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JP2002212630A - Method of measuring atmospheric gas concentration in heating furnace and heating furnace - Google Patents

Method of measuring atmospheric gas concentration in heating furnace and heating furnace

Info

Publication number
JP2002212630A
JP2002212630A JP2001014230A JP2001014230A JP2002212630A JP 2002212630 A JP2002212630 A JP 2002212630A JP 2001014230 A JP2001014230 A JP 2001014230A JP 2001014230 A JP2001014230 A JP 2001014230A JP 2002212630 A JP2002212630 A JP 2002212630A
Authority
JP
Japan
Prior art keywords
exhaust gas
furnace
burner
heating furnace
heating
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
JP2001014230A
Other languages
Japanese (ja)
Inventor
Kenta Karibe
建太 苅部
Kazunari Adachi
一成 安達
Ichiro Sugimoto
一郎 杉本
Akihiro Furukawa
誠博 古川
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.)
JFE Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP2001014230A priority Critical patent/JP2002212630A/en
Priority to KR1020027012192A priority patent/KR100634776B1/en
Priority to US10/220,726 priority patent/US6644962B2/en
Priority to EP06018722A priority patent/EP1757707A3/en
Priority to EP01273342A priority patent/EP1275740B1/en
Priority to CNB018092470A priority patent/CN100338236C/en
Priority to DE60124691T priority patent/DE60124691T2/en
Priority to BR0109303-7A priority patent/BR0109303A/en
Priority to AT01273342T priority patent/ATE346172T1/en
Priority to CA002403221A priority patent/CA2403221C/en
Priority to PCT/JP2001/011508 priority patent/WO2002057501A1/en
Priority to CA002639404A priority patent/CA2639404A1/en
Priority to TW091100620A priority patent/TW524956B/en
Publication of JP2002212630A publication Critical patent/JP2002212630A/en
Pending 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)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Furnace Details (AREA)

Abstract

(57)【要約】 【課題】 加熱炉内雰囲気における成分ガスの濃度測
定を、既存の設備を利用して正確に行うことのできる方
法について提案する。 【解決手段】 加熱源として、蓄熱体が付帯されたバ
ーナの対を向かい合わせに配設した蓄熱式バーナを有す
る、加熱炉において、蓄熱式バーナの各対のバーナを交
互に燃焼させると共に、非燃焼時のバーナから炉内の排
ガスを吸引し、上記蓄熱体に排ガスを導入して排ガス中
の熱を蓄熱体に回収し、この回収した熱を燃焼時のバー
ナの燃焼用空気の加熱に利用して、加熱炉の操業を行う
に当り、上記バーナから吸引した排ガスの一部を分析器
に導いて、排ガス中の成分濃度を測定する。
(57) [Problem] To propose a method for accurately measuring the concentration of a component gas in an atmosphere in a heating furnace by using existing equipment. SOLUTION: In a heating furnace having, as a heating source, a regenerative burner in which a pair of burners provided with a heat storage element are arranged to face each other, the burners of each pair of the regenerative burners are alternately burned. Exhaust gas in the furnace is sucked from the burner during combustion, the exhaust gas is introduced into the regenerator, heat in the exhaust gas is collected in the regenerator, and the recovered heat is used for heating the combustion air of the burner during combustion. Then, when operating the heating furnace, a part of the exhaust gas sucked from the burner is led to an analyzer to measure the component concentration in the exhaust gas.

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】この発明は、加熱炉内の雰囲
気ガス濃度の測定方法および加熱炉に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for measuring an atmospheric gas concentration in a heating furnace and a heating furnace.

【0002】[0002]

【従来の技術】例えば、鋼材の加熱炉は、分塊工場で粗
圧延された鋼片や、連続鋳造された鋳片を最終製品に圧
延するため、その圧延に適した所定の温度に再加熱する
場合に主に用いられている。この加熱炉は、バッチ式と
連続式とに大別されるが、それぞれ長所および短所があ
るため、その目的に応じて選択使用されている。中で
も、連続式加熱炉は、近年の大量生産に適しているとこ
ろから、製鉄所などで多用されている。
2. Description of the Related Art For example, a heating furnace for steel products reheats a steel slab roughly rolled in a lump mill or a continuously cast slab to a final product at a predetermined temperature suitable for the rolling. It is mainly used when The heating furnace is roughly classified into a batch type and a continuous type, but each has an advantage and a disadvantage, and thus is selectively used according to its purpose. Above all, continuous heating furnaces are widely used in steel mills and the like because they are suitable for mass production in recent years.

【0003】この連続式加熱炉は、その典型例を図1に
示すように、鋼材の装入側から順に予熱帯1、加熱帯2
および均熱帯3から成るのが一般的であり、少なくとも
加熱帯2および均熱帯3は、バーナ4によって所定温度
に加熱保持されている。そして、装入扉1aから予熱帯
1に導入された鋼材5は、搬送路6上を移動されて加熱
帯2そして均熱帯3を経て均熱帯3出側の抽出扉3aか
ら炉外へ搬出される間に、所定温度に加熱される。な
お、バーナ4の燃焼によって生じた排ガスは、予熱帯1
の入側に設けられた煙道7から炉外に排出される。ま
た、7aは煙道排ガス顕熱をバーナ燃焼用空気の顕熱に
熱交換するためのレキュペレータおよび7bは炉圧制御
用のダンパーである。
[0003] As shown in Fig. 1, a typical example of this continuous heating furnace is a pre-tropical zone 1 and a heating zone 2 in order from the steel material charging side.
In general, the heating zone 2 and the soaking zone 3 are heated and maintained at a predetermined temperature by the burner 4. Then, the steel material 5 introduced from the charging door 1a into the pre-tropical zone 1 is moved on the transport path 6 and is carried out of the furnace through the heating zone 2 and the leveling zone 3 through the extraction door 3a on the exit side of the leveling zone 3. During this time, it is heated to a predetermined temperature. The exhaust gas generated by the combustion of the burner 4 is in the pre-tropical zone 1
From the flue 7 provided on the inlet side of the furnace. Reference numeral 7a denotes a recuperator for exchanging sensible heat of flue gas into sensible heat of burner combustion air, and 7b denotes a damper for controlling furnace pressure.

【0004】ここに、連続式加熱炉は、その後の圧延工
程に適した温度に鋼材を加熱するものであるため、当然
炉内温度を厳密に制御する必要があるが、この温度の要
件に併せて、加熱中の鋼材の表面を良好な状態に維持す
るために、炉内の雰囲気を厳密に制御することも重要で
ある。例えば、炉内雰囲気における酸素濃度が上昇する
と、炉内に装入した鋼材などの被加熱材の表面酸化、窒
化或いは脱炭等が促進され、そのまま圧延を行うと製品
における表面品質の低下をまねくことになる。従って、
製品品質を向上または維持するには、炉内雰囲気におけ
る酸素濃度の上昇を抑制する必要があり、そのためには
炉内雰囲気における酸素濃度を正確に測定することが重
要になる。
Here, since the continuous heating furnace heats the steel material to a temperature suitable for the subsequent rolling process, it is naturally necessary to strictly control the furnace temperature. It is also important that the atmosphere in the furnace be strictly controlled in order to maintain the surface of the steel material being heated in a good state. For example, when the oxygen concentration in the furnace atmosphere increases, the surface oxidation, nitridation, or decarburization of the material to be heated such as a steel material charged into the furnace is promoted, and if the rolling is performed as it is, the surface quality of the product is deteriorated. Will be. Therefore,
In order to improve or maintain product quality, it is necessary to suppress an increase in the oxygen concentration in the furnace atmosphere. For that purpose, it is important to accurately measure the oxygen concentration in the furnace atmosphere.

【0005】また、酸素濃度の他にも、炉内雰囲気にお
ける窒素、一酸化炭素や窒素酸化物などについても、同
様に濃度を正確に測定することが有意義である。すなわ
ち、窒素は鋼材表面の窒化に影響を与え、一酸化炭素は
バーナの不完全燃焼の検知に利用可能であり、さらに窒
素酸化物は環境排出基準値の管理に必要である。
[0005] In addition to the oxygen concentration, it is significant to accurately measure the concentration of nitrogen, carbon monoxide, nitrogen oxide, and the like in the furnace atmosphere. That is, nitrogen affects the nitridation of the steel surface, carbon monoxide can be used to detect incomplete combustion of the burner, and nitrogen oxides are necessary for controlling environmental emission standards.

【0006】ここで、特開昭62−40312 号公報には、加
熱炉内の酸素濃度およびCO濃度を測定するための各プ
ローブを移動自在として、複数の測定位置にて濃度測定
を行い、平均濃度値を求めることによって、バーナの空
気比を修正制御することが開示されている。
Japanese Patent Application Laid-Open No. 62-40312 discloses that each probe for measuring the oxygen concentration and the CO concentration in a heating furnace is freely movable, and the concentration is measured at a plurality of measurement positions. It is disclosed to correct and control the air ratio of the burner by determining the concentration value.

【0007】しかしながら、濃度を測定するために、駆
動系や制御系を新たに設ける必要があるため、初期投資
に要する費用が嵩むとともに、そのメンテナンスが煩雑
である等の問題があり、しかもダクトや付設機器類が複
雑に入り組む構成の加熱炉では、配置スペースの問題か
ら、駆動系や制御系を新たに設けることが困難な場合が
多かった。
However, in order to measure the concentration, it is necessary to newly provide a drive system and a control system, so that the cost required for the initial investment increases and the maintenance thereof is complicated. In a heating furnace having a configuration in which attached equipment is complicated, it is often difficult to newly provide a drive system and a control system due to a problem of arrangement space.

【0008】また、特開平9−53120 号公報には、加熱
炉抽出側の炉壁内側かつスキッドの下側に、炉幅方向に
仕切壁を設置し、この仕切壁と抽出側炉壁との間に、酸
素濃度計および雰囲気ガスを炉外に排出する排気管を備
えた加熱炉において、上記酸素濃度計を用いて酸素濃度
を測定しつつ、排気管内の流量制御を行うことが開示さ
れている。
In Japanese Patent Application Laid-Open No. 9-53120, a partition wall is provided in the furnace width direction inside the furnace wall on the extraction side of the heating furnace and below the skid, and the partition wall and the extraction-side furnace wall are connected to each other. In the meantime, it is disclosed that in a heating furnace having an oxygen concentration meter and an exhaust pipe for exhausting the atmosphere gas out of the furnace, the flow rate in the exhaust pipe is controlled while measuring the oxygen concentration using the oxygen concentration meter. I have.

【0009】しかし、仕切壁と抽出側炉壁との間の酸素
濃度計で測定を行うためには、炉床または炉壁からプロ
ーブを挿入する必要があり、炉床からプローブを挿入す
ると、スケール等の落下そして堆積によりプローブに破
損や詰まりが発生するため、長期にわたり信頼性のある
濃度測定を行うことが難しい。また、炉壁からプローブ
を挿入すると、炉内の高温域にプローブが晒されて撓む
ために、測定点がずれたり損傷を生じる、おそれがあ
る。
However, in order to perform measurement using an oxygen concentration meter between the partition wall and the extraction furnace wall, it is necessary to insert a probe from the hearth or the furnace wall. The probe may be damaged or clogged due to the drop and accumulation of the like, so that it is difficult to perform a reliable concentration measurement for a long time. Further, when the probe is inserted from the furnace wall, the probe is exposed to a high-temperature region in the furnace and bends, so that a measurement point may be shifted or damaged.

【0010】[0010]

【発明が解決しようとする課題】そこで、この発明は、
加熱炉内雰囲気における成分ガスの濃度測定を、既存の
設備を利用して正確に行うことのできる方法について提
案することを目的とする。また、この発明の別の目的
は、加熱炉内雰囲気における成分ガスの濃度測定が可能
である、加熱炉を提供することにある。
SUMMARY OF THE INVENTION Therefore, the present invention
An object of the present invention is to propose a method capable of accurately measuring the concentration of a component gas in an atmosphere in a heating furnace by using existing equipment. Another object of the present invention is to provide a heating furnace capable of measuring the concentration of a component gas in the atmosphere inside the heating furnace.

【0011】[0011]

【課題を解決するための手段】近年、連続式加熱炉の加
熱源に蓄熱式バーナを用いて、排ガス中の熱をバーナの
燃焼用空気の予熱に再利用する、熱損失の少ない加熱炉
の操業が行われている。すなわち、蓄熱式バーナは、図
2に示すように、例えば加熱炉均熱帯3の両側壁間で向
かい合わせに配置した、一対のバーナ40aおよび40b
と、各バーナ40aおよび40bに炉外から燃焼用空気を導
き、また炉内の排ガスを各バーナを介して炉外に導くた
めの兼用通路41aおよび41bと、図示例では各通路のバ
ーナ側開口に配設した蓄熱体42aおよび42bと、から成
る。この蓄熱式バーナは、そのバーナ対を交互に燃焼さ
せる際、例えば図2(a) に示すように、バーナ40aに兼
用通路41aから燃焼用空気を供給するとともに燃料43a
を供給し、バーナ40aを燃焼させた際には、これと対向
するバーナ40bから炉内の排ガスを吸引し、この排ガス
を蓄熱体42bに通して熱を回収してから、兼用通路41b
に導いて炉外に排出する。
In recent years, a regenerative burner has been used as a heating source of a continuous heating furnace, and heat in exhaust gas is reused for preheating combustion air for the burner. Operations are taking place. That is, as shown in FIG. 2, the regenerative burner is, for example, a pair of burners 40a and 40b disposed face to face between both side walls of the heating furnace soaker 3.
And dual passages 41a and 41b for guiding combustion air from outside the furnace to the respective burners 40a and 40b, and for guiding exhaust gas in the furnace to the outside of the furnace through the respective burners. And the heat storage bodies 42a and 42b disposed in the In this regenerative burner, when the burner pairs are alternately burned, for example, as shown in FIG. 2A, the burner 40a is supplied with combustion air from a shared passage 41a and a fuel 43a.
When the burner 40a is burned, the exhaust gas in the furnace is sucked from the burner 40b opposed to the burner 40a, and the exhaust gas is passed through the regenerator 42b to recover the heat.
And discharge it outside the furnace.

【0012】次いで、バーナの燃焼運転を切り換え、か
つ、その際兼用通路41aおよび41bの切換弁44を切り換
えて、上記した空気および排ガスの導管との接続を変更
したのち、図2(b) に示すように、バーナ40bに兼用通
路41bから蓄熱体42bを介して燃焼用空気を供給するに
当り、先に図2(a) に示した工程にて蓄熱体42bに回収
した熱を利用して燃焼用空気の予熱を図りながら供給
し、併せて燃料43bを供給してバーナ40bを燃焼させ
る。同時に、これと対向するバーナ40aから炉内の排ガ
スを吸引し、この排ガスを蓄熱体42aに通して熱を回収
してから、兼用通路41aに導いて炉外に排出する。以上
の図2(a) および(b) に示した工程を、例えば数十秒毎
に繰り返して、加熱を行うことによって、熱損失の少な
い加熱炉操業が実現するのである。
Next, after the combustion operation of the burner is switched, and at that time, the switching valve 44 of the shared passage 41a and 41b is switched to change the connection of the air and exhaust gas to the above-mentioned conduit, and FIG. As shown, in supplying the combustion air from the shared passage 41b to the burner 40b via the heat storage body 42b, the heat recovered in the heat storage body 42b in the step shown in FIG. The combustion air is supplied while preheating is performed, and at the same time, the fuel 43b is supplied to burn the burner 40b. At the same time, the exhaust gas in the furnace is sucked from the burner 40a opposed thereto, the exhaust gas is passed through the regenerator 42a to recover heat, and then guided to the shared passage 41a to be discharged out of the furnace. By repeating the above-described steps shown in FIGS. 2A and 2B, for example, every several tens of seconds to perform heating, a heating furnace operation with little heat loss is realized.

【0013】かような蓄熱式バーナを用いた加熱炉の操
業において、蓄熱式バーナの排ガス吸引は高速で行われ
るため、炉幅方向に分布する排ガスを広い範囲にわたり
吸引している。発明者らは、この現象に着目し、蓄熱式
バーナから吸引された炉内の排ガスが、炉内雰囲気を良
く再現していることから、蓄熱式バーナから吸引された
排ガスについて成分濃度の測定を行えば、炉内雰囲気に
おける成分濃度が正確に測定されることを見出し、この
発明を完成するに到った。
In the operation of a heating furnace using such a regenerative burner, the exhaust gas of the regenerative burner is sucked at a high speed, so that exhaust gas distributed in the furnace width direction is sucked over a wide range. The inventors focused on this phenomenon, and since the exhaust gas in the furnace sucked from the regenerative burner reproduced the atmosphere inside the furnace well, we measured the component concentration of the exhaust gas sucked from the regenerative burner. By doing so, they found that the component concentration in the furnace atmosphere was accurately measured, and completed the present invention.

【0014】すなわち、この発明の要旨構成は、次のと
おりである。 (1) 加熱源として、蓄熱体が付帯されたバーナの対を向
かい合わせに配設した蓄熱式バーナを有する、加熱炉に
おいて、蓄熱式バーナの各対のバーナを交互に燃焼させ
ると共に、非燃焼時のバーナから炉内の排ガスを吸引
し、上記蓄熱体に排ガスを導入して排ガス中の熱を蓄熱
体に回収し、この回収した熱を燃焼時のバーナの燃焼用
空気の加熱に利用して、加熱炉の操業を行うに当り、上
記バーナから吸引した排ガスの一部を分析器に導いて、
排ガス中の成分濃度を測定することを特徴とする加熱炉
内の雰囲気ガス濃度の測定方法。
That is, the gist configuration of the present invention is as follows. (1) In a heating furnace having a regenerative burner in which a pair of burners provided with a heat storage body are arranged facing each other as a heating source, the burners of each pair of the regenerative burners are alternately burned and non-burned. The exhaust gas in the furnace is sucked from the burner at the time, the exhaust gas is introduced into the regenerator and the heat in the exhaust gas is collected in the regenerator, and the recovered heat is used for heating the combustion air of the burner during combustion. In operating the heating furnace, a part of the exhaust gas sucked from the burner was guided to an analyzer,
A method for measuring the concentration of an atmosphere gas in a heating furnace, comprising measuring the concentration of a component in an exhaust gas.

【0015】(2) 上記(1) において、蓄熱式バーナから
吸引した排ガスの成分濃度測定値を、該蓄熱式バーナが
設けられた加熱炉内の帯における成分濃度の代表値とし
て用いることを特徴とする加熱炉内の雰囲気ガス濃度の
測定方法。
(2) In the above item (1), the measured value of the component concentration of the exhaust gas sucked from the regenerative burner is used as a representative value of the component concentration in a zone in a heating furnace provided with the regenerative burner. Method for measuring the concentration of atmospheric gas in a heating furnace.

【0016】(3) 加熱源として、蓄熱体が付帯されたバ
ーナの対を向かい合わせに配設した蓄熱式バーナを有
し、該蓄熱式バーナの各対のバーナを交互に燃焼させる
と共に、非燃焼時のバーナから炉内の排ガスを吸引し、
上記蓄熱体に排ガスを導入して排ガス中の熱を蓄熱体に
回収し、この回収した熱を燃焼時のバーナの燃焼用空気
の加熱に利用して操業を行う、加熱炉において、該加熱
炉内の排ガスを非燃焼時のバーナから蓄熱体を介して排
出する経路の途中に、排ガスの一部を採取するプローブ
および採取した排ガスの成分濃度を測定する分析器を設
けたことを特徴とする加熱炉。
(3) As a heating source, a regenerative burner having a pair of burners provided with regenerators is provided so as to face each other. Exhaust gas in the furnace is sucked from the burner during combustion,
An exhaust gas is introduced into the heat storage body, heat in the exhaust gas is recovered in the heat storage body, and the recovered heat is used for heating combustion air of a burner during combustion, and the operation is performed. A probe for sampling a part of the exhaust gas and an analyzer for measuring a component concentration of the collected exhaust gas are provided in the middle of a path for discharging the exhaust gas from the burner through a heat storage unit when the combustion is not performed. heating furnace.

【0017】[0017]

【発明の実施の形態】以下、この発明の方法について、
図面を参照して詳細に説明する。さて、図2に示したよ
うに、蓄熱式バーナにおいて、バーナ40aまたは40bか
ら吸引した排ガスは、兼用通路41aまたは41bを介して
炉外へ導かれるが、その排ガスの吸引は、図3に示す経
路にて行われる。すなわち、複数組の蓄熱式バーナから
延びる兼用通路41aおよび41bを、炉壁の一方側と他方
側とのバーナ群毎にそれぞれ設けた排ガスダクト8aお
よび8bに集約し、さらにこれら排ガスダクト8aおよ
び8bを1本の導管9に集約し、この導管9を吸引ファ
ン10を介して加熱炉の煙道7に連通させている。そし
て、吸引ファン10の吸引力によって、兼用通路41aおよ
び41b、排ガスダクト8aおよび8b、そして導管9を
介して、排ガスを煙道7へと導き、炉外に排出してい
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the method of the present invention will be described.
This will be described in detail with reference to the drawings. Now, as shown in FIG. 2, in the regenerative burner, the exhaust gas sucked from the burner 40a or 40b is guided to the outside of the furnace through the shared passage 41a or 41b, and the exhaust gas is sucked as shown in FIG. It is done on the route. That is, dual-use passages 41a and 41b extending from a plurality of sets of regenerative burners are combined into exhaust gas ducts 8a and 8b provided for each of the burner groups on one side and the other side of the furnace wall, and further, these exhaust gas ducts 8a and 8b Into a single conduit 9, which communicates with the flue 7 of the heating furnace via a suction fan 10. Then, the exhaust gas is guided to the flue 7 by the suction force of the suction fan 10 via the shared passages 41a and 41b, the exhaust gas ducts 8a and 8b, and the conduit 9, and discharged to the outside of the furnace.

【0018】以上の排ガスの排出経路において、図3に
示す例では導管9の途上において、プローブ11を挿入、
配置し、このプローブ11から導管9を流れる排ガスの一
部を採取し、この採取した排ガスについて分析器12を用
いて、各種成分の濃度を測定する。かくして得られる各
種の測定濃度値は、上述のように、炉内雰囲気の特に炉
幅方向分布を良く示しているため、これを蓄熱式バーナ
を設置した帯、例えば均熱帯3における、成分濃度の代
表値として用いることができる。
In the exhaust gas discharging path described above, in the example shown in FIG.
A part of the exhaust gas flowing through the conduit 9 is sampled from the probe 11 and the concentrations of various components are measured using the analyzer 12 with respect to the sampled exhaust gas. As described above, the various measured concentration values thus obtained show well the distribution of the atmosphere in the furnace, particularly in the furnace width direction. It can be used as a representative value.

【0019】ここで、上記の蓄熱式バーナから吸引した
排ガスを採取して酸素濃度を測定した場合と、炉壁から
挿入したプローブを介して酸素濃度を測定した場合とに
ついて、炉内平均酸素濃度に対する誤差を調査した。そ
の結果を図4に示すように、蓄熱式バーナから吸引した
排ガスを採取して酸素濃度を測定した場合は、実際の炉
内平均酸素濃度との差が極めて小さいことがわかる。す
なわち、蓄熱式バーナから吸引した排ガスを調査するこ
とによって、実際の炉内雰囲気に則した成分濃度の測定
が可能になるのである。なお、炉内平均酸素濃度は、抽
出扉および装入扉が閉、かつ(炉内侵入空気)≒0Nm3
/hとなる炉圧設定の条件下において、バーナに投入す
るガス流量、成分および空気比から理論的に求められ
る、炉内酸素濃度の計算値である。その他の条件は、後
述の実施例において詳しく示す。
Here, the average oxygen concentration in the furnace was measured for a case where the exhaust gas sucked from the regenerative burner was sampled and the oxygen concentration was measured, and a case where the oxygen concentration was measured via a probe inserted from the furnace wall. The error for was investigated. As shown in FIG. 4, when the exhaust gas sucked from the regenerative burner was sampled and the oxygen concentration was measured, the difference from the actual average oxygen concentration in the furnace was found to be extremely small. That is, by examining the exhaust gas sucked from the regenerative burner, it is possible to measure the component concentration in accordance with the actual furnace atmosphere. In addition, the average oxygen concentration in the furnace was obtained by closing the extraction door and the charging door and (air entering the furnace) ≒ 0 Nm 3
It is a calculated value of the oxygen concentration in the furnace, which is theoretically obtained from the gas flow rate, the component, and the air ratio supplied to the burner under the condition of the furnace pressure setting of / h. Other conditions will be described in detail in Examples described later.

【0020】また、蓄熱式バーナから吸引した排ガスを
採取する位置は、図3に示したように、蓄熱式バーナの
蓄熱体の下流側であることが望ましい。なぜなら、蓄熱
体によって熱が回収された排ガスは、当然炉内温度より
低温になっているため、蓄熱体の下流側でプローブを挿
入すれば、プローブが高温雰囲気に晒されることがな
く、その耐久寿命を延長することができるからである。
Further, as shown in FIG. 3, it is desirable that the position where the exhaust gas sucked from the regenerative burner is collected is located downstream of the regenerator of the regenerative burner. Because the exhaust gas from which heat is recovered by the regenerator is naturally lower than the furnace temperature, inserting the probe downstream of the regenerator prevents the probe from being exposed to a high-temperature atmosphere, and its durability. This is because the life can be extended.

【0021】なお、以上の事例は連続式加熱炉を用いた
場合を説明したが、バッチ式加熱炉や回転炉床式加熱炉
などにも、この発明は有利に適合する。
In the above case, a case where a continuous heating furnace is used has been described. However, the present invention is advantageously applicable to a batch heating furnace, a rotary hearth heating furnace, and the like.

【0022】[0022]

【実施例】図1に示した連続式加熱炉(搬送路高さ:炉
底から0.5 m)を用いて、厚み:220mm 、幅:1200mmお
よび長さ9800mmの鋼スラブを導入して、室温から1230℃
まで加熱する操業を行った。なお、加熱炉の均熱帯に配
した4組の蓄熱式バーナの仕様は、下記のとおりであ
る。 記 燃焼容量:2,000,000 (kcal/H・バーナ) 燃焼負荷:10〜100 % バーナ対間での燃焼切換え時期:60s/回 排ガス吸引率:60〜90%
EXAMPLE A steel slab having a thickness of 220 mm, a width of 1200 mm and a length of 9800 mm was introduced using the continuous heating furnace (transport path height: 0.5 m from the furnace bottom) shown in FIG. 1230 ℃
Operation was performed until heating. The specifications of the four sets of regenerative burners arranged in the soaking zone of the heating furnace are as follows. Note Combustion capacity: 2,000,000 (kcal / H. Burner) Combustion load: 10 to 100% Combustion switching time between a pair of burners: 60 s / time Exhaust gas suction rate: 60 to 90%

【0023】上記の加熱炉の操業において、蓄熱式バー
ナから吸引した排ガスを蓄熱体に通したのち、導管9の
途上に挿入したプローブ11から排ガスの一部を採取し、
この採取した排ガスについて分析器12を用いて酸素濃度
を測定した。なお、炉内酸素濃度測定範囲は0〜21 vol
%であり、また導管9における管内雰囲気温度は200℃
であった。また、比較として、均熱帯の炉壁から挿入し
たプローブを介して酸素濃度を測定した。
In the operation of the heating furnace described above, after the exhaust gas sucked from the regenerative burner is passed through the regenerator, a part of the exhaust gas is collected from the probe 11 inserted on the way of the conduit 9,
The analyzer 12 was used to measure the oxygen concentration of the collected exhaust gas. The furnace oxygen concentration measurement range is 0 to 21 vol.
%, And the ambient temperature in the pipe 9 is 200 ° C.
Met. As a comparison, the oxygen concentration was measured via a probe inserted from a furnace wall in a solitary zone.

【0024】これらの測定濃度値を炉内平均酸素濃度と
対比した結果は、図4に示したとおりであり、この発明
に従って蓄熱式バーナから吸引した排ガスによって測定
した場合は、炉内平均酸素濃度値との誤差は0.5 %未満
であった。これに対して、炉壁から挿入したプローブを
介して酸素濃度を測定した場合は、炉内平均酸素濃度値
との誤差は1〜3%であった。
The results of comparing these measured concentration values with the average oxygen concentration in the furnace are shown in FIG. 4. In the case of measuring with the exhaust gas sucked from the regenerative burner according to the present invention, the average oxygen concentration in the furnace was measured. The deviation from the value was less than 0.5%. On the other hand, when the oxygen concentration was measured via the probe inserted from the furnace wall, the error from the average oxygen concentration in the furnace was 1 to 3%.

【0025】[0025]

【発明の効果】以上述べたように、この発明によれば、
加熱炉内雰囲気の成分濃度の測定を正確に行えるため、
この測定値に基づく炉内雰囲気制御によって、高品質の
製品を生み出すことができる。また、この発明の加熱炉
内雰囲気の成分濃度の測定方法は、既存の設備を利用し
て行うことが容易であり、新たな設備投資が必要でな
く、低コストで実現することが可能である。
As described above, according to the present invention,
Since the concentration of components in the furnace atmosphere can be measured accurately,
High quality products can be produced by controlling the furnace atmosphere based on the measured values. Further, the method for measuring the component concentration in the atmosphere in the heating furnace according to the present invention can be easily performed using existing equipment, does not require new equipment investment, and can be realized at low cost. .

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

【図1】 連続式加熱炉の構造を示す図である。FIG. 1 is a diagram showing the structure of a continuous heating furnace.

【図2】 蓄熱式バーナの構造を示す図である。FIG. 2 is a view showing a structure of a regenerative burner.

【図3】 蓄熱式バーナからの排ガスの排出経路を示す
図である。
FIG. 3 is a diagram showing a discharge path of exhaust gas from a regenerative burner.

【図4】 種々の手法による炉内酸素濃度の測定値と炉
内平均酸素濃度とを比較した図である。
FIG. 4 is a diagram comparing measured values of the in-furnace oxygen concentration by various methods and the average in-furnace oxygen concentration.

【符号の説明】[Explanation of symbols]

1 予熱帯 1a 装入扉 2 加熱炉 3 均熱帯 3a 抽出扉 4 バーナ 5 搬送路 6 鋼材 7 煙道 7a レキュペレータ 7b ダンパー 8a,8b 排ガスダクト 9 導管 10 吸引ファン 11 プローブ 12 分析器 40a,40b バーナ 42a,42b 蓄熱体 DESCRIPTION OF SYMBOLS 1 Pre-tropical 1a Loading door 2 Heating furnace 3 Uniform tropical 3a Extraction door 4 Burner 5 Conveyance path 6 Steel material 7 Flue 7a Recuperator 7b Damper 8a, 8b Exhaust gas duct 9 Conduit 10 Suction fan 11 Probe 12 Analyzer 40a, 40b Burner 42a , 42b heat storage

───────────────────────────────────────────────────── フロントページの続き (72)発明者 杉本 一郎 岡山県倉敷市水島川崎通1丁目(番地な し) 川崎製鉄株式会社水島製鉄所内 (72)発明者 古川 誠博 岡山県倉敷市水島川崎通1丁目(番地な し) 川崎製鉄株式会社水島製鉄所内 Fターム(参考) 3K023 QA03 QB02 QC05 SA01 4K056 AA08 BA02 BB01 CA02 DA27 DA32 FA15 4K063 AA08 BA02 CA02 CA03 DA34 ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Ichiro Sugimoto 1-chome, Mizushima Kawasaki-dori, Kurashiki-shi, Okayama Prefecture (without address) Inside Mizushima Works, Kawasaki Steel Corporation (72) Inventor, Masahiro Furukawa Mizushima-Kawasaki-dori, Kurashiki-shi, Okayama 1-chome (without address) Mizushima Works, Kawasaki Steel F-term (reference) 3K023 QA03 QB02 QC05 SA01 4K056 AA08 BA02 BB01 CA02 DA27 DA32 FA15 4K063 AA08 BA02 CA02 CA03 DA34

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 加熱源として、蓄熱体が付帯されたバー
ナの対を向かい合わせに配設した蓄熱式バーナを有す
る、加熱炉において、蓄熱式バーナの各対のバーナを交
互に燃焼させると共に、非燃焼時のバーナから炉内の排
ガスを吸引し、上記蓄熱体に排ガスを導入して排ガス中
の熱を蓄熱体に回収し、この回収した熱を燃焼時のバー
ナの燃焼用空気の加熱に利用して、加熱炉の操業を行う
に当り、上記バーナから吸引した排ガスの一部を分析器
に導いて、排ガス中の成分濃度を測定することを特徴と
する加熱炉内の雰囲気ガス濃度の測定方法。
1. A heating furnace having a regenerative burner in which a pair of burners provided with a regenerator is provided facing each other as a heating source. In a heating furnace, the burners of each pair of regenerative burners are alternately burned, Exhaust gas in the furnace is sucked from the burner during non-combustion, the exhaust gas is introduced into the regenerator and heat in the exhaust gas is collected in the regenerator, and the recovered heat is used for heating the combustion air of the burner during combustion. Utilizing and operating the heating furnace, a part of the exhaust gas sucked from the burner is guided to an analyzer to measure the component concentration in the exhaust gas, and the concentration of the atmosphere gas in the heating furnace is measured. Measuring method.
【請求項2】 請求項1において、蓄熱式バーナから吸
引した排ガスの成分濃度測定値を、該蓄熱式バーナが設
けられた加熱炉内の帯における成分濃度の代表値として
用いることを特徴とする加熱炉内の雰囲気ガス濃度の測
定方法。
2. The method according to claim 1, wherein the measured value of the component concentration of the exhaust gas sucked from the regenerative burner is used as a representative value of the component concentration in a zone in a heating furnace provided with the regenerative burner. A method for measuring the concentration of atmospheric gas in a heating furnace.
【請求項3】 加熱源として、蓄熱体が付帯されたバー
ナの対を向かい合わせに配設した蓄熱式バーナを有し、
該蓄熱式バーナの各対のバーナを交互に燃焼させると共
に、非燃焼時のバーナから炉内の排ガスを吸引し、上記
蓄熱体に排ガスを導入して排ガス中の熱を蓄熱体に回収
し、この回収した熱を燃焼時のバーナの燃焼用空気の加
熱に利用して操業を行う、加熱炉において、該加熱炉内
の排ガスを非燃焼時のバーナから蓄熱体を介して排出す
る経路の途中に、排ガスの一部を採取するプローブおよ
び採取した排ガスの成分濃度を測定する分析器を設けた
ことを特徴とする加熱炉。
3. A regenerative burner in which a pair of burners provided with a regenerator is disposed facing each other as a heating source,
While alternately burning each pair of burners of the regenerative burner, the exhaust gas in the furnace is sucked from the non-burning burner, the exhaust gas is introduced into the regenerator, and the heat in the exhaust gas is recovered in the regenerator, The collected heat is used for heating the combustion air of the burner during combustion, and the operation is performed. In a heating furnace, the exhaust gas in the heating furnace is discharged from the burner during non-combustion via a heat storage body in the course of a path. A heating furnace provided with a probe for sampling a part of the exhaust gas and an analyzer for measuring a component concentration of the collected exhaust gas.
JP2001014230A 2001-01-17 2001-01-23 Method of measuring atmospheric gas concentration in heating furnace and heating furnace Pending JP2002212630A (en)

Priority Applications (13)

Application Number Priority Date Filing Date Title
JP2001014230A JP2002212630A (en) 2001-01-23 2001-01-23 Method of measuring atmospheric gas concentration in heating furnace and heating furnace
KR1020027012192A KR100634776B1 (en) 2001-01-17 2001-12-27 Heating furnace with regenerative burner and operating method thereof
US10/220,726 US6644962B2 (en) 2001-01-17 2001-12-27 Heating furnace having heat regenerating burners and operation method thereof
EP06018722A EP1757707A3 (en) 2001-01-17 2001-12-27 Heating furnace having heat regenerating burners and operation method thereof
EP01273342A EP1275740B1 (en) 2001-01-17 2001-12-27 Method of operating a heating furnace with regenerative burners
CNB018092470A CN100338236C (en) 2001-01-17 2001-12-27 Furnace with regenerative burner and method of operation thereof
DE60124691T DE60124691T2 (en) 2001-01-17 2001-12-27 METHOD FOR OPERATING A HEATER WITH REGENERATIVE BURNERS
BR0109303-7A BR0109303A (en) 2001-01-17 2001-12-27 Heating furnace having heat regeneration burners and their method of operation
AT01273342T ATE346172T1 (en) 2001-01-17 2001-12-27 METHOD FOR OPERATING A HEATING FURNACE WITH REGENERATIVE BURNERS
CA002403221A CA2403221C (en) 2001-01-17 2001-12-27 Heating furnace with regenerative burners and method of operating the heating furnace
PCT/JP2001/011508 WO2002057501A1 (en) 2001-01-17 2001-12-27 Heating furnace with regenerative burners and method of operating the heating furnace
CA002639404A CA2639404A1 (en) 2001-01-17 2001-12-27 Heating furnace with regenerative burners and method of operating the heating furnace
TW091100620A TW524956B (en) 2001-01-17 2002-01-16 Heating furnace with regenerative burners and method of operating the heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001014230A JP2002212630A (en) 2001-01-23 2001-01-23 Method of measuring atmospheric gas concentration in heating furnace and heating furnace

Publications (1)

Publication Number Publication Date
JP2002212630A true JP2002212630A (en) 2002-07-31

Family

ID=18880952

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001014230A Pending JP2002212630A (en) 2001-01-17 2001-01-23 Method of measuring atmospheric gas concentration in heating furnace and heating furnace

Country Status (1)

Country Link
JP (1) JP2002212630A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101839638A (en) * 2010-04-29 2010-09-22 北京首钢国际工程技术有限公司 Heat accumulating and preheating combined heating method of slag-drip high-temperature silicon steel plate blank heating furnace
JP2022176424A (en) * 2022-08-31 2022-11-29 中外炉工業株式会社 Combustion control method for combustion equipment

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101839638A (en) * 2010-04-29 2010-09-22 北京首钢国际工程技术有限公司 Heat accumulating and preheating combined heating method of slag-drip high-temperature silicon steel plate blank heating furnace
JP2022176424A (en) * 2022-08-31 2022-11-29 中外炉工業株式会社 Combustion control method for combustion equipment
JP7220971B2 (en) 2022-08-31 2023-02-13 中外炉工業株式会社 Combustion control method for combustion equipment

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