JPH04128505A - Steam pressure control method of plural boiler and power generator - Google Patents
Steam pressure control method of plural boiler and power generatorInfo
- Publication number
- JPH04128505A JPH04128505A JP24632990A JP24632990A JPH04128505A JP H04128505 A JPH04128505 A JP H04128505A JP 24632990 A JP24632990 A JP 24632990A JP 24632990 A JP24632990 A JP 24632990A JP H04128505 A JPH04128505 A JP H04128505A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- boiler
- load
- steam
- 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.)
- Granted
Links
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- 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、複数のボイラーおよび発電機を並列運転する
製紙プラントや石油化学プラント、製紙プラントの自家
発電所における高圧蒸気を供給および消費する設備の蒸
気圧力制御方法に関するものである。Detailed Description of the Invention [Industrial Application Field] The present invention is applicable to equipment that supplies and consumes high-pressure steam in paper plants, petrochemical plants, and private power plants of paper plants that operate multiple boilers and generators in parallel. The present invention relates to a steam pressure control method.
[従来の技術]
複数のボイラーおよび発電機を並列運転する製鉄プラン
トや石油化学プラン1〜.製紙プラントの自家発電所に
おける高圧蒸気を供給し且つ消費する設備の蒸気圧力制
御の方法として、複数のボイラー負荷制御を1台の圧力
コントローラーの下にそれぞれの負荷比率を設定するこ
とにより並列運転する制御は広く一般的に行われている
。[Conventional technology] Steel plants and petrochemical plans 1 to 1 in which multiple boilers and generators are operated in parallel. As a method of controlling the steam pressure of equipment that supplies and consumes high-pressure steam in a private power plant of a paper manufacturing plant, multiple boiler load controls are operated in parallel by setting their respective load ratios under one pressure controller. Control is widely practiced.
また、それぞれのボイラーの使用範囲を限定し、順序制
御することにより蒸気圧力制御する方法も提案されてい
る。Furthermore, a method has been proposed in which steam pressure is controlled by limiting the usage range of each boiler and controlling the order.
更には、ボイラーの供給使方範囲を超大だ場合に発電機
の負荷を補助的に変更して蒸気圧力制御する方法も提案
されている。Furthermore, a method has also been proposed in which the steam pressure is controlled by supplementarily changing the load on the generator when the boiler supply usage range is extremely large.
[発明か解決しようとする課R]
従来の、複数のボイラーによる蒸気圧力制御では1台の
圧力コントローラーの下に、それぞれの負荷比率を設定
することにより並列運転する方法の場合、また、それぞ
れのボイラーの使用範囲を限定し順序制御する方法の場
合ては、発電機を含む消費側の負荷かボイラーの供給能
力範囲を超えると、ボイラーによる蒸気圧力制御か不能
となる難点を有していた。[Invention or Section R to be solved] In the conventional steam pressure control using multiple boilers, in the case of a method of parallel operation by setting the load ratio of each under one pressure controller, In the case of the method of limiting the usage range of the boiler and sequentially controlling it, the problem was that if the load on the consumption side, including the generator, exceeded the boiler's supply capacity range, the boiler could no longer control the steam pressure.
また、この問題を解決するための、ボイラーの供給能力
範囲を超えた場合に発電機の負荷を補助的に変更して蒸
気圧力制御する方法では、発電機での圧力制御完了後に
発電機負荷か圧力制御前の値に戻らないという難点を有
していた。In addition, in order to solve this problem, the steam pressure is controlled by changing the generator load in an auxiliary manner when the boiler's supply capacity range is exceeded. The problem was that it did not return to the value before pressure control.
本発明は、これらの問題点を有利に解決することを目的
とするものである。The present invention aims to advantageously solve these problems.
[課題を解決するための17段]
本発明は、複数のボイラーと発電機の並列運転を行う発
電所での1蒸気圧力を一足に保つための圧力制御におい
て、ボイラーの負荷調節による圧力制御コントローラー
と発電機の負荷調節による圧力制御コントローラーを設
け、ボイラーの負荷調節代がある時にはボイラーの圧力
制御コントローラーを、また、ボイラーの負荷調節代が
ない時には発電機の圧力制御コントローラーを使用する
ように自動的に切り科えることを特徴とする複数のボイ
ラーおよび発電機の蒸気圧力制御方法、および蒸気の圧
力制御において発11A、機の圧力制御コントローラー
からボイラーの圧力制御コントローラーに切り替わる時
に発電機の出力か圧力制御開始前の伯に戻ることを特徴
とする圧力制御方法である。[17 steps to solve the problem] The present invention provides a pressure control controller that adjusts the load of the boiler in pressure control to maintain one steam pressure at a power plant where a plurality of boilers and generators are operated in parallel. and a pressure control controller that adjusts the load of the generator, and automatically uses the boiler pressure controller when there is an allowance for adjusting the boiler load, and uses the generator pressure controller when there is no allowance for adjusting the boiler load. A steam pressure control method for a plurality of boilers and generators, which is characterized in that the steam pressure control method is characterized in that the steam pressure control method is characterized in that the steam pressure control method is characterized in that the output of the generator is This is a pressure control method characterized by returning to a state before starting pressure control.
「作用」
複数のボイラーおよび発電機を並列運転する自家発電所
における高圧蒸気を供給し且つ消費する設備の蒸気圧力
制御方法において、ボイラーの負荷調節による圧力制御
コントローラーと発電機の負荷調節による圧力制御コン
l−ローラーを設は発電機を含む消費側の負荷かボイラ
ーの供給能力範囲に入り蒸気圧力か設定値に対して所定
の範囲内に入っている場合には、ボイラーによる蒸気圧
力制御だけを実施し、発電機による圧力制御は設定値を
測定値にトラッキングさせ、制御出力を基準値に固定し
制御を停止するか、発電機を含む消費側の負荷かボイラ
ーの供給能力範囲を超え、ボイラーによる蒸気圧力制御
か不能となり、蒸気圧力か設定値に対して所定の範囲内
から外れた場合には、設定値を固定し制御を開始する。"Operation" In a steam pressure control method for equipment that supplies and consumes high-pressure steam in a private power plant where multiple boilers and generators are operated in parallel, pressure control controller by adjusting the load of the boiler and pressure control by adjusting the load of the generator. When the controller roller is installed, if the load on the consumption side, including the generator, falls within the supply capacity range of the boiler, and the steam pressure is within a predetermined range for the set value, only the steam pressure can be controlled by the boiler. For pressure control by the generator, either set value tracks the measured value, fixes the control output to the reference value and stops the control, or the load on the consumption side including the generator exceeds the supply capacity range of the boiler, and the boiler If steam pressure control becomes impossible and the steam pressure deviates from a predetermined range with respect to the set value, the set value is fixed and control is started.
次に、圧力か回復し発電機による圧力制御の制御出力か
基準値に対して所定の範囲内に入った場合には、設定イ
めを測定値にトラッキングさせ、制御出力を基準イメに
固定し制御を停止する。これらの動作により発電機の圧
力制御コントローラーからボイラーの圧力制御コントロ
ーラーに切り替わる時に、発電機の出力か圧力制御開始
前の値に戻るようにし1、ボイラーて圧力制御を実施し
ているときは所定の負荷で充電機の運転かてきる蒸気圧
力制御を可能とするものである。Next, when the pressure recovers and the control output for pressure control by the generator falls within a predetermined range with respect to the reference value, the set value is tracked to the measured value and the control output is fixed to the reference value. Stop control. Through these operations, when switching from the generator's pressure controller to the boiler's pressure controller, the generator's output returns to the value before starting pressure control 1, and when the boiler is performing pressure control, the predetermined This enables steam pressure control to operate the charger based on the load.
[実施例]
本発明を、第1図に示した製鉄所の自家発電所での実施
例によって、さらに詳細に説明する。[Example] The present invention will be explained in more detail with reference to an example in a private power plant of a steelworks shown in FIG.
この自家発電所では、6基のボイラー2および5基の発
tJ13を並列運転し、高圧蒸気を供給し且つ消費して
いる。1は高圧蒸気へ・ンダーおよび配管、4は蒸気加
減弁である。蒸気圧力J5て測定された蒸気圧力測定値
は、圧力設定器10てボイラー圧力調節計6に設定され
ているボイラー蒸気圧力設定値と比較してPID制御演
算を行い、その出力をそれぞれのボイラー負荷配分設定
器8へ負荷設定値として与える。この設定値によりボイ
ラーは発生蒸気量を調節する。一方、蒸気圧力、H5て
測定された蒸気圧力測定値は、圧力設定器lOでボイラ
ー圧力調節計7に設定されているボイラー蒸気圧力設定
値と比較し、圧力測定イめかボイラー圧力設定値に対し
て所定の範囲内に入っている場合には、発電Ia蒸気圧
力設定値を蒸気圧力測定値にトラッキングさせ制御出力
を基準値に固定し、負荷設定器11て加算器9に設定さ
れている発電機負荷設定値と加算し、発を機へ負荷指令
とし・てダーえる。また、前記の圧力測定値かボイラー
圧力設定値に対して所定の範囲内から外れた場合には、
直ちに発電4m蒸気圧力設定値を固定しPID制御演算
を行い、その出力をそれぞれの発電機の加算器9に設定
されている発電機負荷設定値と加算し、発電機へ負荷指
令として与える。In this private power plant, six boilers 2 and five steam generators 13 are operated in parallel to supply and consume high-pressure steam. 1 is a high pressure steam heater and piping, and 4 is a steam control valve. The steam pressure value measured by the steam pressure J5 is compared with the boiler steam pressure setting value set in the boiler pressure controller 6 using the pressure setting device 10, PID control calculation is performed, and the output is adjusted to each boiler load. It is given to the distribution setter 8 as a load setting value. The boiler adjusts the amount of steam generated by this set value. On the other hand, the steam pressure value measured by H5 is compared with the boiler steam pressure setting value set in the boiler pressure controller 7 using the pressure setting device 1O, and the pressure measurement value is compared to the boiler pressure setting value. If it is within a predetermined range, the power generation Ia steam pressure setting value is tracked to the steam pressure measurement value, the control output is fixed to the reference value, and the load setter 11 adjusts the power generation value set in the adder 9. It is added to the machine load setting value and sent to the machine as a load command. In addition, if the pressure measurement value or the boiler pressure set value is outside the specified range,
Immediately, the power generation 4m steam pressure set value is fixed, PID control calculation is performed, the output is added to the generator load set value set in the adder 9 of each generator, and the result is given to the generator as a load command.
第2図に示すように、蒸気圧力測定値の上昇時に所定範
囲のhllJi(めに到達するまでは、発電機蒸気圧力
設定値は蒸気圧力設定値にトラッキングさせ、制御出力
は基準値に固定する。As shown in Figure 2, when the measured steam pressure value rises, the generator steam pressure set value is made to track the steam pressure set value and the control output is fixed at the reference value until it reaches a predetermined range of hllJi (me). .
次に、測定値か所定範囲の上限値に到達したら、発電機
蒸気圧力設定値は所定範囲の上限値て固定し、PID制
御を開始し、圧力の1−昇と共に制御出力を増加し圧力
制御を行う。圧力か回復し圧力測定値か発電機圧力設定
値を下回ると、制御出力は徐々にX半値に近づき所定範
囲1−限値以下になった時点てPID制御を停止し、発
電機蒸気圧力設定値を蒸気圧力設定値にトラッキングさ
せ制御出力は基?!値に固定する。然気圧力測定値の下
縫時も図に示すように、上昇時と回し様に動作する。こ
のような構成によって、実施した蒸気圧力制御により制
御性を損なうことなく設備能力を有効に活用てきる蒸気
圧力制御か可能になった。Next, when the measured value reaches the upper limit of the predetermined range, the generator steam pressure set value is fixed at the upper limit of the predetermined range, PID control is started, and the control output is increased as the pressure increases by 1 to control the pressure. I do. When the pressure recovers and the measured pressure falls below the generator pressure set value, the control output gradually approaches half the value of Is the control output based on the steam pressure set value? ! Fixed to value. As shown in the figure, the sewing machine operates in the same manner as when it is rising and when sewing the bottom of the air pressure measurement value. With such a configuration, it has become possible to perform steam pressure control that effectively utilizes the facility capacity without impairing controllability.
[発明の効果]
以−1−のように、本発明方法によれば、複数のボイラ
ーと発電様の1列芹転を行う発電所での主蒸気圧力を、
・定に保つための圧力制御方法において、ボイラーの負
荷調節による圧力制御コントローラーと光電機の負荷調
節による圧力制御コントローラーを設け、ボイラーの負
荷調節代がある時にはボイラーの圧力制御コントローラ
ーを、また、ボイラーの負荷調節代がない時には、発電
機の圧力制御コン1−ローラーを使用するよ・)に自動
的に切り科えることにより、いかなる場合にも安定した
主蒸気圧力制御を実施できる。[Effects of the Invention] As described in -1- below, according to the method of the present invention, the main steam pressure in a power plant that performs single-row rotation for power generation with a plurality of boilers,
・In the pressure control method to keep the pressure constant, a pressure control controller that adjusts the boiler load and a pressure control controller that adjusts the photoelectric load are installed, and when there is a need to adjust the boiler load, the boiler pressure control controller is When there is no load adjustment allowance, the generator's pressure control controller 1-roller is automatically used to control the main steam pressure in a stable manner under any circumstances.
また、発電機を含む消費側の負荷かボイラーの供給能力
範囲を超えた場合には、自動的に発電機の負荷を補助的
に変更して蒸気圧力制御をするに際して、発電機での圧
力制御完了後に、発電機負荷か圧力制御前の値に自動的
に戻るようにしたので、制御性を損なうことなく設備能
力を有効に活用てき、負荷変動に対する応答性を確保し
つつ、常に最大の効率での運転な可能にし、省エネルギ
ーは勿論のこと、完全な自動化による省力化をも実現す
るものである。In addition, if the load on the consumption side, including the generator, exceeds the supply capacity range of the boiler, the load on the generator will be automatically changed to supplement the steam pressure control. After completion, the generator load automatically returns to the value before pressure control, making effective use of equipment capacity without compromising controllability, ensuring responsiveness to load fluctuations, and always maintaining maximum efficiency. This not only saves energy, but also saves labor through complete automation.
第1図は本発明の一実施例の構成を示すブロック図、第
2図は本発明の動作説明のための実施例を示す図である
。
図中。
1:高圧蒸気ヘッダー
2 ボイラー 3:発電機
4 蒸気加減方
5 蒸気圧力計
6.7 ボイラー圧力調節計
8、ボイラー負荷配分設定器
9:加算器
lO:圧力設定器
負荷設定器FIG. 1 is a block diagram showing the configuration of an embodiment of the invention, and FIG. 2 is a diagram showing an embodiment for explaining the operation of the invention. In the figure. 1: High pressure steam header 2 Boiler 3: Generator 4 Steam adjustment method 5 Steam pressure gauge 6.7 Boiler pressure controller 8, Boiler load distribution setting device 9: Adder IO: Pressure setting device Load setting device
Claims (2)
での主蒸気圧力を一定に保つための圧力制御方法におい
て、ボイラーの負荷調節による圧力制御コントローラー
と発電機の負荷調節による圧力制御コントローラーを設
け、ボイラーの負荷調節代がある時にはボイラーの圧力
制御コントローラーを、また、ボイラーの負荷調節代が
ない時には発電機の圧力制御コントローラーを使用する
ように自動的に切り替えることを特徴とする複数のボイ
ラーおよび発電機の蒸気圧力制御方法。(1) In a pressure control method for keeping the main steam pressure constant in a power plant that operates multiple boilers and generators in parallel, there is a pressure control controller that adjusts the load of the boiler and a pressure control controller that adjusts the load of the generator. The system automatically switches to use the boiler pressure control controller when there is an allowance for boiler load adjustment, and to use the generator pressure control controller when there is no boiler load adjustment allowance. Steam pressure control method for boilers and generators.
圧力制御コントローラーからボイラーの圧力制御コント
ローラーに切り替わる時に発電機の出力が圧力制御開始
前の値に戻ることを特徴とする複数のボイラーおよび発
電機の蒸気圧力制御方法。(2) In the pressure control method according to claim (1), the output of the generator returns to the value before starting the pressure control when switching from the pressure control controller of the generator to the pressure control controller of the boiler. and a generator steam pressure control method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2246329A JP2566487B2 (en) | 1990-09-18 | 1990-09-18 | Steam pressure control method for multiple boilers and generators |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2246329A JP2566487B2 (en) | 1990-09-18 | 1990-09-18 | Steam pressure control method for multiple boilers and generators |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04128505A true JPH04128505A (en) | 1992-04-30 |
| JP2566487B2 JP2566487B2 (en) | 1996-12-25 |
Family
ID=17146948
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2246329A Expired - Lifetime JP2566487B2 (en) | 1990-09-18 | 1990-09-18 | Steam pressure control method for multiple boilers and generators |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2566487B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009162424A (en) * | 2008-01-07 | 2009-07-23 | Sumitomo Chemical Co Ltd | Low pressure steam supply device |
| JP2009198024A (en) * | 2008-02-19 | 2009-09-03 | Sumitomo Chemical Co Ltd | Steam supply device and pressure control method in the stream supply device |
| KR20110137780A (en) | 2009-03-24 | 2011-12-23 | 후지필름 가부시키가이샤 | Capsule type endoscope |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56107907A (en) * | 1980-01-30 | 1981-08-27 | Hitachi Ltd | Load distribution control system of steam turbine |
-
1990
- 1990-09-18 JP JP2246329A patent/JP2566487B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56107907A (en) * | 1980-01-30 | 1981-08-27 | Hitachi Ltd | Load distribution control system of steam turbine |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009162424A (en) * | 2008-01-07 | 2009-07-23 | Sumitomo Chemical Co Ltd | Low pressure steam supply device |
| JP2009198024A (en) * | 2008-02-19 | 2009-09-03 | Sumitomo Chemical Co Ltd | Steam supply device and pressure control method in the stream supply device |
| KR20110137780A (en) | 2009-03-24 | 2011-12-23 | 후지필름 가부시키가이샤 | Capsule type endoscope |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2566487B2 (en) | 1996-12-25 |
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