JP3356595B2 - Heating furnace combustion control method - Google Patents
Heating furnace combustion control methodInfo
- Publication number
- JP3356595B2 JP3356595B2 JP20875795A JP20875795A JP3356595B2 JP 3356595 B2 JP3356595 B2 JP 3356595B2 JP 20875795 A JP20875795 A JP 20875795A JP 20875795 A JP20875795 A JP 20875795A JP 3356595 B2 JP3356595 B2 JP 3356595B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- heating
- time
- exhaust gas
- heated
- 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 - Lifetime
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Description
【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。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling combustion in 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 Casting slabs (slabs), billets (strips), blooms, etc. are charged into a heating furnace and heated to a temperature suitable for hot rolling. Is generally composed of a pre-tropical zone, a heated zone and a tropical zone,
The material to be heated such as a slab is heated by sequentially moving the pre-tropical zone, the heating zone and the soaking zone, and in order to improve the heating efficiency, a regenerative burner is used to move the heated material in the heating furnace in the direction in which the material to be heated advances. A burner group is arranged opposite to both sides, one burner group raises the combustion air through the heat storage and supplies it to the burner to burn fuel, and the other burner group stops burning, The combustion exhaust gas in the furnace is exhausted through the heat storage body, and heat energy in the exhaust gas is stored. Japanese Patent Application Laid-Open No. 5-118764 discloses that heating is performed continuously by so-called regenerative alternating combustion in which combustion and heat storage are alternately performed.
It is disclosed in Japanese Patent Application Laid-Open No. H6-194054.
【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 regenerative 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 the combustion efficiency is high and excellent combustion heating is possible. It is. When the material to be heated is uniformly heated in this manner, a large time difference occurs between the leading end and the trailing end of the slab during hot rolling in a long slab or the like. The temperature becomes low and the finished temperature of the rolled material becomes non-uniform, so that a uniform material cannot be obtained, and the shape deteriorates, so that the quality deteriorates and the yield decreases. Therefore, from the temperature of the tip of the material to be heated in the heating furnace,
It is necessary to perform inclined heating for heating the rear end temperature to a high temperature to prevent the temperature of the rear end of the rolled material from lowering due to a 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。[0004] However, in the regenerative alternating combustion as described above, uniform heating is premised, and the burner is structurally configured so that both the amount of combustion and the combustion time are the same. There is a problem that the material to be heated cannot be inclinedly heated by changing the distribution. The method of the present invention has been made to advantageously solve such a problem, and provides a combustion control method for a heating furnace in which a combustion control is performed by asymmetrically setting a combustion heating time in regenerative alternating combustion heating. It is intended for.
【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、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よう
に、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。The method of the present invention is characterized in that one side combustion heating and the other side heat storage are alternately arranged by a group of regenerative burners disposed oppositely on both sides of the heating furnace in the direction of the material to be heated. During the heat storage type alternating combustion heating, the combustion heating time is set asymmetrically, and the exhaust gas of the long-time combustion heating burner group is set.
Increase exhaust gas suction ratio during exhaust to lower preheated air temperature
Combustion during the short-time combustion heating burner group
Increasing the ratio of baked air to increase the amount of heat removed from the heat storage
In addition, there is provided a combustion control method for a heating furnace , wherein alternating combustion heating is performed.
【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。そし
て、この場合、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ように、
交番燃焼加熱する。 DESCRIPTION OF THE PREFERRED EMBODIMENTS 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 on one side is shorter or longer than the combustion heating time on the other side. It is to set the time for alternating combustion heating, but in the pre-tropical zone of the heating furnace, any zone or two or more zones in the heating zone and the solitary zone, for example, the thickness of the material to be heated, size such as length, Determine the asymmetrical combustion heating time according to the material, heating temperature, the time to transport the material to be heated after heating in the heating furnace to the hot rolling mill, the thickness of the plate after finish rolling, etc. It is to be heated. Soshi
In this case, exhaust gas exhaust from the long-time combustion heating burner group
At times, increase the exhaust gas suction ratio to prevent a drop in preheated air temperature.
The burner is stopped and the combustion
As the air ratio is increased to increase the amount of heat removed from the heat storage,
Alternating combustion heating.
【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 regenerative burner 4 provided with a regenerator 3 is provided opposite to both sides in the traveling direction of a material 2 to be heated of a heating furnace 1, and the regenerative burners 4 of a regenerative burner 4 group on one side B1 are provided. The combustion air switching valve A1 is fully opened via a switching controller (not shown), and air is supplied to each regenerator 3 to increase the heat and supplied to each burner. At the same time, fully open the fuel switching valve F1,
The 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 burner group 4 on the other side B2.
The heat energy of the exhaust gas is stored in the heat storage 3 and then exhausted. Thus, one side B1 for a certain time
After the combustion heating by the regenerative burners 4 group, the combustion air switching valve A1 is fully closed, the combustion air switching valve A2 is fully opened, and the fuel is turned on, as shown in FIG. 2 by a command from a switching controller (not shown). Switching valve F1 fully closed, fuel switching valve F2 fully open,
The exhaust gas switching valve E1 is fully closed, the exhaust gas switching valve E2 is fully opened, and the combustion is switched to the combustion of the four burners on the other side B2 of the heating furnace 1. At the same time, the combustion exhaust gas in the heating furnace 1 is switched from the four burners on the one side B1. Is sucked and passed through the heat storage body 3 of each burner 4, and the heat energy of the exhaust gas is stored and exhausted.
【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。At the time of the regenerative alternating combustion as described above, the switching controller sets the combustion time of the first side B1 of the heating furnace 1 to 40 seconds as shown in FIG. 3 and the combustion time of the other side B2 to 30 seconds asymmetrically in advance. In addition, alternating combustion heating is performed according to a command from the switching controller, and inclined heating is performed to heat the rear end portion of the material to be heated 2 from the front end portion to a high temperature.
【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 regenerative alternating combustion, as in the case of uniform heating of a material to be heated by the same combustion time and alternating combustion heating of heat storage, the combustion air ratio m = 1.1 and the exhaust gas suction ratio is set to about 80%. , The one-side B1 burner group 4 has a relatively long combustion time, and as the heat storage time (exhaust gas suction time), the exhaust gas whose combustion time is relatively short is sucked and stored. In combustion, the preheating of the combustion air takes a long time.
Since the amount of heat removed by the combustion air is large, the amount of heat stored in the heat storage body gradually decreases with time, so that the temperature of the preheated air decreases and the thermal efficiency deteriorates. On the other hand, in the group of burners 4 on the other side B2 whose combustion time is relatively short, the amount of heat removed by the combustion air is small with respect to the amount of heat received from the exhaust gas. Then, 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. Sometimes.
【0010】このような難点を解消するため、本発明で
は、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
ようにしている。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 difficulties, the present invention
Reduces the preheat air temperature by increasing the exhaust gas suction ratio when exhaust gas is exhausted from the long-time combustion heating burner group B1, and increases the combustion air ratio during combustion heating of the short-time combustion heating burner group B2. Increase the amount of heat removed from
Like that . For example, when exhaust gas is being exhausted by four groups of the one-side B1 burners whose combustion time is relatively long, the exhaust gas suction ratio is increased from 80% to 110% to increase the heat storage amount and to increase the preheated air temperature. Prevent drop.
The burner 4 on the other side B2 having a relatively short combustion time.
When the group is burning, the combustion air ratio is increased from m = 1.1 to m = 1.25 to increase the amount of heat removed from the heat storage unit 3 and suppress the rise in the exhaust gas temperature on the exit side of the heat storage unit 3. Is preferred. By doing so, the combustion time of the first group of B1 burners 4 and the fourth group of burners 4 of the other side B2 can be set freely according to the size of the material 2 to be heated, while suppressing fluctuations in the amount of heat stored. By appropriately setting and controlling the combustion air ratio and the exhaust gas suction ratio according to time, stable inclined 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 to be uniformly heated, a switching controller (not shown) is provided with one side B1 as shown in FIG.
The combustion time and exhaust gas exhaust time of the burner 4 group on the other side B2 are set to be the same as each other, and the combustion air switching valves A1, A2, the fuel switching valves F1, F2, The exhaust gas switching valves E1 and E2 are operated to perform alternating combustion.
【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。From the viewpoint of combustion stability and thermal efficiency, the combustion air flow rate of the regenerative alternating combustion heating is about 10% excessive (air ratio m = air ratio) over the theoretical air ratio obtained from the fuel composition.
1.1) It is common to supply. On the other hand, the flow rate of the combustion exhaust gas sucked through the burner is set so that about 80% of the exhaust gas amount generated by the combustion reaction is sucked in order not to largely change the heat storage amount of the heat storage body during a long operation. This is a value 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 takes heat from the heat storage body. Therefore, about 20% that is not sucked from the burner
The exhaust gas flows through, for example, a heating furnace, is sucked into a flue from a charging side of a material to be heated, 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。Next, examples of the method of the present invention will be described 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: The material to be heated 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% slab composed of remaining inevitable components and Fe. Note 2: The heating conditions (heating furnace) consist of a pre-tropical zone, a heating zone, and a solitary zone. The combustion time was set as in Example 1, and the fuel was heated and heated by regenerative alternating combustion using the coke oven generated gas as fuel. Note 3: Furnace time is the total time of pre-tropical zone, heating zone, and solitary zone. Note 4: Heating of the front end of the heating material and the rear end of the heating material are the average temperature in the thickness direction of the front and rear ends in the length direction of the heated material immediately after the heat extraction. Note 5: In the embodiment, the exhaust gas suction ratio of the one-side burner group is 1
10%, combustion air ratio m of the other-side burner group m = 1.25. In the comparative example, the exhaust gas suction ratio of the one side and the other side burner groups was 8
The operation was performed at 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 regenerative alternating combustion, and the function of the heating furnace can be greatly improved. In addition, since accurate inclined heating can be performed, a rolled material in hot rolling can be rolled at a uniform temperature, and the material and shape can be made uniform, so that excellent effects such as improvement in quality can be provided. Can be.
【図面の簡単な説明】[Brief description of the 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 main part plan view 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 plan view of a main part 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 flowchart showing an example of inclined heating by regenerative alternating combustion in 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 flowchart showing an example of uniform heating by regenerative alternating combustion.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−200321(JP,A) 特開 平5−118764(JP,A) 特開 昭57−35615(JP,A) 特開 平7−158845(JP,A) 特開 昭53−43609(JP,A) 実開 平4−13655(JP,U) 特公 昭60−49695(JP,B2) (58)調査した分野(Int.Cl.7,DB名) C21D 1/52 C21D 9/00 101 F23L 15/02 F27D 17/00 101 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-6-200321 (JP, A) JP-A-5-118764 (JP, A) JP-A-57-35615 (JP, A) JP-A-7-35 158845 (JP, A) JP-A-53-43609 (JP, A) JP-A-4-13655 (JP, U) JP-B-60-49695 (JP, B2) (58) Fields investigated (Int. 7 , DB name) C21D 1/52 C21D 9/00 101 F23L 15/02 F27D 17/00 101
Claims (1)
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、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
ように、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. A regenerative burner group disposed on both sides of a heating furnace in a direction in which a material to be heated advances in an asymmetrical manner in a regenerative type alternating combustion heating in which one-side combustion heating and the other-side heat storage are alternately performed. Set to discharge the long-time combustion heating burner group.
When exhausting gas, increase the exhaust gas suction ratio to reduce the preheated air temperature.
Prevention of drop and short-time combustion heating burner group during combustion heating
Increase the amount of heat removed from the heat storage by increasing the combustion air ratio
As described above, a method for controlling combustion in a heating furnace , wherein alternating combustion heating is performed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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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 JPH0953114A (en) | 1997-02-25 |
JP3356595B2 true JP3356595B2 (en) | 2002-12-16 |
Family
ID=16561585
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JP20875795A Expired - Lifetime JP3356595B2 (en) | 1995-08-16 | 1995-08-16 | Heating furnace combustion control method |
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JP (1) | JP3356595B2 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2777095B2 (en) * | 1995-10-16 | 1998-07-16 | 中外炉工業株式会社 | Combustion system of regenerative burner in continuous heating furnace |
JP3959773B2 (en) * | 1997-02-28 | 2007-08-15 | Jfeスチール株式会社 | Thermal storage type atmospheric gas heating method and thermal storage type atmospheric gas heating device |
JPH1194239A (en) * | 1997-09-26 | 1999-04-09 | Nippon Furnace Kogyo Kaisha Ltd | Alternate changing-over heat storage regenerative burner system and method of controlling its combustion |
JP4910450B2 (en) * | 2006-03-29 | 2012-04-04 | 株式会社Ihi | Heating furnace atmosphere control method |
JP2009276026A (en) * | 2008-05-16 | 2009-11-26 | Sanken Sangyo Co Ltd | Regenerative burner control method and control system |
JP5398685B2 (en) * | 2010-11-18 | 2014-01-29 | 中外炉工業株式会社 | Combustion control method of regenerative burner in heating furnace |
JP6254754B2 (en) * | 2012-01-05 | 2017-12-27 | 新日鐵住金株式会社 | Heating method of heated material |
CN106868287B (en) * | 2016-12-28 | 2018-06-19 | 武汉钢铁有限公司 | The fired heat duty distribution control method of CSP sheet billet roller-bottom types tunnel heating furnace |
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1995
- 1995-08-16 JP JP20875795A patent/JP3356595B2/en not_active Expired - Lifetime
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JPH0953114A (en) | 1997-02-25 |
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