JPH0315082B2 - - Google Patents
Info
- Publication number
- JPH0315082B2 JPH0315082B2 JP56061222A JP6122281A JPH0315082B2 JP H0315082 B2 JPH0315082 B2 JP H0315082B2 JP 56061222 A JP56061222 A JP 56061222A JP 6122281 A JP6122281 A JP 6122281A JP H0315082 B2 JPH0315082 B2 JP H0315082B2
- Authority
- JP
- Japan
- Prior art keywords
- inlet damper
- gas
- damper
- flow rate
- furnace
- 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.)
- Expired - Lifetime
Links
- 239000007789 gas Substances 0.000 claims description 49
- 238000002485 combustion reaction Methods 0.000 claims description 7
- 230000007423 decrease Effects 0.000 claims description 6
- 239000000567 combustion gas Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 claims 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 1
Landscapes
- Regulation And Control Of Combustion (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はガス再循環を行なうボイラの制御装置
に係り、特にガス再循環フアン入口ダンパー(以
下GRF入力ダンパーと略す)で再熱蒸気温度を
制御し、さらに一次ガス入口ダンパー、混合ガス
入口ダンパー、火炉ホツパー入口ダンパーの最適
な開閉制御に依り窒素酸化物(以下NOx)を低
減するボイラの制御装置に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a control device for a boiler that performs gas recirculation, and particularly to a control device for controlling a boiler that performs gas recirculation, and in particular controls the temperature of reheated steam using a gas recirculation fan inlet damper (hereinafter abbreviated as GRF input damper). The present invention relates to a boiler control device that reduces nitrogen oxides (hereinafter referred to as NOx) through optimal opening/closing control of a primary gas inlet damper, a mixed gas inlet damper, and a furnace hopper inlet damper.
第1図に火力プラントの煙風道概略図を示す。 Figure 1 shows a schematic diagram of the smoke duct of a thermal power plant.
同図において、ボイラ自動制御装置1は負荷の
要求に見合つて燃料制御弁12および押込通風機
8のダンパー9を制御し、これに応じた燃料およ
び空気をバーナ13に導き、燃焼させる。一方、
生成された燃焼ガスは火炉14を通り、一部はガ
ス再循環フアン3により再び火炉へ戻り、残りは
大気中へ排出される。なお、第1図において、2
はボイラ、4はGRF入口ダンパー、5は火炉ホ
ツパー入口ダンパー、6は一次ガス入口ダンパ
ー、7は混合ガス入口ダンパー、10は流量検出
器、11は温度検出器、15は再熱器である。 In the figure, an automatic boiler control device 1 controls a fuel control valve 12 and a damper 9 of a forced draft fan 8 in accordance with load requirements, and guides fuel and air in accordance with this to a burner 13 for combustion. on the other hand,
The generated combustion gas passes through the furnace 14, a part of which is returned to the furnace again by the gas recirculation fan 3, and the rest is discharged into the atmosphere. In addition, in Figure 1, 2
4 is a boiler, 4 is a GRF inlet damper, 5 is a furnace hopper inlet damper, 6 is a primary gas inlet damper, 7 is a mixed gas inlet damper, 10 is a flow rate detector, 11 is a temperature detector, and 15 is a reheater.
第2図により、従来の再循環ガス制御方式を説
明する。同図aにおいて、温度検出器11により
検出された再熱蒸気温度16は信号発生器17で
定められた再熱蒸気温度設定値18と比較され、
その偏差19を比例、積分器20にて演算する。
この信号に、ボイラ負荷指令21から関数発生器
221により作成した先行信号を加え、GRF入
口ダンパーを操作し、再熱蒸気温度を制御する。 A conventional recirculation gas control system will be explained with reference to FIG. In the same figure a, the reheat steam temperature 16 detected by the temperature detector 11 is compared with the reheat steam temperature set value 18 determined by the signal generator 17,
The deviation 19 is calculated by a proportional integrator 20.
A preceding signal generated by the function generator 221 from the boiler load command 21 is added to this signal to operate the GRF inlet damper and control the reheat steam temperature.
また、GRF入口ダンパーにより再循環された
排ガスは混合ガス入口ダンパー、一次ガス入口ダ
ンパー、火炉ホツパー入口ダンパーにより配分し
て火炉内へ戻す。すなわち第2図bにおいて、流
量検出器10で検出された混合ガス流量値23は
負荷指令値21に基づいて関数発生器222によ
り定められた混合ガス流量設定値と比較され、そ
の偏差24は比例、積分器20にて演算される。
この信号に、負荷指令21から関数発生器223
により作成した先行信号を加え、混合ガス入口ダ
ンパーを操作する。同様にして、一次ガス入口ダ
ンパー、火炉ホツパー入口ダンパーは混合ガス入
口ダンパー開度指令にバイアス25,26を加え
た信号で操作する。 In addition, the exhaust gas recirculated by the GRF inlet damper is distributed by the mixed gas inlet damper, primary gas inlet damper, and furnace hopper inlet damper and returned to the furnace. That is, in FIG. 2b, the mixed gas flow rate value 23 detected by the flow rate detector 10 is compared with the mixed gas flow rate set value determined by the function generator 222 based on the load command value 21, and the deviation 24 is proportional to , are calculated by the integrator 20.
This signal is applied to the function generator 223 from the load command 21.
Add the preceding signal created by , and operate the mixed gas inlet damper. Similarly, the primary gas inlet damper and the furnace hopper inlet damper are operated by a signal obtained by adding biases 25 and 26 to the mixed gas inlet damper opening command.
ここで、本方式における欠点は負荷指令に基づ
く先行プログラム制御において、GRF入口ダン
パー開閉に対し、混合ガス入口ダンパー、一次ガ
ス入口ダンパー、火炉ホツパー入口ダンパーを一
様に開閉している点にある。
The drawback of this method is that in advance program control based on load commands, the mixed gas inlet damper, primary gas inlet damper, and furnace hopper inlet damper are uniformly opened and closed in response to the opening and closing of the GRF inlet damper.
すなわち、負荷上昇時再熱蒸気温度が上昇する
傾向にあるのに対し、GRF入口ダンパーは先行
的に閉じる制御としているため再循環ガス流量が
減少する。一方、混合ガスダンパー、一次ガス入
口ダンパー、火炉ホツパー入口ダンパーは一様に
開くだけであるため混合ガス流量、一次ガス流量
が負荷指令に対して不足するため、燃焼空気中の
酸素濃度が増加し、結果的にNOx値が上昇する
という欠点を持つ。 That is, while the reheated steam temperature tends to rise when the load increases, the GRF inlet damper is controlled to close in advance, so the recirculation gas flow rate decreases. On the other hand, since the mixed gas damper, primary gas inlet damper, and furnace hopper inlet damper only open uniformly, the mixed gas flow rate and primary gas flow rate are insufficient for the load command, and the oxygen concentration in the combustion air increases. However, this has the disadvantage that the NOx value increases as a result.
本発明の目的は、ガス再循環を行なうボイラで
負荷上昇時にNOxが上昇する上述の欠点を改善
することにある。 An object of the present invention is to improve the above-mentioned drawback that NOx increases when the load increases in a boiler that performs gas recirculation.
このため、本発明は、特に負荷上昇時の再循環
ガス量の変動分を火炉ホツパー入口ダンパーで吸
収し、その変動を抑制する制御系を採用すること
により、混合ガス流量、一次ガス流量の変動を押
え、燃焼空気中の酸素濃度を負荷に見合つたもの
としNOxを下げる制御装置を提案するものであ
る。
For this reason, the present invention absorbs fluctuations in the amount of recirculated gas especially when the load increases with the furnace hopper inlet damper, and adopts a control system that suppresses the fluctuations. This paper proposes a control device that reduces NOx by controlling the oxygen concentration in the combustion air to match the load.
本発明によれば、例えば負荷上昇時先行的に火
炉ホツパー入口ダンパーを閉じる方向に制御し、
混合ガス流量、一次ガス流量を負荷に見合つたも
のとすることができるので、燃焼空気中の酸素濃
度を押えNOx値を低減することができる。
According to the present invention, for example, when the load increases, the furnace hopper inlet damper is controlled in the direction of closing in advance,
Since the mixed gas flow rate and the primary gas flow rate can be adjusted to match the load, the oxygen concentration in the combustion air can be suppressed and the NOx value can be reduced.
本発明の実施例を第3図に示す。第2図に示す
ものと同一又は同等分には同一符号を付した。
An embodiment of the invention is shown in FIG. Components that are the same or equivalent to those shown in FIG. 2 are given the same reference numerals.
本実施例では、第2図bと第3図を対照して明
らかなように、火炉ホツパー入口ダンパー開度指
令27(火炉への再循環ガス量指令に匹敵)を、
負荷指令21の変化率を微分器28で検出し、こ
の変化率に見合つたゲインを関数発生器224に
より作成し掛算器29により補正することによつ
て得る点に特徴がある。本方式により従来、負荷
上昇時において混合ガスダンパー、一次ガスダン
パー、火炉ホツパー入口ダンパーが同様な先行信
号により一様な開閉していたのに対し、火炉ホツ
パー入口ダンパーを絞り込むことにより再循環ガ
ス量の減少があつても混合ガス流量、一次ガス流
量の減少を防止することに特徴がある。 In this embodiment, as is clear by comparing FIG. 2b and FIG. 3, the furnace hopper inlet damper opening command 27 (comparable to the recirculation gas amount command to the furnace) is
It is characterized in that the rate of change of the load command 21 is detected by the differentiator 28, a gain commensurate with this rate of change is created by the function generator 224, and the gain is corrected by the multiplier 29. With this system, whereas conventionally the mixed gas damper, primary gas damper, and furnace hopper inlet damper were uniformly opened and closed by the same preceding signal when the load increased, by narrowing down the furnace hopper inlet damper, the amount of recirculated gas is increased. The feature is that even if there is a decrease in the mixed gas flow rate and primary gas flow rate, the decrease in the mixed gas flow rate and the primary gas flow rate is prevented.
本実施例に依れば、ガス再循環を行なうボイラ
においてGRF入口ダンパーで再熱蒸気温度を制
御し、さらに混合ガス入口ダンパー、一次ガス入
口ダンパー、火炉ホツパー入口ダンパーに依り
NOxを制御する場合、特に負荷上昇時に火炉ホ
ツパー入口ダンパーを先行的に絞ることにより、
再熱蒸気温度制御のためGRF入口ダンパーが絞
られ、再循環ガス量が減少しても混合ガス量、一
次ガス量の減少を防止することが可能となつた。 According to this embodiment, in a boiler that performs gas recirculation, the reheated steam temperature is controlled by a GRF inlet damper, and further by a mixed gas inlet damper, a primary gas inlet damper, and a furnace hopper inlet damper.
When controlling NOx, especially when the load increases, by preemptively throttling the furnace hopper inlet damper,
The GRF inlet damper is throttled to control the temperature of reheated steam, making it possible to prevent a decrease in the amount of mixed gas and primary gas even if the amount of recirculated gas decreases.
以上のように、本発明によれば常に燃焼用空気
中の酸素濃度を負荷指令に見合つたものとし、
NOx値の上昇を防止し好適な再循環ガス制御が
得られる。
As described above, according to the present invention, the oxygen concentration in the combustion air is always made to match the load command,
A rise in NOx value can be prevented and suitable recirculation gas control can be obtained.
第1図は火力プラントの煙風道概略図を示す。
第2図は従来の再循環ガス制御方式を、第3図は
本発明による再循環ガス制御方式をそれぞれ示
す。
16……再熱蒸気温度、17……信号発生器、
18……再熱蒸気温度設定、19……温度偏差、
20……比例積分器、21……負荷指令、23…
…混合ガス流量、24……混合ガス流量偏差、2
5,26……バイアス、221,222,22
3,224……関数発生器。
Figure 1 shows a schematic diagram of the smoke duct of a thermal power plant.
FIG. 2 shows a conventional recirculation gas control system, and FIG. 3 shows a recirculation gas control system according to the present invention. 16...Reheat steam temperature, 17...Signal generator,
18...Reheat steam temperature setting, 19...Temperature deviation,
20...Proportional integrator, 21...Load command, 23...
...Mixed gas flow rate, 24...Mixed gas flow rate deviation, 2
5, 26...Bias, 221, 222, 22
3,224...Function generator.
Claims (1)
分けて再循環させる構造を有するボイラの制御装
置において、負荷指令信号を取込み該負荷指令の
変動に対応した制御信号を発生させる制御要素を
有し、この制御信号に応じて、上記負荷指令の変
動に基づく上記燃焼材料供給部への再循環ガス量
の減少を抑制するように上記火炉への再循環ガス
量を制御する制御系を有することを特徴とするボ
イラ自動制御装置。1. A boiler control device having a structure in which a part of the combustion gas is divided and recirculated to the furnace and the combustion material supply section, which includes a control element that receives a load command signal and generates a control signal corresponding to fluctuations in the load command. and a control system that controls the amount of recirculated gas to the furnace in accordance with this control signal so as to suppress a decrease in the amount of recirculated gas to the combustion material supply section based on fluctuations in the load command. A boiler automatic control device featuring:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6122281A JPS57175803A (en) | 1981-04-24 | 1981-04-24 | Automatic boiler controller |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6122281A JPS57175803A (en) | 1981-04-24 | 1981-04-24 | Automatic boiler controller |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57175803A JPS57175803A (en) | 1982-10-28 |
JPH0315082B2 true JPH0315082B2 (en) | 1991-02-28 |
Family
ID=13164955
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6122281A Granted JPS57175803A (en) | 1981-04-24 | 1981-04-24 | Automatic boiler controller |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS57175803A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5591710A (en) * | 1978-12-28 | 1980-07-11 | Hitachi Ltd | Controlling device of steam generating apparatus |
-
1981
- 1981-04-24 JP JP6122281A patent/JPS57175803A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5591710A (en) * | 1978-12-28 | 1980-07-11 | Hitachi Ltd | Controlling device of steam generating apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPS57175803A (en) | 1982-10-28 |
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