JPS60226604A - Controller for temperature of steam from coal burning boiler - Google Patents

Controller for temperature of steam from coal burning boiler

Info

Publication number
JPS60226604A
JPS60226604A JP8280284A JP8280284A JPS60226604A JP S60226604 A JPS60226604 A JP S60226604A JP 8280284 A JP8280284 A JP 8280284A JP 8280284 A JP8280284 A JP 8280284A JP S60226604 A JPS60226604 A JP S60226604A
Authority
JP
Japan
Prior art keywords
steam temperature
soot blower
temperature
steam
heat transfer
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
JP8280284A
Other languages
Japanese (ja)
Inventor
岸川 忠弘
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 JP8280284A priority Critical patent/JPS60226604A/en
Publication of JPS60226604A publication Critical patent/JPS60226604A/en
Pending legal-status Critical Current

Links

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】 きボイラの蒸気温度制御装置に関する。[Detailed description of the invention] The present invention relates to a steam temperature control device for a boiler.

従来の石炭焚きボイラの蒸気温度制御は、制御する蒸気
温度を計測し、設定との差を(比例士積分)機能による
フードバック方式によって蒸気温度を設定値に保つ方式
である。
Conventional steam temperature control for coal-fired boilers is a method that measures the steam temperature to be controlled and maintains the steam temperature at a set value using a feedback method using a proportional integral function to calculate the difference from the set value.

この蒸気温度を設定値に保つ手段は、ドラム形ボイラで
は冷水噴霧の減温、バーナチルト、ガス再循環及びガス
ダンパ方式などがあり、また超臨界圧ボイラではドラム
形ボイラに加えて水燃比率方式がとられている。
Methods for keeping the steam temperature at the set value include cooling water spray, burner tilt, gas recirculation, and gas damper methods for drum-type boilers, and water-fuel ratio methods for supercritical pressure boilers in addition to drum-type boilers. It is taken.

一方、石炭焚きボイラのスートブロワは現在省エネルギ
の観点から回数を大巾に減する方向にあるが、スートブ
ロワ稼動によって伝熱面の汚れを落す効果も大きい。従
来の蒸気温度と設定値との偏差による制御方式では、蒸
気温度の変動中が太き(なりつつある。
On the other hand, the current trend is to drastically reduce the number of soot blowers used in coal-fired boilers in order to save energy, but operating the soot blower also has a great effect in removing dirt from heat transfer surfaces. In the conventional control method based on the deviation between the steam temperature and the set value, the deviation of the steam temperature becomes large (and is becoming large).

しかして、従来によれば、伝熱面の熱吸収量が低下して
(ると、スートブロワ起動盤からの指令によってスート
ブロワを動作によって伝熱面の熱吸収が良好になり、伝
熱面の出口蒸気温度が上昇する。この上昇した温度を下
げるためには、減温器に冷水を多(噴霧させ、伝熱面の
入口蓋゛気温度を下げる必要がある。
However, according to the conventional method, when the amount of heat absorption on the heat transfer surface decreases, the soot blower is operated according to a command from the soot blower startup board, which improves the heat absorption on the heat transfer surface, and the outlet of the heat transfer surface The steam temperature rises. In order to lower this increased temperature, it is necessary to spray a large amount of cold water into the desuperheater to lower the air temperature at the inlet lid of the heat transfer surface.

しかし、従来は、伝熱面の出口蒸気温度によって制御し
ていたため、スートブロワの動作によって熱吸収が良好
となり、それによる入口蒸気温度を下げる必要があるの
に、瞬間的なズレが生じ、そのため減温器の作動が遅れ
るという欠点があった。
However, in the past, control was performed by the outlet steam temperature of the heat transfer surface, and although the soot blower operation would improve heat absorption and thereby lower the inlet steam temperature, a momentary deviation would occur, resulting in a reduction in heat absorption. The drawback was that the warmer was delayed in operation.

本発明は、このような従来の問題を解消するためになさ
れたもので、スートブロワ稼動による伝熱面クリーニン
グで必然的に発生する蒸気温度の変動を考慮して、現状
制御方式の先行動作とすることにより、スートブロワ稼
動時の蒸気温度変動をなくす蒸気温度制御装置を提供す
ることを目的とする。
The present invention has been made to solve these conventional problems, and takes into consideration the fluctuations in steam temperature that inevitably occur when cleaning the heat transfer surface by operating the soot blower, and makes it an advance operation of the current control method. Therefore, it is an object of the present invention to provide a steam temperature control device that eliminates steam temperature fluctuations during operation of a soot blower.

以下図面を参照して本発明の好適な一実施例について詳
述する。
A preferred embodiment of the present invention will be described in detail below with reference to the drawings.

図面は、スートブロワを装備した石炭焚きボイラの蒸気
温度制御装置の一例を示す。
The drawing shows an example of a steam temperature control device for a coal-fired boiler equipped with a soot blower.

蒸気温度検出計1で計測された温度は蒸気温度設定器2
と偏差をとって制御器3Aで演算し、冷水調節弁4を開
閉して伝熱面5Aを出た蒸気に減温器6部で冷水を噴霧
させて温度を下げ、伝熱面5Bでの熱吸収後、蒸気温度
検出計1で計測される蒸気温度が設定器2と偏差がない
ようにしている。
The temperature measured by the steam temperature detector 1 is determined by the steam temperature setting device 2.
The deviation is calculated by the controller 3A, and the cold water control valve 4 is opened and closed to spray cold water onto the steam exiting the heat transfer surface 5A in the desuperheater 6 to lower the temperature. After heat absorption, the steam temperature measured by the steam temperature detector 1 is made to have no deviation from the setting device 2.

しかして、本実施例では、伝熱面5Bにスートブロワ7
が設置されており、伝熱面が灰で汚れて伝熱面5Bの熱
吸収が下がり、冷水調節弁4は閉つて行きやがて全閉と
なり、更に汚れれば蒸気温度が設定温度より下がること
になる。そういう時期に、伝熱面5Bの汚れをクリーニ
ングするために、スートブロワ7が動作する。その結果
、伝熱面5Bの熱吸収が良好になれば、当然ながら、伝
熱面5Bの入口温度を下げる必要がある。この入口温度
を下げるためには、冷水調節弁4を開がなければならな
い。
Therefore, in this embodiment, the soot blower 7 is placed on the heat transfer surface 5B.
is installed, the heat transfer surface becomes dirty with ash, the heat absorption of the heat transfer surface 5B decreases, the cold water control valve 4 closes and eventually becomes fully closed, and if it gets even more dirty, the steam temperature will drop below the set temperature. Become. At such times, the soot blower 7 operates to clean the dirt on the heat transfer surface 5B. As a result, if the heat absorption of the heat transfer surface 5B becomes good, it is naturally necessary to lower the inlet temperature of the heat transfer surface 5B. In order to lower this inlet temperature, the cold water control valve 4 must be opened.

そこで、スートブロワ起動盤8のスートブロワ起動信号
を蒸気温度制御の先行信号として、制御器3Bの演算信
号全制御器3Aの演算信号に加算し、冷水調節弁4の開
閉信号とする。
Therefore, the soot blower activation signal from the soot blower activation board 8 is added to the calculation signal of the controller 3B and the calculation signal of all controllers 3A as a preceding signal for steam temperature control, and is used as an opening/closing signal for the cold water control valve 4.

以上述べたように、伝熱面5Bの熱吸収量が低下してく
ると、スートブロワ起動盤8からの指令によってスート
ブロワ7を動作させる。スートブロワ7の動作によって
伝熱面5Bの熱吸収が良好になり、伝熱面5Bの出口蒸
気温度が上昇する。
As described above, when the heat absorption amount of the heat transfer surface 5B decreases, the soot blower 7 is operated by a command from the soot blower activation board 8. The operation of the soot blower 7 improves the heat absorption of the heat transfer surface 5B, and the outlet steam temperature of the heat transfer surface 5B increases.

この上昇した温度を下げるためには、減温器6に )冷
水を多く噴霧させ、伝熱面5Bの入口蒸気温度を下げる
必要がある。この操作は、スートブロワ7が動作すると
、必然的に発生させる必要がある。
In order to lower this increased temperature, it is necessary to spray a large amount of cold water into the desuperheater 6 to lower the inlet steam temperature of the heat transfer surface 5B. This operation necessarily needs to occur when the soot blower 7 operates.

そこで、蒸気温度検出計1によって計測した温度が蒸気
温度設定器2との偏差が出る前に、スートブロワ起動盤
8のスートブロワ動作信号を制御器3Bでスートブロワ
7の動作による蒸気温度上昇と、それを相殺する冷水調
節弁4の開方向量の演算を行い、制御器3Aの演算信号
に先行動作として加算し、冷水調節弁4を動作し、スー
トブロワ7の動作による蒸気温度の変動を少なくする制
御をする。
Therefore, before the temperature measured by the steam temperature detector 1 deviates from the steam temperature setting device 2, the soot blower operation signal from the soot blower activation board 8 is sent to the controller 3B to detect the rise in steam temperature caused by the operation of the soot blower 7 and the increase in steam temperature. Calculate the opening direction amount of the cold water control valve 4 to offset, add it to the calculation signal of the controller 3A as a preliminary operation, operate the cold water control valve 4, and perform control to reduce fluctuations in steam temperature due to the operation of the soot blower 7. do.

したがって、本発明によれば、石炭焚きボイラのスート
ブロワ稼動時の蒸気温度変動値を先行動作情報として蒸
気温度制御回路に組み込むことにより、スートブロワの
動作による温度の変動を少な(することができる。
Therefore, according to the present invention, temperature fluctuations due to the operation of the soot blower can be reduced by incorporating the steam temperature fluctuation value during operation of the soot blower of a coal-fired boiler into the steam temperature control circuit as advance operation information.

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

図面は、本発明による石炭焚きボイラの蒸気温度制御装
置の一例を示す図である。 l・・蒸気温度検出計、2・・蒸気温度設定器、3A、
3B・・制御器、4・・冷水調節弁、5A。 5B・・伝熱面、6・・減温器、7・・スートブロワ、
8・◆スートブロワ起動盤。
The drawing is a diagram showing an example of a steam temperature control device for a coal-fired boiler according to the present invention. l...Steam temperature detector, 2...Steam temperature setting device, 3A,
3B...Controller, 4...Cold water control valve, 5A. 5B...Heat transfer surface, 6...Desuperheater, 7...Soot blower,
8.◆Soot blower starting board.

Claims (1)

【特許請求の範囲】[Claims] 石炭焚きボイラのスートブロワ稼動時の蒸気温度変動値
を先行動作情報として蒸気温度制御回路に組み込んだこ
とを特徴とする石炭焚きボイラの蒸気温度制御装置。
A steam temperature control device for a coal-fired boiler, characterized in that a steam temperature fluctuation value during operation of a soot blower of the coal-fired boiler is incorporated into a steam temperature control circuit as advance operation information.
JP8280284A 1984-04-26 1984-04-26 Controller for temperature of steam from coal burning boiler Pending JPS60226604A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8280284A JPS60226604A (en) 1984-04-26 1984-04-26 Controller for temperature of steam from coal burning boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8280284A JPS60226604A (en) 1984-04-26 1984-04-26 Controller for temperature of steam from coal burning boiler

Publications (1)

Publication Number Publication Date
JPS60226604A true JPS60226604A (en) 1985-11-11

Family

ID=13784535

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8280284A Pending JPS60226604A (en) 1984-04-26 1984-04-26 Controller for temperature of steam from coal burning boiler

Country Status (1)

Country Link
JP (1) JPS60226604A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62217006A (en) * 1986-03-19 1987-09-24 株式会社日立製作所 Automatic controller for boiler
JPS6365206A (en) * 1986-09-05 1988-03-23 株式会社東芝 Boiler steam temperature controller
JP2015007511A (en) * 2013-06-26 2015-01-15 株式会社日立製作所 Boiler control device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62217006A (en) * 1986-03-19 1987-09-24 株式会社日立製作所 Automatic controller for boiler
JPS6365206A (en) * 1986-09-05 1988-03-23 株式会社東芝 Boiler steam temperature controller
JP2015007511A (en) * 2013-06-26 2015-01-15 株式会社日立製作所 Boiler control device

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