23.23a,
The coal ash for analysis is temporarily stored in the storage device 9.9a, and when both the analysis device 17 (ignition loss measurement device) and the analysis device 18 (particle size distribution measurement device) become capable of measurement, the coal ash is temporarily stored in the storage device 1f9. Capsule sending device 10 for coal ash 9a
, into a capsule using IDa, and immediately pneumatically conveyed to the capsule receiving device t+6 and divided into two devices 19.
The coal ash is transferred to the tank and analyzed using an analyzer 1F17.18.

サンプリング灰の強2H量が各3wt%未満であれば、
電気集塵機1.1aの石炭灰、あるいは中継タンク2の
石炭灰を回収用サイロ4へ空気搬送し、強熱減量が各3
wt%以上であれば、捨て灰用サイロ3へ空気搬送する
If the amount of strong 2H in the sampled ash is less than 3wt%,
The coal ash in the electrostatic precipitator 1.1a or the coal ash in the relay tank 2 is conveyed by air to the collection silo 4, and the ignition loss is 3 for each.
If it is more than wt%, it is air conveyed to the silo 3 for waste ash.

また、2個のサンプリング灰合計で74μm以上粒子割
合が20%未満であれば1、回収用サイロ4の石炭灰を
製品とし1.20%以十であれば、分級操作にて74μ
m以上粒子割合に応して、分級装置7の回転数を調整し
て、細粉の74μm以」−粒子割合を20%未満とする
In addition, if the total particle ratio of the two sampled ash is 74 μm or more and less than 20%, then 1, and if the product is coal ash from recovery silo 4 and is 1.20% or more, then the classification operation
The rotational speed of the classifier 7 is adjusted according to the proportion of particles larger than 74 μm, so that the proportion of particles larger than 74 μm in the fine powder is less than 20%.

さらに、分級装置7の細粉輸送管のB(又はD)の位置
から、自動サンプリング装置11で石炭灰を200噺1
サンプリングし、−時貯蔵装置12に保管し、分析装置
17.18の両方が測定可能となれば、−時貯蔵装置1
2の石炭灰をカプセルセンディング装置13を用いてカ
プセルに入れ、ただちにカプセルレシービング装置16
に空気搬送し、二分割装置19に石炭灰を移し、分析装
置17.18で分析を行い、出荷用の細粉シイロ乙の石
炭灰の強熱減量が3wt%未満で、74μm以上粒子割
合が20%未満であることをfl!認する。
Furthermore, from the position B (or D) of the fine powder transport pipe of the classification device 7, the automatic sampling device 11 collects 200 pieces of coal ash.
When both of the analyzers 17 and 18 are able to sample, store in the -time storage device 12 and measure, the -time storage device 1
The coal ash from Step 2 is put into a capsule using the capsule sending device 13, and immediately transferred to the capsule receiving device 16.
The coal ash is transported by air to the bisecting device 19, and analyzed using the analyzer 17.18 to determine that the ignition loss of the fine powdered coal ash for shipping is less than 3 wt%, and the proportion of particles of 74 μm or more is fl that it is less than 20%! I approve.

以上の昼夜連続無人運転による石炭灰品質管理方法によ
り、品質の優れた石炭灰を効率よく、かつ、できる限り
多く回収することが可能となる。
The above-described coal ash quality control method using continuous unmanned operation day and night makes it possible to efficiently collect as much coal ash as possible with excellent quality.

なお、分級装置7としては、乾式遠心型のものを用いる
場合を示している。
In addition, as the classification device 7, the case where a dry centrifugal type device is used is shown.

第1図において、14.14a、14bは転換装置、1
5.20.20a、21.22は気流搬送用のブロワ、
24はエアスライダ、26はサンプル搬送管、27.2
7aは余剰石炭灰戻し管である。
In FIG. 1, 14.14a and 14b are conversion devices, 1
5.20.20a, 21.22 are blowers for airflow conveyance,
24 is an air slider, 26 is a sample transport tube, 27.2
7a is a surplus coal ash return pipe.

実施例2 本例は、第2図に示すように、中継タンクを用いないで
、電気集塵機1.1aがら気流搬送される石炭灰を、直
接、回収用サイロ4又は捨て灰用サイロ3に投入するよ
うに構成したものである。
Embodiment 2 In this example, as shown in Fig. 2, coal ash carried by airflow from the electrostatic precipitator 1.1a is directly fed into the recovery silo 4 or the waste ash silo 3 without using a relay tank. It is configured to do so.

他の構成は、実施例1と同様である。The other configurations are the same as in the first embodiment.

実施例3 本例は、第3図に示すように、サンプリングサイクルが
長い場合に適用するために、−時貯蔵装置28を分析装
置17.18の直前に設置し、自動サンプリング装置8
,8a、11の直後の一時貯蔵装置を省略するように構
成し、たちのである。
Embodiment 3 As shown in FIG. 3, in this example, in order to be applied when the sampling cycle is long, the -hour storage device 28 is installed immediately before the analyzer 17, 18, and the automatic sampling device 8 is installed.
, 8a, and 11, the temporary storage device is omitted.

他の構成は、実施例1又は実施例2と同様である。The other configurations are the same as in the first embodiment or the second embodiment.

〔発明の効果〕〔Effect of the invention〕

本発明は上記のように構成されているので、っぎのよう
な効果を奏する。
Since the present invention is configured as described above, it achieves the following effects.

(1)石炭灰品質の良否の判断1分級装置のコントロー
ルによる品質の調整、出荷用石炭灰品質が適正であるこ
との具足めにより、昼夜連続無人運転による石炭灰品質
管理を行うことができる。
(1) Determination of quality of coal ash 1 By adjusting the quality by controlling the classification device and ensuring that the quality of coal ash for shipping is appropriate, it is possible to control the quality of coal ash by continuous unmanned operation day and night.

(2)石炭火力発電所の大型化、多種類の石炭の使用、
1日数回のボイラ負荷変動等に対応でき、品質の優れた
石炭灰を効率よく、がっ、できる限り多く回収すること
ができる。
(2) Larger coal-fired power plants, use of multiple types of coal,
It can respond to boiler load fluctuations that occur several times a day, and can efficiently recover as much high-quality coal ash as possible.

(3)多数のサンプリング及び分析が短時間で可能であ
るため、石炭灰品質精度が高く、がっ、ボイラの燃焼状
態の監視のバックアップが可能である。
(3) Since a large number of samplings and analyzes can be performed in a short period of time, the quality of coal ash is highly accurate, and it is possible to back up the monitoring of the combustion status of the boiler.

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

第1図は本発明の石炭灰品質管理装置の一実施例を示す
システムフロー図、第2図及び第3図は本発明の装置の
他の実施例を示すンステムフロー図である。 A、B、C,D・・・石炭灰サンプリング位置、】、1
a・・・電気集塵機、2・・・中継タンク、3・・・捨
て灰用サイロ、4・・・回収用サイロ、5・・・粗粉サ
イロ、6・・・細粉サイロ、7・・・分級装置、8.8
a・・・自動サンプリング装置、9.9a・・・−時貯
蔵装置、10.10a・・・カプセルセンディング装置
、11・・・自動サンプリング装置、12・・・−時貯
蔵装置、13・・・カプセルセンディング装置、14、
+4a、+4b・・・転換装置、15・・・ブロワ、1
6・・・カプセルレシービング装置、17・・・分析装
置(強熱減量測定装置)、18・・・分析装置(粒度分
布測定装置)、19・・・二分割装置、20.20a、
21.22・・・ブロワ、23.23a・・・気流輸送
管、24・・・エアスライダ、25・・・分析建屋、2
6・・・サンプル搬送管、27.27a・・・余剰石炭
灰戻し管、28・・・−時貯蔵装置 出 願 人  川崎重工業株式会社 出 願 人  中部電力株式会社
FIG. 1 is a system flow diagram showing one embodiment of the coal ash quality control apparatus of the present invention, and FIGS. 2 and 3 are system flow diagrams showing other embodiments of the apparatus of the present invention. A, B, C, D... Coal ash sampling position, ], 1
a... Electrostatic precipitator, 2... Relay tank, 3... Silo for discarded ash, 4... Silo for collection, 5... Coarse powder silo, 6... Fine powder silo, 7...・Classifying device, 8.8
a...Automatic sampling device, 9.9a...-time storage device, 10.10a...capsule sending device, 11...automatic sampling device, 12...-time storage device, 13...・Capsule sending device, 14,
+4a, +4b... conversion device, 15... blower, 1
6... Capsule receiving device, 17... Analyzer (ignition loss measuring device), 18... Analyzer (particle size distribution measuring device), 19... Bisection device, 20.20a,
21.22...Blower, 23.23a...Air flow transport pipe, 24...Air slider, 25...Analysis building, 2
6...Sample transport pipe, 27.27a...Surplus coal ash return pipe, 28...-hour storage device Applicant: Kawasaki Heavy Industries, Ltd. Applicant: Chubu Electric Power Co., Ltd.

Claims (1)

【特許請求の範囲】 1 石炭焚きボイラの電気集塵機(1、1a)捕集灰を
、中継タンク(2)を介して、又は介さずに回収用サイ
ロ(4)又は捨て灰用サイロ(3)に空気搬送し、回収
用サイロ(4)の灰を分級装置(7)に導いて粗粉と細
粉とに分級し、粗粉を粗粉サイロ(5)に、細粉を細粉
サイロ(6)に投入する灰処理方法において、電気集塵
機(1、1a)出口からサイロ(3、4)入口までの間
で石炭灰を自動サンプリングし、この石炭灰をカプセル
に自動充填して分析建屋(25)まで空気搬送し、分析
装置(17、18)で自動分析を行い、その性状分析結
果より、電気集塵、(1、1a)の石炭灰又は中継タン
ク(2)の石炭灰を回収用サイロ(4)に送るか、捨て
灰用サイロ(3)に送るかを判断することを特徴とする
石炭灰品質管理方法。 2 石炭焚きボイラの電気集塵機(1、1a)捕集灰を
、中継タンク(2)を介して、又は介さずに回収用サイ
ロ(4)又は捨て灰用サイロ(3)に空気搬送し、回収
用サイロ(4)の灰を分級装置(7)に導いて粗粉と細
粉とに分級し、粗粉を粗粉サイロ(5)に、細粉を細粉
サイロ(6)に投入する灰処理方法において、電気集塵
機(1、1a)出口からサイロ(3、4)入口までの間
で石炭灰を自動サンプリングし、この石炭灰をカプセル
に自動充填して分析建屋(25)まで空気搬送し、分析
装置(17、18)で自動分析を行い、その性状分析結
果より、回収用サイロ(4)の石炭灰の分級装置(7)
による分級操作条件を調整して、出荷用石炭灰の品質を
調整することを特徴とする石炭灰品質管理方法。 3 石炭焚きボイラの電気集塵機(1、1a)捕集灰を
、中継タンク(2)を介して、又は介さずに回収用サイ
ロ(4)又は捨て灰用サイロ(3)に空気搬送し、回収
用サイロ(4)の灰を分級装置(7)に導いて粗粉と細
粉とに分級し、粗粉を粗粉サイロ(5)に、細粉を細粉
サイロ(6)に投入する灰処理方法において、分級装置
(7)の細粉出口から細粉サイロ(6)入口までの間で
石炭灰を自動サンプリングし、この石炭灰をカプセルに
自動充填して分析建屋(25)まで空気搬送し、分析装
置(17、18)で自動分析を行い、その性状分析結果
より、細粉サイロ(6)の石炭灰の出荷までに性状が適
正かを見定めることを特徴とする石炭灰品質管理方法。 4 自動サンプリングした石炭灰を、分析装置(17、
18)との連係のために一時貯蔵した後、カプセルに自
動充填することを特徴とする請求項1、2又は3記載の
石炭灰品質管理方法。 5 石炭焚きボイラの電気集塵機(1、1a)の下部に
、気流輸送管(23、23a)を介して回収用サイロ(
4)及び捨て灰用サイロ(3)を接続し、この回収用サ
イロ(4)の下部に分級装置(7)を介して粗粉サイロ
(5)及び細粉サイロ(6)を接続した灰処理装置にお
いて、電気集塵機(1、1a)下部若しくは気流輸送管
(23、23a)、及び分級装置(7)の細粉出口若し
くは細粉サイロ(6)入口に自動サンプリング装置(8
、8a、11)を接続し、該自動サンプリング装置と分
析装置(17、18)とをサンプル搬送管(26)を介
して接続したことを特徴とする石炭灰品質管理装置。
[Claims] 1. Collecting ash from an electrostatic precipitator (1, 1a) of a coal-fired boiler, with or without a relay tank (2), into a recovery silo (4) or a waste ash silo (3) The ash in the collection silo (4) is guided to the classifier (7) and classified into coarse powder and fine powder.The coarse powder is transferred to the coarse powder silo (5), and the fine powder is transferred to the fine powder silo (5). 6), coal ash is automatically sampled between the outlet of the electrostatic precipitator (1, 1a) and the entrance of the silo (3, 4), and this coal ash is automatically filled into a capsule and sent to the analysis building ( 25), automatic analysis is performed using analyzers (17, 18), and based on the property analysis results, the coal ash in (1, 1a) or the coal ash in the relay tank (2) is collected by electrostatic precipitator. A coal ash quality control method characterized by determining whether to send to a silo (4) or to a waste ash silo (3). 2 The ash collected by the electrostatic precipitator (1, 1a) of the coal-fired boiler is conveyed by air to the collection silo (4) or waste ash silo (3) via or without the relay tank (2), and collected. The ash in the silo (4) is led to the classifier (7) and classified into coarse powder and fine powder, and the coarse powder is fed into the coarse powder silo (5) and the fine powder is fed into the fine powder silo (6). In the processing method, coal ash is automatically sampled between the outlet of the electrostatic precipitator (1, 1a) and the entrance of the silo (3, 4), and this coal ash is automatically filled into a capsule and transported by air to the analysis building (25). , automatic analysis is performed using analyzers (17, 18), and based on the property analysis results, the coal ash classification device (7) in the recovery silo (4)
A coal ash quality control method characterized by adjusting the quality of coal ash for shipping by adjusting classification operation conditions. 3 The ash collected by the electrostatic precipitator (1, 1a) of the coal-fired boiler is conveyed by air to the collection silo (4) or waste ash silo (3) via or without the relay tank (2), and collected. The ash in the silo (4) is led to the classifier (7) and classified into coarse powder and fine powder, and the coarse powder is fed into the coarse powder silo (5) and the fine powder is fed into the fine powder silo (6). In the processing method, coal ash is automatically sampled between the fine powder outlet of the classification device (7) and the fine powder silo (6) entrance, and this coal ash is automatically filled into capsules and transported by air to the analysis building (25). A coal ash quality control method characterized in that automatic analysis is performed using analyzers (17, 18), and based on the property analysis results, it is determined whether the properties of the coal ash in the fine powder silo (6) are appropriate before shipment. . 4 The automatically sampled coal ash is analyzed using an analyzer (17,
18) The method for quality control of coal ash according to claim 1, 2 or 3, characterized in that the coal ash is automatically filled into capsules after being temporarily stored for cooperation with the coal ash. 5 A collection silo (
4) and a waste ash silo (3) are connected, and a coarse powder silo (5) and a fine powder silo (6) are connected to the lower part of this collection silo (4) via a classifier (7). In the device, an automatic sampling device (8) is installed at the lower part of the electrostatic precipitator (1, 1a) or the air flow transport pipe (23, 23a), and at the fine powder outlet of the classifier (7) or the fine powder silo (6) inlet.
, 8a, 11), and the automatic sampling device and the analysis device (17, 18) are connected via a sample conveyance pipe (26).
JP2189848A 1990-07-18 1990-07-18 Method and device for quality control of coal ash Granted JPH0478481A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2189848A JPH0478481A (en) 1990-07-18 1990-07-18 Method and device for quality control of coal ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2189848A JPH0478481A (en) 1990-07-18 1990-07-18 Method and device for quality control of coal ash

Publications (2)

Publication Number Publication Date
JPH0478481A true JPH0478481A (en) 1992-03-12
JPH0563239B2 JPH0563239B2 (en) 1993-09-10

Family

ID=16248210

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2189848A Granted JPH0478481A (en) 1990-07-18 1990-07-18 Method and device for quality control of coal ash

Country Status (1)

Country Link
JP (1) JPH0478481A (en)

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JP2011031207A (en) * 2009-08-04 2011-02-17 Chugoku Electric Power Co Inc:The Treatment system for ep ash, method for treating ep ash, and program for treating ep ash
JP2014048262A (en) * 2012-09-04 2014-03-17 Chugoku Electric Power Co Inc:The Coal ash sampling method
JP2016080203A (en) * 2014-10-10 2016-05-16 株式会社神戸製鋼所 Process of manufacture of low adhesion coal ash
WO2018168637A1 (en) * 2017-03-14 2018-09-20 株式会社トクヤマ Method for using fly ash
JPWO2018168637A1 (en) * 2017-03-14 2020-01-16 株式会社トクヤマ How to use fly ash
JP2021133325A (en) * 2020-02-28 2021-09-13 福島エコクリート株式会社 Quality control method for coal ash-mixed material

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