JPS5993114A - Combustion air feed method for disolving furnace - Google Patents

Combustion air feed method for disolving furnace

Info

Publication number
JPS5993114A
JPS5993114A JP57202401A JP20240182A JPS5993114A JP S5993114 A JPS5993114 A JP S5993114A JP 57202401 A JP57202401 A JP 57202401A JP 20240182 A JP20240182 A JP 20240182A JP S5993114 A JPS5993114 A JP S5993114A
Authority
JP
Japan
Prior art keywords
burner
blower
air
damper
pressure
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
Application number
JP57202401A
Other languages
Japanese (ja)
Inventor
Tetsuo Shinoda
信田 鉄夫
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.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries 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 Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP57202401A priority Critical patent/JPS5993114A/en
Publication of JPS5993114A publication Critical patent/JPS5993114A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N3/00Regulating air supply or draught
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2225/00Measuring
    • F23N2225/02Measuring filling height in burners
    • 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
    • F23N2235/06Air or combustion gas valves or dampers at the air intake
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N2237/00Controlling
    • F23N2237/02Controlling two or more burners
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23NREGULATING OR CONTROLLING COMBUSTION
    • F23N5/00Systems for controlling combustion
    • F23N5/18Systems for controlling combustion using detectors sensitive to rate of flow of air or fuel

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Regulation And Control Of Combustion (AREA)

Abstract

PURPOSE:To prevent the occurrence of mutual interference between burners, by a method wherein an air pressure control loop consists of a damper device, a damper control device, an air pressure or an air amount detector, and an individual air pressure or an air amount regulator. CONSTITUTION:Control for the number of revolutions of a blower 11 is effected in combination with control for the opening degree of a damper 15 at a burner inlet, and an air pressure control loop consisting of a damper device 15, a damper control device 16, an air pressure or an air amount detector 17, and an individual air pressure or an air amount regulator 19 is mounted to each burner 18. Further, in response to an air pressure or an air amount signal from each burner 18, a pressure loss between the blower 11 and each burner 18 is automatically compensated to obtain an instruction for the number of revolutions to the blower 11. This prevents the occurrence of interference between the burners, and enables arbitrary regulation of a heating power and the high-efficient supply of the air for combustion.

Description

【発明の詳細な説明】 この発明は金属等溶解炉の燃焼空気供給方法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for supplying combustion air to a metal melting furnace.

1台の送風機により燃焼用空気が供給される複数の燃焼
バーナを有する金属等の溶解炉においては、炉の運転状
態に応じて、それぞれのバーナの空気量を適性かつ任意
に調節する必要がある。
In a metal melting furnace that has multiple combustion burners where combustion air is supplied by a single blower, it is necessary to appropriately and arbitrarily adjust the amount of air in each burner depending on the operating state of the furnace. .

従来、空気量の調節は送風機を一定回転数で運転し、各
バーナの入口に設けられたダンパーの開度を手動または
空燃比制御装置などの自動制御装置によりそれぞれ自動
的に変化させることによって行なわれていた。
Conventionally, the amount of air has been adjusted by operating a blower at a constant rotation speed and changing the opening degree of a damper installed at the inlet of each burner either manually or automatically using an automatic control device such as an air-fuel ratio controller. It was

従って、送風機の容量としては、炉の種々の運転状況に
おける最大の風圧、風量が供給できる能力をもつものが
設置されているものの、一般に平均的な炉の運転におい
ては、送風機の能力を最大限に使用する頻度は少なく、
ダンパーをしぼって使用するため、送風機の駆動動力の
減少が少なく、不経済な運転状況にあった。
Therefore, although the blower is installed with the capacity to supply the maximum wind pressure and air volume under the various operating conditions of the furnace, in general, in average furnace operation, the capacity of the blower is set to its maximum capacity. It is used less frequently,
Since the damper was used with a reduced pressure, the drive power of the blower was not significantly reduced, resulting in an uneconomical operating situation.

また最新の炉においては、熱効率を上げるために空気予
熱器などの熱交換器を設置することが多く、この場合空
気ダクト等が長大となり、送風機から各バーナまでの圧
力損失が無視できない大きさとなり、1つのバーナの風
量を変化させると、他のバーナの風量も変化し、火力が
変動する相互干渉が発生する不具合もあった。
In addition, in the latest furnaces, heat exchangers such as air preheaters are often installed to increase thermal efficiency, and in this case, the air ducts etc. become long and the pressure loss from the blower to each burner becomes large enough to not be ignored. However, when the air volume of one burner was changed, the air volume of other burners also changed, causing mutual interference in which the thermal power fluctuated.

一方バーナの空気量の調節はダンパーの圧力損失効果に
よらなくとも送風機の回転数を制御し、吐出圧力変える
ことによっても可能であり、この方法は送風機の機械効
率の低下が少なく駆動動力が回転数の約3乗に比例し、
低下する特性を有するため、単一のバーナまたは複数の
バーナの場合でも単一とみなせるバーナ糸においては広
く応用されている方法である。
On the other hand, the amount of air in the burner can be adjusted by controlling the rotation speed of the blower and changing the discharge pressure, without relying on the pressure loss effect of the damper.This method reduces the mechanical efficiency of the blower and reduces the drive power. Proportional to approximately the third power of the number,
This is a widely applied method for burner threads that have a decreasing characteristic and can therefore be considered single in the case of a single burner or even in the case of multiple burners.

また各バーナの相互干渉の防止については、送風量の吸
込口にタンパーを設置し、各バーナの空気ダクト分岐点
の風圧を検出し、分岐点の風圧を一定に保つよう吸込ダ
ンパーの開度を自動調節し、空気ダクトの圧力損失変動
を自動的に補償する方法がとられている。
In addition, to prevent mutual interference between burners, a tamper is installed at the air intake inlet to detect the wind pressure at the air duct branch point of each burner, and the opening of the suction damper is adjusted to keep the wind pressure at the branch point constant. A method has been adopted that automatically adjusts and automatically compensates for pressure drop fluctuations in the air duct.

しかしながら、単一とみなせない複数のバーナを有し、
かつそれらが相互干渉することなく任意に火力を調節す
る必要のある炉においては、送風機の回転数制御による
高効率運転を兼ねそなえる燃焼用空気の供給方法は実現
されていなかった。
However, it has multiple burners that cannot be considered as a single burner,
In addition, in a furnace where it is necessary to arbitrarily adjust the thermal power without mutual interference between the two, a method for supplying combustion air that can achieve high efficiency operation by controlling the rotation speed of the blower has not been realized.

第1図は上記した従来の燃焼空気の供給方法を示すフロ
ーシートであって、1はモータ2によって駆動する送風
機、3は吸込ダンパー、4は熱交換器、5はバーナであ
ってこれらバーナには夫々入口ダンパー6の駆動装置7
を火力設定器8により手動または自動的に操作してダン
パー6の開度を変化させて任意に調節した風量が送られ
るようになっている。9は定燃比制御装置であり、10
が溶解炉である。
FIG. 1 is a flow sheet showing the conventional combustion air supply method described above, in which 1 is a blower driven by a motor 2, 3 is a suction damper, 4 is a heat exchanger, and 5 is a burner. are the drive device 7 of the inlet damper 6, respectively.
is operated manually or automatically using a thermal power setting device 8 to change the opening degree of the damper 6 to send an arbitrarily adjusted air volume. 9 is a constant fuel ratio control device; 10
is the melting furnace.

この発明は上記した従来の燃焼空気供給方法の欠点に鑑
みて検討の結果、見出されたものであって、その目的は
送風機の回転数制御とバーナ入口ダンパーの開度制御を
併用し、かつ各バーナ毎に風圧または風量制御ループを
設け、さらには各バーナの風圧または風量設定信号によ
り送風機から各バーナ間の圧力損失を自動制御し、送風
機への回転数指令を得る装置を具備することにより、バ
ーナ間の相互干渉を防止し、任意に火力が調節でき、か
つ高効率な燃焼用空気の供給方法を提供しようとするも
のである。
This invention was discovered as a result of studies in view of the drawbacks of the conventional combustion air supply method described above, and its purpose is to combine the rotational speed control of the blower and the opening degree control of the burner inlet damper. By providing a wind pressure or air volume control loop for each burner, and furthermore, by providing a device that automatically controls pressure loss from the blower to each burner based on the wind pressure or air volume setting signal of each burner, and obtains a rotation speed command to the blower. The present invention aims to provide a method for supplying combustion air that prevents mutual interference between burners, allows arbitrary adjustment of thermal power, and is highly efficient.

以下この発明の燃焼空気供給方法を示す第2図のフロー
シートを参照しつつ説明する。
The combustion air supply method of the present invention will be explained below with reference to the flow sheet of FIG. 2.

なお、この発明においてバーナ火力(熱量)を調節する
手段としては、風量制御、風圧制御いずれも使用される
が、風量∝■なる関係より、本質的には同一と考えられ
るので風圧制御を例にとり以下説明する。
In addition, in this invention, both air volume control and wind pressure control are used as a means to adjust the burner thermal power (heat amount), but based on the relationship of air volume ∝■, they are considered to be essentially the same, so we will take wind pressure control as an example. This will be explained below.

(1)まず単一のバーナ18毎(または同一特性を有す
る等の理由により単一とみなせる複数のバーナ群毎)に
ダンパー装置15、ダンパー開閉装置16、風圧または
風量検出器17、個別風圧または風量調節器19で構成
される風圧制御ループを夫々設置する。
(1) First, for each burner 18 (or for each group of burners that can be considered as a single burner due to having the same characteristics, etc.), the damper device 15, damper opening/closing device 16, wind pressure or air volume detector 17, individual wind pressure or A wind pressure control loop consisting of an air volume regulator 19 is installed respectively.

(2)上記各バーナ風圧制御ループに対してバーナ火力
設定器14により風圧設定指令を供給し、各バーナ毎風
圧制御を行なわせる。
(2) A wind pressure setting command is supplied to each burner wind pressure control loop by the burner thermal power setting device 14, and wind pressure control is performed for each burner.

(3)送風機11には送風機可変速駆動および制御装置
12を連設し、最大値選択および圧力損失補償演算器1
3よりの回転数指令により正確に送風機11の回転数を
制御し、所定の風圧を得る。
(3) A blower variable speed drive and control device 12 is connected to the blower 11, and a maximum value selection and pressure loss compensation calculator 1
The rotation speed of the blower 11 is accurately controlled by the rotation speed command from No. 3 to obtain a predetermined wind pressure.

(4)前記最大値選択および圧力損失補償演算器13に
バーナ火力設定器14からの各バーナ18毎の風圧設定
値を入力し、次にのべる原理によりダンパー装置15入
口の風圧が、風圧または風量検出器17で必要とされる
風圧値よりもダンパー装置15と17の風圧または風量
検出器間の圧力損失分だけ僅かに高くなるように必要な
送風機11の回転数を求め、13の演算器へ回転数指令
として出力する。
(4) Input the wind pressure set value for each burner 18 from the burner thermal power setting device 14 into the maximum value selection and pressure loss compensation calculator 13, and according to the principle described next, the wind pressure at the inlet of the damper device 15 is determined as the wind pressure or air volume. The number of revolutions of the blower 11 required to be slightly higher than the wind pressure value required by the detector 17 by the amount of pressure loss between the damper devices 15 and 17 or the air volume detector is determined and sent to the computing unit 13. Output as rotation speed command.

つまり、送風機11の回転数Nと必要吐出圧力HとはN
=K1■(但し、K1は比例定数)またH=MaxSP
+Σ△P 但し、MaxSPは各バーナ設定風圧の最大値Σ△Pは
空気ダクトの全圧力損失 を供給する必要があり、さらに全圧力損失Σ△PはΣ△
P=K2(ΣQ)2 =K2(QA+QB+QC)2 =K2(KA■+KB■+KC■) 但し、K2・・・空気ダクトの形状により定まる比例定
数 ΣQ・・・空気ダクトの全風量 QA,QB,QC・・・各バーナの風量SPA,SPB
,SPC・・・各バーナの設定風圧KA,KB,KC・
・・バーナの形状により定まる比例定数 となる。
In other words, the rotation speed N of the blower 11 and the required discharge pressure H are N
=K1■ (however, K1 is a proportionality constant) and H=MaxSP
+Σ△P However, MaxSP is the maximum value of the wind pressure set for each burner Σ△P must supply the total pressure loss of the air duct, and the total pressure loss Σ△P is Σ△
P=K2(ΣQ)2 =K2(QA+QB+QC)2 =K2(KA■+KB■+KC■) However, K2... proportionality constant determined by the shape of the air duct ΣQ... total air volume of the air duct QA, QB, QC...Air volume of each burner SPA, SPB
, SPC... Setting wind pressure of each burner KA, KB, KC.
...It is a proportionality constant determined by the shape of the burner.

故に送風機回転数Nは N=K1■ により求めることができる。Therefore, the blower rotation speed N is N=K1■ It can be found by

但し、空気ダクトの圧力損失が少ないか、無視できる場
合、または粗に調節を行なう場合、圧カ損失分は一定値
とすることがありうる。
However, if the pressure loss in the air duct is small or negligible, or if it is roughly adjusted, the pressure loss may be kept at a constant value.

以上のように、さきに(1)〜(4)項でのべた制御動
作を行なう装置を具備すれば、炉の平均的な運転におい
て極端に各バーナの設定値が異ならない限り、従来のよ
うに送風機の高い吐出圧力がら設定値までダンパーでし
ばって使用する状態から、送風機は各バーナで要求する
必要最少限の風圧を供給すればよく、また各ダンパーは
最大風圧を設定しているものは、全開となり、その他は
最大値のものから各設定値の差分だけしぼり込む動作に
変更される 従ってこの方式は、各バーナの圧カ制御ループの動作と
も相まって、バーナ間の相互干渉がなく任意に風量を調
節でき、かつ送風機の回転数制御による高効率運転を兼
備したすぐれた燃焼用空気の供給方法とすることができ
るのである。
As described above, if a device that performs the control operations described in items (1) to (4) above is installed, unless the set values of each burner are extremely different during average operation of the furnace, it will be possible to The blower only needs to supply the minimum wind pressure required by each burner, and each damper has a maximum wind pressure set. , fully open, and the others are changed from the maximum value to the operation that is reduced by the difference between each set value. Therefore, this method, coupled with the operation of the pressure control loop of each burner, can be operated arbitrarily without mutual interference between burners. This makes it possible to provide an excellent method of supplying combustion air that allows the air volume to be adjusted and achieves high efficiency operation by controlling the rotational speed of the blower.

なお第2図のフローシートにおいて、20は空燃比制御
装置、21は熱交換器、22は溶解炉であり、SPA,
SPB,SPCは各バーナの設定風圧、ΣQは全風量値
、QA,QB,QCは各バーナの風量値である。
In the flow sheet of FIG. 2, 20 is an air-fuel ratio control device, 21 is a heat exchanger, 22 is a melting furnace, and SPA,
SPB and SPC are the set wind pressures of each burner, ΣQ is the total air volume value, and QA, QB, and QC are the air volume values of each burner.

以上説明したこの発明の燃焼空気の供給方法は、(1)
空気ダクトに流れる全風量を各バーナの風圧または風量
設定信号により、各バーナの特性に合わせて個々に演算
し、求めさらに全風量の値により空気ダクト特性に合わ
せて圧力損失値を求める。
The combustion air supply method of the present invention explained above includes (1)
The total air volume flowing through the air duct is calculated and determined individually according to the characteristics of each burner using the wind pressure or air volume setting signal of each burner, and the pressure loss value is determined based on the value of the total air volume according to the air duct characteristics.

(2)各バーナにダンパー装置と風圧または風量検出器
を設け、バーナ毎に圧力制御ループを構成する。
(2) Each burner is provided with a damper device and a wind pressure or air volume detector, and a pressure control loop is configured for each burner.

(3)(1)項で求めた空気ダクトの圧力損失値と各バ
ーナの風圧設定値、風量設定の場合はバーナ特性に合わ
せて風圧設定値を求め、設定値の最大値と圧力損失値を
加算し、送風機の必要最少限の運転吐出圧を求めるとと
もにバーナの設定風量が変化した場合でも空気ダクトの
圧力損失分を自動補償し、(2)項の圧力制御ループと
合わせて相互干渉を防止する。
(3) The pressure loss value of the air duct obtained in (1) and the wind pressure setting value of each burner. In the case of air volume setting, find the wind pressure setting value according to the burner characteristics, and calculate the maximum setting value and pressure loss value. This function calculates the minimum required operating discharge pressure of the blower, and automatically compensates for the pressure loss in the air duct even if the set air volume of the burner changes, preventing mutual interference in conjunction with the pressure control loop in item (2). do.

などを特徴とするものであり、これによって(1)送風
機の回転数変化により必要最少限の風圧を得る方法であ
るため、同一風量を得る場合、平均的な送風機の駆動動
力を著しく小さくできること。
This method has the following characteristics: (1) Since it is a method of obtaining the minimum necessary wind pressure by changing the rotation speed of the blower, the average driving power of the blower can be significantly reduced when obtaining the same air volume.

(2)空気ダクトの圧力損失変動を自動補償するため、
バーナの風量を変化させてもバーナ相互間の干渉を小さ
くできること。
(2) To automatically compensate for pressure loss fluctuations in air ducts,
To be able to reduce interference between burners even if the air volume of the burners is changed.

(3)各バーナ毎に圧力制御ループを設けているので、
バーナの風量調節における自由度が阻害されない。
(3) Since a pressure control loop is provided for each burner,
The degree of freedom in adjusting the burner air volume is not hindered.

などの効果を委するのである。The effect of such things is entrusted to

かくして実際に鋼の溶解炉において、400KWの駆動
電動機をもつ送風機を12相可変電圧可変周波数制御装
置により駆動し、200時間操業を行なったところ、改
善前の平均電力223KWに対し、この発明の方法では
平均電力51KWと大幅な駆動電力の低減をはかること
ができた。
Thus, in an actual steel melting furnace, a blower with a 400KW drive motor was driven by a 12-phase variable voltage variable frequency control device, and the operation was performed for 200 hours. In this case, we were able to significantly reduce the driving power to an average power of 51KW.

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

第1図は従来の燃焼用空気の供給方法を説明するフロー
シート、第2図はこの発明の燃焼用空気の供給方法を説
明するフローシートである。 11・・・送風機、12・・・送風機可変速駆動および
制御装置、13・・・最大値選択および圧力損失補償演
算器、14・・・バーナ火力設定器、15・・・ダンパ
ー装置、16・・・ダンパー開閉装置17・・・風圧ま
たは風量検出器、18・・・バーナ19・・・個別風圧
または風量調節器、20・・・空燃比制御装置、21・
・・熱交換器特許出願人         狂友電気工
業株式会社代理人    弁理士和1)昭 第1 図 第2図
FIG. 1 is a flow sheet for explaining a conventional combustion air supply method, and FIG. 2 is a flow sheet for explaining a combustion air supply method according to the present invention. DESCRIPTION OF SYMBOLS 11... Blower, 12... Blower variable speed drive and control device, 13... Maximum value selection and pressure loss compensation calculator, 14... Burner thermal power setting device, 15... Damper device, 16. ... Damper opening/closing device 17... Wind pressure or air volume detector, 18... Burner 19... Individual wind pressure or air volume regulator, 20... Air-fuel ratio control device, 21.
... Heat exchanger patent applicant Patent attorney Kazu 1) Showa 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 1台の送風機により共通する空気ダクトを通して多数の
バーナに燃焼用を気を供給する方法において、送風機に
付加した送風機可変速駆動制御装置にて最大値選択およ
び圧力損失補償演算器よりの送風機回転数指令を制御す
るとともに、各バーナに取付けた風量調節装置から予め
設定されている複数個のバーナの風圧または風量信号を
受けて送風機の駆動回転数を制御することを特徴とする
溶解炉の燃焼空気供給方法。
In the method of supplying combustion air to multiple burners through a common air duct by one blower, the maximum value is selected by the blower variable speed drive control device attached to the blower, and the blower rotation speed is determined by the pressure loss compensation calculator. Combustion air for a melting furnace characterized by controlling commands and controlling the driving rotation speed of a blower by receiving preset wind pressure or air volume signals of a plurality of burners from an air volume control device attached to each burner. Supply method.
JP57202401A 1982-11-16 1982-11-16 Combustion air feed method for disolving furnace Pending JPS5993114A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57202401A JPS5993114A (en) 1982-11-16 1982-11-16 Combustion air feed method for disolving furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57202401A JPS5993114A (en) 1982-11-16 1982-11-16 Combustion air feed method for disolving furnace

Publications (1)

Publication Number Publication Date
JPS5993114A true JPS5993114A (en) 1984-05-29

Family

ID=16456885

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57202401A Pending JPS5993114A (en) 1982-11-16 1982-11-16 Combustion air feed method for disolving furnace

Country Status (1)

Country Link
JP (1) JPS5993114A (en)

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