JPH0953114A - Method for controlling combustion in heating furnace - Google Patents

Method for controlling combustion in heating furnace

Info

Publication number
JPH0953114A
JPH0953114A JP7208757A JP20875795A JPH0953114A JP H0953114 A JPH0953114 A JP H0953114A JP 7208757 A JP7208757 A JP 7208757A JP 20875795 A JP20875795 A JP 20875795A JP H0953114 A JPH0953114 A JP H0953114A
Authority
JP
Japan
Prior art keywords
combustion
heating
heat storage
heated
burner
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.)
Granted
Application number
JP7208757A
Other languages
Japanese (ja)
Other versions
JP3356595B2 (en
Inventor
Takeshi Yakubo
剛 矢久保
Kiyoshi Muranaka
清志 村中
Toshihiro Okochi
敏博 大河内
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP20875795A priority Critical patent/JP3356595B2/en
Publication of JPH0953114A publication Critical patent/JPH0953114A/en
Application granted granted Critical
Publication of JP3356595B2 publication Critical patent/JP3356595B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Air Supply (AREA)
  • Control Of Heat Treatment Processes (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

PROBLEM TO BE SOLVED: To freely apply a uniform heating and a gradient heating to a material to be heated by setting asymmetrically a combustion heating time in a heat storage type alternate combustion heating and executing the combustion control of a heating furnace. SOLUTION: Heat storage type burners 4 attaching heat storage bodies 3 faced to both sides in the advancing direction of the material 2 to be heated in the heating furnace 1, are arranged. Fuel is supplied and burnt into the burner 4 group through a change-over controller to each heat storage body 3 in the heat storage type burner 4 group at the one side B1 to heat the material 2 to be heated. After burning and heating with the heat storage type burner 4 group at the one side B1 for a fixed time, the combustion at the one side B1 is changed over to the combustion with the burner 4 group at the other side B2 by a command of a change-over controller. In the heat storage type alternate combustion, the combustion time is asymmetrically preset e.g. such as 40 sec at the one side B1 and 30 sec at the other side B2, and the alternate combustion heating is applied by the command of the change-over controller to execute the gradient heating for heating the rear end part to higher than the front end part of the material 2 to be heated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明方法は、加熱炉の燃焼
制御方法に関するものである。
TECHNICAL FIELD The present invention relates to a combustion control method for a heating furnace.

【0002】[0002]

【従来の技術】鋳造後のスラブ(鋼片)、ビレット(条
鋼)、ブルーム等を加熱炉へ装入し、熱間圧延に好適な
温度に加熱するものであるが、このような加熱炉におい
ては、一般に予熱帯、加熱帯及び均熱帯から構成され、
スラブ等の被加熱材は、順次予熱帯、加熱帯及び均熱帯
を連続的に移動させて加熱するものであり、また加熱効
率を向上させるため、蓄熱式バーナーを加熱炉の被加熱
材進行方向両側に対向してバーナー群を配設し、一側の
バーナー群は蓄熱体を通して燃焼用空気を昇熱してバー
ナーへ供給して燃料を燃焼し、他側のバーナー群は燃焼
を停止して、蓄熱体を通して炉内の燃焼排ガスを排気し
排ガス中の熱エネルギーを蓄熱する。このように燃焼と
蓄熱を交互に行う、いわゆる蓄熱型交番燃焼によって連
続的に加熱することが特開平5−118764号公報、
特開平6−194054号公報に開示されている。
2. Description of the Related Art A slab (steel slab), billet (bar steel), bloom, etc. after casting is charged into a heating furnace and heated to a temperature suitable for hot rolling. Is generally composed of pre-tropics, heating zones and soaking zones,
Materials to be heated such as slabs are heated by sequentially moving the pre-tropical zone, heating zone and soaking zone in order to improve the heating efficiency. The burner groups are arranged facing each other, the one side burner group heats the combustion air through the heat storage body and supplies it to the burner to burn the fuel, and the other side burner group stops the combustion. The combustion exhaust gas in the furnace is exhausted through the heat storage body to store heat energy in the exhaust gas. As described above, continuous heating is performed by so-called heat storage type alternating combustion in which combustion and heat storage are alternately performed.
It is disclosed in Japanese Patent Laid-Open No. 6-194054.

【0003】[0003]

【発明が解決しようとする課題】上記のごとき蓄熱型交
番燃焼においては、被加熱材を均一加熱する、つまり炉
内の温度分布を均一にして、しかも燃焼効率も高く優れ
た燃焼加熱ができるものである。このように被加熱材を
均一加熱すると、長尺スラブ等においては熱間圧延時に
スラブ先端部と後端部とでは、大きな時間差が生じ、従
って熱間圧延時にスラブ先端部は高温、後端部は低温と
なり圧延材の仕上がり温度が不均一になることから均一
な材質が得られず、また形状も悪化させることになり品
質を劣化させるとともに、歩留りも低下させることにな
る。そこで加熱炉における被加熱材の先端部温度より、
後端部温度を高温に加熱する傾斜加熱を施し、圧延時の
時間差による圧延材後端部の温度低下を防止することが
必要になる。
In the heat storage type alternating combustion as described above, the material to be heated is heated uniformly, that is, the temperature distribution in the furnace is made uniform, and excellent combustion heating with high combustion efficiency is possible. Is. When the material to be heated is uniformly heated in this manner, a large time difference occurs between the slab tip and the rear end during hot rolling in a long slab, etc., and therefore the slab tip is hot and the rear end during hot rolling. Is low and the finish temperature of the rolled material is non-uniform, so that a uniform material cannot be obtained, the shape is deteriorated, the quality is deteriorated, and the yield is reduced. Therefore, from the temperature of the tip of the material to be heated in the heating furnace,
It is necessary to perform gradient heating for heating the rear end temperature to a high temperature to prevent the temperature decrease at the rear end of the rolled material due to the time difference during rolling.

【0004】しかして上記のごとき、蓄熱型交番燃焼に
おいては、均一加熱が前提となっており構造上バーナー
は、燃焼量、燃焼時間ともに同一になるように構成され
ており、加熱炉内の温度分布を変化させ被加熱材を傾斜
加熱することはできない等の課題がある。本発明方法
は、このような課題を有利に解決するためなされたもの
であり、蓄熱型交番燃焼加熱において、非対称に燃焼加
熱時間を設定して燃焼制御する加熱炉の燃焼制御方法を
提供することを目的とするものである。
However, in the above-described heat storage type alternating combustion, uniform heating is premised, and the burner is structurally constructed so that the combustion amount and the combustion time are the same, and the temperature in the heating furnace is the same. There is a problem in that the material to be heated cannot be gradient heated by changing the distribution. The method of the present invention has been made in order to advantageously solve such a problem, and provides a combustion control method for a heating furnace in which a combustion heating time is asymmetrically set and combustion is controlled in regenerative alternating combustion heating. The purpose is.

【0005】[0005]

【課題を解決するための手段】本発明方法の特徴とする
ところは、加熱炉の被加熱材進行方向両側に対向配設し
た蓄熱式バーナー群により、一側燃焼加熱、他側蓄熱を
交互に施す蓄熱型交番燃焼加熱に際し、燃焼加熱時間を
非対称に設定して交番燃焼加熱することを特徴とする加
熱炉の燃焼制御方法である。
A feature of the method of the present invention is that the one-side combustion heating and the other-side heat storage are alternately performed by heat storage type burner groups arranged facing each other on both sides of the heating furnace in the traveling direction of the material to be heated. A combustion control method for a heating furnace, characterized in that, when the heat storage type alternating combustion heating is performed, the combustion heating time is set asymmetrically to perform alternating combustion heating.

【0006】[0006]

【発明の実施の形態】本発明方法においては、上記のご
とく燃焼加熱時間を非対称に設定して交番燃焼加熱す
る、つまり一側の燃焼加熱時間を他側の燃焼加熱時間よ
り、短時間または長時間に設定して交番燃焼加熱するも
のであるが、加熱炉の予熱帯、加熱帯及び均熱帯のうち
何れかの帯域または2帯域以上で例えば、被加熱材の厚
み、長さ等のサイズ、材質、加熱温度、加熱炉で加熱後
の被加熱材を熱間圧延機へ搬送する時間、仕上圧延後の
板厚等に応じて非対称に設定する燃焼加熱時間を決定
し、これに基づき交番燃焼加熱するものである。
BEST MODE FOR CARRYING OUT THE INVENTION In the method of the present invention, as described above, the combustion heating time is set asymmetrically to perform alternating combustion heating, that is, the combustion heating time of one side is shorter or longer than the combustion heating time of the other side. Although it is intended to perform alternating combustion heating by setting the time, in any zone of the preheating zone of the heating furnace, the heating zone and the soaking zone or two or more zones, for example, the size of the material to be heated, the length, etc., The combustion heating time, which is set asymmetrically according to the material, the heating temperature, the time to transfer the material to be heated after heating in the heating furnace to the hot rolling mill, the sheet thickness after finish rolling, etc. is determined, and based on this, alternating combustion is performed. It is to heat.

【0007】次に、図面により本発明方法の一例を説明
する。図1において、加熱炉1の被加熱材2の進行方向
両側に対向せしめて蓄熱体3を付設した蓄熱式バーナー
4を配設し、一側B1の蓄熱式バーナー4群の各蓄熱体
3へ切換制御器(図示せず)を介して燃焼用空気切換弁
A1を全開とし、空気を各蓄熱体3へ供給して昇熱し各
バーナーへ供給する。同時に燃料切換弁F1を全開し、
バーナー4群へ燃料を供給して燃焼し被加熱材2を加熱
する。一方排気ガス切換弁E1を全閉とし、排気ガス切
換弁E2を全開して、他側B2の蓄熱式バーナー4群か
ら加熱炉1内の燃焼排気ガスを吸引して、各バーナー4
の蓄熱体3を通過せしめて排気ガスの熱エネルギーを蓄
熱体3へ蓄熱後排気する。このように一定時間一側B1
の蓄熱式バーナー4群で燃焼加熱した後、切換制御器
(図示せず)の指令により図2に示すごとく、それぞれ
燃焼用空気切換弁A1を全閉、燃焼用空気切換弁A2を
全開、燃料切換弁F1を全閉、燃料切換弁F2を全開、
排気ガス切換弁E1を全閉、排気ガス切換弁E2を全開
にして、加熱炉1他側B2のバーナー4群の燃焼に切換
え、同時に一側B1のバーナー4群から加熱炉1内の燃
焼排ガスを吸引して各バーナー4の蓄熱体3を通過せし
め排ガスの熱エネルギーを蓄熱後排気する。
Next, an example of the method of the present invention will be described with reference to the drawings. In FIG. 1, a heat storage type burner 4 having a heat storage body 3 is provided so as to face each other in the traveling direction of the material to be heated 2 of the heating furnace 1, and each heat storage body 3 of the heat storage type burner 4 group on one side B1 is provided. The combustion air switching valve A1 is fully opened via a switching controller (not shown), and air is supplied to each heat storage body 3 to raise its temperature and supplied to each burner. At the same time, fully open the fuel switching valve F1,
Fuel is supplied to the group of burners 4 and burned to heat the material 2 to be heated. On the other hand, the exhaust gas switching valve E1 is fully closed, the exhaust gas switching valve E2 is fully opened, and the combustion exhaust gas in the heating furnace 1 is sucked from the regenerative type burner 4 group on the other side B2, and each burner 4 is operated.
The heat energy of the exhaust gas is passed through the heat storage body 3 of FIG. In this way, one side B1
2 is burned and heated by the heat storage type burner 4 group, the combustion air switching valve A1 is fully closed and the combustion air switching valve A2 is fully opened as shown in FIG. 2 by a command of a switching controller (not shown). Switch valve F1 fully closed, fuel switch valve F2 fully open,
The exhaust gas switching valve E1 is fully closed and the exhaust gas switching valve E2 is fully opened to switch to the combustion of the burner 4 group on the other side B2 of the heating furnace 1. At the same time, the combustion exhaust gas in the heating furnace 1 from the burner 4 group on the one side B1 is switched. Is sucked through and passed through the heat storage body 3 of each burner 4 to store the heat energy of the exhaust gas and then exhaust the heat energy.

【0008】上記のごとき蓄熱型交番燃焼に際し、切換
制御器へ例えば加熱炉1一側B1の燃焼時間を図3よう
に40秒、他側B2の燃焼時間を30秒と非対称に予め
設定しておき、切換制御器の指令によって交番燃焼加熱
を施し、被加熱材2の先端部より後端部を高温に加熱す
る傾斜加熱を行うものである。
In the heat storage type alternating combustion as described above, for example, the combustion time of one side B1 of the heating furnace 1 is set to 40 seconds and the combustion time of the other side B2 is set to 30 seconds asymmetrically in advance in the switching controller. Alternately, alternating combustion heating is performed according to a command from the switching controller, and gradient heating is performed to heat the material 2 to be heated from the front end to the rear end.

【0009】このような蓄熱型交番燃焼においては、同
一燃焼時間、蓄熱の交番燃焼加熱による被加熱材の均一
加熱の場合のごとく、燃焼空気比m=1.1、排ガス吸
引比率を約80%に設定すると、燃焼時間が相対的に長
時間の一側B1バーナー4群は、蓄熱時間(排ガス吸引
時間)としては、燃焼時間が相対的に短時間の排ガスを
吸引して蓄熱するこになり、燃焼時は燃焼用空気の予熱
が長時間となることから排ガスからの受熱量に対して、
燃焼用空気による抜熱量が大きいため経時とともに、蓄
熱体の蓄熱量は漸減することから、予熱空気温度が低下
して熱効率が悪化する。一方、燃焼時間が相対的に短時
間の他側B2のバーナー4群は、排ガスからの受熱量に
対して、燃焼用空気による抜熱量が小さいため経時とと
もに、蓄熱体の蓄熱量は逐次増加し、蓄熱体出側の排ガ
ス温度が高温になり排ガス切換弁E2、排ガス吸引ブロ
ワーが耐熱温度を越える状態に至り、長時間操業におい
ては排ガス切換弁等に作動不良が発生して操業が困難に
なることがある。
In such heat storage type alternating combustion, the combustion air ratio m = 1.1 and the exhaust gas suction ratio are about 80%, as in the case of uniform heating of the material to be heated by the alternating combustion heating of the heat storage for the same combustion time. If set to 1, the one-side B1 burner group 4 having a relatively long combustion time will absorb the exhaust gas having a relatively short combustion time as the heat storage time (exhaust gas suction time) to store heat. During combustion, the preheating of the combustion air takes a long time, so the amount of heat received from the exhaust gas
Since the amount of heat removed by the combustion air is large, the amount of heat stored in the heat storage body gradually decreases over time, so the temperature of the preheated air decreases and the thermal efficiency deteriorates. On the other hand, in the burner group 4 on the other side B2, where the combustion time is relatively short, the amount of heat removed by the combustion air is small compared to the amount of heat received from the exhaust gas, so the heat storage amount of the heat storage body gradually increases over time. , The exhaust gas temperature on the outlet side of the heat storage body becomes high, and the exhaust gas switching valve E2 and the exhaust gas suction blower exceed the heat resistant temperature, and the exhaust gas switching valve etc. malfunctions during long-term operation, making operation difficult. Sometimes.

【0010】このような難点を解消するため、長時間燃
焼加熱バーナー群B1の排ガス排気時に排ガス吸引比率
を増量することにより予熱空気温度の低下を防止し、短
時間燃焼加熱バーナー群B2の燃焼加熱時に燃焼空気比
を増大して蓄熱体からの抜熱量を増加することができ
る。例えば、燃焼時間が相対的に長時間の一側B1バー
ナー4群で排ガスの排気を行っているときには、排ガス
吸引比率を80%から110%に増量して蓄熱量の増大
をはかり予熱空気温度の低下を防止する。また燃焼時間
が相対的に短時間の他側B2のバーナー4群が燃焼して
いるときには、燃焼空気比m=1.1からm=1.25
に増大して蓄熱体3からの抜熱量の増加をはかり、蓄熱
体3出側排ガス温度の上昇を抑制することが好ましい。
かくすることにより、蓄熱量の変動を抑えつつ一側B1
バーナー4群と他側B2のバーナー4群の燃焼時間を被
加熱材2のサイズ等に応じて、燃焼時間を自在に設定
し、燃焼時間に応じた燃焼空気比と排ガス吸引比率を適
正に設定制御することによって、安定した傾斜加熱を施
すことができる。
In order to solve such a problem, the exhaust gas suction ratio is increased when exhausting the exhaust gas of the long-time combustion heating burner group B1 to prevent the preheated air temperature from decreasing, and the short-time combustion heating burner group B2 is heated by combustion. At times, the combustion air ratio can be increased to increase the amount of heat removed from the heat storage body. For example, when exhaust gas is being exhausted by the one-side B1 burner group 4 having a relatively long combustion time, the exhaust gas suction ratio is increased from 80% to 110% to increase the amount of heat storage and increase the preheat air temperature. Prevent decline. When the burner group 4 on the other side B2 is burning for a relatively short burning time, the combustion air ratio m = 1.1 to m = 1.25.
It is preferable that the amount of heat removed from the heat storage body 3 is increased to increase the temperature of the exhaust gas to suppress the rise in exhaust gas temperature on the outlet side of the heat storage body 3.
By doing so, one side B1 while suppressing the fluctuation of the heat storage amount
The combustion time of the burner 4 group and the burner 4 group of the other side B2 is freely set according to the size of the material 2 to be heated, and the combustion air ratio and the exhaust gas suction ratio are appropriately set according to the combustion time. By controlling, stable gradient heating can be performed.

【0011】また被加熱材2を均一加熱する場合は、切
換制御器(図示せず)に予め図4に示すごとき一側B1
と他側B2のバーナー4群の燃焼時間、排ガス排気時間
をそれぞれ同一に設定しておき、切換制御器の指令によ
って40秒毎に燃焼用空気切換弁A1、A2、燃料切換
弁F1、F2、排気ガス切換弁E1、E2を操作して交
番燃焼を施すものである。
When the material to be heated 2 is heated uniformly, a switching controller (not shown) is provided with one side B1 as shown in FIG. 4 in advance.
The combustion time and the exhaust gas exhaust time of the burner 4 group on the other side B2 are set to be the same, and the combustion air switching valves A1 and A2 and the fuel switching valves F1 and F2 are set every 40 seconds according to a command from the switching controller. Alternating combustion is performed by operating the exhaust gas switching valves E1 and E2.

【0012】このような蓄熱型交番燃焼加熱の燃焼用空
気流量は、燃焼の安定性と熱効率の観点から燃料組成か
ら求まる理論空気比より10%程度過剰に(空気比m=
1.1)供給するのが一般的である。一方バーナーを通
して吸引する燃焼排ガス流量は、長時間操業時で蓄熱体
の蓄熱量を大幅に変化させないために、燃焼反応で生成
した排ガス量の約80%を吸引するように設定する。こ
のことは、蓄熱体に熱を供給する排ガスの熱容量と蓄熱
体から熱を奪う燃焼用空気の熱容量から一義的に決まる
値である。従って、バーナーから吸引されない約20%
の排ガスは、例えば加熱炉内を流れ被加熱材の装入側か
ら煙道へ吸引して炉外へ排気する。
The flow rate of combustion air for such heat storage type alternating combustion heating exceeds the theoretical air ratio obtained from the fuel composition by about 10% from the viewpoint of combustion stability and thermal efficiency (air ratio m =
1.1) Generally supplied. On the other hand, the flow rate of the combustion exhaust gas sucked through the burner is set so as to suck about 80% of the exhaust gas amount generated by the combustion reaction in order to prevent the heat storage amount of the heat storage body from being significantly changed during long-term operation. This is a value that is uniquely determined from the heat capacity of the exhaust gas that supplies heat to the heat storage body and the heat capacity of the combustion air that removes heat from the heat storage body. Therefore, about 20% not sucked from the burner
The exhaust gas flows through the heating furnace, for example, from the charging side of the material to be heated to the flue, and is exhausted outside the furnace.

【0013】[0013]

【実施例】次に、本発明方法の実施例を比較例とともに
挙げる。
EXAMPLES Next, examples of the method of the present invention will be given together with comparative examples.

【表1】 注1:被加熱材は、C:0.003 %、Mn:0.35 %、Si:0.01
%、P:0.08%、S:0.002%、SolAl:0.035 %、Nb:0.02
%、Ti:0.008%残り不回避成分及びFeからなるスラブ。 注2:加熱条件(加熱炉)は、予熱帯、加熱帯及び均熱
帯からなり、各帯とも被加熱材進行方向両側(壁)部に
蓄熱体を付設した蓄熱式バーナーを配設し、表1のごと
く燃焼時間を設定して、蓄熱型交番燃焼によりコークス
炉発生ガスを燃料として燃焼加熱した。 注3:在炉時間は、予熱帯、加熱帯及び均熱帯の合計時
間である。 注4:加熱材先端部及び加熱材後端部の加熱は、加熱抽
出直後の被加熱材長さ方向先端部及び後端部の厚み方向
平均温度。 注5:実施例は、一側バーナー群の排ガス吸引比率を1
10%、他側バーナー群の燃焼空気比m=1.25。比
較例は、一側及び他側バーナー群の排ガス吸引比率を8
0%、燃焼空気比m=1.1に設定して操業した。
[Table 1] Note 1: Heated material is C: 0.003%, Mn: 0.35%, Si: 0.01
%, P: 0.08%, S: 0.002%, SolAl: 0.035%, Nb: 0.02
%, Ti: 0.008% A slab composed of the remaining non-avoiding components and Fe. Note 2: Heating conditions (heating furnace) consist of pre-tropical zone, heating zone and soaking zone, and each zone is equipped with a regenerative burner with a regenerator on both sides (walls) The combustion time was set as 1 and the coke oven generated gas was combusted and heated by the heat storage type alternating combustion. Note 3: In-furnace time is the total time of pre-tropical zone, heating zone and soaking zone. Note 4: Heating of the heating material front end and heating material rear end is the average temperature in the thickness direction of the front end and rear end of the heated material immediately after heat extraction. Note 5: In the example, the exhaust gas suction ratio of the one-side burner group is 1
10%, combustion air ratio m = 1.25 of the other side burner group. In the comparative example, the exhaust gas suction ratio of the one side and the other side burner groups was set to 8
The operation was performed by setting 0% and the combustion air ratio m = 1.1.

【0014】[0014]

【発明の効果】本発明方法によれば、蓄熱型交番燃焼に
よる被加熱材の均一加熱と傾斜加熱を自在に施すことが
でき、加熱炉の機能を大幅に向上することができる。ま
た正確な傾斜加熱ができることから、熱間圧延における
圧延材を均一温度で圧延することができ、材質、形状等
を均一にできるので、品質を向上することができる等の
優れた効果をもたらすことができる。
According to the method of the present invention, the material to be heated can be uniformly heated and inclinedly heated by the heat storage type alternating combustion, and the function of the heating furnace can be greatly improved. Further, since accurate gradient heating can be performed, the rolled material in hot rolling can be rolled at a uniform temperature, and the material, shape, etc. can be made uniform, so that excellent effects such as quality improvement can be provided. You can

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

【図1】本発明方法を実施するための一例を示す要部平
面図である。
FIG. 1 is a plan view of an essential part showing an example for carrying out the method of the present invention.

【図2】本発明方法を実施するための一例を示す要部平
面図である。
FIG. 2 is a main part plan view showing an example for carrying out the method of the present invention.

【図3】本発明方法の蓄熱型交番燃焼による傾斜加熱の
一例を示すフロー図である。
FIG. 3 is a flow chart showing an example of gradient heating by heat storage type alternating combustion of the method of the present invention.

【図4】蓄熱型交番燃焼による均一加熱の一例を示すフ
ロー図である。
FIG. 4 is a flow chart showing an example of uniform heating by heat storage type alternating combustion.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F27D 17/00 F27D 17/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location F27D 17/00 F27D 17/00

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 加熱炉の被加熱材進行方向両側に対向配
設した蓄熱式バーナー群により、一側燃焼加熱、他側蓄
熱を交互に施す蓄熱型交番燃焼加熱に際し、燃焼加熱時
間を非対称に設定して交番燃焼加熱することを特徴とす
る加熱炉の燃焼制御方法。
1. An asymmetric combustion heating time in the regenerative alternating combustion heating in which one side combustion heating and the other side heat storage are alternately performed by heat storage type burner groups arranged oppositely on both sides of the heating furnace in the traveling direction of the material to be heated. A combustion control method for a heating furnace, which comprises setting and performing alternating combustion heating.
【請求項2】 長時間燃焼加熱バーナー群の排ガス排気
時に排ガス吸引比率を増量して予熱空気温度の低下を防
止し、短時間燃焼加熱バーナー群の燃焼加熱時に燃焼空
気比を増大して蓄熱体からの抜熱量を増加することを特
徴とする請求項1に記載の加熱炉の燃焼制御方法。
2. A regenerator that increases the exhaust gas suction ratio to prevent a decrease in preheat air temperature when exhausting exhaust gas from a long-time combustion heating burner group, and increases the combustion air ratio during short-time combustion heating burner group combustion heating. The method for controlling combustion in a heating furnace according to claim 1, wherein the amount of heat removed from the furnace is increased.
JP20875795A 1995-08-16 1995-08-16 Heating furnace combustion control method Expired - Lifetime JP3356595B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20875795A JP3356595B2 (en) 1995-08-16 1995-08-16 Heating furnace combustion control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20875795A JP3356595B2 (en) 1995-08-16 1995-08-16 Heating furnace combustion control method

Publications (2)

Publication Number Publication Date
JPH0953114A true JPH0953114A (en) 1997-02-25
JP3356595B2 JP3356595B2 (en) 2002-12-16

Family

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3356595B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09111334A (en) * 1995-10-16 1997-04-28 Chugai Ro Co Ltd Combustion system for regenerative burner in continuous heating furnace
WO1998038344A1 (en) * 1997-02-28 1998-09-03 Kawasaki Steel Corporation Heating method and heating apparatus
WO1999017060A1 (en) * 1997-09-26 1999-04-08 Nippon Furnace Kogyo Kabushiki Kaisha Inter-switching heat accumulating regenerative burner system
JP2007263476A (en) * 2006-03-29 2007-10-11 Ihi Corp Atmosphere control method for heating furnace
JP2009276026A (en) * 2008-05-16 2009-11-26 Sanken Sangyo Co Ltd Regenerative burner control method and control system
JP2012107827A (en) * 2010-11-18 2012-06-07 Chugai Ro Co Ltd Combustion control method of regenerative burner in heating furnace
JP2013139611A (en) * 2012-01-05 2013-07-18 Nippon Steel & Sumitomo Metal Corp Method for heating material to be heated
CN106868287A (en) * 2016-12-28 2017-06-20 武汉钢铁股份有限公司 The fired heat duty distribution control method of CSP sheet billet roller-bottom types tunnel heating furnace

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09111334A (en) * 1995-10-16 1997-04-28 Chugai Ro Co Ltd Combustion system for regenerative burner in continuous heating furnace
WO1998038344A1 (en) * 1997-02-28 1998-09-03 Kawasaki Steel Corporation Heating method and heating apparatus
WO1999017060A1 (en) * 1997-09-26 1999-04-08 Nippon Furnace Kogyo Kabushiki Kaisha Inter-switching heat accumulating regenerative burner system
JP2007263476A (en) * 2006-03-29 2007-10-11 Ihi Corp Atmosphere control method for heating furnace
JP2009276026A (en) * 2008-05-16 2009-11-26 Sanken Sangyo Co Ltd Regenerative burner control method and control system
JP2012107827A (en) * 2010-11-18 2012-06-07 Chugai Ro Co Ltd Combustion control method of regenerative burner in heating furnace
JP2013139611A (en) * 2012-01-05 2013-07-18 Nippon Steel & Sumitomo Metal Corp Method for heating material to be heated
CN106868287A (en) * 2016-12-28 2017-06-20 武汉钢铁股份有限公司 The fired heat duty distribution control method of CSP sheet billet roller-bottom types tunnel heating furnace

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