JPS5974423A - Fuel control method of powdered coal combustion furnace - Google Patents

Fuel control method of powdered coal combustion furnace

Info

Publication number
JPS5974423A
JPS5974423A JP57184060A JP18406082A JPS5974423A JP S5974423 A JPS5974423 A JP S5974423A JP 57184060 A JP57184060 A JP 57184060A JP 18406082 A JP18406082 A JP 18406082A JP S5974423 A JPS5974423 A JP S5974423A
Authority
JP
Japan
Prior art keywords
mill
damper
powdered coal
burner
command
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
JP57184060A
Other languages
Japanese (ja)
Inventor
Hirobumi Furukoshi
古越 博文
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP57184060A priority Critical patent/JPS5974423A/en
Publication of JPS5974423A publication Critical patent/JPS5974423A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/002Regulating fuel supply using electronic means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2235/00Valves, nozzles or pumps
    • F23N2235/02Air or combustion gas valves or dampers
    • F23N2235/06Air or combustion gas valves or dampers at the air intake
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2239/00Fuels
    • F23N2239/02Solid fuels
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

PURPOSE:To make it possible to respond immediately to an additional combustion requirement command and a fire extinguishing command by a method wherein a circuit device adopted to store powdered coal temporarily is provided in a bypass passage formed in a fuel pipe for introducing the powdered coal to a burner of the furnace from a powdered coal device. CONSTITUTION:Powdered coal is introduced to the burner 6 of the combustion furnace such as a boiler through the fuel pipe 4 as it floats on a current of preheated air 3. When a generator output command 12 increases, the additional combustion requirement command 19 is generated from a boiler control device 11 to a damper control device 21 whereupon a damper drive device 22 corresponding to a required mill 1 is turned ON, a damper 9 is opened while a damper 10 is closed and the supply of the powdered coal flowing through a bypass pipe 7 is switched to the burner 6. Further, when the generator output command 12 decreases rapidly or is stopped, the quick fire extinguishing command 20 is generated to the damper control device 21 whereupon the damper drive device 20 corresponding to the required mill 1 is turned OFF, the dampers 9 and 10 are opened and at the same time, the supply of coal 2 to the mill 1 is stopped. In addition, the mill 1 which corresponds to the fire extinguished burner 6 continues to supply the powdered coal to a powdered coal collecting device 8 through the bypass pipe 7 until the interior of the mill 1 becomes empty and the operation of the mill is stopped when mill is emptied.

Description

【発明の詳細な説明】 本発明は微粉炭焚火炉の燃料制御方法に関する。[Detailed description of the invention] The present invention relates to a fuel control method for a pulverized coal furnace.

近年、燃料事情の悪化からボイラ等の火炉における燃料
に微粉炭を用いることが種々考えられており、微粉炭を
安定して供給するために、連続的に供給される石炭(原
炭)を微粉炭装置(ミル)にて微粉化し空気流に乗せて
火炉におけるバーナに導くようにしている。しかしこの
ような装置においでは、急激な負荷の減小のために一部
のバーナの燃焼を止めるべくそれに対応するミルの作動
を停止したり、或いは極端な場合に総てのバーナの燃焼
を停止する必要が生じたとき(トラブルなどが生じたと
き)、単にバーナへの微粉炭の供給を停止すると、ミル
内に予熱空気によって加熱された微粉炭及びその可燃ガ
スが充満し、爆発を起こす危険を有していた。従って、
従来は前記したような早急なバーナの燃焼停止要求が出
されても、ミル内が空になるまでミルの稼動を止めるこ
とができず、バーナの燃焼を早急に停止することができ
ないので、要求に応えることができない。このため出力
側で上記要求を満すべく調整、制御する必要があるが、
トラブルの際にはそれができないために被害を更に大き
くしてしまうという危険を有していた。またバーナ燃焼
の追加要求指令が出た場合も、ミルが空の状態から運転
が開始されるために、定常の微粉炭供給状態になるまで
の所要時間が長く、急激な負荷要求にも応答できない問
題を有していた。
In recent years, due to the worsening fuel situation, various ideas have been given to using pulverized coal as fuel in furnaces such as boilers. The charcoal is pulverized in a charcoal mill and carried through an air stream to the burner in the furnace. However, in such equipment, due to a sudden load reduction, it is necessary to stop the operation of the corresponding mill in order to stop the combustion of some burners, or in extreme cases, to stop the combustion of all burners. If you simply stop supplying pulverized coal to the burner when it becomes necessary to do so (when a problem occurs), the mill will be filled with pulverized coal heated by preheated air and its combustible gas, which could cause an explosion. It had Therefore,
Conventionally, even if an immediate request to stop burner combustion as described above was issued, the mill operation could not be stopped until the inside of the mill was empty, and the burner combustion could not be stopped immediately. cannot respond to Therefore, it is necessary to adjust and control the output side to meet the above requirements.
In the event of a problem, there was a risk that the damage would be even greater because it was not possible to do so. Furthermore, even when an additional request for burner combustion is issued, the mill starts operation from empty, so it takes a long time to reach a steady state of pulverized coal supply, and it is unable to respond to sudden load requests. I had a problem.

本発明は、こうした点に鑑みてなしたもので、微粉炭装
置から火炉のバーナに微粉炭を導く燃料管にバイパス流
路を設け、バイパス流路に微粉炭を導いてスタンバイ状
態にしでおき、火炉の燃焼の追加要求により微粉炭を火
炉側に切換え、また急速消火要求時にはバイパス流路側
に切換えることにより、即座に要求に応えて制御性の向
上を図り、且つトラブル発生時の被害を最小限に止め得
るようにしたものである。
The present invention has been made in view of these points, and includes providing a bypass flow path in a fuel pipe that leads pulverized coal from a pulverized coal device to a burner of a furnace, and guiding the pulverized coal to the bypass flow path and keeping it in a standby state. By switching the pulverized coal to the furnace side when additional combustion is required in the furnace, and switching to the bypass flow path side when rapid fire extinguishing is required, it is possible to immediately respond to requests, improve controllability, and minimize damage in the event of trouble. It was designed so that it could be stopped.

以下本発明の実施例を図面を参照して説明する。Embodiments of the present invention will be described below with reference to the drawings.

図中(1)は微粉炭装置(ミルという)を表わし、石炭
(2)を導入してそれをボールミル方式等によって微粉
化し、その微粉化した微粉炭を予熱空気(3)の空気流
に乗せて燃料管(4)を介しボイラ等の火炉(5)のバ
ーナ(6)に導くようにしている。このとき、ミル(1
)は例えば複数のバーナ列に対応するように複数個設け
られている。前記燃料管(4)K、バイパス管(7)を
接続して冷却機能を有する微粉炭回収装置(8)に導く
ようにし、且つ前記燃料管(4)における分岐点の下流
側位置及び前記バイパス管(7)の夫々にダンパ(9)
 (1@を設ける。
In the figure, (1) represents a pulverized coal equipment (referred to as a mill), which introduces coal (2), pulverizes it using a ball mill method, etc., and carries the pulverized coal into an air stream of preheated air (3). The fuel is then guided through a fuel pipe (4) to a burner (6) of a furnace (5) such as a boiler. At this time, mil (1
) are provided, for example, in a plurality so as to correspond to a plurality of burner rows. The fuel pipe (4) K and the bypass pipe (7) are connected to lead to the pulverized coal recovery device (8) having a cooling function, and the downstream position of the branch point in the fuel pipe (4) and the bypass pipe are connected. A damper (9) for each pipe (7)
(Establish 1@.

また、図中(11)はボイラ制御装置を示し、発電機出
力指令a功、ミルの台数03、給水レベル(14)や蒸
気圧力00並びに炉内圧力010等のボイラ各部の状態
、補機モータ0力θ8)の運転状態が人力されでいる。
In addition, (11) in the figure shows the boiler control device, and the status of each part of the boiler, such as the generator output command a, the number of mills 03, the water supply level (14), the steam pressure 00, and the furnace pressure 010, and the auxiliary motor The operating state of 0 force θ8) is manually operated.

ボイラ制御装置(11)は、指令及び各部の状態によっ
てミル追加要求指令09)又は急速消火指令−をダンパ
制御装置(21)に指令し、指令を受けたダンパ制御装
置(21)はその指令に基づいて必要なミル0)のダン
パ(9) (IQを作動するダンパ駆動装置(イ)をオ
ン・オフ指令@作動する。前記ダンパ(9)θOはダン
パ駆動装置(イ)によって常に逆方向に同時に開閉駆動
されるよう構成されており、例えばダンパ制御装置I2
1)からオ/の信号が発せられると燃料管(4)のダン
パ(9)が開き、バイパス管(7)のダンパθOが閉じ
(図示の状態)、逆にオフの信号が発せられるとダンパ
(9)が閉し、ダンパθOが開くようになっている。
The boiler control device (11) instructs the damper control device (21) with a mill additional request command 09) or a rapid fire extinguishing command depending on the command and the status of each part, and the damper control device (21) that receives the command responds to the command. Based on the required mill 0) damper (9) (IQ), the damper drive device (a) which operates the on/off command @operates. The damper (9) θO is always moved in the opposite direction by the damper drive device (a). For example, the damper control device I2 is configured to be driven to open and close at the same time.
When the OFF signal is issued from 1), the damper (9) of the fuel pipe (4) opens, and the damper θO of the bypass pipe (7) closes (state shown), and conversely, when the OFF signal is issued, the damper (9) of the fuel pipe (4) opens. (9) is closed, and damper θO is opened.

上記において、通常時は発電機出力指令(喝に応じた数
のミル(1)が駆動され、図示するように微粉炭が燃料
管(4)を介して対応するバーナ(0)に供給されて燃
焼している。このとき、休(1−シているミル(1)に
対応する燃料管(4)のダンパ(9)GJ閉じられ、バ
イパス管(7)のダンパ00は開けられている。この状
態から発電機出力指令0功が増加する場合は、休止して
いる所要のミル(1)を前以って起動する。このとき、
休止していたミル(1)内は空の状態であるので、石炭
(2)が供給されて微粉化が行われ、所要量の微粉炭が
排出されるようになるまでには時間がかかるが、この間
、ダンパ(9)が閉、ダンパ00)が開であるので、微
粉炭はバイパス管(7)を介して微粉炭回収装置(8)
に送られており、これにより定常のスタンノ(イ状態に
なるように保持される。
In the above, under normal conditions, the number of mills (1) is driven according to the generator output command (power), and pulverized coal is supplied to the corresponding burner (0) via the fuel pipe (4) as shown in the figure. At this time, the damper (9) GJ of the fuel pipe (4) corresponding to the idle mill (1) is closed, and the damper 00 of the bypass pipe (7) is opened. If the number of generator output commands increases from this state, the required idle mills (1) are started in advance.At this time,
Since the inside of the mill (1), which has been inactive, is empty, it will take some time until the coal (2) is supplied and pulverized, and the required amount of pulverized coal is discharged. During this period, the damper (9) is closed and the damper 00) is open, so the pulverized coal is transferred to the pulverized coal recovery device (8) via the bypass pipe (7).
This keeps it in a steady state of stun.

従って、前記発電機出力指令(¥が増加すると、ボイラ
制御装置0])からダンパ制御装置(21)に追加要求
指令Oすが発せられ、所要のミル(1)K対応するダン
パ駆動装置□□□をオン指令し、ダンパ(9)を開、ダ
ンパ00)を閉としてバイパス管(7)に流していた微
粉炭をバーナ(6)側に切換えて供給するが、このとき
前記ミル(1)は既にスタンバイ状態にあるので、直ち
に追加バーナ(6)の定常燃焼を行わせ、前記指令に即
座に応えることができる。
Therefore, an additional request command is issued to the damper control device (21) from the generator output command (when ¥ increases, the boiler control device 0]), and the required mill (1)K corresponding damper drive device □□ □ is turned on, the damper (9) is opened, and the damper 00) is closed, and the pulverized coal that was flowing through the bypass pipe (7) is switched to the burner (6) side and supplied. Since it is already in a standby state, the additional burner (6) can immediately perform steady combustion to immediately respond to the command.

また、発電機出力指令(6)の急激な減少、或いは停止
、更にはボイラ主要機器等のトラブルの発生時は、ボイ
ラ制御装置01)から急速消火指令(ホ)がダンパ制御
装置(2])に発せられ、所要のミル(1)に対応する
ダンパ駆動装置(イ)にオフ指令を出してダンパ(9)
を閉、ダンパ00を開とし、同時にそのミル(1)への
石炭(2)の供給が停止される。これにより所要のバー
ナ(6)は即座に消火される。また消火されたバーナ(
6)に対応するミル(1)は内部が空になるまでバイパ
ス管(7)を介し微粉炭を微粉炭回収装置(8)に送り
続け、内部が空になったら駆動を停止する。これにより
ミル(1)の爆発の危険をなくすことができ、また微粉
炭回収装置(8)も水散布或いは水浸漬方式等の冷却手
段を有しているので微粉炭を安全に回収することができ
る。またこの回収した微粉炭は再び使用することができ
る。
In addition, if the generator output command (6) suddenly decreases or stops, or if trouble occurs in the boiler's main equipment, etc., a rapid extinguishing command (e) is sent from the boiler control device 01) to the damper control device (2]). A command is issued to the damper drive device (a) corresponding to the required mill (1) to turn off the damper (9).
is closed, damper 00 is opened, and at the same time, the supply of coal (2) to the mill (1) is stopped. This immediately extinguishes the required burner (6). Also, the extinguished burner (
The mill (1) corresponding to 6) continues to send pulverized coal to the pulverized coal recovery device (8) via the bypass pipe (7) until the inside becomes empty, and when the inside becomes empty, the drive is stopped. This eliminates the danger of explosion in the mill (1), and since the pulverized coal recovery device (8) also has cooling means such as water spraying or water immersion, pulverized coal can be recovered safely. can. Moreover, this recovered pulverized coal can be used again.

上記したように、本発明によれば、バーナ(0)の追加
燃焼要求及び消火指令に即座に応えることができるので
、ボイラの制御性が向」−されると共に、トラブル発生
時等の消火を即座に行うことにより被害を最少限度に抑
えることができる。
As described above, according to the present invention, it is possible to immediately respond to requests for additional combustion of burner (0) and extinguishing commands, thereby improving boiler controllability and extinguishing fires when trouble occurs. By doing so immediately, you can minimize the damage.

尚、本発明は」−記実施例にのみ限定されるものではな
く、本発明の要旨を逸脱しない範囲内において種々変更
を加え得るものである。
It should be noted that the present invention is not limited only to the embodiments described above, and various changes may be made without departing from the gist of the present invention.

−J−述した本発明の微粉炭焚火炉の燃料制御方法によ
れば、次のような優れた効果を奏し得る。
-J- According to the fuel control method for a pulverized coal-fired furnace of the present invention described above, the following excellent effects can be achieved.

(1)燃焼の追加要求時に、ミルをバイパス流路を用い
て予めスタンバイ状態としておき、ダンパにより切換え
てバーナに微粉炭を供給することにより、要求の燃焼を
即座に行わしめることができる。
(1) When additional combustion is requested, the mill is placed on standby using a bypass flow path, and the damper is switched to supply pulverized coal to the burner, thereby making it possible to immediately perform the requested combustion.

(11)急速消火要求時に、バーナへの微粉炭をダンパ
によりバイパス流路側に切換えることにより、即座に消
火を行わせることができ、且つ消火後のミル内の燃料を
バイパス流路を介して排出するので、ミルが爆発すると
いった危険性を排除できる。
(11) When rapid extinguishing is requested, by switching the pulverized coal to the burner to the bypass flow path using a damper, the fire can be extinguished immediately, and the fuel in the mill after extinguishing can be discharged via the bypass flow path. This eliminates the risk of the mill exploding.

(iii)  上記(+ ) li)に」;リボイラの
制御性が向上される。
(iii) In (+) li) above, the controllability of the reboiler is improved.

(1v)急速消火が可能となるのでトラブル発生時等の
被害を最小限におさえることができる。
(1v) Since rapid fire extinguishing becomes possible, damage when trouble occurs can be minimized.

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

図面は本発明の一実施例を示す説明図である。 (υは微粉炭装置(ミル)、(2)は石炭、(3)は予
熱空気、(4)は燃料管、(5)は火炉、(6)はバー
ナ、(7)はバイパス管、(8)は微粉炭回収装置、(
9) (10はダンパ、0ηはボイラ制御装置、(6)
は発電機出力指令、θつは追加要求指令、(イ)は急速
消火指令、t21)はダンパ制御装置、(イ)はダンパ
駆動装置を示す。
The drawings are explanatory diagrams showing one embodiment of the present invention. (υ is pulverized coal equipment (mill), (2) is coal, (3) is preheated air, (4) is fuel pipe, (5) is furnace, (6) is burner, (7) is bypass pipe, ( 8) is a pulverized coal recovery device, (
9) (10 is the damper, 0η is the boiler control device, (6)
denotes a generator output command, θ denotes an additional request command, (a) denotes a rapid fire extinguishing command, t21) denotes a damper control device, and (a) denotes a damper drive device.

Claims (1)

【特許請求の範囲】[Claims] 1)火炉に導入する微粉炭燃料をバイパスさせてスタン
バイ状態にしておき、火炉の燃焼の追加要求時に前記微
粉炭を火炉側に切換えで導くことにより即座に要求に応
じ、且つ急速消火要求時に前記微粉炭をバイパスさせる
ことにより火炉への微粉炭の供給を即座に遮断すること
を特徴とする微粉炭焚火炉の燃料制御方法。
1) The pulverized coal fuel introduced into the furnace is bypassed and placed in a standby state, and when additional combustion in the furnace is requested, the pulverized coal is switched to the furnace side to immediately respond to the request, and when rapid extinguishing is requested, the above-mentioned A fuel control method for a pulverized coal furnace, characterized by immediately cutting off the supply of pulverized coal to the furnace by bypassing the pulverized coal.
JP57184060A 1982-10-20 1982-10-20 Fuel control method of powdered coal combustion furnace Pending JPS5974423A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57184060A JPS5974423A (en) 1982-10-20 1982-10-20 Fuel control method of powdered coal combustion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57184060A JPS5974423A (en) 1982-10-20 1982-10-20 Fuel control method of powdered coal combustion furnace

Publications (1)

Publication Number Publication Date
JPS5974423A true JPS5974423A (en) 1984-04-26

Family

ID=16146668

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57184060A Pending JPS5974423A (en) 1982-10-20 1982-10-20 Fuel control method of powdered coal combustion furnace

Country Status (1)

Country Link
JP (1) JPS5974423A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111486472A (en) * 2020-03-27 2020-08-04 扬州第二发电有限责任公司 Medium-speed mill automatic start-stop control system suitable for deep peak shaving of direct-blowing coal-fired unit
CN114811575A (en) * 2022-04-19 2022-07-29 东方电气集团东方锅炉股份有限公司 Coal-fired and natural gas dual-purpose boiler system and using method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111486472A (en) * 2020-03-27 2020-08-04 扬州第二发电有限责任公司 Medium-speed mill automatic start-stop control system suitable for deep peak shaving of direct-blowing coal-fired unit
CN114811575A (en) * 2022-04-19 2022-07-29 东方电气集团东方锅炉股份有限公司 Coal-fired and natural gas dual-purpose boiler system and using method thereof

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