JPS6217479Y2 - - Google Patents

Info

Publication number
JPS6217479Y2
JPS6217479Y2 JP14457381U JP14457381U JPS6217479Y2 JP S6217479 Y2 JPS6217479 Y2 JP S6217479Y2 JP 14457381 U JP14457381 U JP 14457381U JP 14457381 U JP14457381 U JP 14457381U JP S6217479 Y2 JPS6217479 Y2 JP S6217479Y2
Authority
JP
Japan
Prior art keywords
temperature
comparator
furnace
burner
flow rate
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
JP14457381U
Other languages
Japanese (ja)
Other versions
JPS5848772U (en
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 filed Critical
Priority to JP14457381U priority Critical patent/JPS5848772U/en
Publication of JPS5848772U publication Critical patent/JPS5848772U/en
Application granted granted Critical
Publication of JPS6217479Y2 publication Critical patent/JPS6217479Y2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Control Of Heat Treatment Processes (AREA)

Description

【考案の詳細な説明】 本考案は加熱炉の制御装置に関するものであ
る。
[Detailed Description of the Invention] The present invention relates to a control device for a heating furnace.

従来の加熱炉における温度の制御装置として
は、第1図に示す如く、加熱炉a内を移動する金
属材料bを加熱するバーナcの燃焼を、炉内温度
を検出する温度検出器dで検出した温度と、温度
調節計eに設定された温度との差に基づく出力信
号によつて調節弁fを介し燃料流量を調節するこ
とにより制御するようにしている。図中gは流量
計、hは炉尻を示す。
As shown in Fig. 1, a conventional temperature control device for a heating furnace detects the combustion of a burner c that heats a metal material b moving inside a heating furnace a using a temperature detector d that detects the temperature inside the furnace. The fuel flow rate is controlled by adjusting the fuel flow rate via the control valve f based on an output signal based on the difference between the temperature set at the temperature controller e and the temperature set on the temperature controller e. In the figure, g indicates a flowmeter, and h indicates the furnace bottom.

しかし加熱炉a内の温度は、材料b寸法及び材
料bの生産量(材料装入量)の変化により、第2
図に示す曲線i,j,kのように変化するもので
あり、従つて前記従来の如く、例えばバーナcに
近接する位置に設けた温度検出器dの検出温度に
のみ基づいてバーナcの燃焼を制御するようにし
たものにおいては、次に示す如き問題点を有して
いた。
However, due to changes in the dimensions of material b and the production amount (material charging amount) of material b, the temperature inside heating furnace a is
The curves i, j, and k shown in the figure change, and therefore, unlike the conventional method, the combustion of burner c is determined based only on the detected temperature of temperature sensor d installed in the vicinity of burner c, for example. However, in the case where the control is performed, there are the following problems.

(イ) 炉内温度が第2図の曲線iに設定されている
とき、曲線j或いはkの如く温度が変つた場合
には必要以上に炉尻h温度が高くなり、多大な
燃料消費の損失を来していた。
(b) When the furnace temperature is set to curve i in Figure 2, if the temperature changes as shown by curves j or k, the furnace bottom h temperature will become higher than necessary, resulting in a large loss in fuel consumption. was coming.

(ロ) 1つの制御帯の検出にのみ基づいているた
め、炉内温度分布はなりゆきにまかせて変化す
ることになり、特に材料bの低温加熱において
曲線kの如き過熱を生じた場合、材料品質が低
下して使用に耐えぬことも生じていた。
(b) Since it is based on the detection of only one control zone, the temperature distribution in the furnace will change as it happens, and especially if overheating as shown in curve k occurs during low-temperature heating of material b, In some cases, the quality deteriorated and it became unusable.

(ハ) 上記の悪化条件を防止すために、熟練した作
業員がバーナcを手動調整することも多く行わ
れているが、保守に人手を多く必要としてい
た。
(c) In order to prevent the above-mentioned deterioration conditions, skilled workers often manually adjust the burner c, but this requires a lot of manpower for maintenance.

(ニ) 炉尻h付近の温度が高くなり、炉体からの放
熱による熱損失も増大していた。
(d) The temperature near the furnace tail h had increased, and heat loss due to heat radiation from the furnace body had also increased.

本考案は、上記従来装置のもつ問題点を解決す
べくなしたもので、加熱炉におけるバーナの火炎
噴出方向と同一軸上に所要の間隔を有して複数個
の温度検出器を設け、且つ該各温度検出器からの
検出温度を比較する比較器を設け、該比較器から
の最高温度信号により温度調節計及び比率設定器
を介して流量調節計を制御し前記バーナへの燃料
流量の調整を行う回路を設けると共に、前記比較
器からの想定温度との温度差信号により前記比率
設定器において前記温度調節計からの信号を絞る
回路を設けたことを特徴とする加熱炉の制御装
置、に係るものである。
The present invention was made to solve the problems of the conventional device described above, and includes a plurality of temperature detectors arranged at a required interval on the same axis as the flame jet direction of the burner in the heating furnace, and A comparator is provided to compare the detected temperatures from each of the temperature detectors, and a maximum temperature signal from the comparator controls a flow rate controller via a temperature controller and a ratio setting device to adjust the fuel flow rate to the burner. A control device for a heating furnace, characterized in that a circuit is provided for controlling the signal from the temperature controller in the ratio setting device based on a temperature difference signal from the expected temperature from the comparator. This is related.

以下図面について本考案の実施例を説明する。 Embodiments of the present invention will be described below with reference to the drawings.

第3図は本考案の一例を示すもので、加熱炉1
に設けたバーナ2の火炎噴出方向と同一軸上に、
適宜の間隙で複数個の温度検出器3,4,5を設
ける。第3図は3個所に設けた場合であり、例え
ば3は加熱炉1のバーナ2取付部6の内壁から
1m以内程度の位置とし、5はバーナ2の火炎長
さ(約1.5〜8m程度)+1m以内の位置とし、4は
前記3と5の中間部所要位置とする。
Figure 3 shows an example of the present invention.
On the same axis as the flame ejection direction of burner 2 installed in
A plurality of temperature detectors 3, 4, and 5 are provided at appropriate intervals. Fig. 3 shows the case where the burner is installed in three places, for example, 3 is from the inner wall of the burner 2 mounting part 6 of the heating furnace 1.
The position 5 shall be within about 1 m, the position 5 shall be within the length of the flame of burner 2 (approximately 1.5 to 8 m) + 1 m, and 4 shall be the required intermediate position between 3 and 5.

更に、前記温度検出器3,4,5に接続する比
較器7を設け、該比較器7からの出力信号8,9
に基づいて温度調節計10及び比率設定器11を
介し、流量制御弁12の調整を行う流量調節計1
3の制御を行うよう構成する。図中14は炉尻、
15は金属材料を示す。
Further, a comparator 7 connected to the temperature detectors 3, 4, 5 is provided, and output signals 8, 9 from the comparator 7 are provided.
A flow rate controller 1 adjusts a flow rate control valve 12 via a temperature controller 10 and a ratio setting device 11 based on
The system is configured to perform the following control. 14 in the figure is the bottom of the furnace.
15 indicates a metal material.

炉尻14側から加熱炉1内に装入された金属材
料15は、第3図中矢印で示す如く移動されなが
らバーナ2により目的温度に加熱される。このと
き、材料15は炉尻14に近い(装入側)ほど温
度が低いため、炉内温度は一般に第4図の曲線1
6(燃料消費量が最小になるよう設定された温度
曲線)のように想定されている。
The metal material 15 charged into the heating furnace 1 from the furnace tail 14 side is heated to a target temperature by the burner 2 while being moved as shown by the arrow in FIG. At this time, the temperature of the material 15 is lower as it is closer to the bottom of the furnace 14 (on the charging side), so the temperature inside the furnace is generally the same as curve 1 in FIG.
6 (temperature curve set to minimize fuel consumption).

上記炉内温度は温度検出器3,4,5で検出さ
れ比較器7に投入される。投入された信号のうち
温度検出器3又は5からの高い方の温度信号8が
温度調節計10を介して比率設定器11に送ら
れ、更に流量調節計13に送られて流量制御弁1
2の開度制御を行う。
The temperature inside the furnace is detected by temperature detectors 3, 4, and 5 and input to a comparator 7. Among the input signals, the higher temperature signal 8 from the temperature detector 3 or 5 is sent to the ratio setter 11 via the temperature controller 10, and further sent to the flow rate controller 13, which controls the flow rate control valve 1.
2. Opening control is performed.

上記回路では、まだ炉内の温度分布が考慮され
ていないが、本考案は次のようにして炉内の温度
分布を考慮した制御を行うようにしている。
Although the above circuit does not yet take into account the temperature distribution within the furnace, the present invention performs control in consideration of the temperature distribution within the furnace as follows.

即ち、前記比較器7において、前記温度検出器
3,4,5による検出温度を夫々、、とし
た場合、第5図に示す如く温度を基準にして温
度、を想定曲線16と比較し、想定温度差
−=Δt1に対し温度がΔt2だけ高い曲線1
6′の場合には、その温度差信号9を比率設定器
11に送るようにしている。従つて上記温度差信
号9により、比率設定器11が温度調節計10か
らの出力信号を小さくするよう絞り、これにより
流量調節計13へ送られる信号がその分小さく制
御され、流量制御弁12の開度がそれだけ狭めら
れ、バーナ2への燃料流量が減少せしめられる。
That is, in the comparator 7, when the temperatures detected by the temperature detectors 3, 4, and 5 are respectively, the temperature is compared with the assumed curve 16 based on the temperature as shown in FIG. Temperature difference - = Curve 1 where the temperature is higher by Δt 2 than Δt 1
6', the temperature difference signal 9 is sent to the ratio setting device 11. Accordingly, the temperature difference signal 9 causes the ratio setter 11 to throttle down the output signal from the temperature controller 10, thereby controlling the signal sent to the flow rate controller 13 to be correspondingly smaller, thereby reducing the output signal of the flow rate control valve 12. The opening degree is narrowed accordingly, and the fuel flow rate to the burner 2 is reduced.

このとき、流量調節計13の出力信号をIoutと
し、流量制御弁12の入力信号をIinとした場
合、 Iin=Iout×K,0K1 とする。この定数Kは比較器7においてΔt2の量
により決定する。
At this time, when the output signal of the flow rate controller 13 is Iout and the input signal of the flow rate control valve 12 is Iin, Iin=Iout×K, 0K1. This constant K is determined by the amount of Δt 2 in the comparator 7.

このようにすることにより、バーナ2の火炎噴
出方向上方の炉内温度パターンを、想定値に近ず
くように制御することができる。
By doing so, it is possible to control the temperature pattern in the furnace above the flame ejection direction of the burner 2 so that it approaches the expected value.

尚、本考案は上記実施例にのみ限定されるもの
ではなく、温度検出器の数は2個以上であれば
種々変更が可能であること、温度検出器の設置位
置も種々変更できること、その他本考案の要旨を
逸脱しない範囲内において種々変更を加え得るこ
と、等は勿論である。
It should be noted that the present invention is not limited to the above-mentioned embodiments, and that the number of temperature detectors can be changed in various ways as long as it is two or more, the installation position of the temperature detector can be changed in various ways, and other improvements can be made. Of course, various changes may be made without departing from the gist of the invention.

上述した本考案の加熱炉の制御装置によれば、
複数個の温度検出器と、それらの温度比較を行う
比較器を設け、且つ最高温度信号に基づいてバー
ナへの燃料の流量制御を行う回路と、想定温度と
の温度差信号に基づいて上記最高温度信号を絞る
回路を設けたことにより、下記の如き優れた効果
を奏し得る。
According to the heating furnace control device of the present invention described above,
A circuit is provided that includes a plurality of temperature detectors and a comparator that compares the temperatures, and also controls the flow rate of fuel to the burner based on the maximum temperature signal. By providing a circuit that narrows down the temperature signal, the following excellent effects can be achieved.

(i) 金属材料の寸法、特に幅等が変化した場合、
従来の1点検出制御と異なり、炉尻温度の不必
要な過熱を防止でき、燃料消費量の低減が図れ
る。
(i) If the dimensions of the metal material change, especially the width,
Unlike conventional one-point detection control, unnecessary overheating of the bottom temperature of the furnace can be prevented and fuel consumption can be reduced.

(ii) 材料の加熱生産量が大幅に変化した場合、特
に温度検出器3以降の材料が急激に少なくなつ
たような場合にも、前記絞り回路の働きにより
燃料消費量の変動を小さくし、安定した加熱操
業が行い得られる。
(ii) Even if the heating production amount of the material changes significantly, especially if the amount of material after the temperature sensor 3 suddenly decreases, the fluctuation in fuel consumption is reduced by the function of the throttle circuit, Stable heating operation can be achieved.

(iii) 設定炉内温度に対し、過熱を防止でき、低温
材料等の品質、歩留りの向上が図れる。
(iii) Overheating can be prevented with respect to the set furnace temperature, and the quality and yield of low-temperature materials can be improved.

(iv) 自動制御が確保されバーナの人手による調整
を要しない。
(iv) Automatic control is ensured and no manual adjustment of the burner is required.

(v) 炉内温度の変動が小さいため、炉体から熱損
失が少なくなる。
(v) Small fluctuations in furnace temperature reduce heat loss from the furnace body.

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

第1図は従来の加熱炉の制御装置の説明図、第
2図は第1図の炉内温度の説明図、第3図は本考
案の制御装置の一実施例を示す説明図、第4図は
第3図の炉内温度の説明図、第5図は比較器にお
ける温度差検出原理を示す説明図である。 1は加熱炉、2はバーナ、3,4,5は温度検
出器、7は比較器、8は最高温度信号、9は温度
差信号、10は温度調節計、11は比率設定器、
12は流量制御弁、13は流量調節計を示す。
FIG. 1 is an explanatory diagram of a conventional heating furnace control device, FIG. 2 is an explanatory diagram of the furnace temperature in FIG. 1, FIG. 3 is an explanatory diagram showing an embodiment of the control device of the present invention, and FIG. The figure is an explanatory diagram of the furnace temperature in FIG. 3, and FIG. 5 is an explanatory diagram showing the principle of temperature difference detection in a comparator. 1 is a heating furnace, 2 is a burner, 3, 4, 5 is a temperature detector, 7 is a comparator, 8 is a maximum temperature signal, 9 is a temperature difference signal, 10 is a temperature controller, 11 is a ratio setter,
12 is a flow control valve, and 13 is a flow controller.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 加熱炉におけるバーナの火炎噴出方向と同一軸
上に所要の間隔を有して複数個の温度検出器を設
け、且つ該各温度検出器からの検出温度を比較す
る比較器を設け、該比較器からの最高温度信号に
より温度調節計及び比率設定器を介して流量調節
計を制御し前記バーナへの燃料流量の調整を行う
回路を設けると共に、前記比較器からの想定温度
との温度差信号により前記比率設定器において前
記温度調節計からの信号を絞る回路を設けたこと
を特徴とする加熱炉の制御装置。
A plurality of temperature detectors are provided at required intervals on the same axis as the flame jet direction of the burner in the heating furnace, and a comparator is provided to compare the detected temperatures from each of the temperature detectors, and the comparator A circuit is provided which controls a flow rate controller via a temperature controller and a ratio setter to adjust the fuel flow rate to the burner based on the maximum temperature signal from the comparator, and a temperature difference signal from the expected temperature from the comparator. A heating furnace control device, characterized in that the ratio setting device is provided with a circuit that throttles a signal from the temperature controller.
JP14457381U 1981-09-29 1981-09-29 Heating furnace control device Granted JPS5848772U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14457381U JPS5848772U (en) 1981-09-29 1981-09-29 Heating furnace control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14457381U JPS5848772U (en) 1981-09-29 1981-09-29 Heating furnace control device

Publications (2)

Publication Number Publication Date
JPS5848772U JPS5848772U (en) 1983-04-01
JPS6217479Y2 true JPS6217479Y2 (en) 1987-05-06

Family

ID=29937532

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14457381U Granted JPS5848772U (en) 1981-09-29 1981-09-29 Heating furnace control device

Country Status (1)

Country Link
JP (1) JPS5848772U (en)

Also Published As

Publication number Publication date
JPS5848772U (en) 1983-04-01

Similar Documents

Publication Publication Date Title
US4274475A (en) Control apparatus for regulating building perimeter temperature change system
CN109114985A (en) A kind of inspection and control system of online sintering ignition furnace flame combustion even degree
US3947237A (en) Method and apparatus for controlling the air volume in a tunnel kiln according to the batch density
US4577278A (en) Method and system for controlling a selected zone in a fuel fired furnace
GB1420852A (en) Method of regulating and stabilising the temperature of a fluid flowing from the outlet of a conditioning duct
JPS6217479Y2 (en)
EP0091483B1 (en) Automatic adjustment of cooling wind in a forehearth
JPH0626604A (en) Boiler device having water-cooled wall temperature control means
JPH11236824A (en) Fuel gas heating control system for gas turbine
JPS5855615A (en) Control and apparatus for burner
SU723335A1 (en) Method of automatic control of loose material drum-drying process
SU887905A1 (en) Method of automatic control of heat condition in slot-type furnace
SU546379A1 (en) Method for automatic control of thermal processing of refractory materials
SU585832A1 (en) Device for automatic control of tea-curing process
SU691662A1 (en) Method of automatically controlling thermal conditions in a slit furnace
SU726401A1 (en) Method of automatic control of thermal condition in slot-type furnace
JP2600915B2 (en) Water heater
SU1059386A2 (en) Device for automatic control of drying process
SU964404A2 (en) Method of automatic control of raw mixture calcining process
JPH01150741A (en) Control device for feed hot water temperature of hot water feeder
SU885158A1 (en) Method of stabilizing temperature condition of glass smelting furnace
SU411143A1 (en)
JPS5919857Y2 (en) Furnace pressure control device in combustion furnace
SU455920A1 (en) The method of automatic control of the temperature regime of forming glassware
SU826155A2 (en) Apparatus for regulating water temperature in water heating boller output