JPH0227325Y2 - - Google Patents

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Publication number
JPH0227325Y2
JPH0227325Y2 JP1983141273U JP14127383U JPH0227325Y2 JP H0227325 Y2 JPH0227325 Y2 JP H0227325Y2 JP 1983141273 U JP1983141273 U JP 1983141273U JP 14127383 U JP14127383 U JP 14127383U JP H0227325 Y2 JPH0227325 Y2 JP H0227325Y2
Authority
JP
Japan
Prior art keywords
flow rate
exhaust gas
temperature
furnace
value
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
JP1983141273U
Other languages
Japanese (ja)
Other versions
JPS6050337U (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 JP14127383U priority Critical patent/JPS6050337U/en
Publication of JPS6050337U publication Critical patent/JPS6050337U/en
Application granted granted Critical
Publication of JPH0227325Y2 publication Critical patent/JPH0227325Y2/ja
Granted legal-status Critical Current

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  • Control Of Combustion (AREA)
  • Feeding And Controlling Fuel (AREA)
  • Regulation And Control Of Combustion (AREA)

Description

【考案の詳細な説明】 本考案はラジアントチユーブフアーネス(以下
RTFと略す)を用いた燃焼制御装置に関し、更
に詳しくはRTFの最低燃焼時における燃焼制御
方法を改善した燃焼制御装置に関する。
[Detailed explanation of the invention] This invention is based on radiant tube furnaces (hereinafter referred to as
The present invention relates to a combustion control device using RTF (abbreviated as RTF), and more specifically to a combustion control device that improves the combustion control method during the minimum combustion time of RTF.

炉内に製品原料を送り込んで加熱して製品とす
る場合において、製品の種類によつては酸化され
ることを極度に嫌うものがある。この種の製品と
しては例えば長い板状の鉄板が考えられる。この
ような製品を加熱する場合、直接バーナで熱する
ことができないので、炉内にはりめぐらされた
RTFの輻射熱により間接加熱する方法が採られ
る。即ち、チユーブ内でコグ(COG)と空気を
燃焼させその熱でチユーブを熱し熱せられたチユ
ーブより製品に熱を与えている。この種の炉の場
合、炉内温度がある値以上になると燃焼を停止さ
せる以外、冷却する方法がない。しかしながら、
その都度燃焼を中止していたのでは効率がよくな
い。そこでこのような状態のときには、炉温コン
トロールを無視しても燃焼を中止させずに炉温を
下げる必要がある。炉温調節計による炉温制御
は、通常排ガス流量調節弁の弁開度を調節するこ
とにより行われているが、この目的のために炉温
調節計操作出力をある一定リミツト値まで強制的
に絞り込み、最低燃焼をさせながら炉温を下げる
ことが行われる。ここで炉温を下げる具体的シー
ケンスとしては、排ガス流量調節弁が絞られるこ
とにより排ガス流量が下がり、排ガス流量から必
要コグ量を換算しているコグ流量調節計の設定値
も下がり最終的にコグ流量が下がることになる。
When product raw materials are fed into a furnace and heated to produce a product, some types of products are extremely reluctant to be oxidized. An example of this type of product is a long iron plate. When heating such products, it is not possible to heat them directly with a burner, so a
An indirect heating method using RTF radiant heat is used. That is, the COG and air are burned inside the tube, the tube is heated with the heat, and the heated tube gives heat to the product. In the case of this type of furnace, there is no way to cool it other than to stop combustion when the temperature inside the furnace exceeds a certain value. however,
It would not be efficient if combustion was stopped each time. Therefore, in such a situation, it is necessary to lower the furnace temperature without stopping combustion even if the furnace temperature control is ignored. Furnace temperature control using a furnace temperature controller is normally performed by adjusting the valve opening of the exhaust gas flow rate control valve, but for this purpose, the furnace temperature controller operating output is forced to a certain limit value. The furnace temperature is lowered while reducing the amount of fuel and achieving minimum combustion. Here, the specific sequence for lowering the furnace temperature is that the exhaust gas flow rate is reduced by throttling the exhaust gas flow rate control valve, and the set value of the cog flow rate controller, which converts the required cog amount from the exhaust gas flow rate, also decreases, and finally the cog flow rate decreases. The flow rate will decrease.

しかしながら、このような従来の操作出力リミ
ツト値を1点固定する方式では、排ガス温度の変
化に拘らず最低燃焼時における排ガス流量調節弁
の開度は一定になる。従つて、排ガス温度の変化
によつて温度補正されている排ガス流量値は変化
することになる。排ガス流量値が変化すればそれ
を元としているコグ流量調節計の設定値が変化
し、従つてその時の排ガス温度によつてコグ流量
が変化してしまうという不都合が生ずる。
However, in such a conventional system in which the operating output limit value is fixed at one point, the opening degree of the exhaust gas flow rate control valve at the time of minimum combustion remains constant regardless of changes in the exhaust gas temperature. Therefore, the temperature-corrected exhaust gas flow rate value changes due to a change in exhaust gas temperature. If the exhaust gas flow rate value changes, the setting value of the cog flow rate controller based on it changes, and therefore, there is a problem that the cog flow rate changes depending on the exhaust gas temperature at that time.

本考案はこのような点に鑑みてなされたもので
あつて、排ガス温度と排ガス流量調節弁の弁開度
(どの排ガス温度においてもコグ流量調節計設定
値が一定となるような排ガス流量になる弁開度)
との関係を予め記憶した関数発生器を設け、排ガ
ス温度を受ける該関数発生器出力を炉温調節計の
操作出力下限リミツト値とするようにして、排ガ
ス温度の変化に拘らず最低燃焼時には常に一定の
設定値がコグ流量調節計に与えられるようにした
制御性のよい燃焼制御装置を実現したものであ
る。
The present invention was developed in consideration of these points, and it is based on the exhaust gas temperature and the valve opening of the exhaust gas flow rate control valve (the exhaust gas flow rate is such that the cog flow rate controller setting value is constant at any exhaust gas temperature). valve opening)
A function generator is provided in which the relationship between A combustion control device with good controllability is realized in which a constant set value is given to a cog flow rate controller.

以下図面を参照して本考案を詳細に説明する。 The present invention will be described in detail below with reference to the drawings.

図は本考案の一実施例を示す構成図である。図
において、1はその内部で製品を加熱する炉で製
品が流入する入口Aと流出する出口Bを有してい
る。2は該炉の内部にはりめぐらされたRTFで
例えば同一炉中に300本程度設置されている。3
は炉内温度を検出する温度検出器で例えば熱電
対、4は燃料(例えばコグ)流量を調節する調節
弁、5は燃料流量を検出する流量検出器、6は該
流量検出器出力を測定値PVとして受けるコグ流
量調節計で、その操作出力MVは調節弁4に与え
られる。7はRTF出口側の排ガス温度を検出す
る温度検出器、8は排ガス流量を検出する流量検
出器、9は排ガス流量を調節する調節弁、10は
流量検出器8の出力を温度検出器7の出力で補正
し、基準温度における流量を算出する第1の演算
器、11は該第1の演算器出力を受けて酸素補正
演算を行う第2の演算器、12は該第2の演算器
出力を受けて必要なコグ流量目標値を算出する第
3の演算器で該演算器の出力は目標コグ流量値と
してコグ流量調節計6に与えられる。13は排ガ
ス温度を入力して対応した操作出力下限リミツト
値を出力する関数発生器、14は炉内温度検出器
3の出力を測定値PVとする炉内温度調節計であ
る。該炉内温度調節計には関数発生器13から操
作出力下限リミツト値が与えられており、操作出
力MVはあるリミツト値より小さくならないよう
になつている。そしてその操作出力は排ガス流量
調節弁9に与えられ、該調節弁により排ガス流量
を調節することにより炉内温度が調節される。1
5は排ガスを一時的に貯蔵するバツフアタンクで
該タンク内圧は常時に一定負圧に保たれている。
16はダンパ、17は排ガスを強制的に引抜くポ
ンプである。このように構成された装置の動作を
説明すれば、以下のとおりである。
The figure is a configuration diagram showing an embodiment of the present invention. In the figure, 1 is a furnace in which the product is heated, and has an inlet A through which the product flows and an outlet B through which the product flows out. Reference numeral 2 is an RTF installed inside the furnace, and for example, about 300 RTFs are installed in the same furnace. 3
4 is a temperature detector that detects the temperature inside the furnace, such as a thermocouple; 4 is a control valve that adjusts the flow rate of fuel (for example, a cog); 5 is a flow rate detector that detects the fuel flow rate; and 6 is a measured value of the output of the flow rate detector. It is a cog flow rate controller that receives PV, and its operating output MV is given to the control valve 4. 7 is a temperature detector that detects the exhaust gas temperature on the RTF outlet side, 8 is a flow rate detector that detects the exhaust gas flow rate, 9 is a control valve that adjusts the exhaust gas flow rate, and 10 is the output of the flow rate detector 8 that is connected to the temperature detector 7. A first computing unit that corrects the output and calculates the flow rate at a reference temperature; 11 is a second computing unit that receives the output of the first computing unit and performs an oxygen correction calculation; 12 is the output of the second computing unit; A third computing unit calculates a necessary cog flow rate target value based on the received data, and the output of this computing unit is given to the cog flow rate controller 6 as a target cog flow rate value. 13 is a function generator which inputs the exhaust gas temperature and outputs a corresponding lower limit value of the operating output; 14 is an in-furnace temperature controller which uses the output of the in-furnace temperature detector 3 as a measured value PV. A lower limit value of the operating output is given to the furnace temperature controller from the function generator 13, and the operating output MV is set not to become smaller than a certain limit value. The operating output is then given to the exhaust gas flow rate control valve 9, and by adjusting the exhaust gas flow rate with the control valve, the temperature inside the furnace is adjusted. 1
5 is a buffer tank for temporarily storing exhaust gas, and the internal pressure of this tank is always maintained at a constant negative pressure.
16 is a damper, and 17 is a pump for forcibly drawing out exhaust gas. The operation of the device configured as described above will be explained as follows.

排ガスの温度変化は温度検出器7によつて検出
され、関数発生器13に与えられる。該関数発生
器には、前述したようにどの排ガス温度において
もコグ流量調節計6の設定値SVが一定となるよ
うな排ガス流量になる排ガス弁開度が設定されて
いる。従つて、そのときの排ガス温度における操
作出力リミツト値が炉温調節計14に与えられる
ことになり、最低燃焼時には排ガス温度の変化に
拘らず常に一定の設定値がコグ流量調節計6に与
えられるのでコグ流量が変化することはなく、最
低燃焼時のコグ流量最適値を得ることができる。
上述の説明においては燃料としてコグを用いた場
合について説明したが、コグに限る必要はなく他
の例えばBFG(高炉ガス)等を用いてもよい。
A temperature change in the exhaust gas is detected by a temperature detector 7 and provided to a function generator 13 . As described above, the function generator is set with an exhaust gas valve opening degree that provides an exhaust gas flow rate such that the set value SV of the cog flow rate controller 6 is constant at any exhaust gas temperature. Therefore, the operating output limit value at the exhaust gas temperature at that time is given to the furnace temperature controller 14, and a constant set value is always given to the cog flow rate controller 6 at the lowest combustion time regardless of changes in the exhaust gas temperature. Therefore, the cog flow rate does not change, and the optimum value of the cog flow rate at the lowest combustion time can be obtained.
In the above description, a case has been described in which a cog is used as the fuel, but the fuel is not limited to a cog, and other fuels such as BFG (blast furnace gas) may also be used.

以上詳細に説明したように、本考案によれば排
ガス温度と排ガス流量調節弁の弁開度との関係を
予め記憶した関数発生器を設け、該発生器出力を
炉温調節計の操作出力下限リミツト値とするよう
にして排ガス温度の変化に拘らず最低燃焼時には
常に一定の設定値をコグ流量調節計に与えること
により、最低燃焼時においてコグ流量の最適値を
得ることができる。
As explained in detail above, according to the present invention, a function generator is provided that stores the relationship between the exhaust gas temperature and the valve opening of the exhaust gas flow rate control valve in advance, and the output of the generator is set as the lower limit of the operating output of the furnace temperature controller. By setting a limit value and always giving a constant set value to the cog flow rate controller at the time of minimum combustion regardless of changes in exhaust gas temperature, it is possible to obtain the optimum value of the cog flow rate at the time of minimum combustion.

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

図は本考案の一実施例を示す構成図である。 1……炉、2……RTF、3,7……温度検出
器、4,9……調節弁、5,8……流量検出器、
6……コグ流量調節計、10〜12……演算器、
13……関数発生器、14……炉温調節計、15
……バツフアタンク、16……ダンパ、17……
抜取りポンプ。
The figure is a configuration diagram showing an embodiment of the present invention. 1... Furnace, 2... RTF, 3, 7... Temperature detector, 4, 9... Control valve, 5, 8... Flow rate detector,
6... Cog flow rate controller, 10-12... Arithmetic unit,
13...Function generator, 14...Furnace temperature controller, 15
...Batua tank, 16...Damper, 17...
extraction pump.

Claims (1)

【実用新案登録請求の範囲】 炉内温度を測定して、この炉内温度が所定の値
になるようにラジアントチユーブフアーネスの排
ガスの流量を調節する調節弁を制御して、この排
ガス流量値により燃料流量を調整して炉内温度を
制御する燃焼制御装置において、 燃焼ガスの排ガス温度を検出する温度検出器
と、この温度検出器の出力が入力されこの排ガス
温度に対応した操作出力の下限リミツト値を出力
する関数発生器と、この関数発生器の出力及び炉
内温度値が入力され排ガス流量調節弁を制御する
炉温調節計とを有し、 この関数発生器にあらかじめどの排ガス温度に
おいても燃料の流量調節計の設定値を一定にする
排ガス流量になるような排ガス弁の開度を設定
し、最低燃焼時にこの関数発生器の出力を前記炉
温調節計の操作下限リミツト値とするようにし
て、最低燃焼時においては排ガス温度の変化にか
かわらず燃料流量が一定になるようにしたとを特
徴する燃焼制御装置。
[Scope of Claim for Utility Model Registration] The temperature inside the furnace is measured, and the flow rate value of the exhaust gas is determined by controlling a control valve that adjusts the flow rate of the exhaust gas of the radiant tube furnace so that the temperature inside the furnace becomes a predetermined value. In a combustion control device that controls the temperature inside the furnace by adjusting the fuel flow rate, there is a temperature detector that detects the exhaust gas temperature of the combustion gas, and the output of this temperature detector is input to set the lower limit of the operating output corresponding to the exhaust gas temperature. It has a function generator that outputs a limit value, and a furnace temperature controller that receives the output of this function generator and the furnace temperature value and controls the exhaust gas flow rate control valve. Also, the opening degree of the exhaust gas valve is set so that the set value of the fuel flow rate controller becomes constant and the exhaust gas flow rate is maintained, and the output of this function generator at the time of minimum combustion is set as the lower operating limit value of the furnace temperature controller. A combustion control device characterized in that the fuel flow rate is made constant regardless of changes in exhaust gas temperature during the lowest combustion time.
JP14127383U 1983-09-12 1983-09-12 Combustion control device Granted JPS6050337U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14127383U JPS6050337U (en) 1983-09-12 1983-09-12 Combustion control device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14127383U JPS6050337U (en) 1983-09-12 1983-09-12 Combustion control device

Publications (2)

Publication Number Publication Date
JPS6050337U JPS6050337U (en) 1985-04-09
JPH0227325Y2 true JPH0227325Y2 (en) 1990-07-24

Family

ID=30316017

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14127383U Granted JPS6050337U (en) 1983-09-12 1983-09-12 Combustion control device

Country Status (1)

Country Link
JP (1) JPS6050337U (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5855614A (en) * 1981-09-30 1983-04-02 Nippon Steel Corp Air-fuel ratio control method for radiant tube burner unit

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5855614A (en) * 1981-09-30 1983-04-02 Nippon Steel Corp Air-fuel ratio control method for radiant tube burner unit

Also Published As

Publication number Publication date
JPS6050337U (en) 1985-04-09

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