JPH046301A - Water separator pressure control device - Google Patents
Water separator pressure control deviceInfo
- Publication number
- JPH046301A JPH046301A JP10654490A JP10654490A JPH046301A JP H046301 A JPH046301 A JP H046301A JP 10654490 A JP10654490 A JP 10654490A JP 10654490 A JP10654490 A JP 10654490A JP H046301 A JPH046301 A JP H046301A
- Authority
- JP
- Japan
- Prior art keywords
- water separator
- pressure
- set value
- signal
- value
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 238000010586 diagram Methods 0.000 description 2
- 238000010248 power generation Methods 0.000 description 2
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000034 method 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、火力発電用貫流ボイラに使用されるウォータ
セパレータ圧力制御装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a water separator pressure control device used in a once-through boiler for thermal power generation.
[従来の技術]
火力発電用の貫流ボイラに使用されるウォータセパレー
タは、入口に設けられたBE弁から蒸気の供給を受け、
出口からボイラの加熱器へ蒸気を供給する。このウォー
タセパレータ出口から分岐したウォータセパレータ圧力
制御弁(以下「SP弁」と略称する)は、過剰な蒸気を
逃がすことによりウォータセパレータ内の圧力を制御す
るものであるが、従来の圧力制御方法では蒸気供給の有
無にかかわらず常に一定の設定値で制御されて動作する
ようになっていた。[Prior Art] A water separator used in a once-through boiler for thermal power generation receives steam from a BE valve installed at its inlet.
Steam is supplied from the outlet to the boiler heater. The water separator pressure control valve (hereinafter referred to as "SP valve") branched from the water separator outlet controls the pressure inside the water separator by releasing excess steam, but conventional pressure control methods It was always controlled to operate at a constant set value regardless of the presence or absence of steam supply.
[発明が解決しようとする課題]
しかして、ウォータセパレータの使用開始時には、BE
弁が開いて蒸気供給の開始と共にウォータセパレータ内
の圧力も上昇するが、上述した如く上記SP弁は常に最
終目的値を設定値とする圧力制御がなされているため、
ウォータセパレータ内の圧力が最終目的値を越えるまで
は圧力制御を行なわず、大きなオーバーシュートを発生
していた。[Problem to be solved by the invention] However, when the water separator starts to be used, BE
When the valve opens and steam supply starts, the pressure inside the water separator also rises, but as mentioned above, the pressure of the SP valve is always controlled to the final target value as the set value.
Pressure control was not performed until the pressure inside the water separator exceeded the final target value, causing a large overshoot.
本発明は上記のような実情に鑑みてなされたもので、そ
の目的とするところは、オーバーシュートを発生せず、
常にウォータセパレータ内の圧力を最適な圧力に制御す
ることの可能なウォータセパレータ圧力制御装置を提供
することにある。The present invention has been made in view of the above-mentioned circumstances, and its purpose is to avoid overshooting,
An object of the present invention is to provide a water separator pressure control device that can always control the pressure inside a water separator to an optimal pressure.
[課題を解決するための手段]
すなわち本発明は、蒸気供給開始前は最終目標値より低
い設定値を発生し、蒸気供給開始後は最終目標値に向け
て徐々に上昇する設定値を発生する関数発生器を有する
PID(比例、積分、微分)制御系を備えるようにした
ものである。[Means for Solving the Problems] That is, the present invention generates a set value lower than the final target value before the start of steam supply, and generates a set value that gradually increases toward the final target value after the start of steam supply. It is equipped with a PID (proportional, integral, differential) control system having a function generator.
[作用]
上記のような制御系を備えることにより、ウォータセパ
レータに蒸気供給開始後、ウォータセパレータ内の圧力
が最終目標値より低い設定値を越えた時点から圧力制御
を開始し、以後は設定値上昇に伴ってウォータセパレー
タ内の圧力を徐々に上昇させながら最終目標値に至るよ
うにしたので、圧力制御開始の遅れによるオーバーシュ
ートを発生することがなく、常にウォータセパレータ内
の圧力を最適な圧力に制御することができる。[Function] By having the control system as described above, after the start of steam supply to the water separator, pressure control starts from the time when the pressure inside the water separator exceeds a set value lower than the final target value, and from then on, the set value The pressure inside the water separator is gradually increased as the pressure rises until it reaches the final target value, so there is no overshoot caused by a delay in starting pressure control, and the pressure inside the water separator is always maintained at the optimal pressure. can be controlled.
[実施例] 以下図面を参照して本発明の一実施例を説明する。[Example] An embodiment of the present invention will be described below with reference to the drawings.
第1図はその構成を示すもので、1はウォータセパレー
タ圧力発信器、2はこのウォータセパレータ圧力発信器
ユの出力と設定値とを比較する比較器、3は比較器2の
比較出力に応じてウォータセパレータ内の圧力を調整す
る圧力調整器、4は圧力調整器3の調整により作動する
ウォータセパレータ圧力制御弁(SP弁)、5は入力さ
れる急激な変化の信号を一定変化率で徐々に変化する信
号に変換して上記比較器2に与える変化率制限器、6は
蒸気供給開始前の設定値信号を発生する信号発生器、7
は最終目標である設定値信号を発生する信号発生器値、
8は蒸気供給開始前は上記信号発生器6からの信号を、
蒸気供給開始後は信号発生器値7からの信号を切替選択
して上記変化率制限器5に供給する信号切替器であり、
上記変化率制限器5、信号発生器6、信号発生器値7及
び信号切替器8によって関数発生器9を構成する。Figure 1 shows its configuration. 1 is a water separator pressure transmitter, 2 is a comparator that compares the output of this water separator pressure transmitter with a set value, and 3 is a response to the comparison output of comparator 2. 4 is a water separator pressure control valve (SP valve) that is activated by adjusting the pressure regulator 3; 5 is a water separator pressure control valve (SP valve) that gradually adjusts the input sudden change signal at a constant rate of change; 6 is a signal generator that generates a set value signal before starting steam supply, and 7
is the signal generator value that generates the final target setpoint signal,
8 receives the signal from the signal generator 6 before starting the steam supply,
After the steam supply starts, a signal switching device switches and selects the signal from the signal generator value 7 and supplies it to the rate of change limiter 5,
The rate of change limiter 5, signal generator 6, signal generator value 7, and signal switch 8 constitute a function generator 9.
上記のような構成における動作について第2図を用いて
以下に説明する。The operation of the above configuration will be explained below using FIG. 2.
ウォータセパレータへの蒸気供給前は、信号発生器6か
らの設定値信号か信号切替器8で選択されて変化率制限
器5を介し、比較器2に与えられる。ここで、信号発生
器6の発生する設定値信号は信号切替器8の発生する最
終目標である設定値より低く、ウォータセパレータ内で
オーバーシュートが発生することのないような値とされ
るものである。Before steam is supplied to the water separator, a set value signal from the signal generator 6 is selected by the signal switch 8 and is applied to the comparator 2 via the rate of change limiter 5. Here, the set value signal generated by the signal generator 6 is lower than the final target set value generated by the signal switch 8, and is set to a value that does not cause overshoot in the water separator. be.
BE弁が開かれ、ウォータセパレータへの蒸気供給が開
始されると、信号切替器8は信号発生器6からの信号に
代えて信号発生器値7がらの最終目標の設定値信号を切
替選択し、変化率制限器5に送出する。変化率制限器5
は、信号の切替により急激に変化の設定値信号を一定変
化率で徐々に変化する第2図に示すような信号に変換し
て上記比較器2に与える。ウォータセパレータ内の圧力
は蒸気供給の開始と共に急激に上昇するもので、変化率
制限器5からの一定変化率で徐々に変化する設定値信号
に比してウォータセパレータ内の圧力が大きくなった時
点で比較器2がこれを比較検出し、圧力調整器3に検出
信号を送出する。圧力調整器3はこの信号にしたがって
SP弁4を開け、過剰な蒸気を逃がすことによりウォー
タセパレータ内の圧力を下げるよう動作するもので、以
後、変化率制限器5からの徐々に上昇しながら最終目標
値に至る設定値信号に従い、SP弁4が同様にして開閉
制御されるものである。When the BE valve is opened and steam supply to the water separator is started, the signal switch 8 switches and selects the final target set value signal from the signal generator value 7 instead of the signal from the signal generator 6. , is sent to the rate of change limiter 5. Change rate limiter 5
By switching the signal, a set value signal that changes rapidly is converted into a signal that gradually changes at a constant rate of change as shown in FIG. 2, and the converted signal is applied to the comparator 2. The pressure inside the water separator increases rapidly with the start of steam supply, and when the pressure inside the water separator becomes higher than the set value signal that gradually changes at a constant rate of change from the change rate limiter 5. The comparator 2 compares and detects this and sends a detection signal to the pressure regulator 3. The pressure regulator 3 opens the SP valve 4 in accordance with this signal and operates to release excess steam to lower the pressure inside the water separator.Then, the pressure in the water separator is gradually increased from the rate of change limiter 5 until the final The SP valve 4 is similarly controlled to open and close in accordance with the set value signal that reaches the target value.
[発明の効果]
以上に述べた如く本発明によれば、蒸気供給開始前は最
終目標値より低い設定値を発生し、蒸気供給開始後は最
終目標値に向けて徐々に上昇する設定値を発生する関数
発生器を有する制御系を備え、ウォータセパレータへの
蒸気供給を開始した後、ウォータセパレータ内の圧力が
予め設定される最終目標値より低い設定値を越えた時点
から圧力制御を開始し、以後は設定値上昇に伴ってウォ
ータセパレータ内の圧力を徐々に上昇させながら最終目
標値に至るようにしたので、圧力制御開始の遅れによる
オーバーシュートを発生することがなく、常にウォータ
セパレータ内の圧力を最適な圧力に制御することが可能
なウォータセパレータ圧力制御装置を提供することがで
きる。[Effects of the Invention] As described above, according to the present invention, a set value that is lower than the final target value is generated before the start of steam supply, and a set value that gradually increases toward the final target value after the start of steam supply. After starting steam supply to the water separator, pressure control is started from the point when the pressure inside the water separator exceeds a set value lower than a preset final target value. From then on, as the set value increases, the pressure inside the water separator is gradually increased until it reaches the final target value, so there is no overshoot caused by a delay in starting pressure control, and the pressure inside the water separator is always maintained. A water separator pressure control device capable of controlling pressure to an optimum pressure can be provided.
第1図は本発明の一実施例の構成を示す機能ブロック図
、第2図は第1図による圧力制御状態を示す図である。
]・・・ウォータセパレータ圧力発信器、2・・・比較
器、3・・・圧力調整器、4・・・ウォータセパレータ
圧力制御弁(SP弁)、5・・・変化率制限器、6・・
・信号発生器、7・・・信号発生器値、8・・・信号切
替器、9・・・関数発生器。FIG. 1 is a functional block diagram showing the configuration of an embodiment of the present invention, and FIG. 2 is a diagram showing the pressure control state according to FIG. 1. ]... Water separator pressure transmitter, 2... Comparator, 3... Pressure regulator, 4... Water separator pressure control valve (SP valve), 5... Rate of change limiter, 6...・
- Signal generator, 7... Signal generator value, 8... Signal switch, 9... Function generator.
Claims (1)
り低い設定値を発生し、ウォータセパレータへの蒸気供
給開始後は最終目標値に向けて徐々に上昇する設定値を
発生する関数発生器を有する制御手段を備えたことを特
徴とするウォータセパレータ圧力制御装置。A control having a function generator that generates a set value lower than the final target value before the start of steam supply to the water separator, and generates a set value that gradually increases toward the final target value after the start of steam supply to the water separator. A water separator pressure control device characterized by comprising means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10654490A JPH046301A (en) | 1990-04-24 | 1990-04-24 | Water separator pressure control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10654490A JPH046301A (en) | 1990-04-24 | 1990-04-24 | Water separator pressure control device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH046301A true JPH046301A (en) | 1992-01-10 |
Family
ID=14436312
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10654490A Pending JPH046301A (en) | 1990-04-24 | 1990-04-24 | Water separator pressure control device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH046301A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015197234A (en) * | 2014-03-31 | 2015-11-09 | 三浦工業株式会社 | boiler system |
-
1990
- 1990-04-24 JP JP10654490A patent/JPH046301A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015197234A (en) * | 2014-03-31 | 2015-11-09 | 三浦工業株式会社 | boiler system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH0333495A (en) | Control device for condensate pump | |
| JPH046301A (en) | Water separator pressure control device | |
| JP2578328B2 (en) | Output control method for back pressure turbine generator | |
| JPH05272361A (en) | Load controller of combined-cycle power generating plant | |
| JP3673295B2 (en) | Method and apparatus for controlling reheat steam temperature of boiler | |
| JPH062811A (en) | Fuel flow controller for start-up burner in circulating fluidized bed boiler | |
| JPS6239655B2 (en) | ||
| JP3770939B2 (en) | Extraction type BFP turbine pressure regulating valve and control device therefor | |
| JP3693265B2 (en) | Boiler steam temperature control device | |
| JP2670059B2 (en) | Drum level controller for waste heat recovery boiler | |
| SU584083A1 (en) | Device for automatic adjustment of turbine heat load with steam bleeding | |
| JP4459730B2 (en) | Turbine speed control device and pulse modulation control circuit | |
| JPS5447004A (en) | Controlling of steam temperature of boiller | |
| JPH06201102A (en) | Steam supplying device | |
| JPH0549965A (en) | Method for controlling temperature of mill outlet at start-up of milling | |
| JPH0122521B2 (en) | ||
| CZ225988A3 (en) | Apparatus for the control of energetic unit | |
| SU1054555A1 (en) | Method of controlling boiler-back-pressure-turbine power unit | |
| JPS6229602Y2 (en) | ||
| SU1250660A2 (en) | Method of controlling a heat-and-electric turbine | |
| JPH10238309A (en) | Initial pressure regulator of steam turbine | |
| JP3961647B2 (en) | Drum boiler water supply control device | |
| SU954576A1 (en) | Device for automatic regulating of superheated steam temperature in power generating unit | |
| JPH04240310A (en) | Mill temperature control method at start of mill | |
| JPH03164601A (en) | Pressure controller for auxiliary steam mother pipe in boiler |