JPH02157501A - Starting controller for once-through boiler - Google Patents
Starting controller for once-through boilerInfo
- Publication number
- JPH02157501A JPH02157501A JP31101888A JP31101888A JPH02157501A JP H02157501 A JPH02157501 A JP H02157501A JP 31101888 A JP31101888 A JP 31101888A JP 31101888 A JP31101888 A JP 31101888A JP H02157501 A JPH02157501 A JP H02157501A
- Authority
- JP
- Japan
- Prior art keywords
- boiler
- grf
- signal
- damper
- opening degree
- 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.)
- Granted
Links
- 239000000446 fuel Substances 0.000 abstract description 20
- 238000002485 combustion reaction Methods 0.000 abstract description 7
- TVZRAEYQIKYCPH-UHFFFAOYSA-N 3-(trimethylsilyl)propane-1-sulfonic acid Chemical compound C[Si](C)(C)CCCS(O)(=O)=O TVZRAEYQIKYCPH-UHFFFAOYSA-N 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 2
- 230000009467 reduction Effects 0.000 abstract 1
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 16
- 239000002184 metal Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- NJYFRQQXXXRJHK-UHFFFAOYSA-N (4-aminophenyl) thiocyanate Chemical compound NC1=CC=C(SC#N)C=C1 NJYFRQQXXXRJHK-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野〕
本発明は貫流ボイラの制御装置に係り、特に起動初期の
ボイラ各部の温度バランス調節に好適な起動制御装置に
関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a control device for a once-through boiler, and particularly to a startup control device suitable for adjusting the temperature balance of various parts of a boiler at the initial stage of startup.
従来の装置は、ボイラ点火がら併入まで燃料量と空気量
を一定値に保つことで、ボイラ各部の昇温を行っていた
。Conventional equipment raises the temperature of each part of the boiler by keeping the fuel and air volumes at constant values until the boiler is ignited.
しかし、今日火力発電所は中間負荷運用が要求されて来
て、毎日起動停止または週末起動停止を行っており、経
済性の観点から起動時間の短縮を計ることが要求されて
いる。従来は、この要求に対して燃料量をボイラ昇温特
性によりバイアス調整することのみで対処していたため
、燃料量変動により(特に増加の場合)、ボイラ各部の
メタル温度制限値に、温度が上昇し、警報が発生すると
いう不具合が生じていた。However, today, thermal power plants are required to operate under intermediate loads, starting and stopping on a daily basis or on weekends, and from the viewpoint of economic efficiency, it is required to shorten the starting time. Conventionally, this request was dealt with only by bias-adjusting the fuel amount according to the boiler temperature rise characteristics, but due to fuel amount fluctuation (especially when increasing), the temperature rises to the metal temperature limit value of each part of the boiler. However, there was a problem in which an alarm was generated.
特にボイラの加熱器出口温度を、早期にタービンの通気
温度迄上昇することが起動時間短縮につながる訳である
が、貫流ボイラの場合、火炉氷壁の熱容量が大きく、燃
料量の調整は、この時定数を十分配慮する必要があるた
め、大幅な燃料量変化が出来ない。また、貫流ボイラの
場合、低負荷域(25%MCR以下)では、ボイラシス
テムロスが小さく、加熱スプレーは使用出来ないため、
燃料量変化のみにより主蒸気温度制御を行うことになる
。このため、安定に昇温させるためには、燃料量を最適
に制御することが必要であるが、前記したように、ボイ
ラ各部のメタル温度制限値に、温度が過上昇する要因に
もなり、従来技術では起動時間短縮は非常に困難であっ
た。すなわち、燃料量を増加して起動時間を短縮する方
法では限度があった。In particular, raising the boiler heater outlet temperature to the turbine ventilation temperature early will shorten the startup time, but in the case of a once-through boiler, the heat capacity of the furnace ice wall is large, so adjusting the fuel amount is necessary at this time. Since constants must be taken into consideration, drastic changes in fuel amount cannot be made. In addition, in the case of a once-through boiler, boiler system loss is small in the low load range (25% MCR or less) and heating spray cannot be used.
Main steam temperature control is performed only by changing the amount of fuel. Therefore, in order to raise the temperature stably, it is necessary to optimally control the fuel amount, but as mentioned above, the metal temperature limit value of each part of the boiler can be a factor that causes the temperature to rise excessively. With conventional technology, it is extremely difficult to shorten the startup time. That is, there is a limit to the method of shortening the startup time by increasing the amount of fuel.
また、燃料量のバイアス調整は運転員の手動対応という
ことで、運転員の負担もかなり重く、個人差で起動時間
もまちまちの状況にあった。In addition, bias adjustment of the amount of fuel had to be done manually by the operator, which placed a considerable burden on the operator, and the start-up time also varied depending on individual differences.
上記従来技術は、ボイラ昇温制御を燃料調整のみで行わ
せるようにしており、ボイラ各部の温度バランス調整に
ついては配慮されておらず、ボイラ水壁、加熱器のメタ
ル温度制限を守った上での燃料調整のみでは起動時間短
縮は困難であった。In the above conventional technology, boiler temperature increase control is performed only by fuel adjustment, and no consideration is given to temperature balance adjustment of each part of the boiler. It was difficult to shorten the start-up time only by adjusting the fuel.
本発明の目的は、ボイラ起動時の昇温時に各部のメタル
温度の警報が出ないで、起動時間の短縮が可能な貫流ボ
イラ起動制御装置を提供するにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a once-through boiler startup control device that can shorten the startup time without issuing an alarm regarding the metal temperature of each part when the temperature rises when the boiler is started.
上記目的は、従来技術であるボイラ起動時の昇温制御を
燃料量のバイアス制御による方法に加えて、ガス再循環
量調節によりボイラ各部(特に火炉氷壁、加熱器)の温
度バランスを変化させることによって達成される。The above purpose is to change the temperature balance of each part of the boiler (especially the furnace ice wall and heater) by adjusting the amount of gas recirculation, in addition to the conventional method of temperature increase control at boiler startup using bias control of fuel amount. achieved by
ガス再循環量は、貫流ボイラの場合、起動初期、火炉氷
壁保護のため規定量以上に流す必要がある。In the case of a once-through boiler, the amount of gas recirculated must be greater than the specified amount at the beginning of startup to protect the furnace ice wall.
一般にガス再循環量を増加すると火炉を通過するガス量
(燃焼ガスと再循環ガスの総和)が増加し対流効果によ
り、加熱器の熱吸収量が増加する。Generally, when the amount of gas recirculation is increased, the amount of gas passing through the furnace (the sum of combustion gas and recirculated gas) increases, and the amount of heat absorbed by the heater increases due to the convection effect.
また同様にバーナの火炎ものび、火炉での熱吸収量が減
少すると共に、加熱器での熱量が増加する。Similarly, the flame of the burner increases, the amount of heat absorbed in the furnace decreases, and the amount of heat in the heater increases.
この二つの相乗効果で、加熱器を通過する蒸気は上昇す
る。ガス再循環量を減少すれば、上記の逆の効果となる
。The synergistic effect of these two causes the steam passing through the heater to rise. Reducing the amount of gas recirculation will have the opposite effect.
従って、ガス再循環量をボイラ点火から併入まで調整し
て、ボイラ各部のバランスを変化させることにより、燃
料量を大きく変化させな(とも、昇温制御が可能となり
、ボイラ各部のメタル温度上昇も制限値内に保つことが
できる。Therefore, by adjusting the amount of gas recirculation from boiler ignition to combustion, and changing the balance of each part of the boiler, it is possible to avoid large changes in the amount of fuel (also, it is possible to control temperature rise, and to increase the metal temperature of each part of the boiler). can also be kept within limits.
以下、本発明の一実施例を図面を参照して説明する。 Hereinafter, one embodiment of the present invention will be described with reference to the drawings.
第2図はガス再循環tg整特性図である。FIG. 2 is a gas recirculation tg adjustment characteristic diagram.
ボイラの中間負荷運用では、毎日起動停止(以下DSS
と称す)と週末起動停止(以下WSSと称す)がある。During intermediate load operation of boilers, daily start/stop (hereinafter referred to as DSS)
) and Weekend Start-up and Shutdown (hereinafter referred to as WSS).
縦軸はガス再循環量、横軸はボイラ点火からランピング
開始までのブレークポイントを示す。また図において、
T、は−次加熱器出口温度、T2は二次加熱器出口温度
を示す。さらに−点鎖線で囲った部分の特性は後述する
関数発生器lにより設定される。The vertical axis shows the gas recirculation amount, and the horizontal axis shows the break point from boiler ignition to the start of ramping. Also, in the figure,
T indicates the secondary heater outlet temperature, and T2 indicates the secondary heater outlet temperature. Further, the characteristics of the portion surrounded by the dashed line are set by a function generator l, which will be described later.
第1図は本発明の一例を示したガス再循環制御系統を示
す。FIG. 1 shows a gas recirculation control system illustrating an example of the present invention.
ガス再循環量を運転モード毎(DSS/WSS)及び起
動ステップ毎に変化させることができるようにしている
。The amount of gas recirculation can be changed for each operating mode (DSS/WSS) and for each startup step.
また、第1図は第2図のガス再循環変化を回路化したも
のである。ガス再循環量はGRF入ロダンバ5の開度を
変化することにより調節される。Further, FIG. 1 is a circuit diagram of the gas recirculation changes shown in FIG. 2. The amount of gas recirculation is adjusted by changing the opening degree of the GRF entrance rodan bar 5.
GRF入ロゾロダンパ5制御信号は燃焼量指令(FRD
)6から関数発生器1に与えられ、DSS/WSS各モ
ード対応した開度プログラムが作られる(タービン負荷
/ダンパ開度)。各信号は切換器2で、インターロック
的に切り換えられる。The GRF input Rozoro damper 5 control signal is the combustion amount command (FRD
) 6 to the function generator 1, and an opening program corresponding to each DSS/WSS mode is created (turbine load/damper opening). Each signal is switched by a switch 2 in an interlocking manner.
電空変換器3は電流を空気に変換し、GRF入ロプロダ
ンパ5ントロールドライブに空気信号を送り、ダンパ開
度を変化させる。各信号発生器4にて、各ブレークポイ
ント毎のGRF入ロプロダンパ開度設定う。併入以前ま
では燃焼指令6による開度プログラムが作成されないの
で、点火、タービン起動、併入各ステップ毎のGRF入
ロダンバ開度は、信号発生器4にて各モード毎に作られ
る。The electro-pneumatic converter 3 converts the current into air and sends an air signal to the GRF input rotary damper 5 control drive to change the damper opening degree. Each signal generator 4 sets the GRF input rotor damper opening for each break point. Since the opening degree program based on the combustion command 6 is not created before the combination, the GRF input rodan bar opening degree for each step of ignition, turbine startup, and combination is created for each mode by the signal generator 4.
先述したように、ガス再循環量の調整により、ボイラ各
部(氷壁及び加熱器)の温度バランスを変化させること
が可能であるということより、ボイラ点火時の燃料は、
再熱器保護範囲以内で(タービン通気時点まで再熱器に
は蒸気が流れないので、メタル保護より燃料の上限が制
限される)かつボイラ昇温率を制限値以内とするため、
タービン起動までは、基本的に燃料量は一定とし、過熱
器側の昇温を早めるため、GRF入ロダンバ開度を、火
炉保護から決まる再循環ガス量の開度以上にして(DS
SではX+開度、WSSではX2開度)、タービン起動
時点まで早く蒸気温度が上昇するようにする。燃料量は
一定量ゆえ、メタル温度警報は発生しない。タービン起
動時点で、過熱器の出口蒸気温度上昇は高められて来て
おり、温度上昇レートを抑える。このため、GRF入ロ
プロダンパ開度げる(DSSではX2開度、WSSでは
Y2開度)。As mentioned earlier, it is possible to change the temperature balance of each part of the boiler (ice wall and heater) by adjusting the amount of gas recirculation, so the fuel at the time of boiler ignition is
In order to keep the boiler temperature rise rate within the reheater protection range (as steam does not flow into the reheater until the turbine vents, the upper limit of fuel is more restricted than metal protection) and the boiler temperature rise rate is within the limit value,
Until the turbine starts, the fuel amount is basically constant, and in order to accelerate the temperature rise on the superheater side, the GRF input rodan bar opening is set to be equal to or higher than the recirculation gas amount determined by furnace protection (DS
(X+ opening for S, X2 opening for WSS), so that the steam temperature rises quickly until the time of turbine startup. Since the amount of fuel is constant, no metal temperature alarm occurs. At the time of turbine startup, the superheater outlet steam temperature rise has been increased, suppressing the temperature rise rate. Therefore, increase the opening of the GRF input rotary damper (X2 opening for DSS, Y2 opening for WSS).
温度上昇レートを抑えないと、併入時点から燃料量は負
荷信号と一敗するよう制御され増加し、過熱器の温度上
昇レートが高くなり過ぎ、過熱器でのメタル温度警報が
発生することが懸念されるためである。If the temperature rise rate is not suppressed, the fuel amount will be controlled and increased to match the load signal from the time of addition, and the temperature rise rate of the superheater will become too high, causing a metal temperature alarm in the superheater. This is because there are concerns.
併入からは燃焼量指令6により、GRF入ロダンバ5は
関数発生器1で作られたプログラム信号に応じて開く。After joining, the GRF input rodan bar 5 is opened in accordance with the program signal generated by the function generator 1 in accordance with the combustion amount command 6.
従って、DSSとWSSで信号発生器4に設定された開
度X2及びY2は併入時点の関数発生器1でプログラム
された開度と同じ開度とすることによりスムーズに信号
の切り換えができる。Therefore, by setting the opening degrees X2 and Y2 set in the signal generator 4 in DSS and WSS to be the same as the opening degree programmed in the function generator 1 at the time of joining, signals can be switched smoothly.
2次空気量の調整を、本発明の一例に示したガス再循環
調整と同様の動作、制御回路で行うことによって同じ効
果が得られる。The same effect can be obtained by adjusting the amount of secondary air using the same operation and control circuit as the gas recirculation adjustment shown in one example of the present invention.
(発明の効果〕
本発明によれば、起動時間の短縮が計られるので、発電
所の所内動力及び燃料コストの低減が計られることより
、経済的メリットがある。また、ボイラの運転管理とい
う点で、無理のない起動時間短縮が可能となり、運転員
の負担軽減となる。(Effects of the Invention) According to the present invention, since the start-up time can be shortened, there is an economical advantage as the internal power and fuel costs of the power plant can be reduced.Also, there are economic advantages in terms of boiler operation management. This makes it possible to reasonably shorten startup time and reduce the burden on the operator.
第1図は本発明の一実施例に係る貫流ボイラ起動制御装
置の制御系統図、第2図はGRF人ロプロダンパ開度調
整内容すタイムチャートである。
1・・・関数発生器、2・・・切換器、3・・・電空変
換器、4・・・信号発生器、5・・・GRF入ロプロダ
ンパ・・・燃焼量指令。
第1図
第2図FIG. 1 is a control system diagram of a once-through boiler startup control device according to an embodiment of the present invention, and FIG. 2 is a time chart showing the contents of GRF manipulator damper opening adjustment. 1...Function generator, 2...Switcher, 3...Electro-pneumatic converter, 4...Signal generator, 5...GRF input rotary damper...Combustion amount command. Figure 1 Figure 2
Claims (1)
とを特徴とする貫流ボイラ起動制御装置。A once-through boiler startup control device characterized by having a circuit for adjusting gas recirculation when the boiler is started.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63311018A JP2764813B2 (en) | 1988-12-10 | 1988-12-10 | Boiler start control device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63311018A JP2764813B2 (en) | 1988-12-10 | 1988-12-10 | Boiler start control device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02157501A true JPH02157501A (en) | 1990-06-18 |
JP2764813B2 JP2764813B2 (en) | 1998-06-11 |
Family
ID=18012129
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63311018A Expired - Fee Related JP2764813B2 (en) | 1988-12-10 | 1988-12-10 | Boiler start control device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2764813B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007085678A (en) * | 2005-09-26 | 2007-04-05 | Chugoku Electric Power Co Inc:The | Fuel system for steam power generation facility, and its operating method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56105203A (en) * | 1980-01-23 | 1981-08-21 | Hitachi Ltd | Controlling system for boiler reheating steam temperature |
-
1988
- 1988-12-10 JP JP63311018A patent/JP2764813B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56105203A (en) * | 1980-01-23 | 1981-08-21 | Hitachi Ltd | Controlling system for boiler reheating steam temperature |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007085678A (en) * | 2005-09-26 | 2007-04-05 | Chugoku Electric Power Co Inc:The | Fuel system for steam power generation facility, and its operating method |
Also Published As
Publication number | Publication date |
---|---|
JP2764813B2 (en) | 1998-06-11 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |