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JPS6349131B2 - - Google Patents
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JPS6349131B2 - - Google Patents

Info

Publication number
JPS6349131B2
JPS6349131B2 JP55162032A JP16203280A JPS6349131B2 JP S6349131 B2 JPS6349131 B2 JP S6349131B2 JP 55162032 A JP55162032 A JP 55162032A JP 16203280 A JP16203280 A JP 16203280A JP S6349131 B2 JPS6349131 B2 JP S6349131B2
Authority
JP
Japan
Prior art keywords
pulverized coal
coal
pulverized
particle size
pulverizer
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
Application number
JP55162032A
Other languages
Japanese (ja)
Other versions
JPS5786916A (en
Inventor
Yukinori Oono
Shoichi Masuko
Hirohiko Sakuyama
Naoaki Hotsuta
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi 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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP16203280A priority Critical patent/JPS5786916A/en
Publication of JPS5786916A publication Critical patent/JPS5786916A/en
Publication of JPS6349131B2 publication Critical patent/JPS6349131B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N15/00Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
    • G01N15/02Investigating particle size or size distribution

Landscapes

  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Feeding And Controlling Fuel (AREA)
  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】 この発明はボイラ等の燃焼装置に供給する粉砕
炭の濃度、粒径分布等を検知し制御する装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for detecting and controlling the concentration, particle size distribution, etc. of pulverized coal supplied to a combustion device such as a boiler.

最近の燃料事情の変化に伴い石炭の燃料的価値
が高まつているが、発電所用の大型石炭焚きボイ
ラ等にあつては使用する石炭は一定の粒径以下に
粉砕した石炭(以下粒径のきわめて小さい微粉炭
も含めて「粉砕炭」と総称する)をバーナに供給
し燃焼している。粉砕炭は原炭をボールミル等の
粉砕機で粉砕した後空気等により気流輸送されバ
ーナに至るのが一般的であるが粉砕機の経年変
化、炭種等によりバーナに供給される粉砕炭の濃
度および粒径分布は必らずしも安定していない。
加えて微粉炭が粉砕機からバーナに至るまでの気
流輸送の管路は相当屈曲しており、石炭の比重が
空気の比重より大なるため屈曲部で遠心力を受け
粗粒微粉炭の分離を生じ微粉炭の粒度と濃度の分
布は管路横断面につき差異を生ずる。
The value of coal as a fuel has increased with recent changes in the fuel situation, but in the case of large coal-fired boilers for power plants, the coal used is coal that has been pulverized to a certain particle size or less (hereinafter referred to as particle size). The pulverized coal (including extremely small pulverized coal, collectively referred to as ``pulverized coal'') is supplied to the burner and burned. Generally, pulverized coal is produced by pulverizing raw coal using a pulverizer such as a ball mill, and then pneumatically transporting it to the burner, but the concentration of pulverized coal supplied to the burner may vary depending on aging of the pulverizer, coal type, etc. and the particle size distribution is not necessarily stable.
In addition, the air flow transport pipe for pulverized coal from the pulverizer to the burner is quite curved, and since the specific gravity of the coal is greater than the specific gravity of the air, centrifugal force is applied at the bends, making it difficult to separate the coarse pulverized coal. The particle size and concentration distribution of the resulting pulverized coal differs depending on the cross section of the pipe.

このため粉砕機から送出される微粉炭の真正な
濃度、粒度分布を知ることがむつかしい。このた
め定期的に粉砕炭の一部を抽出して濃度、粒径分
布等を測定(以下分析と称す)し、この分析結果
に基づいて粉砕機の分級精度、給炭量を制御し燃
焼装置の燃焼が安定するよう制御する必要があ
る。従来は粉砕炭をバーナに供給する管路にサン
プリング用の座を形成し、常時はこの座を閉止し
ておき、分析の都度この座を開けて粉砕炭を採取
していた。具体的には先ず座を開け、続いてアス
ピレートエアを配管内に噴射して粉砕炭が外部に
噴出するのを防止した上でこの開放された座に対
して人手により微粉炭採取装置を設置し、採取が
終つたならば採取装置を取り外して前記座を再度
閉めかつアスピレートエアを停止し、しかる後採
取した粉砕炭を人手により分析していた。このた
め粉砕炭の採取、分析に多大の手間と時間がかか
り、さらに大量のアスピレートエアを噴射するた
め採取した粉砕炭の濃度も必ずしも正確なもので
はなく分析の精度が低くかつ長時間を要する。こ
のため燃焼装置に供給する粉砕炭の濃度、粒度分
布等の制御が遅れると共に不正確となり、結果的
には燃焼装置の制御が不正確となる。
For this reason, it is difficult to know the true concentration and particle size distribution of pulverized coal sent out from a pulverizer. For this reason, a portion of the pulverized coal is periodically extracted and its concentration, particle size distribution, etc. are measured (hereinafter referred to as analysis), and based on the analysis results, the classification accuracy of the pulverizer and the amount of coal fed are controlled. It is necessary to control the combustion so that it is stable. Conventionally, a sampling seat was formed in the conduit that supplied the pulverized coal to the burner, and this seat was normally closed, and the pulverized coal was opened each time for analysis to sample the pulverized coal. Specifically, the seat is first opened, then aspirate air is injected into the piping to prevent the pulverized coal from spewing out to the outside, and then a pulverized coal collection device is manually installed on the open seat. However, once the sampling was completed, the sampling device was removed, the seat was closed again, and the aspirate air was stopped, and then the collected pulverized coal was analyzed manually. For this reason, it takes a lot of effort and time to collect and analyze the pulverized coal, and since a large amount of aspirate air is injected, the concentration of the collected pulverized coal is not necessarily accurate, and the analysis accuracy is low and takes a long time. . For this reason, control of the concentration, particle size distribution, etc. of the pulverized coal supplied to the combustion device becomes delayed and inaccurate, resulting in inaccurate control of the combustion device.

この発明は燃焼装置に供給する粉砕炭の濃度、
粒径分布を人手によらず常時分析し、かつこの分
析結果に基づいてただちに粉砕炭の制御を行うこ
とのできる装置を提供することにある。
This invention improves the concentration of pulverized coal supplied to a combustion device.
It is an object of the present invention to provide an apparatus capable of constantly analyzing particle size distribution without manual intervention and immediately controlling pulverized coal based on the analysis results.

要するにこの発明はレーザ光線等指向性の高い
光を用いた測定および分析装置と、この分析装置
による分析結果に基づいて粉砕機を制御する装置
とから成ることを特徴とする。
In short, the present invention is characterized by comprising a measurement and analysis device that uses highly directional light such as a laser beam, and a device that controls a crusher based on the analysis results of this analysis device.

以下この発明の一実施例を図面に基づいて説明
する。
An embodiment of the present invention will be described below based on the drawings.

第1図において、ホツパ内の原炭Cは給炭器1
により供給量を調整されながら粉砕機3に至り粉
砕される。一方粉砕炭の搬送と乾燥を行う加熱空
気Aが粉砕機3内に供給され、粉砕炭を分級機に
気流輸送し、分級機のベーン12により旋回力を
与えられて分級された後細粒炭は粉砕炭供給管1
3および各粉砕炭分配管18を経てバーナ14で
燃焼し、一定粒径以上の粗粒炭は再度粉砕され
る。各バーナ14に至る粉砕炭分級管18には粉
砕炭測定装置15が各々配置してあり、この粉砕
炭測定装置15は各々粉砕炭分析装置16に対し
測定結果を光量、電気信号等により伝達可能に接
続している。17は記憶と指令信号を発する制御
箱であつて、粉砕炭分析装置16と回路接続して
いる。この制御箱17はさらに給炭機1の作動を
調節する給炭器調節器2、分級機のベーン12の
開度を調節する分級性能調節手段(ベーン開度調
節器)5、加熱空気Aの流入量を調節するダンパ
10の調節器11と各々回路接続している。
In Figure 1, raw coal C in the hopper is fed to coal feeder 1.
While the supply amount is adjusted by the pulverizer 3, the pulverizer is pulverized. On the other hand, heated air A for transporting and drying the pulverized coal is supplied into the pulverizer 3, and the pulverized coal is airflow transported to the classifier, where the vane 12 of the classifier applies swirling force to classify the fine granulated coal. is crushed coal supply pipe 1
3 and each pulverized coal distribution pipe 18, and is burned in a burner 14, and coarse granulated coal having a certain particle size or more is pulverized again. A pulverized coal measuring device 15 is arranged in each pulverized coal classifier 18 leading to each burner 14, and each pulverized coal measuring device 15 can transmit measurement results to each pulverized coal analyzer 16 by light intensity, electric signal, etc. is connected to. Reference numeral 17 is a control box for storing memory and issuing command signals, and is connected in circuit to the pulverized coal analyzer 16. This control box 17 further includes a coal feeder regulator 2 that adjusts the operation of the coal feeder 1, a classification performance adjusting means (vane opening degree regulator) 5 that adjusts the opening degree of the vane 12 of the classifier, and a control unit for controlling the heated air A. Each circuit is connected to a regulator 11 of a damper 10 that adjusts the inflow amount.

なお微粉炭の粒度については加熱空気量A、ベ
ーン12の開度、給炭機からの給炭量が相互に密
接に関連するものである。
Regarding the particle size of pulverized coal, the amount of heated air A, the opening degree of the vane 12, and the amount of coal fed from the coal feeder are closely related to each other.

第2図および第3図は粉砕炭測定装置を具体的
に示したものであつて粉砕炭分配管18の壁面に
は分配管直径の両端に位置する部分に各々小孔1
9を形成し、この小孔19を通してレーザ光線等
集束性の高い光線Rを照射する。分配管18を横
断した光線Rは凸レンズ27、ミラー28,29
を経て粉砕炭分析装置16に至り、光線の減衰程
度によつて分配管18を通過する粉砕炭の濃度お
よび粒径分布が分析される。なお分配管18に小
孔19を形成したことにより分配管中の粉砕炭が
外部に漏出する虞れがあるので小孔19の周囲か
らシールエアA1を噴射するよう構成しておく。
このシールエアA1は小孔19がきわめて小径で
あるため噴射量も僅かであるから分配管中の粉砕
炭濃度を低下させるなどの心配はない。
FIGS. 2 and 3 specifically show the pulverized coal measuring device. The wall surface of the pulverized coal distribution pipe 18 has small holes located at both ends of the diameter of the distribution pipe.
9 is formed, and a highly focused light R such as a laser beam is irradiated through this small hole 19. The light ray R that crossed the distribution pipe 18 passes through a convex lens 27 and mirrors 28 and 29.
The pulverized coal passes through the distribution tube 18 and reaches the pulverized coal analyzer 16, where the concentration and particle size distribution of the pulverized coal passing through the distribution pipe 18 are analyzed based on the degree of attenuation of the light beam. Since the small holes 19 formed in the distribution pipe 18 may cause the crushed coal in the distribution pipe to leak to the outside, seal air A 1 is injected from around the small holes 19.
Since the small hole 19 of this seal air A1 has an extremely small diameter, the amount of injection is small, so there is no concern that it will reduce the concentration of pulverized coal in the distribution pipe.

次に分析装置16による分析結果は常時制御箱
17に入力され、制御箱17はこの分析結果を総
合し平均値算出等をして粉砕機より送出される微
粉炭の真正な濃度、粒度分布を知り、この算出し
た数値を制御箱が記憶する制御数値と対比し粉砕
装置を制御する。すなわち、第1図において粉砕
炭濃度が低下した場合には制御箱17は給炭器調
節器2に指令信号を発して給炭量を増加させ、ま
た粒度が大きくなつた場合には開度調節器5およ
びダンパ調節装置11に指令信号を発し、ベーン
12の開度を調節すると共に加熱空気の供給量を
増加して分級機の分級精度を高め粒径分布を小さ
くする。制御箱17は以上の操作を適切に組み合
せることにより燃焼装置に供給する粉砕炭の濃
度、粒径分布を調節する。
Next, the analysis results from the analyzer 16 are constantly input into the control box 17, and the control box 17 integrates these analysis results, calculates the average value, etc., and calculates the true concentration and particle size distribution of the pulverized coal sent out from the pulverizer. The pulverizer is controlled by comparing the calculated value with the control value stored in the control box. That is, in FIG. 1, when the pulverized coal concentration decreases, the control box 17 issues a command signal to the coal feeder regulator 2 to increase the amount of coal fed, and when the particle size increases, the opening degree is adjusted. A command signal is issued to the classifier 5 and the damper adjustment device 11 to adjust the opening degree of the vane 12 and increase the amount of heated air supplied to improve the classification accuracy of the classifier and reduce the particle size distribution. The control box 17 adjusts the concentration and particle size distribution of the pulverized coal supplied to the combustion device by appropriately combining the above operations.

この発明を実施することにより粉砕炭の性状を
常時正確に、かつ人手や時間をかけることなく検
知できる。
By carrying out this invention, the properties of pulverized coal can be detected accurately at all times and without requiring manpower or time.

また検知結果に基づいて粉砕機を常に適正に調
節できるので、燃焼装置に供給する粉砕炭の性状
を常に安定させることが可能である。
Furthermore, since the pulverizer can always be adjusted appropriately based on the detection results, it is possible to always stabilize the properties of the pulverized coal supplied to the combustion device.

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

第1図はこの発明に係る粉砕炭分析制御装置の
系統図、第2図は粉砕炭測定装置の系統図、第3
図Aは粉砕炭測定装置を設けた粉砕炭分配管の断
面図、同Bは前記A図のA―A断面図である。 2……給炭器調節器、3……粉砕機、5……ベ
ーン開度調節器、11……ダンパ調節器、15…
…粉砕炭測定装置、16……粉砕炭分析装置、1
7……制御箱、18……粉砕炭分配管。
Fig. 1 is a system diagram of a pulverized coal analysis control device according to the present invention, Fig. 2 is a system diagram of a pulverized coal measuring device, and Fig. 3 is a system diagram of a pulverized coal measuring device.
Figure A is a sectional view of a pulverized coal distribution pipe equipped with a pulverized coal measuring device, and Figure B is a sectional view taken along line AA in Figure A. 2...Coal feeder regulator, 3...Crusher, 5...Vane opening regulator, 11...Damper regulator, 15...
... Crushed coal measuring device, 16... Crushed coal analyzing device, 1
7... Control box, 18... Crushed coal distribution pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 石炭粉砕機から供給される粉砕炭を夫々のバ
ーナに供給する粉砕炭分配管に夫々設けたレーザ
光線を使用する粉砕炭測定装置と、その測定結果
の信号を受ける粉砕炭分析装置と、夫々の分析結
果の信号を受ける一の制御箱と、この制御箱から
の指令信号で制御される分級性能調整手段と石炭
粉砕機に供給する加熱空気量制御用のダンパとを
設けたことを特徴とする粉砕炭分析制御装置。
1. A pulverized coal measuring device using a laser beam installed in each pulverized coal distribution pipe that supplies pulverized coal supplied from a coal pulverizer to each burner, and a pulverized coal analyzer that receives a signal from the measurement results. The present invention is characterized by being provided with one control box that receives a signal of the analysis result, a classification performance adjustment means controlled by a command signal from this control box, and a damper for controlling the amount of heated air supplied to the coal crusher. Pulverized coal analysis control device.
JP16203280A 1980-11-19 1980-11-19 Controller for analysis of ground charcoal Granted JPS5786916A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16203280A JPS5786916A (en) 1980-11-19 1980-11-19 Controller for analysis of ground charcoal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16203280A JPS5786916A (en) 1980-11-19 1980-11-19 Controller for analysis of ground charcoal

Publications (2)

Publication Number Publication Date
JPS5786916A JPS5786916A (en) 1982-05-31
JPS6349131B2 true JPS6349131B2 (en) 1988-10-03

Family

ID=15746777

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16203280A Granted JPS5786916A (en) 1980-11-19 1980-11-19 Controller for analysis of ground charcoal

Country Status (1)

Country Link
JP (1) JPS5786916A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59212619A (en) * 1983-05-18 1984-12-01 Ishikawajima Harima Heavy Ind Co Ltd Combustion furnace control method
JPS60154739U (en) * 1984-03-16 1985-10-15 川崎重工業株式会社 Coal feed pipe blockage detection device in fluidized bed boiler
JPS62230528A (en) * 1986-03-27 1987-10-09 Nippon Steel Corp Thin layering conveyance method for granular material
JPH06285386A (en) * 1993-04-07 1994-10-11 Kurimoto Ltd Control mechanism for pulverizing device and operating method thereof
JP6283204B2 (en) * 2013-11-11 2018-02-21 大阪瓦斯株式会社 Micronizer

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4122684Y1 (en) * 1964-08-11 1966-11-14
JPS6046338B2 (en) * 1978-07-05 1985-10-15 株式会社日立製作所 Combustion system automatic control device

Also Published As

Publication number Publication date
JPS5786916A (en) 1982-05-31

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