JPH06271855A - Estimation of deterioration degree of carbonization chamber in unit coke oven group - Google Patents

Estimation of deterioration degree of carbonization chamber in unit coke oven group

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Publication number
JPH06271855A
JPH06271855A JP5870393A JP5870393A JPH06271855A JP H06271855 A JPH06271855 A JP H06271855A JP 5870393 A JP5870393 A JP 5870393A JP 5870393 A JP5870393 A JP 5870393A JP H06271855 A JPH06271855 A JP H06271855A
Authority
JP
Japan
Prior art keywords
gas
coke oven
chamber
carbonization chamber
combustion
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
JP5870393A
Other languages
Japanese (ja)
Inventor
Kyozo Igai
猪飼恭三
Shoichi Yamaguchi
山口彰一
Tatsuya Kudo
工藤達也
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 JP5870393A priority Critical patent/JPH06271855A/en
Publication of JPH06271855A publication Critical patent/JPH06271855A/en
Pending legal-status Critical Current

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  • Coke Industry (AREA)

Abstract

PURPOSE:To accurately estimate the subject deterioration degree by measuring the contents of S, N2, O2 or H2, etc., in a fuel, etc., supplied to each combustion chamber of each oven group of a coke oven and the contents of these gas components in the combustion exhaust gas and grasping the change of the ratio or difference between the measured values. CONSTITUTION:A gas-supplying pipe 7 and a gas exhaustion pipe 8 are attached to each oven group unit of a coke oven 1 and each pipe is provided with a gas sampling pipe 10, a gas component analyzer 11 and a gas flow meter 12. Contents of one or more components selected from sulfur, nitrogen, oxygen and hydrogen in the fuel and/or combustion-supporting material to be supplied to each combustion chamber of each cake oven unit of the coke oven 1 and contents of one or more components selected from sulfur, nitrogen, oxygen and hydrogen in the combustion exhaust gas are sampled with the gas sampling pipes 10 attached to the gas supplying pipe 7 and the gas exhaustion pipe 8 and measured by the gas component analyzers 11. The ratio or the difference between both measured values is calculated to accurately estimate the deterioration degree of the carbonization chamber of each coke oven unit. The repairing cost can be reduced by efficiently repairing the chamber.

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、多数の炭化室からなる
コークス炉の炉団単位の気密性能、具体的には各炭化室
の劣化度の評価方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for evaluating the airtightness of a coke oven unit having a large number of carbonization chambers, specifically, the degree of deterioration of each carbonization chamber.

【0002】[0002]

【従来の技術】一般に工業用の室炉式コークス炉は、例
えば、50門前後のそれぞれ独立した炭化室と燃焼室を
交互に隣接させて構成して1炉団とし、炉団単位で燃焼
室への燃料ガスと燃料支燃物の供給とガス切替えを、例
えば、20〜30分毎に行い、燃焼排ガスは煙道、煙突
を介して排出される。また、炭化室はコークスの押出側
と押出される側に炉蓋を着脱自在に装備されており、各
炭化室へは、例えば、2〜5門毎に間隔をおいて、炭化
室への石炭装入、乾留、コークス排出等の異なる作業を
配置することで炉団単位の温度分布の均等化を図ってい
る。
2. Description of the Related Art Generally, an industrial chamber furnace type coke oven comprises, for example, an independent carbonization chamber and a combustion chamber of about 50 gates, which are alternately adjacent to each other to form one furnace group. The fuel gas and the fuel-supporting substance are supplied and the gas is switched, for example, every 20 to 30 minutes, and the combustion exhaust gas is discharged through the flue and the chimney. Further, the carbonization chamber is detachably equipped with a furnace lid on the extrusion side of the coke and the extrusion side of the coke. By arranging different operations such as charging, carbonization, and discharge of coke, the temperature distribution of each furnace group is equalized.

【0003】上記室炉式コークス炉を管理する上で最も
重要な事は、装入した石炭を乾留してコークスにするた
めの炭化室の気密性能の維持である。炭化室の気密性が
劣化する原因としては、炭化室と燃焼室を区切ってい
る、耐火煉瓦製壁の加熱冷却の繰り返しに起因する膨張
収縮による煉瓦目地切れにより、炭化室と燃焼室が通気
状態となること、また、各炭化室の両側に着脱自在に設
けた炉蓋の熱変形、付着物等に起因するシール不良によ
って炭化室と炉外が通気状態となること等があり、これ
らの気密性の劣化は炉稼働率によって若干異なるが、操
業を継続することによって短期的あるいは長期的な間隔
で不可避的に発生する。
The most important thing in managing the above-mentioned chamber furnace type coke oven is to maintain the airtightness of the carbonization chamber for carbonizing the charged coal into coke. The reason why the airtightness of the carbonization chamber is deteriorated is that the carbonization chamber and the combustion chamber are aerated because the brick joint breaks due to expansion and contraction caused by repeated heating and cooling of the refractory brick wall that separates the carbonization chamber and the combustion chamber. In addition, the carbonization chamber and the outside of the furnace may be ventilated due to thermal deformation of the furnace lids that are detachably installed on both sides of each carbonization chamber, and defective sealing due to deposits, etc. Deterioration of the property slightly varies depending on the furnace operating rate, but it will inevitably occur at short-term or long-term intervals as the operation continues.

【0004】上記室炉式コークス炉において、炭化室と
燃焼室を区切っている壁に目地切れが発生すると、その
部分が貫通状態となり、乾留時に発生するコークスガス
(以下、COGと称する)のリークが生じ、燃焼室内で
局部的に燃料支燃物の量が不足するため黒煙の発生や乾
留不良となるばかりか、環境上や操業上へも悪影響を及
ぼす事となる。また、炉蓋が変形すると状況によっては
ナイフエッジの叩き出しでは対応できない場合も発生
し、該シール不良部からのCOGが流出し環境上や操業
上へも悪影響を及ぼす。この炉蓋部からのCOGの流出
を防ぐためには発生COGの吸引負荷を高めて炭化室内
圧を低下させればよいが、炭化室内に外気が吸引される
ので、炭化室内でのコークス及びCOGの燃焼、コーク
ス及びCOGの品質低下、歩留り低下が避けられない。
In the above-mentioned chamber furnace type coke oven, when a joint break occurs in the wall that separates the carbonization chamber and the combustion chamber, the portion becomes a through state, and coke gas (hereinafter referred to as COG) leak generated during carbonization. As a result, the amount of fuel supporting materials is locally insufficient in the combustion chamber, which not only causes black smoke and poor carbonization, but also has an adverse effect on the environment and operation. In addition, if the furnace lid is deformed, it may not be possible to deal with it by knocking out the knife edge depending on the situation, and COG flows out from the defective seal portion, which adversely affects the environment and operation. In order to prevent the outflow of COG from the furnace lid, it is sufficient to increase the suction load of generated COG and reduce the pressure in the carbonization chamber. Combustion, coke and COG quality deterioration and yield reduction are inevitable.

【0005】上記炭化室の気密性の劣化状況は、例え
ば、各炭化室毎にコークスを押出作業後に熟練作業者が
観察する事で損傷有無あるいはその部位を判定していた
が、複数炉団を対象とすると、その観察作業は高温雰囲
気下での作業となるので負荷が大きく効率も悪かった。
また、炉蓋のシール不良については炭化室に石炭を装入
した以降にCOGがシール不良部から流出するので作業
者による監視を行うことにより発見でき、ナイフエッジ
の叩き出しあるいは吸引強化によって対応可能である
が、作業負荷が大きく、効率も悪い。
Regarding the deterioration of the airtightness of the carbonization chamber, for example, the presence or absence of damage or the site thereof was judged by observing a skilled worker after extruding the coke in each carbonization chamber. As a target, the observation work was a work in a high temperature atmosphere, so that the load was large and the efficiency was poor.
Also, if the furnace lid has a poor seal, COG will flow out of the poor seal after the coal is charged into the carbonization chamber, so it can be found by monitoring by a worker, and can be dealt with by knocking out the knife edge or strengthening suction. However, the workload is heavy and the efficiency is low.

【0006】上記炭化室内の目地切れの監視を作業者の
直接観察に依ることなく行う方法として、例えば、特開
昭54−041902号は、煙道または煙突に設けた煤
煙濃度計の黒煙検知信号と装入作業のタイミングとの対
応関係を用いた黒煙発生窯の判別方法を開示している。
また、特開昭57−094085号にも前記同様の技術
開示がある。また、特開昭64−033184号は、煙
道でのSO2 濃度を測定し上記同様の判断をする方法を
開示している。
As a method of monitoring the joint breakage in the carbonization chamber without directly observing the operator, for example, Japanese Patent Laid-Open No. 54-041902 discloses black smoke detection by a soot concentration meter provided in a flue or a chimney. Disclosed is a method for determining a black smoke generating kiln using a correspondence relationship between a signal and a charging operation timing.
Further, Japanese Patent Application Laid-Open No. 57-094085 discloses the same technology as described above. Further, Japanese Patent Laid-Open No. 64-033184 discloses a method of measuring the SO 2 concentration in the flue and making the same judgment as above.

【0007】しかし、上記した排ガス中の煤煙濃度等の
測定値と作業タイミングとの対応で判定する方法である
と、上記作業者による直接監視方式より負荷が軽減され
るが、前記したように複数の炭化室のラップ操業とかガ
ス切替え時の配管内残留燃料に起因する黒煙がノイズと
なることがあり、目地切れ炭化室の判定ミスが発生し易
い。
However, if the method is to judge by the correspondence between the measured value of the soot concentration in the exhaust gas and the work timing, the load is reduced as compared with the direct monitoring method by the worker. The black smoke resulting from the residual fuel in the pipe during the lapping operation of the carbonization chamber or the gas switching may cause noise, and the misjudgment of the joint cutting carbonization chamber is likely to occur.

【0008】また、炭化室毎に気密性劣化の検知、補修
という状態で対応する場合は突発的な気密性劣化あるい
は既に炭化室の目地切れがある程度進行して燃焼室内で
不完全燃焼をもたらす状態に至っているという場合に際
しては効果的である。しかし、炉の稼働履歴に伴って複
数の炭化室が特定期間内で気密性劣化を発生し易くなる
という状況下において、初期段階の気密性劣化となった
炭化室が発生していても検出不能であり、そのような炭
化室が複数重なっていてもその検知精度は低い。かかる
突発的な情報にもとづいて、特定炭化室の目地切れを確
認し補修作業を完了しても、測定情報は新たな炭化室劣
化を指示していることもあり、コークス炉作業サイクル
タイムに合った補修計画を組むことができず、コークス
炉の稼働率低下をもたらす。
Further, when the deterioration of the airtightness is detected and repaired for each carbonization chamber, a sudden deterioration of the airtightness or a breakage of the joint in the carbonization chamber has already progressed to a certain extent to cause incomplete combustion in the combustion chamber. It is effective in the case of reaching. However, in a situation where multiple carbonization chambers are likely to cause airtightness deterioration within a specific period due to the operation history of the furnace, it is not possible to detect even if carbonization chambers with airtightness deterioration in the initial stage occur. Therefore, even if a plurality of such carbonization chambers overlap, their detection accuracy is low. Based on such sudden information, even if the joint breakage of the specific carbonization chamber is confirmed and the repair work is completed, the measurement information may indicate a new deterioration of the carbonization chamber, which is suitable for the coke oven work cycle time. It is not possible to formulate a repair plan, resulting in a decrease in the operating rate of the coke oven.

【0009】[0009]

【発明が解決しようとする課題】コークス炉の炭化室の
気密性劣化は定性的には炉稼働履歴にほぼ比例してお
り、気密性劣化の初期段階からその傾向を把握できるこ
とが望まれている。前記したように、炭化室の煉瓦目地
切れとか炉蓋シール不良等による気密性劣化は操業を継
続することによって不可避的に発生するものであり、本
発明は炉団単位で炭化室の気密性劣化の傾向を把握する
ことによって、気密性劣化部位のメンテナンスを計画的
に実行する方法を提供することを目的としている。
Deterioration of the airtightness of the carbonization chamber of the coke oven is qualitatively almost proportional to the furnace operation history, and it is desired to be able to grasp the tendency from the initial stage of the airtightness degradation. . As described above, deterioration of airtightness due to brick joint breakage in the carbonization chamber or defective sealing of the furnace lid is unavoidably caused by continuing operation. It is an object of the present invention to provide a method for systematically executing maintenance of a portion where airtightness is deteriorated by grasping the tendency of.

【0010】[0010]

【課題を解決するための手段】本発明は、コークス炉の
炉団単位毎の各燃焼室に供給する燃料及び/あるいは燃
料支燃物中の硫黄、窒素、酸素あるいは水素の一種ある
いは二種以上の含有量と燃焼排ガス中の硫黄、窒素、酸
素あるいは水素の一種あるいは二種以上の含有量を測定
し、該両測定値の比率あるいは差の推移を把握すること
を特徴とするコークス炉団単位の炭化室劣化度の評価方
法である。
The present invention is directed to one or more of sulfur, nitrogen, oxygen or hydrogen in the fuel and / or fuel combustion support supplied to each combustion chamber of each coke furnace unit. Coke furnace group unit characterized by measuring the content of and the content of one or more of sulfur, nitrogen, oxygen or hydrogen in the combustion exhaust gas, and grasping the transition of the ratio or difference between the two measured values. Is a method for evaluating the degree of deterioration in the carbonization chamber.

【0011】[0011]

【作用】本発明者等は、コークス炉の炭化室の気密性劣
化について、調査検討を進めたところ、コークス炉の稼
働履歴に伴って複数の炭化室が特定期間内で気密性劣化
を発生し易くなるという傾向を示すことを知見した。こ
の炭化室の気密性劣化の発生タイミングはその原因、例
えば、炉蓋シール不良、炭化室壁の目地切れ等によって
異なるが、ほぼ同様な操業形態を踏襲していると炉団毎
の特性を踏まえて、ほぼ特定期間内に劣化が多発すると
いう傾向をもっている。
The inventors of the present invention conducted an investigation and study on the deterioration of the airtightness of the carbonization chamber of the coke oven, and found that the airtightness of the plurality of carbonization chambers deteriorated within a specific period depending on the operation history of the coke oven. It has been found that it tends to be easier. The timing of occurrence of the airtightness deterioration of the carbonization chamber varies depending on the cause, for example, a poor sealing of the furnace lid, a joint breakage of the wall of the carbonization chamber, etc. Therefore, there is a tendency that deterioration frequently occurs within a specific period.

【0012】従って、コークス炉の炉団単位毎の各燃焼
室に供給する燃料及び/あるいは燃料支燃物中の硫黄、
窒素、酸素あるいは水素の一種あるいは二種以上の含有
量と燃料排ガス中の硫黄、窒素、酸素あるいは水素の一
種あるいは二種以上の含有量を測定するので、系内に供
給される硫黄、窒素、酸素あるいは水素の量が把握で
き、石炭乾留用の顕熱として機能した後、系外に排出さ
れる硫黄、窒素、酸素あるいは水素の量が把握できるの
で、この二つの量の比率あるいは差について継続してそ
の推移を見れば、上記供給から排出の過程内において外
部から流入あるいは流出する硫黄、窒素、酸素あるいは
水素の一種あるいは二種以上の含有量の変化傾向、即
ち、炭化室の気密性の劣化傾向が把握できる。
Therefore, the sulfur contained in the fuel and / or the fuel combustion support supplied to each combustion chamber of each unit of the coke oven furnace group,
The content of one or more of nitrogen, oxygen or hydrogen and the content of one, two or more of sulfur, nitrogen, oxygen or hydrogen in the fuel exhaust gas are measured. The amount of oxygen or hydrogen can be grasped, and after functioning as sensible heat for coal carbonization, the amount of sulfur, nitrogen, oxygen or hydrogen discharged outside the system can be grasped. Then, looking at the transition, the change tendency of the content of one or more of sulfur, nitrogen, oxygen, or hydrogen flowing in or out from the outside in the process of supply to discharge, that is, the airtightness of the carbonization chamber The deterioration tendency can be grasped.

【0013】また、コークス炉の稼働率の変更に伴って
供給される燃料及び/あるいは燃料支燃物の量が異なる
が、本発明は各燃焼室に供給される燃料及び/あるいは
燃料支燃物中の硫黄、窒素、酸素あるいは水素の一種あ
るいは二種以上の含有量と燃焼排ガス中の硫黄、窒素、
酸素あるいは水素の一種あるいは二種以上の含有量を測
定し、この二つの量の比率あるいは差の推移を見るの
で、上記操業条件の変動要素を補正した状態で炭化室の
気密性の劣化の初期段階からその傾向を把握できる。
Further, although the amount of fuel and / or fuel supporting material supplied differs according to the change of the operating rate of the coke oven, the present invention is directed to the fuel and / or fuel supporting material supplied to each combustion chamber. The content of one or more of sulfur, nitrogen, oxygen, or hydrogen and sulfur, nitrogen in the combustion exhaust gas,
By measuring the content of one or more of oxygen or hydrogen and observing the transition of the ratio or difference between these two amounts, the initial stage of deterioration of the airtightness of the carbonization chamber should be corrected with the variable factors of the above operating conditions corrected. The tendency can be grasped from the stage.

【0014】以下、本発明を図面に示す実施態様例にも
とづいて具体的に説明する。
The present invention will be specifically described below based on the embodiments shown in the drawings.

【0015】図1はコークス炉の炭化室と燃焼室の配置
態様の一部分を示した断面図である。コークス炉1を構
成する炭化室2の両側には燃焼室3が配置されるよう
に、炭化室2と燃焼室3は交互に配置されている。該炭
化室2と燃焼室3の下方には蓄熱室4が配置されてい
る。各燃焼室3にはその下部の蓄熱室4を通過して燃料
ガス及び燃料支燃ガスが供給され、燃焼排ガスは燃焼室
3の上方より流出し、他の蓄熱室4、煙道及び煙突を介
して排出される。上記コークス炉1において、該炉の型
式によって燃焼排ガスの流路が異なっている。上記炭化
室2で発生したCOGは(図示せず)上昇管、ドライメ
ーン等からなるCOG回収系路によってガス処理されて
回収される。
FIG. 1 is a sectional view showing a part of the arrangement of a carbonization chamber and a combustion chamber of a coke oven. The carbonization chambers 2 and the combustion chambers 3 are alternately arranged so that the combustion chambers 3 are arranged on both sides of the carbonization chamber 2 constituting the coke oven 1. A heat storage chamber 4 is arranged below the carbonization chamber 2 and the combustion chamber 3. Fuel gas and fuel combustion-supporting gas are supplied to each combustion chamber 3 through a heat storage chamber 4 below the combustion chamber 3, and combustion exhaust gas flows out from above the combustion chamber 3 so that the other heat storage chambers 4, flues and chimneys are discharged. Exhausted through. In the above coke oven 1, the flow path of the combustion exhaust gas differs depending on the type of the oven. The COG generated in the carbonization chamber 2 is gas-treated and recovered by a COG recovery system path (not shown) composed of an ascending pipe, dry mains, and the like.

【0016】上記炭化室2と燃焼室3を区切っている耐
火煉瓦で築造されている壁5は長期間にわたる加熱、冷
却の繰り返しに伴う煉瓦の膨張と収縮が原因となって煉
瓦の目地切れあるいは煉瓦の欠落が発生し、通気孔6を
形成する。この通気孔6の存在は炭化室2への石炭装入
後、乾留初期に過剰に発生するCOGの一部が燃焼室3
へ流出してしまう。この結果、燃焼室3内では燃料支燃
ガスが不足するので、不完全燃焼となり、両側の炭化室
2への熱供給量が不足する。また、煤を多量に介在する
黒煙は煙突から大気中に排出される。
The wall 5 made of refractory bricks that separates the carbonization chamber 2 and the combustion chamber 3 from each other is broken or broken due to expansion and contraction of the bricks due to repeated heating and cooling for a long period of time. The brick is missing and the vent hole 6 is formed. The presence of the vent holes 6 means that after the coal is charged into the carbonization chamber 2, a part of the COG excessively generated in the initial stage of carbonization is in the combustion chamber
Will be leaked to. As a result, the fuel supporting gas is insufficient in the combustion chamber 3, resulting in incomplete combustion, and the heat supply amount to the carbonization chambers 2 on both sides is insufficient. Also, black smoke containing a large amount of soot is discharged from the chimney into the atmosphere.

【0017】また、上記炭化室2には(図1の前面と後
面)着脱自在に炉蓋が設置されており、炉内側は加熱さ
れ、炉外側は大気放冷されているので熱歪みによって変
形し易い。微小変形であれば炉蓋に設備されているナイ
フエッジの叩き出しによってシール状態を補正できる
が、長期間の使用により、しばしばナイフエッジの叩き
出しでシール補正できない変形となりシール不良が発生
する。このシール不良は発生COGの流出原因となり、
このCOGの流出状態は作業者の目視観察によって確認
できるので、通常は該炭化室2内の吸引を強化してCO
Gの流出を防止している。
A furnace lid is removably installed in the carbonization chamber 2 (front and rear surfaces in FIG. 1). The inside of the furnace is heated and the outside of the furnace is left to cool in the atmosphere, so that it is deformed by thermal strain. Easy to do. If it is a slight deformation, the sealing condition can be corrected by knocking out the knife edge installed on the furnace lid, but if it is used for a long time, the deformation cannot be corrected by the hammering out of the knife edge, and a sealing failure occurs. This defective seal causes outflow of generated COG,
The outflow state of this COG can be confirmed by visual observation by the operator, so normally, the suction inside the carbonization chamber 2 is strengthened to reduce CO 2.
The outflow of G is prevented.

【0018】図2に示すように、上記炭化室2を、例え
ば、30とか50門を一つの単位とする炉団毎に燃料及
び燃料支燃ガスの供給管路7が設備されており、また、
燃焼排ガスの排出管路8及び煙突9が設備されている。
また、上記のように構成されているコークス炉の両側に
は(図示せず)、コークスの押出機とコークスガイド
車、コークス搬送車が配置されており、これらの移動車
は各炭化室2の炉蓋の前面を所定間隔で通過している。
As shown in FIG. 2, the carbonization chamber 2 is provided with a fuel and fuel-supporting gas supply pipeline 7 for each furnace group having, for example, 30 or 50 gates as one unit. ,
A flue gas discharge pipe 8 and a chimney 9 are provided.
Further, a coke extruder, a coke guide vehicle, and a coke carrier vehicle are arranged on both sides of the coke oven configured as described above (not shown). It passes through the front surface of the furnace lid at predetermined intervals.

【0019】前記本発明は、コークス炉1の炉団単位毎
に供給する燃料と燃料支燃物及び燃焼排ガス中の含有元
素、硫黄、窒素、酸素、水素の量を測定する。具体的に
は、ガス供給管7及びガス排出管8にそれぞれガスサン
プリング管10、ガス成分分析計11、ガス流量計12
を設け、これらの測定、分析値から求める。これらの測
定値は特定の炉団の各燃焼室3に供給した元素及びその
量と排出する元素及びその量を示している。従って、こ
の供給と排出の間において気密性が保たれていると、こ
の二つの量の比率は一定値であり二つの量の差は零とな
る。この関係はコークス炉の操業条件、例えば、稼働率
を変更しても変わらない。
In the present invention, the amounts of the elements, sulfur, nitrogen, oxygen and hydrogen contained in the fuel, the fuel supporting material and the combustion exhaust gas supplied for each unit of the coke oven 1 are measured. Specifically, the gas supply pipe 7 and the gas discharge pipe 8 are respectively connected to a gas sampling pipe 10, a gas component analyzer 11, and a gas flow meter 12
Is provided and determined from these measured and analyzed values. These measured values indicate the elements supplied and their amounts and the elements discharged and their amounts in each combustion chamber 3 of the specific furnace group. Therefore, if the airtightness is maintained between the supply and the discharge, the ratio between the two amounts is a constant value and the difference between the two amounts is zero. This relationship does not change even if the operating condition of the coke oven, for example, the operating rate is changed.

【0020】本発明における炭化室2の気密性の劣化原
因として、例えば、炭化室2に目地切れが発生し、通気
孔6が形成されると、発生COGが燃焼室3内に流入す
る。この結果、COG中には多量の硫黄が含有されてお
り排ガス中の硫黄量は上昇する。上記炭化室2の目地切
れが充分に進行していなくて形成される通気孔6が微小
であっても、圧力差によってCOGの流入は避けられ
ず、微小量の流入であるため燃焼室3内で不完全燃焼に
ならなくても、ガス供給管7からの硫黄量は既知である
ので、COGの流入による硫黄量の増加は把握できる。
また、窒素、水素成分も発生COG中に含有されてお
り、それらの量の増加は目地切れ原因と判定できる。
As a cause of the deterioration of the airtightness of the carbonization chamber 2 in the present invention, for example, when a joint break occurs in the carbonization chamber 2 and a vent hole 6 is formed, the generated COG flows into the combustion chamber 3. As a result, COG contains a large amount of sulfur, and the amount of sulfur in the exhaust gas increases. Even if the vent holes 6 formed when the joint breakage of the carbonization chamber 2 does not proceed sufficiently are minute, the inflow of COG is unavoidable due to the pressure difference, and since a minute amount of inflow is generated, the inside of the combustion chamber 3 is inevitable. Even if incomplete combustion does not occur, the amount of sulfur from the gas supply pipe 7 is known, and therefore the increase in the amount of sulfur due to the inflow of COG can be grasped.
Further, nitrogen and hydrogen components are also contained in the generated COG, and an increase in the amounts thereof can be determined to be the cause of the joint breakage.

【0021】また、本発明における炭化室2の気密性の
劣化原因として、例えば、炉蓋のシール不良が発生する
と、前記したようにコークス炉の両側において、所定時
間毎に走行移動する作業車の運転者によって発生COG
の流出が目視確認でき、コークス炉操作室に通信され
る。上記炉蓋のシール不良による発生COGの流出確認
の他の手段としてはテレビカメラで撮像し、コークス炉
操作室で監視する方式であってもよい。この情報にもと
ずいて対象炭化室2の吸引が強化されCOGの流出防止
措置が取られると、該炭化室2内には外気が流入する、
この外気の流入量はシール不良の程度によって異なって
おり、測定値の窒素、酸素量の増加として把握できる。
Further, as a cause of the deterioration of the airtightness of the carbonization chamber 2 in the present invention, for example, when the furnace lid has a poor seal, as described above, the work vehicle that travels and travels at predetermined intervals on both sides of the coke oven. COG generated by the driver
Can be visually confirmed and communicated to the coke oven control room. As another means for confirming the outflow of COG generated due to the defective sealing of the furnace lid, a method of taking an image with a television camera and monitoring it in the coke oven operating room may be used. Based on this information, when the suction of the target carbonization chamber 2 is strengthened and COG outflow prevention measures are taken, outside air flows into the carbonization chamber 2.
The amount of inflow of outside air varies depending on the degree of sealing failure, and can be grasped as an increase in the measured amounts of nitrogen and oxygen.

【0022】上記コークス炉1の炉団単位毎に供給する
燃料と燃料支燃物及び燃焼排ガス中の含有元素、硫黄、
窒素、酸素、水素の一種あるいは二種以上の含有量の測
定は連続的であってもよく、また、間欠的であってもよ
いものであり、例えば、そのコークス炉団の操業条件の
変更、例えば、稼働率の変更毎に、任意の測定間隔を設
定して測定してもよいものである。重要なことは測定値
の比率あるいは差を継続して把握することであって、そ
の過程での変化状況がその炉団の各炭化室2を総合した
気密性の劣化の程度として把握できる。また、炉蓋のシ
ール不良個数、炭化室2の目地切れ個数についても大ま
かな推定ができる。
The fuel supplied to each unit of the coke oven 1 as a unit, the fuel supporting material, and the elements contained in the combustion exhaust gas, sulfur,
Nitrogen, oxygen, the measurement of the content of one or more of hydrogen may be continuous, or may be intermittent, for example, the change of the operating conditions of the coke oven cluster, For example, the measurement may be performed by setting an arbitrary measurement interval each time the operating rate is changed. What is important is to continuously grasp the ratio or difference of the measured values, and the change situation in the process can be grasped as the degree of deterioration of the airtightness of the entire carbonization chambers 2 of the furnace group. In addition, it is possible to roughly estimate the number of defective seals on the furnace lid and the number of joint breaks in the carbonization chamber 2.

【0023】[0023]

【実施例1】稼働履歴がほぼ30年になる炭化室50門
からなるA炉団について、図2に示す測定機器を用い、
稼働率を120%から100%に変更した時点から毎月
一回定期的にガス供給管7とガス排気管8の硫黄量を測
定し、その差の変化を見ていたところ、本来、入りと出
の硫黄量の差は零であるのが8kg/H増加していた。
その後、継続して3ケ月同一条件で測定した値の差は
8.5kg/Hと若干増加していた。その後、毎週一回
の定期測定に変更して1ケ月測定したが新たな差の増加
は見られなかったが、差の増加量から判断して2〜3門
の炭化室1に目地切れが発生しているのではないかとい
う想定でコークス押出毎に各炭化室2の目視観察を行っ
たところ、目視切れが比較的進行している炭化室が1
門、目地切れが若干進行している炭化室が4門発見でき
た。この結果にもとづいて補修計画を設定し、対象炭化
室を補修したところ、その後の硫黄量の差はほぼ零とな
った。
[Example 1] Using a measuring instrument shown in FIG.
From the time when the operating rate was changed from 120% to 100%, the amount of sulfur in the gas supply pipe 7 and the gas exhaust pipe 8 was measured once a month on a regular basis, and the change in the difference was observed. The difference in the amount of sulfur was zero, which was increased by 8 kg / H.
After that, the difference between the values continuously measured under the same conditions for 3 months was 8.5 kg / H, which was slightly increased. After that, we changed to regular measurement once a week and measured it for one month, but no new increase in the difference was seen, but judging from the amount of increase in the difference, there was a break in the coking chamber 1 of 2-3 gates. As a result of visual observation of each carbonization chamber 2 each time the coke was extruded, it was found that the number of carbonization chambers in which carbonization was relatively low was 1
We found 4 charring chambers where the gates and joints were slightly broken. When a repair plan was set based on this result and the target carbonization chamber was repaired, the difference in sulfur content after that became almost zero.

【0024】[0024]

【実施例2】実施例1と同一のA炉団について、毎月一
回定期的にガス供給管7とガス排出管8の窒素と酸素の
量を測定し、その比率の変化を見ていたところ、本来、
入りと出の窒素と酸素の量の比率は一定値の1.0であ
るのが1.002に増加していた。この間に炉蓋3個か
らCOGの流出確認の連結が入っており、対象の炭化室
の吸引を強化していた。その後、毎週一回の測定に変更
して測定したところ第2週目と第3週目の測定値の比率
が1.002と1.003に増加したので、炉蓋補修計
画を組み、対象炉蓋5個について補修済の炉蓋と交換し
たところ一定値の1.0に回復でき、定常状態の操業で
実施できた。
Example 2 With respect to the same A furnace group as in Example 1, the amounts of nitrogen and oxygen in the gas supply pipe 7 and the gas discharge pipe 8 were measured once a month regularly, and changes in the ratio were observed. , Originally,
The ratio of the amounts of nitrogen and oxygen in and out was a constant value of 1.0, but increased to 1.002. During this period, there was a connection for confirming the outflow of COG from the three furnace lids, and the suction of the target carbonization chamber was strengthened. After that, when the measurement was changed to weekly measurement, the ratio of the measured values in the second week and the third week increased to 1.002 and 1.003. When the five furnace lids were replaced with repaired furnace lids, the value could be restored to a fixed value of 1.0, and the operation could be carried out in a steady state.

【0025】[0025]

【発明の効果】本発明は、コークス炉団単位での炭化室
の劣化度が把握出来ると共にその推移から時間的な劣化
度の進行状況が管理可能となる為、具体的な補修計画に
もとづいて効率的な補修が実施でき、補修コストの低減
が図れる。
The present invention makes it possible to grasp the degree of deterioration of the coking chamber in units of coke oven groups and to manage the progress of the degree of deterioration over time from the transition thereof, so that it is based on a concrete repair plan. Efficient repairs can be performed and repair costs can be reduced.

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

【図1】炭化室と燃焼室の配置態様の断面説明図。FIG. 1 is an explanatory cross-sectional view of an arrangement mode of a carbonization chamber and a combustion chamber.

【図2】コークス炉の燃焼系統概略図。FIG. 2 is a schematic diagram of a combustion system of a coke oven.

【符号の説明】[Explanation of symbols]

1…コークス炉 2…炭化室 3…燃焼室 4…蓄熱室 5…壁 6…通気孔 7…ガス供給管 8…ガス排出管 9…煙突 10…ガスサンプ
リング管 11…ガス成分分析計 12…ガス流量
計。
1 ... Coke oven 2 ... Carbonization chamber 3 ... Combustion chamber 4 ... Heat storage chamber 5 ... Wall 6 ... Vent hole 7 ... Gas supply pipe 8 ... Gas exhaust pipe 9 ... Chimney 10 ... Gas sampling pipe 11 ... Gas component analyzer 12 ... Gas Flowmeter.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 コークス炉の炉団単位毎の各燃焼室に供
給する燃料及び/あるいは燃料支燃物中の硫黄、窒素、
酸素あるいは水素の一種あるいは二種以上の含有量と燃
焼排ガス中の硫黄、窒素、酸素あるいは水素の一種ある
いは二種以上の含有量を測定し、該両測定値の比率ある
いは差の推移を把握することを特徴とするコークス炉団
単位の炭化室劣化度の評価方法。
1. Sulfur and nitrogen in the fuel and / or fuel combustion support supplied to each combustion chamber of each coke furnace group
Measure the content of one or more oxygen or hydrogen and the content of one or more sulfur, nitrogen, oxygen or hydrogen in the combustion exhaust gas, and grasp the transition of the ratio or difference between the two measured values. A method for evaluating the degree of deterioration of a coking furnace unit of a coke oven group, which is characterized by the following.
JP5870393A 1993-03-18 1993-03-18 Estimation of deterioration degree of carbonization chamber in unit coke oven group Pending JPH06271855A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5870393A JPH06271855A (en) 1993-03-18 1993-03-18 Estimation of deterioration degree of carbonization chamber in unit coke oven group

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5870393A JPH06271855A (en) 1993-03-18 1993-03-18 Estimation of deterioration degree of carbonization chamber in unit coke oven group

Publications (1)

Publication Number Publication Date
JPH06271855A true JPH06271855A (en) 1994-09-27

Family

ID=13091881

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5870393A Pending JPH06271855A (en) 1993-03-18 1993-03-18 Estimation of deterioration degree of carbonization chamber in unit coke oven group

Country Status (1)

Country Link
JP (1) JPH06271855A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0718389A2 (en) * 1994-12-21 1996-06-26 Krupp Koppers GmbH Process and device for the reduction of the carbon monoxide content in the flue gases of a coke oven battery, heated with lean gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0718389A2 (en) * 1994-12-21 1996-06-26 Krupp Koppers GmbH Process and device for the reduction of the carbon monoxide content in the flue gases of a coke oven battery, heated with lean gas
EP0718389A3 (en) * 1994-12-21 1997-03-26 Krupp Koppers Gmbh Process and device for the reduction of the carbon monoxide content in the flue gases of a coke oven battery, heated with lean gas

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