JPH08134534A - Heating furnace - Google Patents

Heating furnace

Info

Publication number
JPH08134534A
JPH08134534A JP26963994A JP26963994A JPH08134534A JP H08134534 A JPH08134534 A JP H08134534A JP 26963994 A JP26963994 A JP 26963994A JP 26963994 A JP26963994 A JP 26963994A JP H08134534 A JPH08134534 A JP H08134534A
Authority
JP
Japan
Prior art keywords
combustion
heated
furnace
heating furnace
reducing
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.)
Pending
Application number
JP26963994A
Other languages
Japanese (ja)
Inventor
Masato Fujioka
政人 藤岡
Masataka Hase
政孝 長谷
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 JP26963994A priority Critical patent/JPH08134534A/en
Publication of JPH08134534A publication Critical patent/JPH08134534A/en
Pending legal-status Critical Current

Links

Landscapes

  • Tunnel Furnaces (AREA)

Abstract

PURPOSE: To reduce the producing quantities of NOX and scale on a material to be heated by arranging plural reducing combustion burners close to the material to be heated in the furnace lengthwise direction of the side walls of the furnace body and distributedly arranging plural combustion-assist as supplying devices. CONSTITUTION: Plural reducing combustion burners 5 are arranged close to the material 4 to be heated. The reducing combustion is executed in the condition of oxygen shortage. Since the reducing combustion burners 5 are arranged close to the material 4 to be heated, the reducing gas layer is formed on the surface of the material 4 to be heated and the high temp. oxidation of the material 4 to be heated is restrained and the production of the scale is reduced. The combustion-assist gas such as fuel, high temp. air, high concn. oxygen, is distributedly supplied from plural combustion-assist gas supplying devices 7 arranged at the upper and the lower walls 3a, 3b of the furnace body. Distributed secondary combustion of the reducing combustion flame 6 is executed. Since the fuel is distributedly burnt in the burners 5 and the zone 1 of the heating furnace, the max. temp. of the flame is restrained and the producing quantity of NOX is reduced.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はスラブ、ビレット、スト
リップ等の被加熱材を、高温燃焼バーナで所定の目標温
度まで加熱する加熱炉、熱処理炉等(以下加熱炉と総称
する)に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating furnace, a heat treatment furnace, etc. (hereinafter collectively referred to as a heating furnace) for heating a material to be heated such as a slab, billet or strip to a predetermined target temperature with a high temperature combustion burner. is there.

【0002】[0002]

【従来の技術】従来、この種の加熱炉では省エネのた
め、煙道に間接式の熱交換器を設置して、燃焼排ガスの
顕熱を予熱空気として回収し、燃料の燃焼に使用する方
法が一般的であったが、この間接熱交換方式では熱交換
器の材質、構造等の面から予熱空気の上限温度が600
℃程度に制限されるため、大幅な燃焼火炎温度のアッ
プ、すなわち、被加熱材への放射伝熱量のアップが望め
ず、従って、被加熱材の急速加熱ができないため、加熱
炉がコンパクト化できないという問題点があった。
2. Description of the Related Art Conventionally, in order to save energy in this type of heating furnace, an indirect heat exchanger is installed in the flue to recover the sensible heat of combustion exhaust gas as preheated air and use it for combustion of fuel. However, in this indirect heat exchange system, the upper limit temperature of the preheated air is 600 because of the material and structure of the heat exchanger.
Since the temperature is limited to about ℃, it is not possible to significantly increase the combustion flame temperature, that is, the amount of radiant heat transfer to the material to be heated, and therefore the material to be heated cannot be rapidly heated, so the heating furnace cannot be made compact. There was a problem.

【0003】これに対して、最近燃料を高温空気もしく
は高濃度酸素の支燃ガスで燃焼して、高温の火炎を発生
させ、この高温の火炎で被加熱材を急速加熱する方法が
実用化もしくは研究されており、例えば前者の高温空気
燃焼による方法では、バーナと蓄熱器を一体とした1対
のリジェネバーナを交互に切り換え燃焼して、1000
℃以上の高温空気を発生させ、この高温空気で燃料を燃
焼して高温の火炎を発生させ、被加熱材の急速加熱を行
うものであり、後者の高濃度酸素燃焼による方法では、
燃料と高濃度の酸素を酸素バーナで燃焼することによ
り、燃焼ガス量を減少して高温の火炎を発生して、被加
熱材の急速加熱を行うものである。
On the other hand, recently, a method has been put into practical use, in which a fuel is burned with high temperature air or a combustion gas of high concentration oxygen to generate a high temperature flame and the material to be heated is rapidly heated with this high temperature flame. For example, in the former method using high-temperature air combustion, a pair of regenerative burners in which a burner and a heat accumulator are alternately switched and burned to generate 1000
It generates high temperature air above ℃, burns fuel with this high temperature air to generate high temperature flame, and rapidly heats the material to be heated.In the latter method by high concentration oxygen combustion,
By burning fuel and high-concentration oxygen with an oxygen burner, the amount of combustion gas is reduced and a high-temperature flame is generated to rapidly heat the material to be heated.

【0004】このように、燃料を高温空気もしくは高濃
度酸素の支燃ガスで燃焼して、高温の火炎を発生させる
方法では、高温の火炎から被加熱材への放射伝熱量が増
加するため、被加熱材が急速加熱されて加熱時間が短縮
されるため、加熱炉がコンパクト化できるという長所を
有している反面、燃料を燃焼反応速度が早い高温空気も
しくは高濃度酸素の支燃ガスで燃焼するため、燃焼火炎
が高温の短炎となり、この結果、燃焼ガス中のNOx
(窒素酸化物)と被加熱材のスケールが大幅に増加する
ことに加えて、バーナ軸長方向の炉温分布が不均一とな
るため、被加熱材が均一加熱できないという問題点があ
った。
As described above, in the method of burning high-temperature air or high-concentration oxygen-supporting gas to generate high-temperature flame, the amount of radiative heat transfer from the high-temperature flame to the material to be heated is increased. Since the material to be heated is rapidly heated and the heating time is shortened, it has the advantage that the heating furnace can be made compact, but on the other hand, the fuel is burned with high-temperature air with a fast reaction rate or combustion gas with a high concentration of oxygen. Therefore, the combustion flame becomes a high temperature short flame, and as a result, NOx in the combustion gas is
In addition to a large increase in the scale of (nitrogen oxide) and the material to be heated, there is a problem that the material to be heated cannot be heated uniformly because the furnace temperature distribution in the burner axis length direction becomes uneven.

【0005】これに対して、例えば図4に示す特開昭5
6−82306号公報に示されているような高温焼成炉
用低NOxバーナがある。この技術の特徴は高温燃焼の
NOxの抑制を目的とし、これを達成するために図4に
示すように、バーナタイル13に1次燃焼室11と2次
燃焼室12を異径段違いに設け、燃焼ノズル8から供給
した燃料を、1次空気ノズル9と2次空気ノズル10か
ら供給した燃焼用空気で2段燃焼を行うものである。す
なわち、1次燃焼室11で未燃分を含有した1次燃焼ガ
スを発生させ、2次燃焼室12でこの1次燃焼ガスと2
次空気で2次燃焼を行い、バーナ内での2段燃焼によっ
て、高温燃焼のNOxの抑制を行うものである。
On the other hand, for example, Japanese Unexamined Patent Application Publication No. Sho 5-5 shown in FIG.
There is a low NOx burner for a high temperature firing furnace such as that shown in 6-82306. The feature of this technique is to suppress NOx of high temperature combustion, and in order to achieve this, as shown in FIG. The fuel supplied from the combustion nozzle 8 is subjected to two-stage combustion with the combustion air supplied from the primary air nozzle 9 and the secondary air nozzle 10. That is, in the primary combustion chamber 11, the primary combustion gas containing unburned components is generated, and in the secondary combustion chamber 12, the primary combustion gas and
Secondary combustion is performed with secondary air, and NOx in high temperature combustion is suppressed by two-stage combustion in the burner.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記構
成のバーナでは、予熱空気温度が従来の600℃以下の
NOx低減には有効であるが、最近実用化もしくは研究
されだした予熱空気温度が燃料の着火温度(例えばコー
クス炉ガスでは約700℃)以上の高温空気バーナや高
濃度酸素バーナでは、燃料と支燃ガスの燃焼反応速度が
極端に早いため、バーナによる2段燃焼では、バーナタ
イル内で燃焼が完了して火炎が高温の短炎となるため、
低NOx性と低スケール性、および、均一加熱性が要求
される加熱炉へは適用できないという問題点があった。
However, the burner having the above-mentioned structure is effective for reducing NOx having a preheated air temperature of 600 ° C. or lower as compared with the conventional burner, but the preheated air temperature which has recently been put to practical use or studied has been used as a fuel. In high-temperature air burners and high-concentration oxygen burners that have an ignition temperature (for example, about 700 ° C for coke oven gas) or higher, the combustion reaction rate of fuel and combustion-supporting gas is extremely fast. Since combustion is completed and the flame becomes a high temperature short flame,
There is a problem that it cannot be applied to a heating furnace that requires low NOx property, low scale property, and uniform heating property.

【0007】本発明は上記問題点を解決すべく創案され
たもので、その目的は燃料を高温空気もしくは高濃度酸
素の支燃ガスで燃焼して、被加熱材の急速加熱を行う加
熱炉において、NOxとスケールの生成を抑制すると同
時に、被加熱材の均一加熱に必要なフラットな炉温分布
の確保を図った加熱炉を提供することにある。
The present invention was devised to solve the above problems, and its purpose is to provide a heating furnace for rapidly heating a material to be heated by burning fuel with high temperature air or a combustion supporting gas of high concentration oxygen. , NOx and scale are suppressed, and at the same time, a heating furnace that secures a flat furnace temperature distribution required for uniform heating of a material to be heated is provided.

【0008】[0008]

【課題を解決するための手段】本発明は上記課題を解決
するために次の構成を要旨とする。すなわち、燃料を高
温空気もしくは高濃度酸素の支燃ガスで燃焼して、被加
熱材の加熱を行う加熱炉において、前記加熱炉の炉体側
壁の炉長方向に、被加熱材に近接して、複数の還元燃焼
バーナを配置すると共に、該還元燃焼バーナの延長線上
の炉体上下部壁、もしくは、該還元燃焼バーナの反被加
熱材側の炉体側壁に、複数の支燃ガス供給装置を分散配
置したことを特徴とする。
The present invention has the following features in order to solve the above problems. That is, in a heating furnace that heats a material to be heated by burning fuel with high temperature air or a combustion gas of high concentration oxygen, in the furnace length direction of the furnace body side wall of the heating furnace, close to the material to be heated. , A plurality of reducing combustion burners are arranged, and a plurality of combustion gas supplying devices are provided on the upper and lower walls of the furnace body on the extension line of the reducing combustion burner or on the side wall of the furnace body on the side of the material to be heated of the reducing combustion burner. Are dispersedly arranged.

【0009】[0009]

【作用】燃料を高温空気もしくは高濃度酸素の支燃ガス
で還元燃焼して、この未燃ガスを含有した還元燃焼火炎
を被加熱材の表面に層状に形成して、被加熱材の高温酸
化すなわちスケール生成を抑制する。なお、高温空気も
しくは高濃度酸素の支燃ガスは燃焼反応速度が早いた
め、通常空気バーナの還元燃焼で問題となるススの発生
がない。
[Function] The fuel is reduced and combusted with hot air or a combustion gas of high concentration oxygen to form a reducing combustion flame containing the unburned gas in layers on the surface of the material to be heated, and the high temperature oxidation of the material to be heated is performed. That is, scale generation is suppressed. Since the combustion reaction rate of the high temperature air or the combustion supporting gas of high concentration oxygen is high, soot which is a problem in the reduction combustion of the air burner is not generated.

【0010】さらに、この還元燃焼火炎中の未燃ガス
を、炉体上下部壁もしくは炉体側壁から供給する高温空
気もしくは高濃度酸素の支燃ガスで加熱炉内で2次燃焼
して、炉内温度分布の均一化を行う。また、燃料を還元
燃焼バーナと加熱炉内で分散燃焼するため、最高火炎温
度が低下してNOxの生成が抑制される。
Further, the unburned gas in the reducing combustion flame is secondarily burned in the heating furnace by the hot air supplied from the upper and lower walls of the furnace body or the side wall of the furnace body, or the combustion gas of high concentration oxygen, to be secondarily burned. Uniform the internal temperature distribution. Further, since the fuel is dispersed and burned in the reducing combustion burner and the heating furnace, the maximum flame temperature is lowered and the generation of NOx is suppressed.

【0011】[0011]

【実施例】図1は本発明の加熱炉の実施例を示すサイド
バーナ式加熱炉の1ゾーンの平面図で、図2は図1の加
熱炉のA−A断面での縦断面図である。図1,2に示す
ごとく加熱炉のゾーン1の外殻を耐火物の炉体側壁2と
炉体上部壁3aおよび炉体下部壁3bで構成し、この炉
体側壁2の加熱炉の炉長方向に、被加熱材に近接して複
数の還元燃焼バーナ5を配置し、この還元燃焼バーナ5
に燃料と燃料の着火温度以上の高温空気もしくは高濃度
酸素の支燃ガスを配管で供給して、酸素不足の状態で燃
料の還元燃焼を行い、この未燃ガス(H2 ,CO等)を
含有した高温の還元燃焼火炎6で被加熱材4を加熱する
が、還元燃焼バーナ5が被加熱材4に近接して配置して
あるため、被加熱材4の表面に還元ガス層が形成され、
この結果、被加熱材4の高温酸化が抑制されてスケール
の生成量が減少する。
1 is a plan view of one zone of a side burner type heating furnace showing an embodiment of a heating furnace of the present invention, and FIG. 2 is a vertical sectional view taken along the line AA of the heating furnace of FIG. . As shown in FIGS. 1 and 2, the outer shell of the zone 1 of the heating furnace is composed of the furnace body side wall 2, the furnace body upper wall 3a and the furnace body lower wall 3b, and the furnace length of the furnace body side wall 2 of the furnace. Direction, a plurality of reduction combustion burners 5 are arranged close to the material to be heated.
The fuel and high-temperature air above the ignition temperature of the fuel or combustion-supporting gas of high-concentration oxygen are supplied through the pipe, and the fuel is reduced and burned in the state of lack of oxygen, and this unburned gas (H 2 , CO, etc.) The material to be heated 4 is heated by the contained high-temperature reducing combustion flame 6, but since the reducing combustion burner 5 is arranged close to the material to be heated 4, a reducing gas layer is formed on the surface of the material to be heated 4. ,
As a result, the high temperature oxidation of the material to be heated 4 is suppressed, and the amount of scale formation is reduced.

【0012】さらに、還元燃焼バーナ5のバーナ軸の延
長線上の炉体上下部壁3a,3bに複数の支燃ガス供給
装置7を配置して、この支燃ガス供給装置7から燃料と
の燃焼反応速度が早い高温空気もしくは高濃度酸素の支
燃ガスを、加熱炉のゾーン1内に多段で分散供給して、
還元燃焼バーナ5からの未燃ガスを含有した還元燃焼火
炎6の分散2次燃焼を行い、加熱炉のゾーン1内に均一
な炉温分布を形成して、被加熱材4の均一加熱を行う。
Further, a plurality of combustion-supporting gas supply devices 7 are arranged on the upper and lower walls 3a, 3b of the furnace body on the extension line of the burner shaft of the reduction combustion burner 5, and combustion from this combustion-supporting gas supply device 7 with fuel is performed. High-temperature air or a high-concentration oxygen-supporting gas, which has a fast reaction rate, is dispersed and supplied in multiple stages into zone 1 of the heating furnace,
Dispersion secondary combustion of the reduction combustion flame 6 containing unburned gas from the reduction combustion burner 5 is performed to form a uniform furnace temperature distribution in the zone 1 of the heating furnace and to uniformly heat the material 4 to be heated. .

【0013】通常、加熱炉は図1に示すようなゾーン1
が加熱炉の炉長方向に複数個連接して構成されており、
被加熱材4は加熱炉の炉長方向の一端側の装入扉から加
熱炉内に装入され、ウォーキングビーム等の搬送装置で
加熱炉のゾーン1内を移動しながら所定温度まで加熱さ
れて、他端側の抽出扉から抽出される。また、燃料を高
温空気もしくは高濃度酸素の支燃ガスで高温燃焼する
が、燃料を還元燃焼バーナ5と加熱炉のゾーン1内で分
散燃焼するため、火炎の最高温度が抑制されてNOxの
生成量が減少する。
Usually, the heating furnace is a zone 1 as shown in FIG.
Are connected in the furnace length direction of the heating furnace,
The material to be heated 4 is charged into the heating furnace through a charging door on one end side in the furnace length direction of the heating furnace, and is heated to a predetermined temperature while moving in the zone 1 of the heating furnace by a conveying device such as a walking beam. , Is extracted from the extraction door on the other end side. Further, the fuel is burned at a high temperature with the hot air or the combustion supporting gas of high concentration oxygen, but the fuel is dispersed and burned in the reducing combustion burner 5 and the zone 1 of the heating furnace, so that the maximum flame temperature is suppressed and NOx is generated. The amount decreases.

【0014】図3は本発明の加熱炉の他の実施例を示す
もので、支燃ガス供給装置7を還元燃焼バーナ5の反被
加熱材4側の炉体側壁2に配置したもので、支燃ガスの
炉幅方向の到達距離との関係で、比較的炉幅の狭い加熱
炉に適しており、図2の炉体上下部壁3a,3bに支燃
ガス供給装置7に設けた場合と同様な効果が得られる。
FIG. 3 shows another embodiment of the heating furnace of the present invention, in which the combustion-supporting gas supply device 7 is arranged on the side wall 2 of the reducing combustion burner 5 opposite to the heated material 4, It is suitable for a heating furnace having a relatively narrow furnace width in relation to the reach distance of the combustion supporting gas in the furnace width direction, and when the combustion supporting gas supply device 7 is provided on the upper and lower walls 3a and 3b of the furnace body in FIG. The same effect as can be obtained.

【0015】なお、本発明は前記実施例にのみ限定され
るものではなく、例えば、(1)支燃ガス供給装置7を
既存の炉内仕切り壁もしくはスキッドパイプ、スキッド
サポートパイプ等に取り付けること。(2)支燃ガスの
加熱炉内への分散供給を加熱炉内に装入したガスノズル
で行うこと。(3)還元燃焼バーナ5をリジェネバーナ
とし、このリジェネバーナの予熱空気の一部を支燃ガス
供給装置7に分配供給すること。等も勿論可能で、本発
明の要旨を逸脱しない限り種々変更を加えることは勿論
可能である。
The present invention is not limited to the above embodiment, and for example, (1) the combustion-supporting gas supply device 7 is attached to an existing in-furnace partition wall, skid pipe, skid support pipe, or the like. (2) Dispersing and supplying the combustion-supporting gas into the heating furnace is performed by gas nozzles charged in the heating furnace. (3) The reducing combustion burner 5 is used as a regenerative burner, and a part of the preheated air of the regenerative burner is distributed and supplied to the combustion supporting gas supply device 7. It goes without saying that various changes can be made without departing from the scope of the present invention.

【0016】[0016]

【発明の効果】本発明の加熱炉によれば、(1)炉体側
壁に被加熱材に近接して還元燃焼バーナを配置してある
ため、被加熱材の表面に還元ガス層が形成され、被加熱
材のスケール生成量が減少する。(2)還元燃焼バーナ
からの未燃ガスを、炉体上下部壁もしくは炉体側壁から
の支燃ガスで分散2次燃焼するため、炉温分布が均一化
されて、被加熱材が均一加熱できる。(3)また、燃料
を還元燃焼バーナと加熱炉内で分散燃焼を行うため、最
高火炎温度が抑制されて、NOxの生成量が減少する。
等の優れた効果を奏し得る。
EFFECTS OF THE INVENTION According to the heating furnace of the present invention, (1) since the reducing combustion burner is arranged on the side wall of the furnace body in the vicinity of the material to be heated, a reducing gas layer is formed on the surface of the material to be heated. , The amount of scale generation of the heated material is reduced. (2) The unburned gas from the reduction combustion burner is dispersed and secondarily burned by the combustion-supporting gas from the upper and lower walls of the furnace body or the side wall of the furnace body, so that the furnace temperature distribution is made uniform and the material to be heated is uniformly heated. it can. (3) Since the fuel is dispersed and burned in the reducing combustion burner and the heating furnace, the maximum flame temperature is suppressed and the amount of NOx produced is reduced.
And so on.

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

【図1】本発明の加熱炉の実施例を示すサイドバーナ式
加熱炉の1ゾーンの平面図。
FIG. 1 is a plan view of one zone of a side burner type heating furnace showing an embodiment of a heating furnace of the present invention.

【図2】本発明の加熱炉の実施例を示す炉幅方向の縦断
面図。
FIG. 2 is a vertical sectional view in a furnace width direction showing an embodiment of a heating furnace of the present invention.

【図3】本発明の加熱炉の他の実施例を示す炉幅方向の
縦断面図。
FIG. 3 is a vertical sectional view in a furnace width direction showing another embodiment of the heating furnace of the present invention.

【図4】従来技術を示す高温焼成炉用低NOxバーナの
縦断面図。
FIG. 4 is a longitudinal sectional view of a low NOx burner for a high temperature firing furnace showing a conventional technique.

【符号の説明】[Explanation of symbols]

1 ゾーン 2 炉体側壁 3a,3b 炉体上部壁、炉体下部壁 4 被加熱材 5 還元燃焼バーナ 6 還元燃焼火炎 7 支燃ガス供給装置 8 燃料ノズル 9 1次燃焼空気ノズル 10 2次燃焼空気ノズル 11 1次燃焼室 12 2次燃焼室 13 バーナタイル 1 zone 2 furnace side wall 3a, 3b furnace upper wall, furnace lower wall 4 heated material 5 reducing combustion burner 6 reducing combustion flame 7 combustion-supporting gas supply device 8 fuel nozzle 9 primary combustion air nozzle 10 secondary combustion air Nozzle 11 Primary combustion chamber 12 Secondary combustion chamber 13 Burner tile

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 燃料を高温空気もしくは高濃度酸素の支
燃ガスで燃焼して、被加熱材の加熱を行う加熱炉におい
て、前記加熱炉の炉体側壁の炉長方向に、被加熱材に近
接して、複数の還元燃焼バーナを配置すると共に、該還
元燃焼バーナの延長線上の炉体上下部壁、もしくは、該
還元燃焼バーナの反被加熱材側の炉体側壁に、複数の支
燃ガス供給装置を分散配置したことを特徴とする加熱
炉。
1. A heating furnace for heating a material to be heated by burning fuel with high temperature air or a combustion-enhancing gas of high-concentration oxygen, the material being heated in a furnace longitudinal direction on a side wall of the heating furnace. A plurality of reduction combustion burners are arranged in close proximity to each other, and a plurality of combustion supporters are provided on the upper and lower walls of the furnace body on the extension line of the reduction combustion burner or on the side wall of the furnace body on the side of the material to be heated of the reduction combustion burner. A heating furnace in which gas supply devices are dispersedly arranged.
JP26963994A 1994-11-02 1994-11-02 Heating furnace Pending JPH08134534A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26963994A JPH08134534A (en) 1994-11-02 1994-11-02 Heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26963994A JPH08134534A (en) 1994-11-02 1994-11-02 Heating furnace

Publications (1)

Publication Number Publication Date
JPH08134534A true JPH08134534A (en) 1996-05-28

Family

ID=17475155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26963994A Pending JPH08134534A (en) 1994-11-02 1994-11-02 Heating furnace

Country Status (1)

Country Link
JP (1) JPH08134534A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007514917A (en) * 2003-12-16 2007-06-07 レール・リキード−ソシエテ・アノニム・ア・ディレクトワール・エ・コンセイユ・ドゥ・スールベイランス・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Staged combustion method using preheated oxidant
KR20230023551A (en) 2021-08-10 2023-02-17 쥬가이로 고교 가부시키가이샤 Method for heat treatment, continuous type heating furnace, and batch type heating furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007514917A (en) * 2003-12-16 2007-06-07 レール・リキード−ソシエテ・アノニム・ア・ディレクトワール・エ・コンセイユ・ドゥ・スールベイランス・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Staged combustion method using preheated oxidant
KR20230023551A (en) 2021-08-10 2023-02-17 쥬가이로 고교 가부시키가이샤 Method for heat treatment, continuous type heating furnace, and batch type heating furnace

Similar Documents

Publication Publication Date Title
JP3296974B2 (en) Direct reduction method and rotary bed furnace
CN115574595A (en) Ammonia combustion reduction low NOx emission continuous heating furnace kiln and control method
JPH08134534A (en) Heating furnace
JP3396922B2 (en) Continuous heating furnace and combustion method thereof
JPH0828830A (en) High temperature air burner
JP3337584B2 (en) Heating furnace combustion method
JP3793276B2 (en) Heat storage switching burner
JP3149666B2 (en) Radiant heating device and combustion method thereof
JP3184774B2 (en) Continuous heating furnace
JPH0987750A (en) Method and device for heating strip
JP3893677B2 (en) Furnace with regenerative burner
JP3237345B2 (en) Heating furnace heating method
JP3107352B2 (en) Hot air burner
JP2598345B2 (en) Heating method of steel strip heating furnace
JPS5914717Y2 (en) Surface ignition device for sintered raw material layer
JP2832670B2 (en) Combustion method in a low nitrogen oxide generating furnace
JP2832288B2 (en) Low nitrogen oxide combustion method
SU1295181A1 (en) Fast heating furnace
JP3017013B2 (en) Radiant heating furnace
JPS625531Y2 (en)
JP2755089B2 (en) Combustion method for continuous heating furnace with regenerative burner
JP2894174B2 (en) Combustion control method for continuous heating furnace
JP3859180B2 (en) Roller hearth kiln
JPS6319313Y2 (en)
JPS6248129B2 (en)

Legal Events

Date Code Title Description
A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20021029