JPS6213901A - Method of controlling main steam pressure of high-speed fluidized bed boiler - Google Patents

Method of controlling main steam pressure of high-speed fluidized bed boiler

Info

Publication number
JPS6213901A
JPS6213901A JP15183485A JP15183485A JPS6213901A JP S6213901 A JPS6213901 A JP S6213901A JP 15183485 A JP15183485 A JP 15183485A JP 15183485 A JP15183485 A JP 15183485A JP S6213901 A JPS6213901 A JP S6213901A
Authority
JP
Japan
Prior art keywords
combustor
fluidized bed
bed boiler
drain
main steam
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
JP15183485A
Other languages
Japanese (ja)
Inventor
友一 竹内
藤井 邦比古
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 Heavy Industries Ltd
Original Assignee
Mitsubishi 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP15183485A priority Critical patent/JPS6213901A/en
Publication of JPS6213901A publication Critical patent/JPS6213901A/en
Pending legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、コンバスタと外部熱交換器からなる高速流動
床ボイラで発生する主蒸気の圧力を制御する方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for controlling the pressure of main steam generated in a high-speed fluidized bed boiler consisting of a combustor and an external heat exchanger.

〔従来の技術〕[Conventional technology]

高速流動床ボイラ自体は新しい技術であり、この高速流
動床ボイラは第2図に示すように、高速流動燃焼炉であ
るコンパスフ2.コンバスタ2に粉粒体燃料を供給する
燃料供給装置1.コンバスタ2から飛散しダクト6によ
って導かれた粉粒体燃料を集塵すると共にガスから分離
するサイクロン3.サイクロン3で集塵された粉粒体燃
料をリサイクルドレンとしてサイクロン3より排出する
リサイクルドレン管7.リサイクルドレン管7の途中に
設けられ、一部のリサイクルドレンを直接コンバスタ2
に導き、残りを外部熱交換器5に導くためにリサイクル
ドレンの流量を調整するリサイクルドレン制御弁4.外
部熱交換器5からのリサイクルドレンを再びコンバスタ
2に導くリサイクル管8とで構成されている。
The high-speed fluidized bed boiler itself is a new technology, and as shown in Figure 2, the high-speed fluidized bed boiler is a high-speed fluidized combustion furnace called CompassF2. Fuel supply device 1 that supplies granular fuel to the combustor 2. A cyclone 3 that collects the granular fuel scattered from the combustor 2 and led through the duct 6 and separates it from the gas. 7. A recycle drain pipe that discharges the powdered fuel collected by the cyclone 3 from the cyclone 3 as a recycle drain. It is installed in the middle of the recycle drain pipe 7, and a part of the recycle drain is directly connected to the combustor 2.
4. A recycle drain control valve that adjusts the flow rate of the recycle drain to direct the remainder to the external heat exchanger 5. It is comprised of a recycle pipe 8 that guides the recycle drain from the external heat exchanger 5 to the combustor 2 again.

燃料供給装置1からコンバスタ2内に粉体燃料を供給し
、サイクロン3で分離されたリサイクルドレンをリサイ
クルドレン制御弁4を介して高温のリサイクルドレンの
一部を直接コシバスタ2内に循環すると共に、外部熱交
換器5で熱を奪われて低温となった残りのリサイクルド
レンをリサイクルドレン管8からコンバスタ2内に循環
する。
Powdered fuel is supplied from the fuel supply device 1 into the combustor 2, and a part of the high-temperature recycle drain is directly circulated into the combustor 2 via the recycle drain control valve 4 from the recycled drain separated by the cyclone 3. The remaining recycled drain, which has been reduced in temperature by removing heat in the external heat exchanger 5, is circulated into the combustor 2 through the recycled drain pipe 8.

コンバスタ2内に供給された粉体燃料、リサイクルドレ
ンは図示省略の高圧空気供給装置からコンバスタ2内に
供給される高圧の空気により燃焼しながら流動速度が4
〜10m/sで高速流動して飛散する゛。飛散する固形
分には未燃分を含み、この未燃分がガスとともにサイク
ロン3に導かれ、サイクロン3でガスとリサイクルドレ
ンとに分離される。ガスは煙道9を通って図示省略の再
熱器。
The powdered fuel supplied into the combustor 2 and the recycled drain are combusted by high pressure air supplied into the combustor 2 from a high pressure air supply device (not shown), while the flow rate is increased to 4.
It flows at a high speed of ~10 m/s and scatters. The scattered solid content includes unburned matter, and this unburned matter is led to the cyclone 3 together with the gas, where it is separated into gas and recycled drain. The gas passes through a flue 9 to a reheater (not shown).

過熱器8節炭器等が配置された熱交換部に送られる。一
方リサイクルドレンは上記したように高温と低温とに分
けられてコンバスタ2内に循環される。外部熱交換器5
では給水が送られてきて高温のリサイクルドレンから熱
を吸収し、給水が蒸発して主蒸気を生成する。
It is sent to a heat exchange section where a superheater, 8 economizers, etc. are arranged. On the other hand, the recycled drain is divided into high temperature and low temperature and circulated within the combustor 2 as described above. External heat exchanger 5
In this case, feed water is delivered and absorbs heat from the hot recycle drain, and the feed water evaporates to produce main steam.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

高速流動床ボイラ自体は新しい技術、であり、このため
高速流動床ボイラで発生する主蒸気の圧力を制御する技
術は、まだ確立されておらず、主蒸気−あ圧力を制御す
る技術がのぞまれている。
The high-speed fluidized bed boiler itself is a new technology, so the technology to control the pressure of the main steam generated in the high-speed fluidized bed boiler has not yet been established, and the technology to control the main steam pressure is needed. It is rare.

〔問題点を解決するための手段〕[Means for solving problems]

そのため本発明は、高速流動床ボイラで発生する主蒸気
の圧力を制御するため、炉壁で形成されたコンバスタ内
に粉粒体燃料を供給すると共に。
Therefore, in order to control the pressure of main steam generated in a high-speed fluidized bed boiler, the present invention supplies granular fuel into the combustor formed by the furnace wall.

コンバスタから飛散する粉粒体燃料を集塵してリサイク
ルドレンとして一部を外部熱交換器を介し。
Powdered fuel scattered from the combustor is collected and a portion is recycled as a drain via an external heat exchanger.

残りを直接コンバスタ内に供給する高速流動床ボイラの
主蒸気圧力を制御する方法において、外部熱交換器へ導
入するリサイクルドレン流量と、コンバスタに投入する
粉粒体燃料投入量とを調整する高速流動床ボイラの主蒸
気圧力制御方法を提供している。
In a method of controlling the main steam pressure of a high-speed fluidized bed boiler that supplies the remainder directly into the combustor, the high-speed fluidization system adjusts the flow rate of recycled condensate introduced into the external heat exchanger and the amount of granular fuel input into the combustor. A method for controlling main steam pressure in a floor boiler is provided.

〔作用〕[Effect]

本発明の方法によれば、外部熱交換器へ導入するリサイ
クルドレン流量を調節して、外部熱交換器での蒸発量、
蒸気の圧力をコン1−ロールし、又コンバスタに投入す
る粉粒体燃料投入′量とを調整することにより、燃焼温
度をコントロールする。
According to the method of the present invention, the amount of evaporation in the external heat exchanger can be adjusted by adjusting the flow rate of recycle drain introduced into the external heat exchanger.
Combustion temperature is controlled by controlling the steam pressure and adjusting the amount of powdered fuel input into the combustor.

〔実施例〕〔Example〕

本発明の実施の態様例を第1図a、bに基づいて説明す
る。なお、第1図a、bは本発明を実施するための制御
装置のブロック線図である。
An embodiment of the present invention will be explained based on FIGS. 1a and 1b. Note that FIGS. 1a and 1b are block diagrams of a control device for implementing the present invention.

11は外部熱交換器5で生成された蒸気の圧力を検出す
る圧力発信器で1 この圧力発信器11で検出された値
は信号に変えられ、圧力調節計12に入力される。この
圧力調節計12は2例えば、入力された蒸気圧力の信号
と設定信号とを比較して偏差を求め、この偏差値を積分
するなどの演算をさせて調節信号を求めるものである。
A pressure transmitter 11 detects the pressure of steam generated by the external heat exchanger 5. The value detected by the pressure transmitter 11 is converted into a signal and input to the pressure regulator 12. The pressure regulator 12 compares, for example, an input steam pressure signal with a set signal to obtain a deviation, and performs calculations such as integrating this deviation value to obtain an adjustment signal.

圧力調節計12で求められた信号は、加算器13に入力
され、ここで圧力制御先行信号14が加算され、加算器
13からリサイクルドレン制御弁4の開度をコントロー
ルする操作信号15が出力される。この操作信号に基づ
いてリサイクルドレン制御弁4の開度が調整されて。
The signal obtained by the pressure regulator 12 is input to an adder 13, where a pressure control advance signal 14 is added, and an operation signal 15 for controlling the opening degree of the recycle drain control valve 4 is output from the adder 13. Ru. Based on this operation signal, the opening degree of the recycle drain control valve 4 is adjusted.

外部熱交換器5へ導かれるリサイクルドレンと直接コン
バスタ2内に導かれるリサイクルドレンとの量が調整さ
れる。例えば、外部熱交換器5へ導かれるリサイクルド
レン量が少なくなると、給水が受ける熱量は少なくなり
、給水の蒸発量が少なくなって蒸気の圧力が下がる。
The amounts of recycled drain introduced to the external heat exchanger 5 and recycled drain directly introduced into the combustor 2 are adjusted. For example, when the amount of recycled drain introduced to the external heat exchanger 5 decreases, the amount of heat received by the feed water decreases, the amount of evaporation of the feed water decreases, and the pressure of steam decreases.

16はコンバスタ2内の温度を検出する温度発信器で、
この温度発信器16で検出された値は信号に変えられ、
温度調節計17に入力される。どの温度調節計17は1
例えば、入力された温度の信号と設定信号とを比較して
偏差を求め、この偏差値を積分するなどの演算をさせて
調節信号を求めるものである。温度調節計17で求めら
れた信号は、加算器18に入力され、ここで温度制御先
行信号19が加が調整されて、コンバスタ2内に供給さ
れる燃料       じの投入量が調節される。例え
ば、燃料投入量が少なくなると、燃料の発熱量が少なく
なり、コンパ      17ケ2カ。□7,7□工6
.ヶ9.。73(7)□。   1の伝熱部に流れる排
ガスの温度が下がり、蒸気の過熱度が低下して圧力が低
下すると共に、外部熱交換器5に導かれるリサイクルド
レンの温度も低下するので、給水が受ける熱量は少なく
なり、給水の蒸発量が少なくなって蒸気の圧力が下がる
16 is a temperature transmitter that detects the temperature inside the combustor 2;
The value detected by this temperature transmitter 16 is converted into a signal,
The temperature is input to the temperature controller 17. Which temperature controller 17 is 1
For example, an input temperature signal and a setting signal are compared to find a deviation, and the deviation value is integrated or otherwise calculated to obtain an adjustment signal. The signal obtained by the temperature controller 17 is input to an adder 18, where the addition of the temperature control advance signal 19 is adjusted to adjust the amount of fuel supplied into the combustor 2. For example, when the amount of fuel input decreases, the calorific value of the fuel decreases, resulting in a decrease in the amount of fuel input. □7,7□Eng 6
.. 9. . 73(7)□. The temperature of the exhaust gas flowing into the heat transfer section 1 decreases, the degree of superheating of the steam decreases, and the pressure decreases. At the same time, the temperature of the recycle drain led to the external heat exchanger 5 also decreases, so the amount of heat received by the feed water is small. As a result, the amount of evaporation of the feed water decreases, and the steam pressure decreases.

(効果〕 本発明の方法によれば、外部熱交換器へ導入するリサイ
クルトレン流量を調節することと、コンバスタに投入す
る粉粒体燃料投入量とを調整して燃焼温度をコントロー
ルすることにより、外部熱交換器で給水が受ける熱量を
調節して、蒸気の圧力を調整することができる。
(Effects) According to the method of the present invention, by controlling the combustion temperature by adjusting the flow rate of the recycle train introduced into the external heat exchanger and the amount of granular fuel input into the combustor, By adjusting the amount of heat that the feed water receives in the external heat exchanger, the pressure of the steam can be adjusted.

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

第1図a、bはそれぞれ本発明の方法を実施させるため
の制御装置を示す図、第2図は高速流動床ボイラを示す
図である。 11−圧力発信器、 12− 圧力調節計、13〜−一
一〜加算器、14−−圧力制御先行信号、 15−−一
操作信号。 16一−一温度発信器、 17−−−一温度調節計、 
18−−−一加算器、19− 温度制御先行信号、 2
0−−−−−一操作信号イ梵工里人 板間 暁゛、1゜ 一二二−−1 iPJf印 (し)           (a) p321
FIGS. 1a and 1b are diagrams showing a control device for carrying out the method of the present invention, respectively, and FIG. 2 is a diagram showing a high-speed fluidized bed boiler. 11-pressure transmitter, 12-pressure regulator, 13--11-adder, 14--pressure control advance signal, 15--operation signal. 16--1 temperature transmitter, 17--1 temperature controller,
18--one adder, 19-temperature control advance signal, 2
0-----1 operation signal I Bonkurito Akira Itama, 1゜122--1 iPJf seal (a) p321

Claims (1)

【特許請求の範囲】[Claims] 炉壁で形成されたコンバスタ内に粉粒体燃料を供給する
と共に、前記コンバスタから飛散する粉粒体燃料を集塵
してリサイクルドレンとして一部を外部熱交換器を介し
、残りを直接前記コンバスタ内に供給する高速流動床ボ
イラの主蒸気圧力を制御する方法において、前記外部熱
交換器へ導入するリサイクルドレン流量と、前記コンバ
スタに投入する前記粉粒体燃料投入量とを調整すること
を特徴とする高速流動床ボイラの主蒸気圧力制御方法。
The granular fuel is supplied into the combustor formed by the furnace wall, and the granular fuel scattered from the combustor is collected and used as a recycling drain. A part of it is passed through an external heat exchanger, and the rest is directly sent to the combustor. The method for controlling the main steam pressure of a high-speed fluidized bed boiler supplied to the combustor is characterized by adjusting the flow rate of recycle drain introduced to the external heat exchanger and the amount of the granular fuel input to the combustor. Main steam pressure control method for high speed fluidized bed boiler.
JP15183485A 1985-07-10 1985-07-10 Method of controlling main steam pressure of high-speed fluidized bed boiler Pending JPS6213901A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15183485A JPS6213901A (en) 1985-07-10 1985-07-10 Method of controlling main steam pressure of high-speed fluidized bed boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15183485A JPS6213901A (en) 1985-07-10 1985-07-10 Method of controlling main steam pressure of high-speed fluidized bed boiler

Publications (1)

Publication Number Publication Date
JPS6213901A true JPS6213901A (en) 1987-01-22

Family

ID=15527316

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15183485A Pending JPS6213901A (en) 1985-07-10 1985-07-10 Method of controlling main steam pressure of high-speed fluidized bed boiler

Country Status (1)

Country Link
JP (1) JPS6213901A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH025273A (en) * 1988-06-24 1990-01-10 Asahi Chem Ind Co Ltd Cartridge case for optical disk of large diameter
JPH02287001A (en) * 1989-04-27 1990-11-27 Mitsubishi Heavy Ind Ltd External heat exchanger for recirculation-fluidized bed boiler

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH025273A (en) * 1988-06-24 1990-01-10 Asahi Chem Ind Co Ltd Cartridge case for optical disk of large diameter
JPH02287001A (en) * 1989-04-27 1990-11-27 Mitsubishi Heavy Ind Ltd External heat exchanger for recirculation-fluidized bed boiler

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