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JP2004020090A - Regeneration burner for connecting passage for filling filling fluid to exhaust passage and its operation method - Google Patents

Regeneration burner for connecting passage for filling filling fluid to exhaust passage and its operation method Download PDF

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Publication number
JP2004020090A
JP2004020090A JP2002177050A JP2002177050A JP2004020090A JP 2004020090 A JP2004020090 A JP 2004020090A JP 2002177050 A JP2002177050 A JP 2002177050A JP 2002177050 A JP2002177050 A JP 2002177050A JP 2004020090 A JP2004020090 A JP 2004020090A
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Prior art keywords
exhaust
burner
path
switching valve
filling
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JP2002177050A
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JP3973494B2 (en
Inventor
Isamu Ikeda
池田 勇
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Chugai Ro Co Ltd
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Chugai Ro Co Ltd
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    • 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

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Abstract

<P>PROBLEM TO BE SOLVED: To provide a regeneration burner for connecting a passage for filling a filling fluid to an exhaust passage and for preventing the occurrence of a hindrance to operation of the regeneration burner due to corrosion of a directional control valve for exhaust air installed in a pipe of the exhaust passage, and also to provide its operation method. <P>SOLUTION: This regeneration burner is provided with: burners 2 arranged in a plurality toward the inside of a furnace for generating exhaust gas including an SO<SB>2</SB>component, supplying fuel gas from a fuel supply passage 6 at combustion operation time, supplying combustion air from an air supply passage 3 and exhausting the exhaust gas to the exhaust passage at suction operation time; and a directional control valve 16 for fuel, a directional control valve 14 for air supply and the directional control valve 15 for exhaust air, associatively arranged to the respective burners in the air supply passage and the exhaust passage and opened-closed for switching combustion operation and suction operation of the burners. While putting a part in an operation state among a plurality of burners, a residual burner is connected with a fluid filling passage 22 for filling the fluid in the exhaust passage between the respective burners and the directional control valve for exhaust air when put in a stopping state, by closing all of the directional control valve for fuel, the directional control valve for air supply, and the directional control valve for exhaust air. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、排気経路の配管に取り付けられている排気用切替弁の腐食のためにリジェネバーナの運転に支障をきたすことを防止できる、排気経路に充填用流体を充填する経路を接続したリジェネバーナおよびその運転方法に関する。
【0002】
【従来の技術】
リジェネバーナはよく知られているように、炉内に向けて互いに相対向させて配置される一対で一組のバーナを複数組設備し、これらバーナにはそれぞれ蓄熱器を備え、一対のバーナの一方に燃料ガスと燃焼用空気を供給して燃焼を行わせると同時に、他方のバーナからは排ガスを吸引させ、この燃焼動作と吸引動作を各組の一対のバーナ相互で交互に行わせることにより、吸引動作時には蓄熱器で排ガスから排熱を回収し、燃焼動作時には蓄熱器で回収した排熱で燃焼用空気を加熱するようにして、これにより省エネルギ化を図っている。
【0003】
従来のリジェネバーナaにおける燃焼用空気や排ガス等のバーナbへの供給・排出系統を、図2を参照しつつバーナbの運転状態に従って説明すると、燃焼動作に際しては、燃焼用空気と燃料ガスがバーナbへ供給される。燃焼用空気は、他のバーナへも接続されている給気経路cの分岐部d上流側に設けた給気用電磁弁eを開くと、給気風量制御ベーンfで風量制御されつつ給気ブロアgによって給気経路c内に導入され、さらに分岐部d下流側に設けた各バーナbの給気用切替弁hを開くことにより、蓄熱器iを通過して加熱されつつバーナbへと供給される。燃料ガスは、他のバーナへも接続されている燃料供給経路jの分岐部k上流側に設けた燃料用電磁弁lを開くことで導入され、さらに分岐部k下流側に設けた各バーナbの燃料用切替弁mを開くことにより、バーナbのバーナノズルnへと供給される。燃料ガスとしては通常、コークス炉ガス(以下、COGという)、高炉ガスや転炉ガスにCOGを混合したガス(以下、Mガスという)などが使用される。この燃焼動作時には、排気経路oは各バーナbの排気用切替弁pによって閉じられている。
【0004】
他方、吸引動作に際しては、排ガスが炉から排出される。排ガスは、他のバーナへも接続されている排気経路oの分岐部q下流側の排気用電磁弁rを開いた状態で、分岐部q上流側に設けた各バーナの排気用切替弁pを開くことにより、蓄熱器iを通過して排熱回収されながら排気風量制御ベーンsで風量制御されつつ排気ブロアtによって炉から吸引される。この吸引動作に際しては、給気経路cおよび燃料供給経路jはそれらの切替弁h,mによって閉じられている。また、バーナbには、バーナノズルnに水や空気などの冷却媒体を流通させて冷却するために、冷却媒体供給系uおよび冷却媒体排出系vが接続されている。
【0005】
複数組のバーナbをコントロールするリジェネバーナaの代表的な制御方法は、負荷が100%〜30%程度まではすべてのバーナbを比例的にターンダウンさせる(火力を増減させる)「比例制御」を実行し、それ以下の負荷でのターンダウンについては、すべてのバーナbに対し、これらを適当な間合いで稼働させたり停止させたりする「時間比例ON−OFF制御」を実行し、さらに負荷が低下した場合には、全バーナbのうちのいくつかを停止状態とする「間引き制御」を実行する方法である。間引き制御の対象となった停止状態のバーナbでは、燃焼動作はもちろんのこと、吸引動作も停止され、このバーナbをコントロールする各切替弁m,h,pはすべて閉状態とされる。
【0006】
【発明が解決しようとする課題】
ところで、上述したCOGやMガス等の燃料ガスを燃焼させた後の排ガス中には、SOが含まれる。このSOは、排ガスの温度が酸露点(脱硫COG燃焼排ガスでは一般に、130℃〜140℃)以下に低下すると結露し、水分(HO)と反応して硫酸(HSO)分を生じる。そして従来にあっては、排気経路oの配管に取り付けられている排気用切替弁pに、この硫酸による腐食が発生し、この排気用切替弁pの腐食のためにリジェネバーナaの運転に支障をきたすおそれがあるという課題があった。
【0007】
例えば、腐食のために排気用切替弁pの閉め切り性能が劣化し、これによって間引き制御時などに間引きの対象となったバーナbの排気経路oが適切に遮断されずリークを生ずると、排気ブロアtの吸引作用も手伝って当該バーナbの蓄熱器iの低温側が負圧状態となりやすく、これにより炉内の排ガスがバーナbから排気経路oへと流入し続けて蓄熱器i周辺を含む配管温度が過度に上昇し、この結果リミッターによって上限温度リミットが設定されている蓄熱器i低温側のオーバーヒートを引き起こして、当該バーナbが間引き制御対象から解除されて燃焼動作に移ったとたんにリミッターが作動してしまって、リジェネバーナaの運転を継続し得なくなることが想定される。
【0008】
本発明は上記従来の課題に鑑みて創案されたものであって、排気経路の配管に取り付けられている排気用切替弁の腐食のためにリジェネバーナの運転に支障をきたすことを防止できる、排気経路に充填用流体を充填する経路を接続したリジェネバーナおよびその運転方法を提供することを目的とする。
【0009】
【課題を解決するための手段】
本発明にかかる排気経路に充填用流体を充填する経路を接続したリジェネバーナは、SO成分を含む排ガスが発生する炉内に向けて複数設置され、燃焼動作時には燃料供給経路から燃料ガスが供給されるとともに給気経路から燃焼用空気が供給され、吸引動作時には排気経路へ排ガスを排出するバーナと、これら燃料供給経路、給気経路および排気経路にそれぞれ、各バーナに対応させて設けられ、該バーナの燃焼動作と吸引動作とを切り換えるべく開閉される燃料用切替弁、給気用切替弁および排気用切替弁とを備え、複数のバーナのうち、一部は稼働状態としながら、残りは、その燃料用切替弁、給気用切替弁および排気用切替弁のすべてを閉じて停止状態とするリジェネバーナにおいて、各バーナとその排気用切替弁との間の上記排気経路に、流体を充填するための流体充填経路を接続したことを特徴とする。これにより、排気経路の配管に取り付けられている排気用切替弁の腐食のためにリジェネバーナの運転に支障をきたすことが防止される。
【0010】
また、前記流体充填経路には、充填用流体の流量を調整する流量調整手段が設けられていることを特徴とする。これにより、充填用流体を必要量だけ排気経路へ導入することが可能となる。
【0011】
さらに、前記流体充填経路が、各給気用切替弁上流側の前記給気経路に接続され、充填用流体として上記給気経路の燃焼用空気が導入されることを特徴とする。これにより、安価に設備できる。
【0012】
また、本発明にかかるリジェネバーナの運転方法は、SO成分を含む排ガスが発生する炉内に向けて複数設置され、燃焼動作時には燃料供給経路から燃料ガスが供給されるとともに給気経路から燃焼用空気が供給され、吸引動作時には排気経路へ排ガスを排出するバーナと、これら燃料供給経路、給気経路および排気経路にそれぞれ、各バーナに対応させて設けられ、該バーナの燃焼動作と吸引動作とを切り換えるべく開閉される燃料用切替弁、給気用切替弁および排気用切替弁とを備え、複数のバーナのうち、一部は稼働状態としながら、残りは、その燃料用切替弁、給気用切替弁および排気用切替弁のすべてを閉じて停止状態とする運転が行われるリジェネバーナの運転方法において、バーナを停止状態にしたときに、停止したバーナとその排気用切替弁との間の上記排気経路へ流体を充填するようにしたことを特徴とする。これにより、排気経路の配管に取り付けられている排気用切替弁の腐食のためにリジェネバーナの運転に支障をきたすことが防止される。
【0013】
【発明の実施の形態】
以下に、本発明にかかる排気経路に充填用流体を充填する経路を接続したリジェネバーナおよびその運転方法の好適な一実施形態を、添付図面を参照して詳細に説明する。図1には、本発明にかかるリジェネバーナ1の好適な一実施形態が示されている。本実施形態のリジェネバーナ1における燃焼用空気や燃料ガス、排ガスの供給・排出系統の基本的な構成は、図2に示した従来技術とほぼ同様である。リジェネバーナ1は、炉内に向けて互いに相対向させて配置される一対で一組のバーナ2を複数組備える(図1には、一つのバーナ2が示されている)。
【0014】
これら複数組の複数のバーナ2には、これらへ一括して燃焼用空気を供給するための給気経路3と、炉内の排ガスをこれらから一括して排出するための排気経路4とが接続され、これら給気経路3および排気経路4にはこれらを各バーナ2に接続するために分岐部3a,4aが備えられる。また複数組の複数のバーナ2には、それらにそれぞれ設けられたバーナノズル5へ一括してCOGやMガスなどの燃料ガスを供給するための燃料供給経路6が接続され、この燃料供給経路6にもこれを各バーナに接続するための分岐部6aが備えられる。
【0015】
給気経路3には、その分岐部3aよりも燃焼用空気の流れ方向上流側に、給気経路3を開閉する開閉自在な給気用電磁弁7と、燃焼用空気の風量を制御する給気風量制御ベーン8と、燃焼用空気を給気経路3を介して各バーナ2へ圧送する給気ブロア9とが設けられる。同様に、排気経路4には、その分岐部4aよりも排ガスの流れ方向下流側に、排気経路4を開閉する開閉自在な排気用電磁弁10と、排ガスの風量を制御する排気風量制御ベーン11と、排ガスを排気経路4を介して炉内から吸引する排気ブロア12とが設けられる。また、燃料供給経路6には、その分岐部6aよりも燃料ガスの流れ方向上流側に、燃料供給経路6を開閉する開閉自在な燃料用電磁弁13が設けられる。
【0016】
さらに、給気経路3には、分岐部3aよりも下流側に、各バーナ2それぞれへの燃焼用空気の供給・停止を切り替える開閉自在な給気用切替弁14が設けられる。また、排気経路4には、分岐部4aよりも上流側に、各バーナ2それぞれからの排ガスの排出・停止を切り替える開閉自在な排気用切替弁15が設けられる。さらに、燃料供給経路6には、分岐部6aよりも下流側に、各バーナノズル5それぞれへの燃料ガスの供給・停止を切り替える開閉自在な燃料用切替弁16が設けられる。給気経路3と排気経路4とは、各バーナ2との接続位置前段で集合されて、一括してバーナ2に接続される。
【0017】
各バーナ2には、バーナノズル5と集合された給気経路3および排気経路4との間に配置されて、これを通過して炉内から排気経路4へと排出される排ガスから排熱を回収し、また給気経路3からこれを通過してバーナ2へと供給される燃焼用空気を、回収した排熱で加熱するための蓄熱器17が備えられる。さらに、各バーナ2には、それらのバーナノズル5に水や空気などの冷却媒体を流通させて冷却するために、冷却媒体供給系18および冷却媒体排出系19が接続される。
【0018】
そして、本実施形態にかかる排気経路に充填用流体を充填する経路を接続したリジェネバーナ1は基本的には、各バーナ2とその排気用切替弁15との間の排気経路4に、流体を充填するための流体充填経路22が接続される。また、流体充填経路22には、充填用流体の流量を調整する流量調整手段として充填流体量調整用コック23や絞りが設けられ、さらに好ましくは、流体充填経路22は、各給気用切替弁14上流側の給気経路3に接続され、充填用流体として給気経路3の燃焼用空気が導入される。
【0019】
図示例に従って詳述すると、排気経路4には、各バーナ2の排気用切替弁15よりも排ガスの流れ方向上流側であって、かつ蓄熱器17の低温側に、流体充填経路22の一端が接続され、この流体充填経路22の他端は、同じバーナ2の導入流体量調整用コック21よりも燃焼用空気の流れ方向上流位置で流体導入経路20に接続され、この流体導入経路20を介して給気経路3と接続されて、これにより給気ブロア9で圧送されている燃焼用空気が、排気用切替弁15と蓄熱器17との間に充填されるようになっている。また、充填流体量調整用コック23は、給気経路3から排気経路4への燃焼用空気の充填流量を調整するために開度調整可能に構成される。これにより、燃焼用空気を必要量だけ排気経路4へ導入することができる。
【0020】
また本実施形態にあっては、各バーナ2の排気用切替弁15下流側の排気経路4に、希釈用の流体を導入するための流体導入経路20が接続される。また、流体導入経路20には、希釈用流体の流量を調整する流量調整手段として導入流体量調整用コック21や絞りが設けられ、さらに好ましくは、流体導入経路20は、各給気用切替弁14上流側の給気経路3に接続され、希釈用流体として給気経路3の燃焼用空気が導入される。
【0021】
具体的には、排気経路4には、各バーナ2の排気用切替弁15よりも排ガスの流れ方向下流側であって、かつ分岐部4aの上流位置に、流体導入経路20の一端が接続され、この流体導入経路20の他端は、同じバーナ2の給気用切替弁14よりも燃焼用空気の流れ方向上流側であって、かつ分岐部3aの下流位置で給気経路3に接続され、これにより給気ブロア9で圧送されている燃焼用空気が、排気用切替弁15下流側の排気経路4へ導入されるようになっている。また、導入流体量調整用コック21は、給気経路3から排気経路4への燃焼用空気の導入流量を調整するために、開度調整可能に構成される。これにより、燃焼用空気を必要量だけ排気経路4へ導入することができる。
【0022】
さらに本実施形態にあっては、各バーナ2とその燃料用切替弁16との間の燃料供給経路6に、不活性ガスを導入するための導入経路24が接続される。導入経路24には、燃料供給経路6への不活性ガスの導入・停止を切り替える切替手段として不活性ガス用切替弁25が設けられる。この不活性ガス用切替弁25には、燃料用切替弁16、給気用切替弁14および排気用切替弁15のすべてが閉じられたことを検出して検出信号を出力する検出手段26が接続され、不活性ガス用切替弁25は検出手段26から検出信号が入力されることで燃料供給経路6へ不活性ガスを導入するようになっている。また、導入経路24には、不活性ガスの流量を調整する流量調整手段として不活性ガス導入量調整用コック27や絞りが設けられる。
【0023】
具体的には、燃料供給経路6には、各バーナ2の燃料用切替弁16よりも燃料ガスの流れ方向下流側であって、かつバーナノズル5の上流側に、導入経路24の一端が接続され、この導入経路24の他端に接続された図示されない不活性ガス供給源から、Nガスなどの不活性ガスが燃料用切替弁16とバーナノズル5との間に導入されるようになっている。検出手段26は、通常のシーケンス制御もしくはコンピュータ制御で動作され、燃料用切替弁16、給気用切替弁14および排気用切替弁15の開閉状態を監視し、これら切替弁14〜16すべてが閉じられたときに検出信号を生成して、不活性ガス用切替弁25に出力する。これにより、不活性ガスの供給制御を自動化することができる。不活性ガス用切替弁25は、導入経路24を開閉するために開閉自在に構成され、検出手段26から上記検出信号が入力されたことに応じて導入経路24を開くようになっている。これにより、不活性ガスを必要なときに燃料供給経路6へ導入することができる。また、不活性ガス導入量調整用コック27は、不活性ガス供給源から燃料供給経路6への不活性ガスの導入流量を調整するために、開度調整可能に構成される。これにより、充填用流体を必要量だけ燃料供給経路6へ導入することができる。
【0024】
次に、本実施形態にかかるリジェネバーナ1の運転方法について説明する。リジェネバーナ1は上記従来技術で説明したように、負荷状態に応じて運転状態が切り換えられる。通常は複数組のすべてのバーナ2を稼働状態とし、燃料用切替弁16、給気用切替弁14および排気用切替弁15を開閉制御することにより、一対のバーナ2の一方に燃料ガスと燃焼用空気を供給して燃焼動作させると同時に、他方のバーナ2からは炉内の排ガスを吸引する吸引動作を行わせるようにし、この燃焼動作と吸引動作を各組一対のバーナ2相互で交互に択一的に行わせるようになっている。
【0025】
すなわち、リジェネバーナ1の運転に際しては、すべての電磁弁7,10,13を開くとともに給気ブロア9および排気ブロア12を駆動し、燃料供給経路6からバーナ2へ燃料ガスを供給するとともに、風量制御ベーン8で風量制御しつつ、給気経路3から燃焼用空気をバーナ2へ供給し、排気経路4から排ガスを排出する。この際、複数のバーナ2のうち、燃焼動作させるバーナ2では、その燃料用切替弁16および給気用切替弁14を開くとともに、排気用切替弁15を閉じ、また吸引動作させるバーナ2では、排気用切替弁15を開くとともに、燃料用切替弁16および給気用切替弁14を閉じる制御が実行され、蓄熱器17はバーナ2が吸引動作中であるか、燃焼動作中であるかに応じて、排ガスから排熱を回収したり、燃焼用空気を加熱する。
【0026】
他方、負荷が低下した場合などには、すべてのバーナ2を稼働状態とはせず、一部のバーナ2は、燃焼動作も吸引動作も行わない停止状態にする制御、例えば間引き制御が実行される。停止状態としたバーナ2では、それを制御する各切替弁14〜16がすべて閉じられ、これにより燃料ガスも燃焼用空気も供給されず、また排ガスの排出も停止される。このように複数のバーナ2のうち、一部は稼働状態としながら、残りは、その燃料用切替弁16、給気用切替弁14および排気用切替弁15のすべてを閉じることにより停止状態としてリジェネバーナ1を運転する際、本実施形態では、停止したバーナ2とその排気用切替弁15との間の排気経路4へ流体充填経路22から、充填用流体として給気経路3の燃焼用空気を導入するようになっている。
【0027】
具体的には、充填流体量調整用コック23を開くと、その開き量に応じて、稼働状態にあるバーナ2に向かって燃焼用空気を圧送している給気ブロア9からの燃焼用空気を、閉じられた給気用切替弁14より上流の給気経路3から流体充填経路22を介して、閉じられている排気用切替弁15とバーナ2との間の排気通路4へと導入することができる。これにより、蓄熱器17と排気用切替弁15との間の排気通路4内圧力を上昇させることができ、たとえ腐食により排気用切替弁15の閉め切り性能が劣化してリークを生ずるようなことがあっても、このリークに伴う排気経路4の負圧化を防止でき、これにより排ガスの排気経路4への流入を抑制してそれに伴う蓄熱器17低温側のオーバーヒートを抑制することができて、リジェネバーナ1の継続的な運転を保証することができる。充填される燃焼用空気は排ガスの濃度を希釈することもでき、排ガスの酸露点を下げることができて排気用切替弁15の腐食を防止することも可能である。
【0028】
通常は充填流体量調整用コック23を閉じておき、蓄熱器17低温側でオーバーヒートが頻発するようになったら、徐々に開いて、燃焼用空気を充填すればよい。燃焼用空気の充填量としては主に、リークがあってもそれに抗して排気経路4内圧力が負圧ならない程度の必要最小量に設定すればよい。充填流体量調整用コック23は、上記検出手段26からの検出信号が入力されることに応じて自動的に適宜開度で開かれるように設定してもよい。
【0029】
また本実施形態にあっては、流体導入経路20を備えていて、停止したバーナ2の排気用切替弁15下流側の排気経路4へ流体導入経路20から、希釈用の流体として給気経路3の燃焼用空気を導入するようになっている。具体的には、導入流体量調整用コック21を開くと、その開き量に応じて、稼働状態にあるバーナ2に向かって燃焼用空気を圧送している給気ブロア9からの燃焼用空気を、閉じられた給気用切替弁14より上流の給気経路3から流体導入経路20を介して、閉じられている排気用切替弁15より下流の排気通路4へと導入することができる。
【0030】
従来、排気経路4の配管に、硫酸による腐食が発生するという課題があった。この腐食の発生については、いくつかの原因があり、例えばリジェネバーナ1の運転制御に関連して引き起こされる場合があった。具体的に説明すると、リジェネバーナ1の高負荷運転状態では、吸引動作により蓄熱器17を出た直後の排ガスの温度は通常200℃前後に設定されていて、腐食を生ずることのない十分に高い温度設定がなされている。しかしながら、低負荷状態になると、排ガス温度は低下し、排気経路4を流通している間に酸露点以下になってしまう場合がある。また特に、負荷の低下によりリジェネバーナ1を間引き制御に移行させた場合、間引き制御の対象となった停止状態のバーナ2の排気経路4では、排気用切替弁15が閉じられて吸引動作が停止され、排ガスの流通が停止される。この吸引動作の停止によって排気用切替弁15の下流側に滞留した排ガスの温度は次第に下がっていき、そして間引き時間が長引けば長引くほどその温度が低下して、酸露点以下になってしまう。また他方、例えば配管構造上、排気経路4の配管長さが長ければ長いほど排ガス温度の低下傾向は顕著になり、酸露点以下に下がってしまうおそれがあった。これらいずれの原因にあっても、排気経路4中の排ガス温度が酸露点以下に至ることで硫酸分を生じ、これにより配管に腐食が発生していた。
【0031】
COGやMガスを燃焼させることで発生する排ガスの酸露点は、その濃度を希釈することによって低下させることができ、本実施形態にあっては、排気経路4への燃焼用空気の導入による排気用切替弁15下流側における排ガス濃度の希釈化により、硫酸の生成を押さえることができ、排気経路4の配管が腐食することを防止することができる。従ってまた、排気用切替弁15の腐食も防ぐことができる。また、流体導入経路20を介して排気用切替弁15下流側に燃焼用空気を導入することにより、排気用切替弁15周囲の排気経路4の内圧を高めて排気用切替弁15からのリークを抑えることができ、この面からも蓄熱器17低温側でのオーバーヒートを抑制することができる。
【0032】
燃焼用空気の導入量としては、排ガスの酸露点を、排気経路4の配管内温度よりも下げることができる必要最小量に設定すればよい。また導入流体量調整用コック21は、上記検出手段26からの検出信号が入力されることに応じて自動的に適宜開度で開かれるように設定してもよい。
【0033】
上記流体導入経路20および流体充填経路22いずれにあっても、これらを給気経路3に接続して燃焼用空気により希釈や充填を行うようにしたので、別途独立に経路を設備する場合に比べて、安価に構成することができる。
【0034】
さらに本実施形態にあっては、導入経路24を備えていて、停止したバーナ2とその燃料用切替弁16との間の燃料供給経路6へ導入経路24から不活性ガス、例えばNガスを導入するようになっている。具体的には、検出手段26により各切替弁14〜16が閉じられてバーナ2の停止状態が検出されるとこれに応じて自動的に不活性ガス用切替弁25が開かれ、これにより不活性ガス導入量調整用コック27の開度に応じて、不活性ガスが不活性ガス供給源から導入経路24を介して、閉じられている燃料用切替弁16とバーナ2との間の燃料供給通路6へと導入される。
【0035】
従来、排ガスが燃料供給経路6へと侵入して、硫酸により燃料供給経路6の配管に腐食が発生するおそれがあった。そしてこの腐食の原因となる排ガスの燃料供給経路6への侵入が、リジェネバーナ1の運転制御に関連して引き起こされる場合があった。例えば、負荷の低下によりリジェネバーナ1を間引き制御に移行させた場合、間引き制御の対象となったバーナ2の燃料用切替弁16が閉じられるが、この閉止された燃料用切替弁16とバーナ2との間の燃料供給経路6に、炉内に晒されているバーナノズル5から炉内の排ガスが侵入して拡散する。このバーナノズル5は上述したように冷却されるため、この冷却によってバーナノズル5と燃料用切替弁16との間の配管部分に拡散した排ガスはその温度が酸露点以下に低下し、この結果バーナノズル5やその周辺の配管、燃料用切替弁16などに腐食を生じさせてしまう。燃料用切替弁16が腐食するとその閉め切り性能が劣化して、リジェネバーナ1の切替動作不良を引き起こしやすくなる。そしてこの燃料供給経路6の腐食の問題は特に、バーナノズル5の口径が大きい場合に顕著であった。バーナノズル5の口径は、発熱量が小さく燃焼に大流量を要する燃料、例えば上記COGやMガスなどを使用する場合、また、鉄鋼加熱炉用など燃料流量として600万kcal/hにも達する場合などに、大きく設計される。そしてこのような大口径のバーナノズル5では排ガスが侵入して拡散しやすく、上記問題が起こる可能性が高かった。
【0036】
本実施形態にあっては、バーナ2と燃料用切替弁16との間の燃料供給経路6へ不活性ガスを導入することができるので、排ガスがバーナノズル5から侵入するのを抑制できるとともに、当該不活性ガスによって燃料供給経路6内の排ガスの濃度を希釈してその酸露点を下げることができ、バーナノズル5やその周辺の配管、燃料用切替弁16などが腐食することを防止することができる。また、不活性ガスを燃料供給経路6へ導入するようにしたので、安全性を確保することができる。不活性ガスの導入量もしくは導入速度としては、排ガスの酸露点を、燃料供給経路6の配管内温度よりも下げることができる程度、もしくはバーナノズル5からの排ガスの侵入速度を超える程度に設定すればよい。
【0037】
上記実施形態にあっては、流体導入経路20および流体充填経路22を給気経路3に接続する場合を例にとって説明したが、これに限定されることはなく、また使用流体も燃焼用空気に限られるものではなくて、独立に経路を設け、また流体として外気などを導入するようにしてもよいことはもちろんである。また、不活性ガス導入量調整用コック27は、不活性ガス用切替弁25によって不活性ガスの供給・停止を切り替えることができるので、必須の要素ではなく、必要に応じて備えればよい。
【0038】
さらに、上記実施形態で説明した導入流体量調整用コック21、充填流体量調整用コック23および不活性ガス用切替弁25は排気経路4および燃料供給経路6の状況に応じて、択一的に開いても、あるいはいずれか2つ、さらにはすべてを同時に開くようにしてもよく、これら導入流体量調整用コック21、充填流体量調整用コック23および不活性ガス用切替弁25の開閉操作の連携や不活性ガス導入量調整用コック27の調整による燃焼用空気の排気経路4への導入や充填、不活性ガスの燃料供給経路6への導入によって配管各部の腐食や各切替弁14〜16の性能劣化などを効果的に防ぐことができ、これによりリジェネバーナ1の適正な稼働を保証することができる。
【0039】
【発明の効果】
以上要するに、本発明にかかる排気経路に充填用流体を充填する経路を接続したリジェネバーナおよびその運転方法にあっては、排気経路の配管に取り付けられている排気用切替弁の腐食のためにリジェネバーナの運転に支障をきたすことを防止することができる。
【図面の簡単な説明】
【図1】本発明にかかる排気経路に充填用流体を充填する経路を接続したリジェネバーナの好適な一実施形態を示す系統図である。
【図2】従来のリジェネバーナを示す系統図である。
【符号の説明】
1 リジェネバーナ
2 バーナ
3 給気経路
4 排気経路
6 燃料供給経路
14 給気用切替弁
15 排気用切替弁
16 燃料用切替弁
22 流体充填経路
23 充填流体量調整用コック
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a regenerative burner in which a path for charging a filling fluid is connected to an exhaust path, which can prevent the operation of the regenerative burner from being hindered due to corrosion of an exhaust switching valve attached to a pipe of the exhaust path. And its operation method.
[0002]
[Prior art]
As is well known, a regenerative burner is provided with a plurality of sets of a pair of burners arranged facing each other toward the inside of the furnace, each of these burners is provided with a regenerator, and a pair of burners is provided. At the same time, fuel gas and combustion air are supplied to one side to perform combustion, and at the same time, exhaust gas is sucked from the other burner, and this combustion operation and suction operation are alternately performed by each pair of burners. The exhaust heat is recovered from the exhaust gas by the regenerator during the suction operation, and the combustion air is heated by the exhaust heat recovered by the regenerator during the combustion operation, thereby saving energy.
[0003]
A system for supplying and discharging combustion air and exhaust gas to the burner b in the conventional regenerative burner a will be described according to the operating state of the burner b with reference to FIG. 2. It is supplied to burner b. When the air supply solenoid valve e provided on the upstream side of the branch portion d of the air supply path c connected to another burner is opened, the combustion air is supplied while the air volume is controlled by the air supply volume control vane f. The gas is introduced into the air supply path c by the blower g, and further, by opening the air supply switching valve h of each burner b provided on the downstream side of the branch portion d, the gas passes through the regenerator i and is heated to the burner b. Supplied. The fuel gas is introduced by opening the fuel solenoid valve l provided on the upstream side of the branch k of the fuel supply path j connected to another burner, and furthermore, each burner b provided downstream of the branch k. Is opened, the fuel is supplied to the burner nozzle n of the burner b. As the fuel gas, a coke oven gas (hereinafter, referred to as COG), a gas obtained by mixing COG with a blast furnace gas or a converter gas (hereinafter, referred to as M gas), or the like is used. During this combustion operation, the exhaust path o is closed by the exhaust switching valve p of each burner b.
[0004]
On the other hand, during the suction operation, the exhaust gas is discharged from the furnace. The exhaust gas passes through the exhaust switching valve p of each burner provided on the upstream side of the branch q while the exhaust electromagnetic valve r on the downstream side of the branch q of the exhaust path o connected to another burner is opened. By being opened, the exhaust air is controlled by the exhaust air flow control vanes s while being exhausted and recovered through the regenerator i, and is sucked from the furnace by the exhaust blower t. During this suction operation, the air supply path c and the fuel supply path j are closed by the switching valves h and m. Further, a cooling medium supply system u and a cooling medium discharge system v are connected to the burner b in order to allow a cooling medium such as water or air to flow through the burner nozzle n for cooling.
[0005]
A typical control method of the regenerative burner a that controls a plurality of sets of burners b is “proportional control” in which all burners b are proportionally turned down (increase or decrease the thermal power) until the load is about 100% to 30%. For the turndown with a load less than that, execute “time proportional ON-OFF control” for all burners b to start and stop them at appropriate intervals. When the temperature decreases, a method of executing “thinning control” in which some of the burners b are stopped is performed. In the burner b in the stopped state subjected to the thinning control, not only the combustion operation but also the suction operation is stopped, and the switching valves m, h, and p for controlling the burner b are all closed.
[0006]
[Problems to be solved by the invention]
Incidentally, in the exhaust gas after burning a fuel gas such as a COG or M gas described above, it includes SO 2. When the temperature of the exhaust gas falls below the acid dew point (generally 130 ° C. to 140 ° C. for desulfurized COG combustion exhaust gas), the SO 2 condenses and reacts with water (H 2 O) to produce sulfuric acid (H 2 SO 4 ). Is generated. Conventionally, the sulfuric acid causes corrosion in the exhaust switching valve p attached to the pipe of the exhaust path o, and the corrosion of the exhaust switching valve p hinders the operation of the regenerative burner a. There was a problem that there was a possibility of causing.
[0007]
For example, if the closing performance of the exhaust switching valve p is deteriorated due to corrosion, and if the exhaust path o of the burner b to be thinned out is not properly shut off during thinning control or the like and a leak occurs, the exhaust blower The low temperature side of the regenerator i of the burner b is liable to be in a negative pressure state due to the suction effect of t, whereby the exhaust gas in the furnace continues to flow from the burner b to the exhaust path o, and the pipe temperature including the area around the regenerator i Excessively rises, and as a result, the overheat of the low temperature side of the regenerator i for which the upper limit temperature limit is set by the limiter is caused, and the limiter is activated as soon as the burner b is released from the thinning control target and the combustion operation is started. It is assumed that the operation of the regenerating burner a cannot be continued.
[0008]
The present invention has been made in view of the above-mentioned conventional problems, and it is possible to prevent an exhaust gas from being hindered from operating due to corrosion of an exhaust switching valve attached to a pipe of an exhaust path. An object of the present invention is to provide a regenerative burner in which a path for filling a filling fluid is connected to the path, and an operation method thereof.
[0009]
[Means for Solving the Problems]
A plurality of regenerative burners, each having an exhaust path according to the present invention connected to a path for filling a filling fluid, are installed toward a furnace in which exhaust gas containing SO 2 components is generated, and a fuel gas is supplied from a fuel supply path during a combustion operation. The burner is supplied with combustion air from an air supply path and discharges exhaust gas to an exhaust path during a suction operation, and the fuel supply path, the air supply path, and the exhaust path are respectively provided corresponding to each burner, A fuel switching valve, an air supply switching valve, and an exhaust switching valve that are opened / closed to switch between a combustion operation and a suction operation of the burner. In a regenerative burner in which all of the fuel switching valve, the air supply switching valve, and the exhaust switching valve are closed and stopped, the exhaust gas between each burner and the exhaust switching valve is closed. A fluid filling path for filling a fluid is connected to the air path. As a result, it is possible to prevent the operation of the regenerating burner from being hindered due to corrosion of the exhaust gas switching valve attached to the exhaust path piping.
[0010]
Further, the fluid filling path is provided with flow rate adjusting means for adjusting a flow rate of the filling fluid. This makes it possible to introduce a required amount of the filling fluid into the exhaust path.
[0011]
Further, the fluid filling path is connected to the supply path upstream of each supply switching valve, and combustion air in the supply path is introduced as a filling fluid. Thereby, equipment can be provided at low cost.
[0012]
In addition, the method for operating a regenerative burner according to the present invention is provided such that a plurality of regenerative burners are installed toward a furnace in which exhaust gas containing SO 2 components is generated, and during combustion operation, fuel gas is supplied from a fuel supply path and combustion is performed from an air supply path. And a burner that supplies exhaust air and discharges exhaust gas to an exhaust path during a suction operation, and is provided in correspondence with each burner in the fuel supply path, the air supply path, and the exhaust path. A switching valve for fuel, a switching valve for air supply, and a switching valve for exhaust, which are opened and closed to switch between the burner and the fuel supply switching valve. In the regenerative burner operating method in which all of the air switching valve and the exhaust switching valve are closed and the operation is stopped, the burner stopped when the burner was stopped. A fluid is filled into the exhaust path between the exhaust gas and the exhaust switching valve. As a result, it is possible to prevent the operation of the regenerating burner from being hindered due to corrosion of the exhaust gas switching valve attached to the exhaust path piping.
[0013]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, a preferred embodiment of a regenerative burner in which a path for charging a filling fluid is connected to an exhaust path according to the present invention and a method for operating the regenerative burner will be described in detail with reference to the accompanying drawings. FIG. 1 shows a preferred embodiment of a regenerative burner 1 according to the present invention. The basic configuration of a supply / discharge system for combustion air, fuel gas, and exhaust gas in the regenerative burner 1 of the present embodiment is almost the same as the conventional technology shown in FIG. The regenerative burner 1 includes a plurality of pairs of burners 2 (one burner 2 is shown in FIG. 1), which are arranged in a furnace so as to face each other.
[0014]
The plurality of burners 2 are connected to an air supply path 3 for collectively supplying combustion air thereto and an exhaust path 4 for collectively discharging exhaust gas in the furnace therefrom. The supply path 3 and the exhaust path 4 are provided with branch portions 3a and 4a for connecting them to the respective burners 2. Further, a fuel supply path 6 for collectively supplying a fuel gas such as COG or M gas to a burner nozzle 5 provided in each of the plural sets of the plurality of burners 2 is connected. Also, a branch 6a for connecting this to each burner is provided.
[0015]
The air supply path 3 has a solenoid valve 7 for opening and closing the air supply path 3 that opens and closes the air supply path 3 upstream of the branch portion 3 a in the flow direction of the combustion air, and a supply air supply that controls the air volume of the combustion air. An air volume control vane 8 and an air supply blower 9 for feeding combustion air to each burner 2 via the air supply path 3 are provided. Similarly, the exhaust passage 4 has an exhaust solenoid valve 10 that can be opened and closed to open and close the exhaust passage 4, and an exhaust air volume control vane 11 that controls the air volume of the exhaust gas, on the downstream side of the branch portion 4 a in the exhaust gas flow direction. And an exhaust blower 12 for sucking exhaust gas from the furnace through the exhaust path 4. The fuel supply path 6 is provided with an openable and closable fuel solenoid valve 13 for opening and closing the fuel supply path 6 on the upstream side of the branch portion 6a in the fuel gas flow direction.
[0016]
Further, the air supply path 3 is provided with an air supply switching valve 14 that can be opened and closed to switch between supply and stop of the combustion air to each of the burners 2 downstream of the branch portion 3a. Further, the exhaust path 4 is provided with an openable and closable exhaust switching valve 15 for switching between discharge and stop of exhaust gas from each burner 2 on the upstream side of the branching portion 4a. Further, the fuel supply path 6 is provided with a fuel switching valve 16 that can be opened and closed to switch between supply and stop of fuel gas to each of the burner nozzles 5 downstream of the branch portion 6a. The air supply path 3 and the exhaust path 4 are gathered before the connection position with each burner 2 and are connected to the burner 2 collectively.
[0017]
Each burner 2 is disposed between a burner nozzle 5 and an air supply path 3 and an exhaust path 4 which are gathered, and recovers exhaust heat from exhaust gas passing therethrough and discharged from the furnace to the exhaust path 4. Further, a regenerator 17 is provided for heating the combustion air supplied from the air supply path 3 to the burner 2 through the air supply path 3 with the recovered exhaust heat. Further, a cooling medium supply system 18 and a cooling medium discharge system 19 are connected to each burner 2 in order to allow a cooling medium such as water or air to flow through the burner nozzles 5 for cooling.
[0018]
In addition, the regenerative burner 1 in which the path for filling the filling fluid is connected to the exhaust path according to the present embodiment basically transmits the fluid to the exhaust path 4 between each burner 2 and the exhaust switching valve 15. A fluid filling path 22 for filling is connected. The fluid filling path 22 is provided with a filling fluid amount adjusting cock 23 and a throttle as flow rate adjusting means for adjusting the flow rate of the filling fluid, and more preferably, the fluid filling path 22 is provided with a switching valve for each air supply. 14 is connected to the supply path 3 on the upstream side, and combustion air in the supply path 3 is introduced as a filling fluid.
[0019]
More specifically, according to the illustrated example, one end of the fluid charging path 22 is provided in the exhaust path 4 on the upstream side in the exhaust gas flow direction from the exhaust switching valve 15 of each burner 2 and on the low temperature side of the regenerator 17. The other end of the fluid filling path 22 is connected to the fluid introduction path 20 at a position upstream of the introduction fluid amount adjusting cock 21 of the same burner 2 in the flow direction of the combustion air. Thus, the combustion air being pumped by the air supply blower 9 is filled between the exhaust switching valve 15 and the regenerator 17. Further, the filling fluid amount adjusting cock 23 is configured to be capable of adjusting the opening degree in order to adjust the filling flow rate of the combustion air from the air supply passage 3 to the exhaust passage 4. As a result, a required amount of combustion air can be introduced into the exhaust path 4.
[0020]
In the present embodiment, a fluid introduction path 20 for introducing a fluid for dilution is connected to the exhaust path 4 on the downstream side of the exhaust switching valve 15 of each burner 2. In addition, the fluid introduction path 20 is provided with an introduction fluid amount adjusting cock 21 and a throttle as flow rate adjusting means for adjusting the flow rate of the dilution fluid. More preferably, the fluid introduction path 20 is provided with a switching valve for each air supply. 14 is connected to the air supply path 3 on the upstream side, and the combustion air in the air supply path 3 is introduced as a dilution fluid.
[0021]
Specifically, one end of the fluid introduction path 20 is connected to the exhaust path 4 at a position downstream of the exhaust switching valve 15 of each burner 2 in the exhaust gas flow direction and at an upstream position of the branch portion 4a. The other end of the fluid introduction path 20 is connected to the air supply path 3 at a position upstream of the air supply switching valve 14 of the same burner 2 in the flow direction of the combustion air and at a downstream position of the branch portion 3a. Thus, the combustion air being pressure-fed by the air supply blower 9 is introduced into the exhaust path 4 downstream of the exhaust switching valve 15. Further, the introduction fluid amount adjusting cock 21 is configured to be capable of adjusting the opening degree in order to adjust the introduction flow rate of the combustion air from the air supply passage 3 to the exhaust passage 4. As a result, a required amount of combustion air can be introduced into the exhaust path 4.
[0022]
Further, in the present embodiment, an introduction path 24 for introducing an inert gas is connected to the fuel supply path 6 between each burner 2 and its fuel switching valve 16. In the introduction path 24, an inert gas switching valve 25 is provided as switching means for switching the introduction / stop of the inert gas into the fuel supply path 6. A detection means 26 for detecting that all of the fuel switching valve 16, the air supply switching valve 14, and the exhaust switching valve 15 are closed and outputting a detection signal is connected to the inert gas switching valve 25. The inert gas switching valve 25 is configured to introduce an inert gas into the fuel supply path 6 when a detection signal is input from the detection means 26. In addition, the introduction path 24 is provided with an inert gas introduction amount adjusting cock 27 and a throttle as flow rate adjusting means for adjusting the flow rate of the inert gas.
[0023]
Specifically, one end of the introduction path 24 is connected to the fuel supply path 6 on the downstream side in the fuel gas flow direction from the fuel switching valve 16 of each burner 2 and on the upstream side of the burner nozzle 5. An inert gas such as N 2 gas is introduced between the fuel switching valve 16 and the burner nozzle 5 from an unillustrated inert gas supply source connected to the other end of the introduction path 24. . The detection means 26 is operated under normal sequence control or computer control, monitors the open / close state of the fuel switching valve 16, the air supply switching valve 14, and the exhaust switching valve 15, and closes all of these switching valves 14 to 16. When it is detected, a detection signal is generated and output to the inert gas switching valve 25. Thereby, the supply control of the inert gas can be automated. The inert gas switching valve 25 is configured to be openable and closable to open and close the introduction path 24, and opens the introduction path 24 in response to the detection signal being input from the detection unit 26. Thus, the inert gas can be introduced into the fuel supply path 6 when necessary. The inert gas introduction amount adjusting cock 27 is configured to be capable of adjusting the opening degree in order to adjust the introduction flow rate of the inert gas from the inert gas supply source to the fuel supply path 6. Thereby, the required amount of the filling fluid can be introduced into the fuel supply path 6.
[0024]
Next, an operation method of the regenerative burner 1 according to the present embodiment will be described. The operating state of the regenerative burner 1 is switched according to the load state, as described in the related art. Normally, by setting all the burners 2 in a plurality of operating states and controlling the opening and closing of the fuel switching valve 16, the air supply switching valve 14, and the exhaust switching valve 15, the fuel gas and the combustion gas are supplied to one of the pair of burners 2. At the same time as supplying air for combustion and performing a burning operation, a suction operation for sucking exhaust gas in the furnace is performed from the other burner 2, and the combustion operation and the suction operation are alternately performed by a pair of the burners 2 in each set. It is designed to be performed alternatively.
[0025]
That is, when the regenerative burner 1 is operated, all the solenoid valves 7, 10, 13 are opened and the air supply blower 9 and the exhaust blower 12 are driven to supply the fuel gas from the fuel supply path 6 to the burner 2 and to reduce the air volume. While controlling the air volume by the control vane 8, the combustion air is supplied from the air supply path 3 to the burner 2, and the exhaust gas is discharged from the exhaust path 4. At this time, of the plurality of burners 2, the burner 2 that performs combustion operation opens the fuel switching valve 16 and the air supply switching valve 14, closes the exhaust switching valve 15, and performs the suction operation. Control to open the exhaust switching valve 15 and close the fuel switching valve 16 and the air supply switching valve 14 is performed, and the regenerator 17 determines whether the burner 2 is performing the suction operation or the combustion operation. To recover the exhaust heat from the exhaust gas or heat the combustion air.
[0026]
On the other hand, when the load is reduced, all the burners 2 are not brought into the operating state, and some of the burners 2 are put into a stop state in which neither the combustion operation nor the suction operation is performed, for example, thinning control is performed. You. In the burner 2 in the stopped state, all the switching valves 14 to 16 for controlling the burner 2 are closed, so that neither the fuel gas nor the combustion air is supplied, and the discharge of the exhaust gas is stopped. As described above, while a part of the plurality of burners 2 is in the operating state, the remaining one is closed by closing all of the fuel switching valve 16, the air supply switching valve 14, and the exhaust switching valve 15. When the burner 1 is operated, in the present embodiment, the combustion air in the air supply path 3 is supplied as a filling fluid from the fluid filling path 22 to the exhaust path 4 between the stopped burner 2 and the exhaust switching valve 15. It is supposed to be introduced.
[0027]
Specifically, when the filling fluid amount adjusting cock 23 is opened, the combustion air from the air supply blower 9 that is forcing the combustion air toward the burner 2 in the operating state according to the opening amount. Introducing from the air supply path 3 upstream of the closed air supply switching valve 14 to the exhaust passage 4 between the closed exhaust gas switching valve 15 and the burner 2 via the fluid filling path 22. Can be. As a result, the pressure in the exhaust passage 4 between the regenerator 17 and the exhaust switching valve 15 can be increased, and even if the closing performance of the exhaust switching valve 15 is deteriorated due to corrosion, a leak may occur. Even so, it is possible to prevent the exhaust path 4 from becoming negative pressure due to this leak, thereby suppressing the flow of exhaust gas into the exhaust path 4 and suppressing the overheating on the low temperature side of the regenerator 17 due to this. Continuous operation of the regenerating burner 1 can be guaranteed. The filled combustion air can also dilute the concentration of the exhaust gas, lower the acid dew point of the exhaust gas, and prevent the exhaust switching valve 15 from being corroded.
[0028]
Normally, the filling fluid amount adjusting cock 23 is closed, and if overheating frequently occurs on the low-temperature side of the heat storage unit 17, it may be gradually opened and filled with combustion air. The filling amount of the combustion air may be set to a necessary minimum amount such that the pressure in the exhaust passage 4 does not become negative even if there is a leak. The filling fluid amount adjusting cock 23 may be set so as to be automatically opened at an appropriate opening in response to the detection signal from the detecting means 26 being input.
[0029]
Further, in this embodiment, a fluid introduction path 20 is provided, and the supply path 3 is used as a dilution fluid from the fluid introduction path 20 to the exhaust path 4 on the downstream side of the exhaust switching valve 15 of the burner 2 that has stopped. The air for combustion is introduced. Specifically, when the introduction fluid amount adjusting cock 21 is opened, the combustion air from the air supply blower 9 that is forcing the combustion air toward the burner 2 in the operating state according to the opening amount. The fluid can be introduced from the supply path 3 upstream of the closed supply switching valve 14 to the exhaust passage 4 downstream of the closed exhaust switching valve 15 via the fluid introduction path 20.
[0030]
Conventionally, there has been a problem that corrosion due to sulfuric acid occurs in the piping of the exhaust path 4. There are several causes for the occurrence of the corrosion, for example, the corrosion may be caused in connection with the operation control of the regenerative burner 1. More specifically, in the high-load operation state of the regenerative burner 1, the temperature of the exhaust gas immediately after leaving the regenerator 17 by the suction operation is usually set to about 200 ° C., and is sufficiently high without causing corrosion. The temperature has been set. However, when the load becomes low, the temperature of the exhaust gas decreases, and sometimes drops below the acid dew point while flowing through the exhaust path 4. In particular, when the regenerative burner 1 is shifted to the thinning control due to a decrease in the load, the exhaust switching valve 15 is closed and the suction operation is stopped in the exhaust path 4 of the burner 2 in the stopped state, which is the target of the thinning control. Then, the flow of the exhaust gas is stopped. Due to the stop of the suction operation, the temperature of the exhaust gas that has accumulated on the downstream side of the exhaust switching valve 15 gradually decreases, and the longer the thinning time, the lower the temperature and the temperature becomes lower than the acid dew point. On the other hand, for example, due to the piping structure, the longer the piping length of the exhaust path 4 is, the more the exhaust gas temperature tends to decrease, and there is a possibility that the exhaust gas temperature may drop below the acid dew point. Regardless of any of these causes, sulfuric acid was generated when the temperature of the exhaust gas in the exhaust path 4 reached the acid dew point or lower, thereby causing corrosion in the piping.
[0031]
The acid dew point of the exhaust gas generated by burning COG or M gas can be lowered by diluting the concentration, and in the present embodiment, the exhaust gas due to the introduction of combustion air into the exhaust path 4 is exhausted. By diluting the exhaust gas concentration on the downstream side of the switching valve 15, the generation of sulfuric acid can be suppressed, and the piping of the exhaust path 4 can be prevented from being corroded. Therefore, corrosion of the exhaust switching valve 15 can also be prevented. In addition, by introducing combustion air downstream of the exhaust switching valve 15 via the fluid introduction path 20, the internal pressure of the exhaust path 4 around the exhaust switching valve 15 is increased to reduce leakage from the exhaust switching valve 15. It is possible to suppress overheating on the low temperature side of the heat storage device 17 from this aspect as well.
[0032]
The introduction amount of the combustion air may be set to a necessary minimum amount that can lower the acid dew point of the exhaust gas below the temperature in the pipe of the exhaust path 4. The cock 21 for adjusting the amount of introduced fluid may be set so as to be automatically opened at an appropriate opening in response to a detection signal from the detection means 26 being input.
[0033]
Regardless of which of the fluid introduction path 20 and the fluid filling path 22 is used, these are connected to the air supply path 3 to perform dilution and filling with combustion air. Therefore, it can be configured at low cost.
[0034]
Further, in the present embodiment, an introduction path 24 is provided, and an inert gas such as N 2 gas is supplied from the introduction path 24 to the fuel supply path 6 between the stopped burner 2 and the fuel switching valve 16. It is supposed to be introduced. More specifically, when the switching valves 14 to 16 are closed by the detecting means 26 and the stop state of the burner 2 is detected, the inert gas switching valve 25 is automatically opened in response to this, whereby According to the opening degree of the cock 27 for adjusting the amount of the active gas introduced, the inert gas is supplied from the inert gas supply source via the introduction path 24 to the fuel supply between the closed fuel switching valve 16 and the burner 2. It is introduced into the passage 6.
[0035]
Conventionally, the exhaust gas may enter the fuel supply path 6 and cause corrosion of the piping of the fuel supply path 6 due to sulfuric acid. In some cases, intrusion of the exhaust gas causing the corrosion into the fuel supply path 6 is caused in connection with the operation control of the regenerative burner 1. For example, when the regenerative burner 1 is shifted to the thinning control due to a decrease in load, the fuel switching valve 16 of the burner 2 subjected to the thinning control is closed, and the closed fuel switching valve 16 and the burner 2 are closed. Exhaust gas in the furnace intrudes from the burner nozzle 5 exposed in the furnace and diffuses into the fuel supply path 6 between the furnace. Since the burner nozzle 5 is cooled as described above, the temperature of the exhaust gas diffused into the pipe portion between the burner nozzle 5 and the fuel switching valve 16 due to the cooling is reduced to the acid dew point or lower, and as a result, the burner nozzle 5 Corrosion is caused in the surrounding pipes, the fuel switching valve 16 and the like. If the fuel switching valve 16 is corroded, the closing performance of the fuel switching valve 16 is degraded, and the switching operation failure of the regenerating burner 1 is easily caused. The problem of corrosion of the fuel supply path 6 was particularly remarkable when the burner nozzle 5 had a large diameter. The caliber of the burner nozzle 5 is small when the calorific value is small, and a fuel requiring a large flow rate for combustion, such as the above-mentioned COG or M gas, or when the fuel flow rate for a steel heating furnace reaches 6 million kcal / h, etc. It is designed to be large. In such a large-diameter burner nozzle 5, exhaust gas easily enters and diffuses, and the possibility of the above-described problem is high.
[0036]
In the present embodiment, since the inert gas can be introduced into the fuel supply path 6 between the burner 2 and the fuel switching valve 16, the exhaust gas can be prevented from entering from the burner nozzle 5, and The concentration of the exhaust gas in the fuel supply path 6 can be diluted by the inert gas to lower the acid dew point, and the burner nozzle 5 and its surrounding piping, the fuel switching valve 16 and the like can be prevented from being corroded. . In addition, since the inert gas is introduced into the fuel supply path 6, safety can be ensured. The introduction amount or introduction speed of the inert gas is set so that the acid dew point of the exhaust gas can be set lower than the temperature in the pipe of the fuel supply path 6, or more than the intrusion speed of the exhaust gas from the burner nozzle 5. Good.
[0037]
In the above embodiment, the case where the fluid introduction path 20 and the fluid filling path 22 are connected to the air supply path 3 has been described as an example. However, the present invention is not limited to this, and the fluid used is also combustion air. It is needless to say that the present invention is not limited to this. For example, an independent path may be provided, and outside air may be introduced as a fluid. In addition, the inert gas introduction amount adjusting cock 27 can be switched between supply and stop of the inert gas by the inert gas switching valve 25. Therefore, the cock 27 is not an essential element and may be provided as necessary.
[0038]
Further, the cock 21 for adjusting the amount of the introduced fluid, the cock 23 for adjusting the amount of the filled fluid, and the switching valve 25 for the inert gas, which have been described in the above embodiment, are alternatively provided according to the conditions of the exhaust path 4 and the fuel supply path 6. It may be opened, or any two or even all of them may be opened at the same time. The opening / closing operation of the introduction fluid amount adjusting cock 21, the filling fluid amount adjusting cock 23, and the inert gas switching valve 25 is performed. The introduction and filling of the combustion air into the exhaust path 4 by the coordination and the adjustment of the inert gas introduction amount adjusting cock 27 and the introduction of the inert gas into the fuel supply path 6 corrode the pipes and cause the switching valves 14 to 16. Thus, it is possible to effectively prevent the performance of the regenerative burner 1 from being deteriorated, so that the proper operation of the regenerative burner 1 can be guaranteed.
[0039]
【The invention's effect】
In short, in the regenerative burner and the operation method thereof according to the present invention in which the path for filling the filling fluid is connected to the exhaust path, the regenerative burner is attached to the exhaust path piping due to corrosion. It is possible to prevent the operation of the burner from being hindered.
[Brief description of the drawings]
FIG. 1 is a system diagram showing a preferred embodiment of a regenerative burner in which a path for filling a filling fluid is connected to an exhaust path according to the present invention.
FIG. 2 is a system diagram showing a conventional regenerative burner.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Regenerative burner 2 Burner 3 Air supply path 4 Exhaust path 6 Fuel supply path 14 Air supply switching valve 15 Exhaust switching valve 16 Fuel switching valve 22 Fluid filling path 23 Filling fluid amount adjusting cock

Claims (4)

SO成分を含む排ガスが発生する炉内に向けて複数設置され、燃焼動作時には燃料供給経路から燃料ガスが供給されるとともに給気経路から燃焼用空気が供給され、吸引動作時には排気経路へ排ガスを排出するバーナと、これら燃料供給経路、給気経路および排気経路にそれぞれ、各バーナに対応させて設けられ、該バーナの燃焼動作と吸引動作とを切り換えるべく開閉される燃料用切替弁、給気用切替弁および排気用切替弁とを備え、複数のバーナのうち、一部は稼働状態としながら、残りは、その燃料用切替弁、給気用切替弁および排気用切替弁のすべてを閉じて停止状態とするリジェネバーナにおいて、各バーナとその排気用切替弁との間の上記排気経路に、流体を充填するための流体充填経路を接続したことを特徴とする排気経路に充填用流体を充填する経路を接続したリジェネバーナ。Towards a furnace exhaust gas is generated containing SO 2 component is more established, during the combustion operation is supplied with combustion air from the air supply path together with the fuel gas is supplied from the fuel supply path, the exhaust gas during the suction operation to the exhaust passage And a fuel switching valve, which is provided in the fuel supply path, the air supply path, and the exhaust path in correspondence with each burner, and is opened / closed to switch the combustion operation and the suction operation of the burner. A switching valve for air and a switching valve for exhaust are provided, and some of the plurality of burners are in an operating state, while the rest closes all of the switching valve for fuel, the switching valve for air supply, and the switching valve for exhaust. In a regenerative burner which is brought into a stopped state, a fluid filling path for filling a fluid is connected to the exhaust path between each burner and its exhaust switching valve. A regenerative burner connected to a path for filling a filling fluid. 前記流体充填経路には、充填用流体の流量を調整する流量調整手段が設けられていることを特徴とする請求項1に記載の排気経路に充填用流体を充填する経路を接続したリジェネバーナ。The regenerative burner according to claim 1, wherein a flow rate adjusting means for adjusting a flow rate of the filling fluid is provided in the fluid filling path. 前記流体充填経路が、各給気用切替弁上流側の前記給気経路に接続され、充填用流体として上記給気経路の燃焼用空気が導入されることを特徴とする請求項1または2に記載の排気経路に充填用流体を充填する経路を接続したリジェネバーナ。The fluid filling path is connected to the supply path upstream of each supply switching valve, and combustion air in the supply path is introduced as a filling fluid. A regenerating burner in which a path for filling a filling fluid is connected to the exhaust path described in the above. SO成分を含む排ガスが発生する炉内に向けて複数設置され、燃焼動作時には燃料供給経路から燃料ガスが供給されるとともに給気経路から燃焼用空気が供給され、吸引動作時には排気経路へ排ガスを排出するバーナと、これら燃料供給経路、給気経路および排気経路にそれぞれ、各バーナに対応させて設けられ、該バーナの燃焼動作と吸引動作とを切り換えるべく開閉される燃料用切替弁、給気用切替弁および排気用切替弁とを備え、複数のバーナのうち、一部は稼働状態としながら、残りは、その燃料用切替弁、給気用切替弁および排気用切替弁のすべてを閉じて停止状態とする運転が行われるリジェネバーナの運転方法において、バーナを停止状態にしたときに、停止したバーナとその排気用切替弁との間の上記排気経路へ流体を充填するようにしたことを特徴とするリジェネバーナの運転方法。Towards a furnace exhaust gas is generated containing SO 2 component is more established, during the combustion operation is supplied with combustion air from the air supply path together with the fuel gas is supplied from the fuel supply path, the exhaust gas during the suction operation to the exhaust passage And a fuel switching valve, which is provided in the fuel supply path, the air supply path, and the exhaust path in correspondence with each burner, and is opened / closed to switch the combustion operation and the suction operation of the burner. A switching valve for air and a switching valve for exhaust are provided, and some of the plurality of burners are in an operating state, while the rest closes all of the switching valve for fuel, the switching valve for air supply, and the switching valve for exhaust. In a regenerative burner operating method in which the burner is brought into a stopped state, when the burner is brought into a stopped state, a fluid is filled in the exhaust path between the stopped burner and its exhaust switching valve. A method for operating a regenerative burner, characterized in that the regenerative burner is charged.
JP2002177050A 2002-06-18 2002-06-18 Regenerative burner and its operation method Expired - Lifetime JP3973494B2 (en)

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