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JPH0160734B2 - - Google Patents
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JPH0160734B2 - - Google Patents

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Publication number
JPH0160734B2
JPH0160734B2 JP56140138A JP14013881A JPH0160734B2 JP H0160734 B2 JPH0160734 B2 JP H0160734B2 JP 56140138 A JP56140138 A JP 56140138A JP 14013881 A JP14013881 A JP 14013881A JP H0160734 B2 JPH0160734 B2 JP H0160734B2
Authority
JP
Japan
Prior art keywords
air
fuel
flow rate
temperature
fuel ratio
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
Application number
JP56140138A
Other languages
Japanese (ja)
Other versions
JPS5840425A (en
Inventor
Tadao Senba
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP56140138A priority Critical patent/JPS5840425A/en
Publication of JPS5840425A publication Critical patent/JPS5840425A/en
Publication of JPH0160734B2 publication Critical patent/JPH0160734B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N1/00Regulating fuel supply
    • F23N1/02Regulating fuel supply conjointly with air supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2235/00Valves, nozzles or pumps
    • F23N2235/02Air or combustion gas valves or dampers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2235/00Valves, nozzles or pumps
    • F23N2235/12Fuel valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2237/00Controlling
    • F23N2237/02Controlling two or more burners

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Control Of Combustion (AREA)
  • Regulation And Control Of Combustion (AREA)

Description

【発明の詳細な説明】 本発明は燃焼炉加熱用の複数のバーナのそれぞ
れへの燃料供給量と空気供給量とを各バーナに対
応する炉内温度と各バーナへの分配前における総
空気供給量と総燃料供給量との比である空燃比と
にもとずいて制御し炉内の温度分布を設定温度に
維持できるようにした燃焼炉の温度制御装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for determining the amount of fuel supplied and the amount of air supplied to each of a plurality of burners for heating a combustion furnace, based on the furnace temperature corresponding to each burner and the total air supply before distribution to each burner. The present invention relates to a temperature control device for a combustion furnace that maintains the temperature distribution within the furnace at a set temperature by controlling the air-fuel ratio, which is the ratio between the amount of fuel supplied and the total amount of fuel supplied.

従来、燃焼炉の温度制御装置としては炉内温度
分布を良好にするため、燃焼炉に設けられた複数
のバーナを、燃焼炉の各ゾーン別設定温度に従つ
て個々に空燃比を調節しながら最適制御してい
た。この例としては、第1図に示す温度制御装置
がある。
Conventionally, temperature control devices for combustion furnaces have been used to control the air-fuel ratio of multiple burners installed in the combustion furnace individually according to the set temperature for each zone of the combustion furnace, in order to improve the temperature distribution inside the furnace. It was under optimal control. An example of this is the temperature control device shown in FIG.

この温度制御装置は個々のバーナ1の燃料配管
2と空気配管3に燃料流量検出器4と燃料流量調
節弁5及び空気流量検出器6と空気流量調節弁7
とを設けている。そして燃料流量検出器4と空気
流量検出器6からの各出力を入力として測定空燃
比に対応した信号を出力する空燃比演算器8と、
該演算器8からの信号と空燃比設定器9からの設
定空燃比に対応した出力信号Rとを入力として例
えばPI演算を行ない空燃比偏差に対応した修正
信号Sを発生する空燃比調節器10と、図示しな
い炉内温度検出装置による検出炉温と内蔵する炉
温設定器による設定炉温との偏差に応じた流量設
定信号Qを出力する温度調節器11と、炉内温度
を一定以上に保持するためのローリミツタ12と
をそれぞれ備えるとともに、温度調節器11から
の流量設定信号Qにローリミツタ12を介しての
出力と空燃比調節器10からの修正記号Sとを入
力とする乗算器13からの燃料流量修正信号P1
を加算した加算器14からの弁調節信号と、温度
調節器11からの流量設定信号Qから乗算器13
からの空気流量修正信号P2を減算した減算器1
5からの他の弁調節信号とによつて夫々燃料流量
調節弁5と空気流量調節弁7とを制御している。
This temperature control device includes a fuel pipe 2 and an air pipe 3 of each burner 1, a fuel flow detector 4, a fuel flow control valve 5, an air flow detector 6, and an air flow control valve 7.
and. and an air-fuel ratio calculator 8 which inputs each output from the fuel flow rate detector 4 and the air flow rate detector 6 and outputs a signal corresponding to the measured air-fuel ratio;
An air-fuel ratio regulator 10 receives the signal from the calculator 8 and the output signal R corresponding to the set air-fuel ratio from the air-fuel ratio setting device 9 and performs, for example, PI calculation to generate a correction signal S corresponding to the air-fuel ratio deviation. and a temperature controller 11 that outputs a flow rate setting signal Q according to the deviation between the furnace temperature detected by an internal furnace temperature detection device (not shown) and the furnace temperature set by a built-in furnace temperature setting device, and and a multiplier 13 which inputs the output via the low limiter 12 and the correction symbol S from the air-fuel ratio controller 10 to the flow rate setting signal Q from the temperature controller 11. Fuel flow rate correction signal P1
The multiplier 13 uses the valve control signal from the adder 14 which has been added together with the flow rate setting signal Q from the temperature controller
Subtractor 1 that subtracted the air flow rate correction signal P2 from
The fuel flow control valve 5 and the air flow control valve 7 are respectively controlled by other valve control signals from the control valve 5.

従つて、この場合、各バーナ1への燃料供給量
と空気供給量は各バーナ1別に個々に設けた温度
調節器11と空燃比設定器9とによつて最適制御
される反面、各バーナ1毎に独立した温度制御装
置と空燃比制御装置を必要とするため燃焼炉の温
度制御には相当の設備費を要すると云う欠点があ
つた。
Therefore, in this case, the amount of fuel supplied and the amount of air supplied to each burner 1 are optimally controlled by the temperature controller 11 and air-fuel ratio setting device 9 provided individually for each burner 1; Since each combustion furnace requires an independent temperature control device and air-fuel ratio control device, temperature control of the combustion furnace has the drawback of requiring considerable equipment costs.

又、この空燃比を含む温度制御装置を簡潔にし
たものとしては第2図のように温度調節器11に
よつて空気流量調節弁7を制御するとともに、こ
の空気流量に対応した空燃比調節器10からの出
力によつて燃料流量調節弁5を制御したものがあ
るが、この場合にしても、一方の流量の変化に対
応して空燃比を制御するため、急激な変化に対し
ては応答遅れがでるといつた根本的な欠点の他
に、各バーナ1毎に高価な燃料流量検出器4、空
気流量検出器6、温度調節器11等を必要とする
ことから燃焼炉の温度制御には相当の設備費を要
すると云う欠点があつた。
In addition, as a simplified temperature control device including this air-fuel ratio, as shown in FIG. There is a system in which the fuel flow control valve 5 is controlled by the output from 10, but even in this case, the air-fuel ratio is controlled in response to changes in one flow rate, so it does not respond to sudden changes. In addition to the fundamental drawback of delays, the need for expensive fuel flow rate detectors 4, air flow rate detectors 6, temperature regulators 11, etc. for each burner 1 makes it difficult to control the temperature of the combustion furnace. The disadvantage was that it required considerable equipment costs.

本発明の目的は炉内温度分布を良好に維持する
ことができしかも燃焼炉の温度制御に要する設備
費を大巾に低減することができる燃焼炉の温度制
御装置を提供することにある。そのため本発明は
燃焼炉に設けられた複数個の単位バーナに対し
て、流体燃料供給用の主燃料配管からの燃料と空
気供給用の主空気配管からの空気とを各単位バー
ナ別分岐燃料配管と分岐空気配管とを介して供給
するとともに主燃料配管と主空気配管とに単位バ
ーナ群への総燃料供給量と総空気供給量とを検出
する燃料流量検出器と空気流量検出器とを設け、
各分岐燃料配管と分岐空気配管とに夫々単位バー
ナ別燃料流量調節弁と空気流量調節弁とを設け、
かつ、燃焼炉内温度を検出するとともに該炉内温
度と予め設定した設定温度との差に対応した温度
差出力を発生させる温度調節器を各バーナ別に設
け、更に、前記各単位バーナ別燃料流量調節弁と
空気流量調節弁とによる調節流量を、各単位バー
ナ別温度調節器からの温度差出力によつて該温度
差をなくす方向に増減させるとともに、前記燃料
流量調節弁と空気流量調節弁とによる調節流量の
流量比を、前記燃料流量検出器と空気流量検出器
の各出力によつて求められた測定空燃比と予め設
定された設定空燃比との差に対応した空燃比調節
器からの空燃比差出力によつて該空燃比差をなく
す方向に変化させることを特徴とする。
SUMMARY OF THE INVENTION An object of the present invention is to provide a temperature control device for a combustion furnace that can maintain a good temperature distribution in the furnace and can significantly reduce the equipment cost required for temperature control of the combustion furnace. Therefore, the present invention provides for a plurality of unit burners installed in a combustion furnace to be supplied with fuel from a main fuel pipe for fluid fuel supply and air from a main air pipe for air supply through branch fuel pipes for each unit burner. A fuel flow rate detector and an air flow rate detector are provided in the main fuel piping and the main air piping to detect the total fuel supply amount and the total air supply amount to the unit burner group. ,
Each branch fuel pipe and branch air pipe are provided with a fuel flow rate control valve and an air flow rate control valve for each unit burner, respectively.
Further, each burner is provided with a temperature regulator that detects the temperature inside the combustion furnace and generates a temperature difference output corresponding to the difference between the inside temperature of the furnace and a preset temperature, and furthermore, the fuel flow rate for each unit burner is adjusted. The flow rate controlled by the control valve and the air flow control valve is increased or decreased in a direction to eliminate the temperature difference according to the temperature difference output from the temperature controller for each unit burner, and the flow rate controlled by the fuel flow control valve and the air flow control valve is The flow rate ratio of the adjusted flow rate is calculated from the air-fuel ratio controller corresponding to the difference between the measured air-fuel ratio obtained from each output of the fuel flow rate detector and the air flow rate detector and the preset set air-fuel ratio. It is characterized in that the air-fuel ratio difference is changed in the direction of eliminating the air-fuel ratio difference by the air-fuel ratio difference output.

次に本発明の一実施例の構成を第3図によつて
説明する。なお第1図、第2図における構成部品
と同一の部品等については同一の番号及び符号を
用いる。
Next, the configuration of an embodiment of the present invention will be explained with reference to FIG. Note that the same numbers and symbols are used for the same components as those in FIGS. 1 and 2.

燃焼炉に設けられた複数個の各バーナ1には流
体燃料供給用の主燃料配管16からの燃料と、空
気供給用の主空気配管17からの空気が各バーナ
1別分岐燃料配管18と分岐空気配管19を介し
て供給されるとともに、主燃料配管16と主空気
配管17とには各バーナ1全休への総燃料供給量
と総空気供給量とを検出するための燃料流量検出
器4と空気流量検出器6とが取付けられ、各バー
ナ1別分岐燃料配管18と分岐空気配管19には
各バーナ1別に燃料流量と空気流量を調節するた
めの燃料流量調節弁5と空気流量調節弁7とが取
付けられている。また燃焼炉には図示しない炉内
温度検出装置による各バーナ1に対応した検出炉
温と内蔵する炉温設定器による設定炉温との偏差
に応じた流量設定信号Qを出力させる温度調節器
11と炉内温度を一定以上に保持するためのロー
リミツタ12とが各バーナ1別に設けられてい
る。更に燃料流量検出器4と空気流量検出器6か
らの各出力を入力として空燃比演算器8から発生
される測定空燃比に対応した出力と空燃比設定器
9からの設定空燃比に対応した出力信号Rとを入
力として空燃比偏差に対応したPI演算の修正信
号Sを発生させる空燃比調節器10が全バーナ1
に対して1個設けられている。時に温度調節器1
1からの流量設定信号Qに対して、該温度調節器
11からのローリミツタ12を介しての出力と空
燃比調節器10からの出力信号Sとを入力とする
乗算器13からの燃料流量修正信号P1を加算し
て燃料流量調節弁5に弁調節信号を入力させる加
算器14と、温度調節器11からの流量設定信号
Qに対して乗算器13からの空気流量修正信号P
2を減算して空気流量調節弁7に弁調節信号を入
力させる減算器15と、該減算器15からの弁調
節信号を補正して空燃比を各バーナ1別に補正す
るための弁特性補正器20とが各バーナ1別に設
けられている。
Fuel from a main fuel pipe 16 for fluid fuel supply and air from a main air pipe 17 for air supply are supplied to each of the plurality of burners 1 provided in the combustion furnace, and branch to branch fuel pipes 18 for each burner 1. The main fuel pipe 16 and the main air pipe 17 are provided with a fuel flow rate detector 4 for detecting the total amount of fuel supplied to each burner 1 and the total amount of air supplied to each burner 1. An air flow rate detector 6 is attached to the branch fuel pipe 18 and branch air pipe 19 for each burner 1, and a fuel flow control valve 5 and an air flow control valve 7 for adjusting the fuel flow rate and air flow rate for each burner 1 are attached. is installed. Further, in the combustion furnace, a temperature controller 11 outputs a flow rate setting signal Q according to the deviation between the furnace temperature detected by the furnace temperature detection device (not shown) corresponding to each burner 1 and the furnace temperature set by the built-in furnace temperature setting device. and a low limiter 12 for maintaining the furnace temperature above a certain level are provided for each burner 1. Furthermore, each output from the fuel flow rate detector 4 and the air flow rate detector 6 is inputted, and an output corresponding to the measured air-fuel ratio generated from the air-fuel ratio calculator 8 and an output corresponding to the set air-fuel ratio from the air-fuel ratio setting device 9 are generated. An air-fuel ratio regulator 10 that receives a signal R as an input and generates a correction signal S for PI calculation corresponding to an air-fuel ratio deviation is connected to all burners 1.
One is provided for each. Temperature controller 1
1, a fuel flow rate correction signal is sent from a multiplier 13 which receives the output from the temperature regulator 11 via the low limiter 12 and the output signal S from the air-fuel ratio regulator 10 as input. an adder 14 that adds P1 and inputs a valve control signal to the fuel flow rate control valve 5; and an air flow rate correction signal P from the multiplier 13 for the flow rate setting signal Q from the temperature controller 11;
a subtracter 15 that inputs a valve adjustment signal to the air flow rate adjustment valve 7 by subtracting 2, and a valve characteristic corrector that corrects the air-fuel ratio for each burner 1 by correcting the valve adjustment signal from the subtractor 15. 20 are provided separately for each burner 1.

次に本実施例の作用について説明する。 Next, the operation of this embodiment will be explained.

このように構成された燃焼炉の温度制御装置に
おいて、各バーナ1の燃料流量調節弁5と空気流
量調節弁7とには共通した1個の空燃比制御装置
21が対応しているが、各バーナ1個々に対応し
た燃焼炉の各ゾーン別空燃比は各バーナ1別弁特
性補正器20による補正量で定まり、従つて、空
燃比設定器9には全バーナ1の平均的空燃比が設
定された状態で、個々のバーナ1の空燃比は各バ
ーナ1別弁特性補正器20で補正して設定し、か
つ、図示省略炉温設定器によつて炉温を設定す
る。
In the combustion furnace temperature control device configured in this way, one common air-fuel ratio control device 21 corresponds to the fuel flow rate control valve 5 and the air flow rate control valve 7 of each burner 1, but each The air-fuel ratio for each zone of the combustion furnace corresponding to each burner 1 is determined by the correction amount by the valve characteristic corrector 20 for each burner 1, and therefore, the average air-fuel ratio of all burners 1 is set in the air-fuel ratio setting device 9. In this state, the air-fuel ratio of each burner 1 is corrected and set by a valve characteristic corrector 20 for each burner 1, and the furnace temperature is set by a furnace temperature setting device (not shown).

その結果全バーナ1への燃料供給量と空気供給
量とによる測定空燃比が空燃比設定器9による設
定空燃比と比較された状態の空燃比偏差をPI演
算した修正信号Sが空燃比調節器10から各バー
ナ1別温度制御の乗算器13に入力され、各バー
ナ1の燃料流量調節弁5と空気流量調節弁7は各
バーナ1別温度調節器11からの流量設定信号Q
と空燃比調節器10からの修正信号Sとによつて
制御されるものの、減算器15からの弁調節信号
は弁特性補正器20によつて各バーナ1別空燃比
に対応して補正されるため、燃焼炉は実質的に、
各バーナ1別に空燃比制御装置を設けた第1図の
場合と同様に、各バーナ1別に空燃比とともに温
度制御される。
As a result, a correction signal S, which is a PI calculation of the air-fuel ratio deviation in a state where the measured air-fuel ratio based on the fuel supply amount and air supply amount to all burners 1 is compared with the air-fuel ratio set by the air-fuel ratio setting device 9, is sent to the air-fuel ratio controller. 10 to the multiplier 13 for temperature control for each burner 1, and the fuel flow rate control valve 5 and air flow rate control valve 7 of each burner 1 receive the flow rate setting signal Q from the temperature control device 11 for each burner 1.
The valve adjustment signal from the subtractor 15 is corrected by a valve characteristic corrector 20 in accordance with the air-fuel ratio of each burner 1. Therefore, the combustion furnace is essentially
As in the case of FIG. 1 in which an air-fuel ratio control device is provided for each burner 1, the air-fuel ratio and temperature are controlled for each burner 1.

なお燃料と燃焼空気の流量調節弁の特性やタン
ダウン比の小さい炉の場合には弁特性補正器20
を省くことができる他炉の設定温度と許容変動巾
等によつてはローリミツタ12を省くことがで
き、又、この温度制御は第4図のように、炉の各
ゾーン別或は炉上位置のバーナ1等、任意の個数
のバーナ1を単位として温度制御することもで
き、又空燃比制御装置21は複数の単位バーナ1
毎に設けることができる。
In addition, in the case of a furnace with a small characteristic of the fuel and combustion air flow control valve or a small turndown ratio, a valve characteristic corrector 20 is used.
The low limiter 12 can be omitted depending on the set temperature of the furnace and the allowable fluctuation range, etc., and this temperature control can be performed separately for each zone of the furnace or at a position on the furnace, as shown in Fig. 4. It is also possible to control the temperature of an arbitrary number of burners 1 as a unit, such as burners 1 of
It can be provided for each.

このように本発明は燃焼炉の各バーナ全体に供
給される燃料供給量と空気供給量を対象にして複
数の単位バーナからなるバーナ全体を一括して空
燃比制御した状態で各単位バーナ別に温度制御す
ることによつて炉内温度分布を良好に維持できし
かも炉の温度制御に要する設備費を大巾に低減す
ることができる効果がある。
In this way, the present invention targets the fuel supply amount and air supply amount supplied to each burner of a combustion furnace, and controls the temperature of each unit burner while collectively controlling the air-fuel ratio of the entire burner consisting of a plurality of unit burners. By controlling the temperature, it is possible to maintain a good temperature distribution in the furnace, and the equipment cost required for controlling the temperature of the furnace can be significantly reduced.

【図面の簡単な説明】[Brief explanation of drawings]

第1図と第2図は従来の実施例の温度制御系統
図、第3図は本発明の一実施例の温度制御系統
図、第4図は本発明の他の実施例の温度制御系統
図を示す。 1……バーナ、4……燃料流量検出器、5……
燃料流量調節器、6……空気流量検出器、7……
空気流量調節弁、8……空燃比演算器、9……空
燃比設定器、10……空燃比調節器、11……温
度調節器、13……乗算器、14……加算器、1
5……減算器、16……主燃料配管、17……主
空気配管、18……分岐燃料配管、19……分岐
空気配管、21……空燃比制御装置。
Figures 1 and 2 are temperature control system diagrams of a conventional embodiment, Figure 3 is a temperature control system diagram of an embodiment of the present invention, and Figure 4 is a temperature control system diagram of another embodiment of the present invention. shows. 1...Burner, 4...Fuel flow rate detector, 5...
Fuel flow rate regulator, 6...Air flow rate detector, 7...
Air flow control valve, 8... Air-fuel ratio calculator, 9... Air-fuel ratio setter, 10... Air-fuel ratio regulator, 11... Temperature controller, 13... Multiplier, 14... Adder, 1
5... Subtractor, 16... Main fuel pipe, 17... Main air pipe, 18... Branch fuel pipe, 19... Branch air pipe, 21... Air-fuel ratio control device.

Claims (1)

【特許請求の範囲】 1 燃焼炉に設けられた複数個の単位バーナに対
して、流体燃料供給用の主燃料配管からの燃料と
空気供給用の主空気配管からの空気とを各単位バ
ーナ別分岐燃料配管と分岐空気配管とを介して供
給するとともに、主燃料配管と主空気配管とに単
位バーナ群への総燃料供給量と総空気供給量とを
検出する燃料流量検出器と空気流量検出器とを設
け、各分岐燃料配管と分岐空気配管とに夫々単位
バーナ別燃料流量調節弁と空気流量調節弁とを設
け、かつ、燃焼炉内温度を検出するとともに該炉
内温度と予め設定した設定温度との差に対応した
温度差出力を発生させる温度調節器を各バーナ別
に設け、更に、前記各単位バーナ別燃料流量調節
弁と空気流量調節弁とによる調節流量を、各単位
バーナ別温度調節器からの温度差出力によつて該
温度差をなくす方向に増減させるとともに、前記
燃料流量調節弁と空気流量調節弁とによる調節流
量の流量比を前記燃料流量検出器と空気流量検出
器の各出力によつて求められた測定空燃比と予め
設定された設定空燃比との差に対応した空燃比調
節器からの空燃比差出力によつて該空燃比差をな
くす方向に変化させることを特徴とする燃焼炉の
温度制御装置。 2 燃焼炉に設けられた複数個の単位バーナに対
して流体燃料供給用の主燃料配管からの燃料と空
気供給用の主空気配管からの空気とを各単位バー
ナ別分岐燃料配管と分岐空気配管とを介して供給
するとともに、主燃料配管と主空気配管とに単位
バーナ群への総燃料供給量と総空気供給量とを検
出する燃料流量検出器と空気流量検出器とを設
け、各分岐燃料配管と分岐空気配管とに夫々単位
バーナ別燃料流量調節弁と空気流量調節弁とを設
け、かつ、前記燃料流量検出器と空気流量検出器
からの出力を入力とする空燃比演算器からの測定
空燃比に対応した出力と空燃比設定器からの設定
空燃比に対応した出力とを入力として空燃比偏差
に対応した出力を発生させる空燃比調節器を設け
るとともに燃焼炉内温度を検出して該炉内温度と
予め設定した設定温度との差に対応した温度差出
力を発生させる温度調節器を各単位バーナ別に設
け、更に、各単位バーナ別燃料流量調節弁と空気
流量調節弁とを、各温度調節器からの出力に対し
て、該温度調節器からの出力と空燃比調節器から
の出力とを入力とする乗算器からの出力を加算し
た一方の弁調節信号と減算した他方の弁調節信号
によつて制御することを特徴とする燃焼炉の温度
制御装置。 3 温度調節器からの出力を、燃焼炉の温度を一
定以上に保持するためのローリミツタを介して乗
算器に入力させることを特徴とする前記特許請求
の範囲第2項に記載の燃焼炉の温度制御装置。 4 各単位バーナ別空気流量調節弁に対して、空
燃比を各単位バーナ別に補正するための弁特性補
正器を介して弁調節用信号を入力させることを特
徴とする前記特許請求の範囲第2項又は第3項に
記載の燃焼炉の温度制御装置。
[Scope of Claims] 1. For a plurality of unit burners provided in a combustion furnace, fuel from a main fuel pipe for fluid fuel supply and air from a main air pipe for air supply are distributed to each unit burner separately. A fuel flow rate detector and an air flow rate detector are installed in the main fuel piping and the main air piping to detect the total amount of fuel supplied and the total amount of air supplied to the unit burner group. A fuel flow rate control valve and an air flow rate control valve for each unit burner are provided in each branch fuel pipe and branch air pipe, respectively, and the temperature inside the combustion furnace is detected and set in advance to the temperature inside the combustion furnace. A temperature controller is provided for each burner to generate a temperature difference output corresponding to the difference from the set temperature, and the flow rate adjusted by the fuel flow rate control valve for each unit burner and the air flow rate control valve is adjusted to the temperature for each unit burner. The temperature difference output from the regulator is used to increase or decrease the temperature difference in the direction of eliminating the temperature difference, and the flow rate ratio between the flow rates adjusted by the fuel flow rate control valve and the air flow rate control valve is adjusted between the fuel flow rate detector and the air flow rate detector. The air-fuel ratio difference output from the air-fuel ratio controller corresponding to the difference between the measured air-fuel ratio determined by each output and the preset set air-fuel ratio is used to change the air-fuel ratio in a direction to eliminate the air-fuel ratio difference. Characteristic combustion furnace temperature control device. 2 Fuel from the main fuel piping for fluid fuel supply and air from the main air piping for air supply to multiple unit burners installed in the combustion furnace through branch fuel piping and branch air piping for each unit burner. At the same time, a fuel flow rate detector and an air flow rate detector are installed in the main fuel piping and the main air piping to detect the total fuel supply amount and total air supply amount to the unit burner group. A fuel flow rate control valve and an air flow rate control valve for each unit burner are provided in the fuel pipe and the branch air pipe, respectively, and an air-fuel ratio calculator is provided with outputs from the fuel flow rate detector and the air flow rate detector as inputs. An air-fuel ratio regulator is provided which receives an output corresponding to the measured air-fuel ratio and an output corresponding to the set air-fuel ratio from the air-fuel ratio setting device as input and generates an output corresponding to the air-fuel ratio deviation, and also detects the temperature inside the combustion furnace. A temperature controller that generates a temperature difference output corresponding to the difference between the temperature inside the furnace and a preset temperature is provided for each unit burner, and a fuel flow rate control valve and an air flow rate control valve are provided for each unit burner, One valve control signal is obtained by adding the output from a multiplier whose inputs are the output from the temperature regulator and the output from the air-fuel ratio regulator, and the output from the other valve is subtracted from the output from each temperature regulator. A temperature control device for a combustion furnace, characterized in that it is controlled by an adjustment signal. 3. The temperature of the combustion furnace according to claim 2, characterized in that the output from the temperature controller is input to the multiplier via a low limiter for maintaining the temperature of the combustion furnace above a certain level. Control device. 4. The second aspect of the present invention is characterized in that a valve adjustment signal is inputted to each unit burner-specific air flow rate control valve via a valve characteristic corrector for correcting the air-fuel ratio for each unit burner. The temperature control device for a combustion furnace according to item 1 or 3.
JP56140138A 1981-09-04 1981-09-04 Combustion furnace temperature control device Granted JPS5840425A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56140138A JPS5840425A (en) 1981-09-04 1981-09-04 Combustion furnace temperature control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56140138A JPS5840425A (en) 1981-09-04 1981-09-04 Combustion furnace temperature control device

Publications (2)

Publication Number Publication Date
JPS5840425A JPS5840425A (en) 1983-03-09
JPH0160734B2 true JPH0160734B2 (en) 1989-12-25

Family

ID=15261758

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56140138A Granted JPS5840425A (en) 1981-09-04 1981-09-04 Combustion furnace temperature control device

Country Status (1)

Country Link
JP (1) JPS5840425A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2024042824A (en) * 2022-09-16 2024-03-29 三菱重工業株式会社 BOILER CONTROL DEVICE, BOILER CONTROL METHOD, AND BOILER CONTROL PROGRAM

Also Published As

Publication number Publication date
JPS5840425A (en) 1983-03-09

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