JPH0159517B2 - - Google Patents
Info
- Publication number
- JPH0159517B2 JPH0159517B2 JP6514483A JP6514483A JPH0159517B2 JP H0159517 B2 JPH0159517 B2 JP H0159517B2 JP 6514483 A JP6514483 A JP 6514483A JP 6514483 A JP6514483 A JP 6514483A JP H0159517 B2 JPH0159517 B2 JP H0159517B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- scrap
- differential pressure
- preheating device
- blower
- 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
Links
- 238000009423 ventilation Methods 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 4
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Furnace Details (AREA)
Description
【発明の詳細な説明】
本発明はアーク炉等の炉の排ガスダクトにバイ
パスダクトを設け該バイパスダクトを流れる排ガ
スによりスクラツプを予熱する装置において該バ
イパスダクトを流れる排ガス量を制御する方法に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the amount of exhaust gas flowing through the bypass duct in an apparatus in which a bypass duct is provided in the exhaust gas duct of a furnace such as an arc furnace, and scrap is preheated by the exhaust gas flowing through the bypass duct.
アーク炉から発生する排ガスの量は溶解期、精
練期等のその炉の操業状況によつて変動する。こ
のため排ガスダクトを通して排出すべき排ガス量
はメインコントローラに予めプログラミングされ
た流量指令信号によつて排気ブロワの回転数を制
御し或いは排ガスダクト中のダンパ開度を制御し
炉内圧力が大きく変動しないように構成してい
る。 The amount of exhaust gas generated from an arc furnace varies depending on the operating conditions of the furnace, such as during the melting period and scouring period. For this reason, the amount of exhaust gas to be discharged through the exhaust gas duct is controlled by controlling the rotation speed of the exhaust blower or the opening degree of the damper in the exhaust gas duct using a flow rate command signal programmed in advance in the main controller, so that the pressure inside the furnace does not fluctuate greatly. It is configured as follows.
ところで上記排ガスは高温であるのでその熱を
アーク炉で溶解させるスクラツプの予熱に利用し
省エネルギー化を図ることが従来から行なわれて
いる。即ち、排ガスダクトにバイパスダクトを接
続し、該バイパスダクトに設けたスクラツプ予熱
装置にアーク炉へ原料として装入せんとするスク
ラツプを投入し該スクラツプ中に高温の排ガスを
貫流させることによつて熱エネルギーを授受させ
スクラツプを予熱することが行なわれている。し
かるにスクラツプ予熱装置に投入されるスクラツ
プの形状或いは積込状況などは投入の度毎に違う
ため排ガスの通気抵抗は大きく変動する。そのた
めに場合によつては所期の予熱効果が達せられな
いばかりか排ガスの排出量が流量指令どおりにな
らないために炉内圧力が大きく変動し事故に継が
る惧れもあつた。 By the way, since the above exhaust gas has a high temperature, it has been conventionally done to save energy by utilizing the heat to preheat the scrap to be melted in an arc furnace. That is, a bypass duct is connected to the exhaust gas duct, and the scrap to be charged as a raw material to the arc furnace is charged into a scrap preheating device installed in the bypass duct, and the high temperature exhaust gas flows through the scrap to generate heat. The process involves preheating the scrap by sending and receiving energy. However, since the shape and loading conditions of the scraps fed into the scrap preheating device vary each time they are fed, the ventilation resistance of the exhaust gas varies greatly. As a result, in some cases, not only the desired preheating effect could not be achieved, but also the amount of exhaust gas discharged could not match the flow rate command, causing large fluctuations in the pressure inside the furnace, which could lead to an accident.
本発明は上記欠点を解消せんとするもので、排
ガスダクトを通して排出すべき排ガス量を炉の操
業状況に則してプログラム制御するものにおい
て、該排ガスダクトにバイパスダクトを設け、該
バイパスダクトにスクラツプ予熱装置と送風機と
を直列に介在させ、該スクラツプ予熱装置の入側
の気圧と出側の気圧との差圧を検出し、その差圧
検出値が所定の差圧設定値になるよう送風機の回
転数を自動制御するに際し、該差圧設定値は、前
記スクラツプ予熱装置に搬入されたスクラツプの
通気抵抗係数と、前記プログラム制御によつて指
令されたバイパスダクトを通して排出されるべき
排ガスの目標流量とを変数として演算により求め
るようにしたスクラツプ予熱装置の風量制御方法
である。 The present invention aims to solve the above-mentioned drawbacks, and is intended to programmatically control the amount of exhaust gas to be discharged through an exhaust gas duct in accordance with the operational status of the furnace. A preheating device and a blower are interposed in series, the pressure difference between the inlet side and the outlet side of the scrap preheating device is detected, and the blower is adjusted so that the detected differential pressure value becomes a predetermined differential pressure setting value. When automatically controlling the rotation speed, the differential pressure setting value is based on the ventilation resistance coefficient of the scrap carried into the scrap preheating device and the target flow rate of exhaust gas to be discharged through the bypass duct as instructed by the program control. This is a method for controlling the air volume of a scrap preheating device, in which the air volume is determined by calculation using as a variable.
以下に本発明の一実施例を図面と共に説明す
る。第1図において、1はアーク炉、2はその排
ガスダクト、3は排気ブロワ、4はダンパ、5は
スクラツプ予熱装置6と送風機7とを直列に継い
でなるバイパスダクト、8,9は該バイパスダク
トの両端部に設けられた開閉弁である。スクラツ
プ予熱装置6の入側と出側にそのダクト中の気圧
を測定し電気信号に変換する圧力伝送器10,1
1を設けると共に該各圧力伝送器からの信号を受
けてその入側と出側との差圧を演算する演算器1
2を設ける。即ちいま入側の気圧をP1、出側の
気圧をP2とすると演算器12はΔP=P1−P
2を算出し制御装置13にその差圧検出値を出力
する。メインコントローラ14にはアーク炉1の
操業状況に従つて排出すべき排ガス量が予めプロ
グラミングされており、その順序に従いダンパ4
の開度を制御する流量指令信号を出す。15は送
風機7の出側に設けられた温度計で排ガス温度を
測定しこれを電気信号に変換して制御装置13に
入力させる。16は送風機7を回転駆動する駆動
用モータ、17は該駆動用モータから送風機7へ
の回転伝動を制御し送風機7の回転数を制御する
コントロールモータである。しかして制御装置1
3は、スクラツプ予熱装置6に予熱用のスクラツ
プを装入して操業中に、演算器12から得られる
差圧検出値ΔPが所定の差圧設定値PSになるよう
にコントロールモータ17に制御信号出力MVを
出して送風機7の回転数をPID制御により自動制
御する。即ち、PID制御は、周知のように、差圧
検出値の比例項と積分項と微分項とを調節要素と
するもので、
MV=KP(e+1/T1∫edt+TD・de/dt) ……(1)
ただしMV;制御信号出力
KP;比例定数
T1;積分定数
TD;微分定数
e;偏差(PS−ΔP)
により制御信号出力MVを演算し制御する。 An embodiment of the present invention will be described below with reference to the drawings. In FIG. 1, 1 is an arc furnace, 2 is its exhaust gas duct, 3 is an exhaust blower, 4 is a damper, 5 is a bypass duct formed by connecting a scrap preheating device 6 and a blower 7 in series, and 8 and 9 are the bypass ducts. This is an on-off valve provided at both ends of the duct. Pressure transmitters 10 and 1 on the inlet and outlet sides of the scrap preheating device 6 measure the atmospheric pressure in the duct and convert it into an electrical signal.
1, and receives signals from each pressure transmitter to calculate the differential pressure between the input side and the output side.
2 will be provided. That is, if the pressure on the inlet side is P1 and the pressure on the outlet side is P2, the calculator 12 calculates ΔP=P1-P.
2 and outputs the detected differential pressure value to the control device 13. The amount of exhaust gas to be discharged is programmed in the main controller 14 in advance according to the operating status of the arc furnace 1, and the damper 4 is programmed in accordance with that order.
Issues a flow rate command signal to control the opening of the valve. Reference numeral 15 measures the exhaust gas temperature with a thermometer provided on the outlet side of the blower 7, converts it into an electrical signal, and inputs it to the control device 13. Reference numeral 16 denotes a drive motor that rotationally drives the blower 7, and 17 denotes a control motor that controls rotational transmission from the drive motor to the blower 7 and controls the rotational speed of the blower 7. However, the control device 1
3 sends a control signal to the control motor 17 so that the differential pressure detection value ΔP obtained from the calculator 12 becomes a predetermined differential pressure setting value PS while the scrap for preheating is loaded into the scrap preheating device 6 and the scrap is in operation. The output MV is output and the rotation speed of the blower 7 is automatically controlled by PID control. That is, as is well known, PID control uses the proportional term, integral term, and differential term of the detected differential pressure value as adjustment elements, and MV=K P (e+1/T 1 ∫edt+T D・de/dt) ...(1) However, the control signal output MV is calculated and controlled using MV; control signal output K P ; proportional constant T 1 ; integral constant T D ; differential constant e; deviation (PS - ΔP).
しかして本発明では、上記差圧設定値PSを、
投入されたスクラツプの通気抵抗係数KDと、前
記メインコントローラ14のプログラム制御によ
つて指令されたバイパスダクト5を通して排出さ
れるべき排ガスの目標流量Qとを変数として次式
により求める。 However, in the present invention, the differential pressure setting value PS is
The ventilation resistance coefficient K D of the input scrap and the target flow rate Q of the exhaust gas to be discharged through the bypass duct 5, which is commanded by the program control of the main controller 14, are used as variables and are determined by the following equation.
PS=273+T/273・Q2/KD 2 ……(2) ただし T;排ガス温度(℃) なお(2)式中通気抵抗係数KDは、 KD=QO/√ΔPO ……(3) で得られる。 PS=273+T/273・Q 2 /K D 2 ...(2) Where T: Exhaust gas temperature (℃) The ventilation resistance coefficient K D in formula (2) is: K D = Q O /√ΔP O ...( 3).
ここで、ΔPOは、スクラツプを予熱装置6に搬
入し予熱を開始する前に送風機7を定速回転させ
そのときの差圧検出値P1−P2を代入する。ま
た、QOは、第2図に示した送風機7の性能曲線
を用いてΔPOから求める。即ち、その一例を説明
すれば、送風機7の定速回転数を750rpmに設定
したときΔPOがいま400mmAqを示したとすると、
第2図に破線で示したようにこの性能曲線から
QO=550m3/minであることが判るので、その値
を(3)式に代入し、
KD=550/√400
を算出する。なおこのKDの算出は予熱装置6に
新らたなスクラツプを搬入する度に行う。 Here, for ΔP O , the differential pressure detected value P1-P2 at that time when the blower 7 is rotated at a constant speed before carrying the scrap into the preheating device 6 and starting preheating is substituted. Further, Q O is determined from ΔP O using the performance curve of the blower 7 shown in FIG. That is, to explain one example, if the constant rotation speed of the blower 7 is set to 750 rpm and ΔP O now shows 400 mmAq,
From this performance curve, as shown by the broken line in Figure 2,
Since it is known that Q O =550m 3 /min, substitute that value into equation (3) to calculate K D =550/√400. Note that this calculation of K D is performed every time new scrap is brought into the preheating device 6.
(2)式の目標流量Qは、メインコントローラ14
のプログラミングによつて指定される。よつて差
圧設定値PSは(2)式を用い演算により求められる。 The target flow rate Q in equation (2) is the main controller 14
specified by the programming of Therefore, the differential pressure setting value PS can be calculated using equation (2).
このように本発明では差圧設定値PSをスクラ
ツプの形状、積載状況等によつて変位する通気抵
抗係数KDと、プログラム制御によつて指令され
る目標流量Qから演算により求め、その求められ
た差圧設定値PSに操業中の差圧検出値ΔPが追値
するようにバイパスダクトの送風機の回転数を自
動制御するものであるので、スクラツプの形状や
積込状況が搬入の度毎に大きく違つていてもバイ
パスダクトを流れる排ガスの流量はメインコント
ローラからのプログラム制御指令に従い確実に所
期の流量に制御することができる。このため、充
分な予熱効果が達せられると共に、炉内圧力を適
正に保ち得る等の有益な効果がある。 In this way, in the present invention, the differential pressure set value PS is calculated from the ventilation resistance coefficient K D , which varies depending on the scrap shape, loading situation, etc., and the target flow rate Q, which is commanded by program control. Since the rotation speed of the bypass duct blower is automatically controlled so that the detected differential pressure value ΔP during operation is added to the differential pressure set value PS, the shape of the scrap and the loading condition are changed each time it is brought in. Even if the flow rate of the exhaust gas flowing through the bypass duct is different, the flow rate of the exhaust gas flowing through the bypass duct can be reliably controlled to the desired flow rate according to the program control command from the main controller. Therefore, a sufficient preheating effect can be achieved, and there are other beneficial effects such as being able to keep the pressure inside the furnace at an appropriate level.
第1図は本発明の一実施例に示した制御系統
図、第2図は送風機の性能曲線を示した線図であ
る。
1…アーク炉、2…排ガスダクト、5…バイパ
スダクト、6…スクラツプ予熱装置、7…送風
機、10,11…圧力伝送器、12…演算器、1
3…制御装置、14…メインコントローラ。
FIG. 1 is a control system diagram according to an embodiment of the present invention, and FIG. 2 is a diagram showing a performance curve of a blower. DESCRIPTION OF SYMBOLS 1... Arc furnace, 2... Exhaust gas duct, 5... Bypass duct, 6... Scrap preheating device, 7... Blower, 10, 11... Pressure transmitter, 12... Arithmetic unit, 1
3...Control device, 14...Main controller.
Claims (1)
炉の操業状況に則してプログラム制御するものに
おいて、該排ガスダクトにバイパスダクトを設
け、該バイパスダクトにスクラツプ予熱装置と送
風機とを直列に介在させ、該スクラツプ予熱装置
の入側の気圧と出側の気圧との差圧を検出し、そ
の差圧検出値が所定の差圧設定値になるよう前記
送風機の回転数を自動制御するに際し、該差圧設
定値は、前記スクラツプ予熱装置に搬入されたス
クラツプの通気抵抗係数と、前起プログラム制御
によつて指令されたバイパスダクトを通して排出
されるべき排ガスの目標流量とを変数として演算
により求めるようにしたことを特徴とするスクラ
ツプ予熱装置の風量制御方法。1. In a device that programmatically controls the amount of exhaust gas to be discharged through an exhaust gas duct according to the operational status of the furnace, a bypass duct is provided in the exhaust gas duct, a scrap preheating device and a blower are interposed in series in the bypass duct, and the When detecting the differential pressure between the inlet side and outlet side of the scrap preheating device, and automatically controlling the rotation speed of the blower so that the detected differential pressure value becomes a predetermined differential pressure setting value, the differential pressure The set value is calculated by using as variables the ventilation resistance coefficient of the scrap carried into the scrap preheating device and the target flow rate of the exhaust gas to be discharged through the bypass duct, which is commanded by the advance program control. An air volume control method for a scrap preheating device, characterized in that:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6514483A JPS59189289A (en) | 1983-04-13 | 1983-04-13 | Method of controlling air flow rate of scrap preheater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6514483A JPS59189289A (en) | 1983-04-13 | 1983-04-13 | Method of controlling air flow rate of scrap preheater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59189289A JPS59189289A (en) | 1984-10-26 |
| JPH0159517B2 true JPH0159517B2 (en) | 1989-12-18 |
Family
ID=13278390
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6514483A Granted JPS59189289A (en) | 1983-04-13 | 1983-04-13 | Method of controlling air flow rate of scrap preheater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59189289A (en) |
-
1983
- 1983-04-13 JP JP6514483A patent/JPS59189289A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59189289A (en) | 1984-10-26 |
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