JPH0742906A - Method and apparatus for controlling temperature of steam in boiler - Google Patents

Method and apparatus for controlling temperature of steam in boiler

Info

Publication number
JPH0742906A
JPH0742906A JP19101493A JP19101493A JPH0742906A JP H0742906 A JPH0742906 A JP H0742906A JP 19101493 A JP19101493 A JP 19101493A JP 19101493 A JP19101493 A JP 19101493A JP H0742906 A JPH0742906 A JP H0742906A
Authority
JP
Japan
Prior art keywords
boiler
load
steam temperature
flow rate
water injection
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
JP19101493A
Other languages
Japanese (ja)
Inventor
Masaru Morio
勝 森尾
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 JP19101493A priority Critical patent/JPH0742906A/en
Publication of JPH0742906A publication Critical patent/JPH0742906A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a control system for controlling a temperature of steam of a boiler in which the number of ON-OFF times of a fed water flow rate adjusting valve is reduced in respect to a variation in load in high frequent operation and an adjustment of a temperature of steam is performed safely without damaging an over-heat reducing device. CONSTITUTION:A temperature of reheated steam is detected by a reheated steam temperature sensor 17 of a boiler when a boiler load is set, a degree of opening of a fed water flow rate adjusting valve 15 for an over-heating reducer for a reheater is controlled in response to difference between the detected value and a value of a steam temperature setting device 19. At this time, when the boiler load is set, the degree of opening of the valve is set to be zero. Then, when the load is varied in a high frequent manner, the adjusting valve 15 is not operated when a minute load is varied during an increasing of load, but a degree of opening of the adjusting valve 15 is determined in response to a signal of a reheated steam temperature setting device 24 for the variation of load under an operation of a changing- over device 23 only when the load is substantially changed during an increasing of the load. In this way, the number of times of ON-OFF of the adjusting valve 15 can be reduced by about 1/10 as compared with that of the prior art and further a thermal shock of the over- heating reducer can be eliminated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は過熱低減器を有するボイ
ラの蒸気温度制御方式に係り、特に高頻度負荷変化に好
適なボイラの再熱蒸気温度制御方式に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam temperature control system for a boiler having an overheat reducer, and more particularly to a reheat steam temperature control system for a boiler suitable for frequent load changes.

【0002】[0002]

【従来の技術】従来の過熱低減器を有するボイラの蒸気
温度制御方式における過熱低減器注水制御系統図を図3
に示す。図3の前記制御系統図において、蒸気温度の制
御は次のように行われる。主蒸気温度検出器16でボイ
ラの蒸気温度を検出し、蒸気温度設定器19の蒸気温度
設定値との差を減算器18で求め、この値を比例積分器
20で比例積分した後、温度制御を良好に行うために加
算器21において負荷などの先行回路演算器22の先行
信号と加算して、この加算値により手動−自動切替器2
8を介してボイラの過熱器の過熱低減器(図示せず)の
注水流量調節弁14を制御するものである。
2. Description of the Related Art A conventional superheat reducer water injection control system in a steam temperature control system for a boiler having a superheat reducer is shown in FIG.
Shown in. In the control system diagram of FIG. 3, control of the steam temperature is performed as follows. The steam temperature of the boiler is detected by the main steam temperature detector 16, the difference from the steam temperature set value of the steam temperature setter 19 is obtained by the subtracter 18, and this value is proportionally integrated by the proportional integrator 20 and then temperature controlled. In order to satisfactorily perform the above, the adder 21 adds the preceding signal from the preceding circuit calculator 22 such as a load, and the added value causes the manual-automatic switch 2
8 for controlling the water injection flow rate control valve 14 of the overheat reducer (not shown) of the boiler superheater.

【0003】図3に示す蒸気温度制御方式において、ボ
イラの蒸気温度が規定値以上に上昇すると過熱器注水流
量調節弁14は開動作し、蒸気温度が規定値よりも低下
すると注水流量調節弁14は全閉動作をする。高頻度負
荷変化に対して注水流量調節弁14はON−OFFを繰
り返し、過熱器の過熱低減器に熱衝撃を与えることとな
り過熱低減器の損傷が懸念されていた。また、図示して
いないが、再熱器の過熱低減器の注水流量調節弁も図3
と同様な方法で制御され、再熱温度の調整が行われる。
In the steam temperature control system shown in FIG. 3, when the steam temperature of the boiler rises above a specified value, the superheater water injection flow rate control valve 14 opens, and when the steam temperature falls below the specified value, the water injection flow rate control valve 14 Is fully closed. The water injection flow rate control valve 14 is repeatedly turned on and off in response to a high frequency load change, and thermal shock is given to the overheat reducer of the superheater, which may cause damage to the overheat reducer. Although not shown, the water injection flow rate control valve of the overheat reducer of the reheater is also shown in FIG.
The reheat temperature is adjusted in the same manner as described above.

【0004】[0004]

【発明が解決しようとする課題】上記従来技術は過熱低
減器の損傷についての配慮がされておらず高頻度負荷変
化が制約されるという問題があった。そこで、本発明の
目的は高頻度負荷変化に対して注水流量調節弁のON−
OFF回数を低減し、過熱低減器を損傷させることなく
安全に蒸気温度の調整を図るボイラ蒸気温度の制御方式
を提供することである。
The above-mentioned prior art has a problem in that damage to the overheat reducer is not taken into consideration and high-frequency load change is restricted. Therefore, an object of the present invention is to turn on the water injection flow control valve for high-frequency load changes.
It is an object of the present invention to provide a boiler steam temperature control method that reduces the number of times of turning OFF and safely adjusts the steam temperature without damaging the overheat reducer.

【0005】[0005]

【課題を解決するための手段】本発明の上記目的は次の
構成によって達成される。すなわち、ボイラの下流部の
蒸気温度を検出し、その検出値と蒸気温度設定値との偏
差に基づきボイラと過熱器との間、またはボイラと再熱
器の間に設置される過熱低減器への注水流量を制御する
ボイラ蒸気温度制御方法において、ボイラ負荷整定状態
では、前記過熱低減器への注水流量は行わず、高頻度の
負荷変化時には、負荷上昇中において微小負荷変化があ
る場合には注水流量調節を行わず、大幅な負荷変化があ
る場合にのみ前記過熱低減器への注水流量を調節するボ
イラ蒸気温度制御方法、または、ボイラの下流部の蒸気
温度を検出する蒸気温度検出器と、該検出器の蒸気温度
検出値と蒸気温度設定値との偏差の演算器と、該演算器
の演算値に基づきボイラと過熱器との間またはボイラと
再熱器との間に設置される過熱低減器への注水配管の流
量を制御する注水流量調節弁と、ボイラ負荷整定状態で
は前記注水流量調節弁を作動させず、高頻度負荷変化時
には負荷上昇中の大幅な負荷変化がある場合のみ前記注
水流量調節弁を作動させ、前記過熱低減器への注水流量
を調節する注水流量制御装置とを備えたボイラ蒸気温度
制御装置である。
The above objects of the present invention can be achieved by the following constitutions. That is, the steam temperature in the downstream portion of the boiler is detected, and based on the deviation between the detected value and the steam temperature set value, between the boiler and the superheater, or to the overheat reducer installed between the boiler and the reheater. In the boiler steam temperature control method for controlling the water injection flow rate, in the boiler load settling state, the water injection flow rate to the superheat reducer is not performed, and when there is a minute load change during load increase during high-frequency load changes. A boiler steam temperature control method that adjusts the water injection flow rate to the superheat reducer only when there is a large load change without adjusting the water injection flow rate, or a steam temperature detector that detects the steam temperature in the downstream part of the boiler. , A calculator of the deviation between the detected steam temperature value of the detector and the set value of the steam temperature, and is installed between the boiler and the superheater or between the boiler and the reheater based on the calculated value of the calculator Note to overheat reducer Do not operate the pouring water flow rate control valve that controls the flow rate of the pipe and the pouring water flow rate control valve in the boiler load settling state, and set the pouring water flow rate control valve only when there is a large load change during load increase during high frequency load changes. It is a boiler steam temperature control device provided with a water injection flow rate control device which is operated and adjusts the water injection flow rate to the superheat reducer.

【0006】[0006]

【作用】ボイラの過熱蒸気温度を過熱蒸気配管に設けら
れた検出器で検出し、その検出値と過熱蒸気温度設定器
の値との偏差に基づき過熱器過熱低減器への注水流量を
調節する各調節弁の開度を制御するが、このとき、前記
注水流量調節のON−OFF回数の低減を図るためにボ
イラ負荷整定時には弁開度をゼロとし、高頻度の負荷変
化時には、負荷上昇中において微小負荷変化のときは注
水流量調節弁を作動させず、負荷上昇中において大幅な
負荷変化がある場合にのみ前記注水流量調節弁の開度を
負荷変化に応じた値に変える。こうして、注水流量調節
弁のON−OFF回数を従来に比べて約1/10に低減
することができ、過熱低減器の熱衝撃をなくすことが可
能となった。この結果過熱低減器を損傷することなく安
全に過熱蒸気温度の調整を行うことが可能となった。上
記過熱蒸気温度制御方式を再熱蒸気温度の制御に適用
し、再熱器の過熱低減器の損傷を防ぎながら、再熱蒸気
温度の調整を行うこともできる。
[Operation] The superheated steam temperature of the boiler is detected by the detector installed in the superheated steam piping, and the flow rate of water injected to the superheater overheat reducer is adjusted based on the deviation between the detected value and the value of the superheated steam temperature setting device. The opening of each control valve is controlled. At this time, in order to reduce the number of ON-OFF of the water injection flow rate control, the valve opening is set to zero at the boiler load settling, and the load is increasing during frequent load changes. In the case of a small load change, the water injection flow rate control valve is not operated, and the opening degree of the water injection flow rate control valve is changed to a value according to the load change only when a large load change occurs while the load is increasing. In this way, the number of times the water injection flow rate control valve is turned on and off can be reduced to about 1/10 of that of the conventional case, and the thermal shock of the overheat reducer can be eliminated. As a result, it became possible to adjust the superheated steam temperature safely without damaging the superheat reducer. The above superheated steam temperature control method can be applied to control the reheated steam temperature, and the reheated steam temperature can be adjusted while preventing damage to the superheat reducer of the reheater.

【0007】[0007]

【実施例】本発明の一実施例を図面と共に説明する。本
実施例のボイラ系統図を図2に示す。ボイラ4への給水
は、まず、給水ポンプ1から高圧給水加熱器2に送られ
て加熱された後、節炭器3を経てボイラ4に送られる。
ボイラ4で生成した蒸気は一次過熱器5、過熱器過熱低
減器12および二次過熱器6を経て高圧タービン7へ送
られる。高圧タービン7の排気は一次再熱器8、再熱器
過熱低減器13および二次再熱器9を経て中圧タービン
10へ蒸気を送るよう系統構成されている。なお、中圧
タービン10から排出される蒸気は復水器11で熱回収
される。高圧タービン7へ供給される蒸気の配管には主
蒸気温度検出器16が、中圧タービン10へ供給される
蒸気の配管には再熱蒸気温度検出器17がそれぞれ設け
られている。また、高圧給水加熱器2で加熱され、ボイ
ラ4へ供給される給水の一部は、節炭器3の入口部から
抽水されて過熱器注水流量調節弁14の設けられた分岐
配管から過熱器過熱低減器12に供給される。また、給
水ポンプ1の中段からの圧力の低い給水の一部は、抽水
されて再熱器注水流量調節弁15が設けられた分岐配管
から再熱器過熱低減器13に供給可能である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to the drawings. A boiler system diagram of this embodiment is shown in FIG. The water supplied to the boiler 4 is first sent from the water supply pump 1 to the high-pressure feed water heater 2 and heated, and then sent to the boiler 4 via the economizer 3.
The steam generated in the boiler 4 is sent to the high-pressure turbine 7 via the primary superheater 5, the superheater superheat reducer 12 and the secondary superheater 6. The exhaust of the high-pressure turbine 7 is systematically configured to send steam to the intermediate-pressure turbine 10 via the primary reheater 8, the reheater overheat reducer 13 and the secondary reheater 9. The steam discharged from the intermediate-pressure turbine 10 is recovered in the condenser 11. A main steam temperature detector 16 is provided in a pipe of steam supplied to the high-pressure turbine 7, and a reheat steam temperature detector 17 is provided in a pipe of steam supplied to the intermediate-pressure turbine 10. Further, a part of the feed water heated by the high-pressure feed water heater 2 and supplied to the boiler 4 is extracted from the inlet of the economizer 3, and is discharged from the branch pipe provided with the superheater water injection flow rate control valve 14 to the superheater. It is supplied to the overheat reducer 12. Further, a part of the low-pressure water supply from the middle stage of the water supply pump 1 can be extracted and supplied to the reheater overheat reducer 13 from the branch pipe provided with the reheater water injection flow rate control valve 15.

【0008】上記構成からなる本実施例において、過熱
器過熱低減器12は主蒸気温度を規定値に調整するよう
に主蒸気温度検出器16の検出主蒸気温度に基づき過熱
器注水流量調節弁14を調整する。一方、再熱蒸気温度
は再熱蒸気温度検出器17と再熱器注水流量調節弁15
により規定値になるように調整される。また、本実施例
による蒸気温度制御系統図を図1に示す。再熱蒸気温度
は再熱蒸気温度検出器17により検出し、該検出蒸気温
度と定格温度の蒸気温度設定器19との偏差を減算器1
8により開度調整信号を作成する。蒸気温度制御を良好
に行うために負荷などの先行回路演算器22と加算器2
1により先行的に制御する。
In this embodiment having the above structure, the superheater / superheat reducer 12 adjusts the main steam temperature to a specified value on the basis of the detected main steam temperature of the main steam temperature detector 16 to superheater water injection flow control valve 14 Adjust. On the other hand, the reheated steam temperature is determined by the reheated steam temperature detector 17 and the reheater water injection flow control valve 15
Is adjusted to the specified value. A steam temperature control system diagram according to the present embodiment is shown in FIG. The reheated steam temperature is detected by the reheated steam temperature detector 17, and the difference between the detected steam temperature and the steam temperature setter 19 of the rated temperature is subtracted by the subtracter 1
An opening adjustment signal is created by 8. The preceding circuit calculator 22 such as a load and the adder 2 in order to perform good steam temperature control
1 to control in advance.

【0009】ボイラの負荷整定状態では蒸気温度設定器
19は非常時にのみ作動する蒸気温度設定器としてお
り、このため再熱器注水流量調節弁15は全閉となる。
また、高頻度負荷変化のときの負荷上昇時は負荷に見合
ってボイラへの燃料量が増となるため再熱蒸気温度は上
昇傾向となるので、このようなときは負荷変化用の再熱
蒸気温度設定器24の設定温度を定格温度+αの値とし
切替器23により注水流量調節弁15が作動するように
して再熱蒸気温度を規定値に調整する。再熱蒸気温度設
定器24は再熱蒸気温度の温度上昇率が所定値(a℃)
/分以上であり、しかも大幅な負荷変化があった時にの
み作動する構成としているので、高頻度負荷変化であっ
ても微小負荷変化時は再熱器注水流量調節弁15を作動
させることがない。そのため、本実施例の蒸気温度制御
方式では、図3に示す従来の蒸気温度制御方式のよう
に、高頻度負荷変化時の微小負荷変化に対しては注水流
量調節弁15はON−OFF回数を繰り返すことがな
く、従って、再熱器過熱低減器13に損傷を与えるよう
なことはない。
In the boiler load settling state, the steam temperature setting device 19 is a steam temperature setting device that operates only in an emergency, so that the reheater water injection flow rate control valve 15 is fully closed.
Also, when the load increases during high-frequency load changes, the amount of fuel to the boiler increases in proportion to the load, and the reheat steam temperature tends to rise. The reheat steam temperature is adjusted to a specified value by setting the set temperature of the temperature setter 24 to the value of the rated temperature + α so that the water injection flow rate control valve 15 is operated by the switch 23. The reheat steam temperature setter 24 has a predetermined rate (a ° C.) for the temperature rise rate of the reheat steam temperature.
/ Min or more, and since it is configured to operate only when there is a large load change, the reheater water injection flow rate control valve 15 is not operated even when the load is high, even when the load is high. . Therefore, in the steam temperature control method of the present embodiment, as in the conventional steam temperature control method shown in FIG. 3, the pouring water flow rate control valve 15 sets the ON-OFF frequency to a small load change at the time of a high frequency load change. It does not repeat and therefore does not damage the reheater overheat reducer 13.

【0010】非常用の蒸気温度設定器19からの再熱蒸
気温度設定器24への切替器23による切り替えは再熱
蒸気温度が温度上昇率a℃/分以上であることと、負荷
信号と負荷信号の遅れ動作器25からの出力信号との偏
差を減算器26で計算し、それが大巾負荷変化に相当す
ることを信号検出器27で検出することの両方の検出信
号により行われる。こうして、ボイラが高頻度で負荷変
化していても、その負荷変化が微小負荷変化時は再熱器
注水流量調節弁15は作動しない。しかし、大巾な負荷
変化で、かつ再熱蒸気温度が上昇傾向にあるときは再熱
蒸気温度設定器24の設定温度を定格温度+αの値とす
ることにより注水流量調節弁15を作動させて、再熱蒸
気温度を規定値に調整することが可能となる。また、ボ
イラ負荷整定状態では切替器23により非常用の蒸気温
度設定器19側に切り替わるため、注水流量調節弁15
は全閉であり運用上何んら支障とならない。
Switching from the emergency steam temperature setting device 19 to the reheat steam temperature setting device 24 by means of the switching device 23 means that the reheat steam temperature is equal to or higher than the temperature rise rate a ° C./min, the load signal and the load. The difference between the signal and the output signal from the delay operation unit 25 is calculated by the subtractor 26, and the signal detector 27 detects that it corresponds to a large load change. Thus, even if the boiler changes its load at a high frequency, the reheater water injection flow rate control valve 15 does not operate when the change in load is minute. However, when there is a large change in load and the reheat steam temperature tends to rise, the water injection flow rate control valve 15 is operated by setting the set temperature of the reheat steam temperature setter 24 to the value of the rated temperature + α. It becomes possible to adjust the reheat steam temperature to a specified value. Further, in the boiler load settling state, since the switching device 23 switches to the emergency steam temperature setting device 19 side, the water injection flow control valve 15
Is fully closed and does not hinder operation.

【0011】こうして、本実施例の蒸気温度制御方式で
はボイラの高頻度負荷変化の微小負荷変化に対しては注
水流量調節弁15はON−OFF回数を繰り返すことが
なく、再熱器過熱低減器13に損傷を与えるおそれはな
い。また、本実施例の蒸気温度制御方式は過熱器過熱低
減器12の注水流量調節弁14にも同様な制御方式が適
用でき、注水流量調節弁14のON−OFF回数を繰り
返すことがなく、従って過熱器過熱低減器12に損傷を
与えるおそれもない。なお、図1のボイラの注水系統図
は再熱蒸気温度の制御方式を図示したものであるが、注
水流量調節弁14、15のON−OFF回数を低減する
方法として蒸気温度設定値を定格値よりも低くする方法
がある。しかし、この制御方法は蒸気温度が低下した状
態での運転を行うこととなりプラント効率低下の運用と
なるため、あまり適した方法とは言えないが、プラント
効率の低下をいとわない場合は採用できる。
In this way, in the steam temperature control system of this embodiment, the water injection flow rate control valve 15 does not repeat the ON-OFF times for a minute load change of the high frequency load change of the boiler, and the reheater overheat reducer is not required. There is no danger of damaging 13. In addition, the steam temperature control method of the present embodiment can be applied to the water injection flow rate control valve 14 of the superheater / overheat reducer 12 as well, and the number of times the water injection flow rate control valve 14 is turned ON / OFF is not repeated. There is also no risk of damaging the superheater overheat reducer 12. Although the boiler water injection system diagram of FIG. 1 illustrates the control method of the reheated steam temperature, the steam temperature set value is a rated value as a method for reducing the number of ON-OFF times of the water injection flow rate control valves 14 and 15. There is a way to lower it. However, this control method cannot be said to be a very suitable method because the operation is performed in a state where the steam temperature is lowered and the plant efficiency is lowered. However, this control method can be adopted when the reduction in plant efficiency is acceptable.

【0012】[0012]

【発明の効果】本発明によれば注水流量調節弁のON−
OFF回数低減を図ることができるので高頻度負荷変化
に対しても過熱器過熱低減器または再熱器過熱低減器を
損傷することなく安全に蒸気温度調整を行うことができ
る。
According to the present invention, the water flow rate control valve is turned on.
Since the number of times of OFF can be reduced, the steam temperature can be adjusted safely even if the load changes frequently, without damaging the overheater overheat reducer or the reheater overheat reducer.

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

【図1】 本発明の一実施例のボイラ注水制御系統図で
ある。
FIG. 1 is a boiler water injection control system diagram of an embodiment of the present invention.

【図2】 本発明の一実施例に用いられる一般的なボイ
ラ系統図である。
FIG. 2 is a general boiler system diagram used in one embodiment of the present invention.

【図3】 従来技術のボイラ注水制御系統図である。FIG. 3 is a diagram of a conventional boiler water injection control system.

【符号の説明】[Explanation of symbols]

1…給水ポンプ、2…高圧給水加熱器、3…節炭器、4
…ボイラ、5…一次過熱器、6…二次過熱器、7…高圧
タービン、8…一次再熱器、9…二次再熱器、10…中
圧タービン、11…復水器、12…過熱器過熱低減器、
13…再熱器過熱低減器、14…過熱器注水流量調節
弁、15…再熱器注水流量調節弁、16…主蒸気温度検
出器、17…再熱蒸気温度検出器、19…蒸気温度設定
器、22…先行回路演算器、23…切替器、24…再熱
蒸気温度設定器
1 ... water supply pump, 2 ... high pressure water heater, 3 ... economizer, 4
... Boiler, 5 ... Primary superheater, 6 ... Secondary superheater, 7 ... High pressure turbine, 8 ... Primary reheater, 9 ... Secondary reheater, 10 ... Medium pressure turbine, 11 ... Condenser, 12 ... Superheater overheat reducer,
13 ... Reheater overheat reducer, 14 ... Superheater water injection flow rate control valve, 15 ... Reheater water injection flow rate control valve, 16 ... Main steam temperature detector, 17 ... Reheat steam temperature detector, 19 ... Steam temperature setting Unit, 22 ... Advance circuit calculator, 23 ... Switching unit, 24 ... Reheat steam temperature setting unit

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ボイラの下流部の蒸気温度を検出し、そ
の検出値と蒸気温度設定値との偏差に基づきボイラと過
熱器との間、またはボイラと再熱器の間に設置される過
熱低減器への注水流量を制御するボイラ蒸気温度制御方
法において、 ボイラ負荷整定状態では、前記過熱低減器への注水流量
は行わず、高頻度の負荷変化時には、負荷上昇中におい
て微小負荷変化がある場合には注水流量調節を行わず、
大幅な負荷変化がある場合にのみ前記過熱低減器への注
水流量を調節することを特徴とするボイラ蒸気温度制御
方法。
1. Superheat installed between a boiler and a superheater, or between a boiler and a reheater, based on a deviation between a detected value and a steam temperature set value, the steam temperature being detected downstream of the boiler. In the boiler steam temperature control method that controls the flow rate of water injected to the reducer, in the boiler load settling state, the flow rate of water injected to the overheat reducer is not performed, and when the load changes frequently, there is a small load change during load increase. In case of not adjusting the water injection flow rate,
A boiler steam temperature control method, wherein the flow rate of water injected into the superheat reducer is adjusted only when there is a large change in load.
【請求項2】 ボイラの下流部の蒸気温度を検出する蒸
気温度検出器と、該検出器の蒸気温度検出値と蒸気温度
設定値との偏差の演算器と、該演算器の演算値に基づき
ボイラと過熱器との間またはボイラと再熱器との間に設
置される過熱低減器への注水配管の流量を制御する注水
流量調節弁と、ボイラ負荷整定状態では前記注水流量調
節弁を作動させず、高頻度負荷変化時には負荷上昇中の
大幅な負荷変化がある場合のみ前記注水流量調節弁を作
動させ、前記過熱低減器への注水流量を調節する注水流
量制御装置とを備えたことを特徴とするボイラ蒸気温度
制御装置。
2. A steam temperature detector for detecting a steam temperature in a downstream portion of a boiler, a calculator of a deviation between a steam temperature detection value of the detector and a steam temperature set value, and a calculation value of the calculator. A water injection flow rate control valve that controls the flow rate of the water injection pipe to the superheat reducer installed between the boiler and the superheater or between the boiler and the reheater, and the water injection flow rate control valve is operated in the boiler load settling state. In the case of a high frequency load change, the water injection flow rate control device that operates the water injection flow rate control valve only when there is a large load change during load increase and adjusts the water injection flow rate to the superheat reducer is provided. Characteristic boiler steam temperature control device.
JP19101493A 1993-08-02 1993-08-02 Method and apparatus for controlling temperature of steam in boiler Pending JPH0742906A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19101493A JPH0742906A (en) 1993-08-02 1993-08-02 Method and apparatus for controlling temperature of steam in boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19101493A JPH0742906A (en) 1993-08-02 1993-08-02 Method and apparatus for controlling temperature of steam in boiler

Publications (1)

Publication Number Publication Date
JPH0742906A true JPH0742906A (en) 1995-02-10

Family

ID=16267448

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19101493A Pending JPH0742906A (en) 1993-08-02 1993-08-02 Method and apparatus for controlling temperature of steam in boiler

Country Status (1)

Country Link
JP (1) JPH0742906A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109084291A (en) * 2018-08-21 2018-12-25 北京富士特锅炉有限公司 Tubular steam boiler is applied to beer production anticipation feedback group control system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109084291A (en) * 2018-08-21 2018-12-25 北京富士特锅炉有限公司 Tubular steam boiler is applied to beer production anticipation feedback group control system
CN109084291B (en) * 2018-08-21 2023-11-03 北京富士特锅炉有限公司 Pre-judging feedback group control system for through-flow steam boiler in beer production process

Similar Documents

Publication Publication Date Title
JP4734184B2 (en) Steam turbine control device and steam turbine control method
JP3752568B2 (en) Gas turbine fuel heating system
JPH0742906A (en) Method and apparatus for controlling temperature of steam in boiler
JP3673295B2 (en) Method and apparatus for controlling reheat steam temperature of boiler
JP2578328B2 (en) Output control method for back pressure turbine generator
JP3932375B2 (en) Frequency control apparatus and method for thermal power plant
JP3026049B2 (en) Turbine control device
JPS61184306A (en) Steam-turbine reheater heating-steam pressure controller
JPH07293809A (en) Method and device for controlling injection of water to desuperheater
JPH07158812A (en) Controlling method for boiler and control device for boiler
JP3693265B2 (en) Boiler steam temperature control device
JP2645129B2 (en) Condensate recirculation flow control device
JPH05272361A (en) Load controller of combined-cycle power generating plant
JPS6115008A (en) Heating steam pressure controller for reheater of steam turbine
JPH10103020A (en) Controller and control method for turbine bypass valve in combined plant
JP2620124B2 (en) Bleed turbine control method and apparatus
JP2554704B2 (en) Turbine controller
JPH07224610A (en) Load control device for steam turbine
JPH0252904A (en) Control method of steam temperature and controller
JPH06241410A (en) Water level controller for supply water heater
JPH0719411A (en) Method and apparatus for controlling reheat steam temperature
JP2523493B2 (en) Turbin bypass system
JPS562405A (en) Load control device
JPS59170410A (en) Stand-by method of turbine bypass valve
JPH0642706A (en) Circuit for setting and controlling steam temperature in boiler