JPH0413001A - Method for controlling steam temperature - Google Patents
Method for controlling steam temperatureInfo
- Publication number
- JPH0413001A JPH0413001A JP11504390A JP11504390A JPH0413001A JP H0413001 A JPH0413001 A JP H0413001A JP 11504390 A JP11504390 A JP 11504390A JP 11504390 A JP11504390 A JP 11504390A JP H0413001 A JPH0413001 A JP H0413001A
- Authority
- JP
- Japan
- Prior art keywords
- damper
- opening
- steam temperature
- control
- boiler
- 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
- 238000000034 method Methods 0.000 title claims description 12
- 238000010586 diagram Methods 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 3
- 230000005611 electricity Effects 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〕 本発明はボイラの蒸気温度制御方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a boiler steam temperature control method.
従来の方法を第4図と第5図により説明する。 The conventional method will be explained with reference to FIGS. 4 and 5.
第4図に示すようにボイラ火炉1のガスは過熱器2と再
熱器8とに分れて通過し、それぞれのダンパ5−2.5
−8を経て混合装置6で混合された後、ボイラ出ロアか
ら排出される。As shown in FIG. 4, the gas in the boiler furnace 1 is divided into a superheater 2 and a reheater 8, and passes through each damper 5-2.5.
-8 and then mixed in the mixing device 6, and then discharged from the boiler outlet lower.
従来は再熱器8の再熱蒸気温度を定格に保つようにダン
パ5−8の開度を調節して制御していた。Conventionally, the opening degree of the damper 5-8 was controlled to maintain the reheated steam temperature of the reheater 8 at the rated value.
このダンパ開度プログラムは第5図に示すように1つの
パスのダンパ5−8のダンパ開度が曲線aに従って調節
されるとそれに伴ないもう1つのパスのダンパ5−2の
開度が曲線すで示されるように一意的に決定されるよう
になっている。This damper opening degree program is as shown in FIG. As shown above, it is uniquely determined.
上記従来の制御方法は次のような問題があった。 The conventional control method described above has the following problems.
(1)従来は制御すべき対象がただ1つのみの再熱火炉
の後部煙道が3つ以上のパスに分割され、制御すべき対
象が2つ以上ある場合には、従来の方式ではダンパ開度
が不定となってしまう。(1) Conventionally, there was only one object to be controlled.If the rear flue of a reheat furnace is divided into three or more paths, and there are two or more objects to be controlled, the conventional method uses a damper. The opening degree becomes unstable.
(2)従来方式では、例えば再熱蒸気温度を制御するた
めにダンパ開度が一意的に決定される。これを、例えば
ある特定の負荷においてはガス側の圧力損失を抑制する
ためにダンパ開度を開き気味に設定したい場合があると
き、このような制御ができない。(2) In the conventional method, the damper opening degree is uniquely determined, for example, in order to control the reheat steam temperature. For example, when it is desired to set the damper opening slightly open in order to suppress pressure loss on the gas side under a certain load, such control cannot be performed.
本発明は上記課題を解決するため次の手段を講する。 The present invention takes the following measures to solve the above problems.
すなわち、蒸気温度制御方法として、後部煙道部を複数
のパスに仕切り、そのそれぞれのパスを流れるガス量を
、それぞれのパスに設置したダンパの開度を変えること
により変化させ、それにより主蒸気温度や再熱1気温度
をM御するボイラにおいて、すべてのダンパ開度の和又
はある特定のダンパ開度をボイラ負荷の値に基いて一義
的に決定し、所定のダンパ開度はそれぞれの制御対象機
器の出口蒸気温度を制御するように調節する。In other words, as a steam temperature control method, the rear flue section is divided into multiple paths, and the amount of gas flowing through each path is changed by changing the opening degree of the damper installed in each path. In a boiler that controls temperature and reheat temperature M, the sum of all damper opening degrees or a certain damper opening degree is uniquely determined based on the boiler load value, and the predetermined damper opening degree is determined by each damper opening degree. Adjust to control the outlet steam temperature of the controlled equipment.
上記手段により、例えば後部煙道部のパスが3つに仕切
られ制御すべき対象が2つある場合、ボイラ負荷の値に
基いて3つのダンパ開度の和または1つのダンパ開度が
決定され、制御対象機器用の2つのダンパ開度は、それ
ぞれの制御対象機器の出口蒸気温度を制御するように決
定される。このようにしてボイラ負荷に応しるとともに
制御対象機器の出口蒸気温度が制御されるように各ダン
パ開度が調節される。With the above means, for example, when the path in the rear flue section is divided into three and there are two objects to be controlled, the sum of three damper openings or one damper opening is determined based on the boiler load value. , the two damper opening degrees for the controlled devices are determined to control the outlet steam temperature of each controlled device. In this way, the opening degree of each damper is adjusted so as to correspond to the boiler load and to control the outlet steam temperature of the equipment to be controlled.
本発明の方法に係る一実施例を第1図ないし第3図によ
り煙道のパスが3つある場合について説明する。第1図
にて、ボイラ火炉1の煙道は3分割されていて、それぞ
れのパスに過熱器2、−役回熱rG3、二段再熱器4が
設けられる。またこれらの後流はそれぞれダンパ5−2
.5−3.54を経て混合器6につながれる。図中7は
ボイラ出口を示す。以上の構成において、第2図に示す
ようにボイラ負荷(−)に応じて、各ダンパ5−25−
3.5−4.のダンパ開度A1.Ax、Asの和Aが決
定され、かつ−役回熱器3、二段再熱器4用のダンパ5
−3.5−4は一段再熱器3の出口蒸気温度、二段再熱
器4の出口蒸気温度を所定の値に維持するようその開度
がそれぞれ制御調節される。An embodiment of the method of the present invention will be described with reference to FIGS. 1 to 3 in the case where there are three flue paths. In FIG. 1, the flue of the boiler furnace 1 is divided into three, and a superheater 2, a recuperator rG3, and a two-stage reheater 4 are provided in each path. In addition, these wakes are each damped by a damper 5-2.
.. It is connected to the mixer 6 via 5-3.54. In the figure, 7 indicates the boiler outlet. In the above configuration, as shown in FIG. 2, each damper 5-25-
3.5-4. Damper opening degree A1. The sum A of Ax and As is determined, and - the damper 5 for the role reheater 3 and the two-stage reheater 4
-3.5-4, the opening degree thereof is controlled and adjusted so as to maintain the outlet steam temperature of the first-stage reheater 3 and the outlet steam temperature of the second-stage reheater 4 at predetermined values.
第3図に以上の方法を自動的に行う制御系のブロック図
を示す、−役回熱器3の出口蒸気温度の偏差信号12s
はコントローラ18aを経てダンパ53へ送られる。ま
た二段再熱器4の出口蒸気温度の偏差信号13sはコン
トローラ18bを経てダンパ5−4へ送られる。さらに
負荷信号IIsは関数発住F;19を軽で加減算器2o
へ加電入力される。加減算器20はさらにコントーラ1
8a、18bの出力を減電入力して自己の出力をダンパ
5−2へ送る。FIG. 3 shows a block diagram of a control system that automatically performs the above method. - Deviation signal 12s of steam temperature at the outlet of the recuperator 3
is sent to the damper 53 via the controller 18a. Further, a deviation signal 13s of the outlet steam temperature of the two-stage reheater 4 is sent to the damper 5-4 via the controller 18b. Furthermore, the load signal IIs is a function generator F;
Electricity is input to. The adder/subtractor 20 further includes a controller 1
The outputs of 8a and 18b are inputted with reduced voltage and their own output is sent to the damper 5-2.
以上の構成において、前述したように関数発生器19が
負荷信号11s、Wを受は第2図に示すダンパ開度の和
信号14s、Aを出力する。一方ダンパ5−3はコント
ローラ18aからのダンパ開度信号16s、A、により
開度がiJJ節される。ダンパ54も同様にコントロー
ラ18bからのダンパ開度信号17s、Atにより開度
が調節される。さらにダンパ5−2は加減算器20の出
力、ダンパ開度信号15s、 (A−(A++At)
)により開度が調節される。このようにして、ボイラの
荷負に、全体的に応しるとともに、かつ−役回熱器15
−3の出口蒸気温度と二段再熱器15−4の出口蒸気温
度がそれぞれ所定値に制御維持されるようになる。In the above configuration, as described above, the function generator 19 receives the load signal 11s, W and outputs the sum signal 14s, A of the damper opening shown in FIG. On the other hand, the opening degree of the damper 5-3 is set to iJJ by the damper opening signal 16s, A from the controller 18a. Similarly, the opening degree of the damper 54 is adjusted by the damper opening degree signals 17s and At from the controller 18b. Furthermore, the damper 5-2 receives the output of the adder/subtractor 20, the damper opening signal 15s, (A-(A++At)
) to adjust the opening degree. In this way, the load on the boiler can be met as a whole, and the load on the boiler can be met.
-3 and the outlet steam temperature of the two-stage reheater 15-4 are controlled and maintained at predetermined values, respectively.
この方法によれば、例えば複数のボイラがあるとき、こ
のダンパ開度の和を、各ボイラ負荷ごとに異なる任意の
組合せ、すなわち、設計者の意のままの組合せを選択す
ることができる。According to this method, for example, when there are a plurality of boilers, it is possible to select an arbitrary combination of the sum of the damper opening degrees for each boiler load, that is, a combination at the designer's discretion.
なお、以上では全てのパスのダンパ開度の和をボイラ負
荷により規定する方法を述べたが、これをある1つのパ
スのダンパ開度、例えばダンパ52の開度をボイラ負荷
により規定するようにしても、これと同等の効果を得る
ことができる。In addition, above, a method was described in which the sum of the damper openings of all paths is specified by the boiler load, but this can also be done by specifying the damper opening of one path, for example, the opening of the damper 52, by the boiler load. However, the same effect can be obtained.
中兜今目圀■渫=−
以上の方法によれば制御すべき対象が2つ以上あり、制
御する手段が3つ以上ある場合の制御がきわめて容品に
可能となる。また、制御すべき対象が1つの場合におい
ても、異なる条件の下で制御条件を変更することが可能
となる。さらにより最適な制御条件を設定することが可
能となる。According to the above method, it is possible to control the objects in a case where there are two or more objects to be controlled and three or more means to control them in a very simple manner. Further, even when there is only one object to be controlled, the control conditions can be changed under different conditions. Furthermore, it becomes possible to set more optimal control conditions.
(発明の効果〕
以上に説明したように本発明の方法によれば、複数のダ
ンパの開度の和、またはある特定のダンパ開度がボイラ
負荷の値に応じて決められ、かつ制御対象機器用のダン
パ開度がその出口蒸気温度を所定値に維持するように制
御される。このようにして複数のダンパがある場合の制
御がきわめて容易にできるようになる。またより最適な
制御条件を設定することができるようになる。(Effects of the Invention) As explained above, according to the method of the present invention, the sum of the opening degrees of a plurality of dampers or a certain damper opening degree is determined according to the boiler load value, and the control target equipment The opening degree of each damper is controlled to maintain the outlet steam temperature at a predetermined value.In this way, control when there are multiple dampers becomes extremely easy.Also, more optimal control conditions can be achieved. You will be able to set it.
第1図は、本発明の方法に係る一実施例の系統図、第2
図は同実施例の作用説明図、第3図は同実施例のダンパ
制御系のブロック図、第4図は、従来例の系統図、第5
図は同従来例の作用説明図である。
■・・・ボイラ火炉、 2・・・通熱器3・・・
−役回熱器、 4・・・二段再熱器5〜2.5−
3.5−4・・・ダンパ。
代理人 弁理士 坂 間 暁 外2名第1図FIG. 1 is a system diagram of one embodiment of the method of the present invention;
3 is a block diagram of the damper control system of the same embodiment. FIG. 4 is a system diagram of the conventional example.
The figure is an explanatory diagram of the operation of the conventional example. ■... Boiler furnace, 2... Heat exchanger 3...
-Reheater, 4...Two-stage reheater 5~2.5-
3.5-4...Damper. Agent: Patent attorney Akira Sakama and two others Figure 1
Claims (1)
を流れるガス量を、それぞれのパスに設置したダンパの
開度を変えることにより変化させ、それにより主蒸気温
度や再熱蒸気温度を制御するボイラにおいて、すべての
ダンパ開度の和又はある特定のダンパ開度をボイラ負荷
の値に基いて一義的に決定し、所定のダンパ開度はそれ
ぞれの制御対象機器の出口蒸気温度を制御するように調
節することを特徴とする蒸気温度制御方法。The rear flue section is divided into multiple paths, and the amount of gas flowing through each path is changed by changing the opening degree of the damper installed in each path, thereby controlling the main steam temperature and reheat steam temperature. In a boiler that operates, the sum of all damper openings or a specific damper opening is uniquely determined based on the boiler load value, and the predetermined damper opening controls the outlet steam temperature of each controlled device. A steam temperature control method characterized in that the steam temperature is adjusted as follows.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11504390A JPH0413001A (en) | 1990-05-02 | 1990-05-02 | Method for controlling steam temperature |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11504390A JPH0413001A (en) | 1990-05-02 | 1990-05-02 | Method for controlling steam temperature |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0413001A true JPH0413001A (en) | 1992-01-17 |
Family
ID=14652775
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11504390A Pending JPH0413001A (en) | 1990-05-02 | 1990-05-02 | Method for controlling steam temperature |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0413001A (en) |
-
1990
- 1990-05-02 JP JP11504390A patent/JPH0413001A/en active Pending
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