JP2872343B2 - Prediction method of fire time of coke oven - Google Patents

Prediction method of fire time of coke oven

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Publication number
JP2872343B2
JP2872343B2 JP10892390A JP10892390A JP2872343B2 JP 2872343 B2 JP2872343 B2 JP 2872343B2 JP 10892390 A JP10892390 A JP 10892390A JP 10892390 A JP10892390 A JP 10892390A JP 2872343 B2 JP2872343 B2 JP 2872343B2
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JP
Japan
Prior art keywords
temperature
time
coal
coke oven
coke
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
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JP10892390A
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Japanese (ja)
Other versions
JPH048797A (en
Inventor
信吾 丁亀
和利 佐藤
正嗣 木村
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Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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Priority to JP10892390A priority Critical patent/JP2872343B2/en
Publication of JPH048797A publication Critical patent/JPH048797A/en
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Publication of JP2872343B2 publication Critical patent/JP2872343B2/en
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Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、コークス炉の火落ち時間予測方法に関
し、さらに詳しくは、石炭が乾留するコークス炉におい
て、コークスの生成が完了する時間、いわゆる火落ち時
間を自動的に精度よく予測するための方法の改良に係る
ものである。
Description: FIELD OF THE INVENTION The present invention relates to a method for estimating a burn-out time of a coke oven, and more specifically, a time required to complete the generation of coke in a coke oven where coal is carbonized, that is, a so-called fire. The present invention relates to an improvement in a method for automatically and accurately predicting a falling time.

〔従来の技術〕[Conventional technology]

一般にコークス炉においては、相互に隣接する複数の
乾留室内に原料石炭を順次に装入させた状態で、これを
1100℃程度の高温によって乾留処理し、当該乾留操作の
終了,ひいてはコークスの生成完了後、押出し機を用い
て各乾留室内から生成されたコークスを順次に押出すよ
うにしており、この押出し操作に先立つて、各乾留室内
の被処理石炭の乾留が完了したか否かを判定する必要が
ある。
Generally, in a coke oven, raw coal is sequentially charged into a plurality of carbonization chambers adjacent to each other, and
A carbonization treatment is performed at a high temperature of about 1100 ° C., and after the completion of the carbonization operation and, consequently, the production of coke, the coke generated from each carbonization chamber is sequentially extruded using an extruder. Prior to this, it is necessary to determine whether or not the carbonization of the coal to be treated in each carbonization chamber has been completed.

従来、この種のコークス炉における前記火落ち時間の
判定は、通常の場合、いわゆる“火見”と呼ばれる石炭
乾留処理操作の熟練者によつて行なわれており、その手
段としては、装入された原料石炭の乾留操作中に、コー
クス炉のガス上昇管のトップカバーを開放した上で、当
該ガス上昇管から外部に放出されるガスの色合いを観察
し、このときのガスの色合いから経験的に火落ち時間を
判定するものであった。
Conventionally, the determination of the burn-off time in this type of coke oven is usually performed by a skilled person of a coal dry distillation operation called "Himi". During the carbonization of the raw coal, open the top cover of the gas riser of the coke oven and observe the color of the gas released from the gas riser to the outside. Was used to determine the time of fire.

しかしながら、この“火見”手段による火落ち時間の
判定、つまり、ガス上昇管からの放出ガスの色合いを観
察かつ判断してなされる火落ち時間の判定には、十分な
熟練を必要として、必ずしも正確な判定を期待すること
ができず、しかも、このような人為的な判定手段の場
合、その判定精度を効果的に高めるためには、必然的に
ガス上昇管のトップカバー開放による目視判定の頻度を
高めざるを得ないものであつて、多大の労力を必要とす
るばかりか、一方では、トップカバーを開放する度毎
に、これに伴う発生ガスの外部への放出,漏洩によつて
周辺環境の悪化を招くとか、エネルギー源としての発生
ガスの損失の度合いが増し、かつ生成されるコークスの
品質が低下するなどの不都合がある。
However, the determination of the burn-out time by the "fire watching" means, that is, the determination of the fire-burning time performed by observing and determining the color of the gas released from the gas riser requires sufficient skill, and is not necessarily required. Accurate judgment cannot be expected, and in the case of such artificial judgment means, in order to effectively increase the judgment accuracy, it is inevitable to perform visual judgment by opening the top cover of the gas riser. The frequency must be increased and not only requires a great deal of labor, but also every time the top cover is opened, the generated gas is released and leaked to the outside due to this. There are inconveniences such as deterioration of the environment, an increase in the loss of generated gas as an energy source, and a decrease in the quality of the generated coke.

そこで、本発明者らは、このような不利を理論的に改
善するための一つの手段として、先に、特開昭58-14128
7号公報により、コークス炉におけるガス上昇管内での
発生ガス温度を基準にして火落ち時間を判定するための
火落ち判定方法を提案した。また一方、特公昭62-56197
号公報には、当該火落ち判定方法を応用する火落ち予測
方法も提案されている。
Therefore, the present inventors, as one means for theoretically improving such disadvantages, first described in Japanese Patent Laid-Open No. 58-14128.
No. 7 proposes a method for determining a burn-out for determining a burn-out time based on a gas temperature generated in a gas riser in a coke oven. Meanwhile, Japanese Patent Publication No. 62-56197
In Japanese Patent Laid-Open Publication No. H11-264, there has also been proposed a method for predicting a fire that applies the method for determining a fire.

〔課題を解決するための手段〕[Means for solving the problem]

しかしながら、前記の本発明者らによつて提案された
特開昭58-141287号公報によるコークス炉での火落ち時
間の判定方法の場合は、装入石炭の乾留が完了した火落
ち時点を判定するに留まるもので、装入石炭の乾留が完
了する以前に当該火落ち時点を予測し得ないという不利
があり、また、特公昭62-56197号公報による火落ち時間
の判定方法の場合は、発生ガスの絶対温度を基準にして
火落ち時間を算出する手段であるために、必ずしも高精
度での火落ち時間の予測をなし得ないという問題点があ
つた。
However, in the case of the method for judging the burn-out time in a coke oven disclosed in Japanese Patent Application Laid-Open No. 58-141287 proposed by the present inventors, the fire-burning point at which the carbonization of the charged coal is completed is judged. However, there is a disadvantage that it is not possible to predict the time of the burnout before the dry distillation of the charged coal is completed, and in the case of the method of determining the burnout time according to Japanese Patent Publication No. 62-56197, There is a problem that the burn-out time cannot be predicted with high accuracy because it is a means for calculating the burn-out time based on the absolute temperature of the generated gas.

この発明は、従来のこのような問題点を解消するため
になされたもので、その目的とするところは、コークス
の生成が完了する火落ち時間を自動的に精度よく予測し
得るようにした、この種のコークス炉の火落ち時間予測
方法を提供することである。
The present invention has been made in order to solve such a conventional problem, and its purpose is to be able to automatically and accurately predict the burn-out time when coke generation is completed. It is an object of the present invention to provide a method for predicting the fire time of a coke oven.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者らによる研究開発の結果、コークスの生成に
際し、原料石炭の乾留中に発生するガス温度の経時変化
が、装入時点での温度域から、実質的に平均化された温
度となる水平温度域を経て、一旦最高温度に達した後、
再度実質水平温度域に下降するまでの時間Xと、コーク
スの生成が完了する火落ち時間Yとの間に密接な関係が
あつて、こゝでは、関係式Y=aX+b(同式中、a,bは
炉形式、操業温度および装入炭水分、装入炭量などの装
入条件によつて決定される定数)が成立することが判明
した。
As a result of research and development by the present inventors, the change over time of the gas temperature generated during carbonization of the raw coal during the production of coke, from the temperature range at the time of charging, becomes a substantially averaged temperature. After reaching the maximum temperature once through the temperature range,
There is a close relationship between the time X until the temperature falls to the substantially horizontal temperature range again and the burnout time Y when the coke generation is completed. In this case, the relational expression Y = aX + b (where a , b are constants determined by the charging conditions such as the furnace type, operating temperature, charged coal moisture, and charged coal amount).

仍つて、この発明に係るコークス炉の火落ち時間予測
方法においては、前記関係式に基づき、予め同式の定数
a,bを求めておき、これによつて、実質水平温度域にお
ける平均ガス温度から、火落ち時点における発生ガス温
度を算出し、コークスの生成完了に先立つて所要の火落
ち時点を予測するようにしたものである。
Therefore, in the method for predicting a fire time of a coke oven according to the present invention, the constant
a and b are calculated in advance, and the generated gas temperature at the time of burnout is calculated from the average gas temperature in the substantially horizontal temperature range, and the required burnout time is predicted before the completion of coke generation. It was made.

すなわち、この発明は、石炭を乾留処理してコークス
を得るコークス炉において、当該コークス炉の上昇管ま
たは上昇管ベンド部に設けた温度測定手段により、原料
石炭の乾留中に発生するガス温度を測定して、予め当該
ガス温度の経時変化が、原料石炭の装入時点での温度域
から、実質的に平均化された温度となる水平温度域を経
て、最高温度に上昇した後、再度、平均温度域に下降す
るまでの時間Xと、コークスの生成が完了する火落ち時
間Yとの関係式 Y=aX+b 式中、a,bは炉形式、操業温度および装入炭水分、装
入炭量などの装入条件によつて決定される定数 を求めておき、前記温度測定手段により、乾留中の発生
ガス温度を逐次に測定して、前記実質水平温度域の平均
温度を算出し、当該算出温度から前記関係式に基づいて
火落ち時間を事前に予測し得るようにしたことを特徴と
するコークス炉の火落ち時間予測方法である。
That is, the present invention measures the temperature of gas generated during carbonization of raw coal by using a temperature measuring means provided in a riser or a riser bend portion of the coke oven in a coke oven for obtaining coke by carbonization of coal. Then, the gas temperature change with time in advance, from the temperature range at the time of charging of the raw coal, through a horizontal temperature range to be substantially averaged temperature, after rising to the maximum temperature, again averaged A relational expression between the time X required to fall to the temperature range and the burn-out time Y at which coke generation is completed Y = aX + b where a and b are the furnace type, operating temperature and charged coal moisture, and the charged coal quantity. Constants determined according to charging conditions such as the above, the temperature of the gas generated during carbonization is sequentially measured by the temperature measuring means, and the average temperature in the substantially horizontal temperature range is calculated. Fire from temperature based on the above relational expression A fire fall time prediction method of the coke oven, characterized in that it has adapted to predict the time in advance.

〔作用〕[Action]

この発明方法によれば、コークスの生成に際して、原
料石炭の乾留中に発生するガス温度の経時変化が、装入
時点での温度域から、実質的に平均化された温度となる
水平温度域を経て、一旦最高温度に達した後、再度実質
水平温度域に下降するまでの時間Xと、コークスの生成
が完了する火落ち時間Yとの間に、関係式Y=aX+b
(同式中、a,bは炉形式、操業温度および装入炭水分、
装入炭量などの装入条件によつて決定される定数)が成
立する点に鑑み、予め同式の定数a,bを求め、実質水平
温度域における平均ガス温度から、火落ち時点における
発生ガス温度を算出することで、コークスの生成完了に
先立ち、こゝでの所要の火落ち時点を極めて容易に、し
かも高精度で予測することができる。
According to the method of the present invention, in the production of coke, the change over time in the gas temperature generated during the dry distillation of the raw coal is changed from the temperature range at the time of charging to a horizontal temperature range in which the temperature is substantially averaged. After that, once the temperature reaches the maximum temperature, a relational expression Y = aX + b is established between the time X until the temperature falls to the substantially horizontal temperature range again and the burnout time Y when the coke generation is completed.
(Where a and b are furnace type, operating temperature and charged coal moisture,
In consideration of the fact that the constants determined by the charging conditions such as the amount of coal charged, etc.), the constants a and b of the same equation are obtained in advance, and the average gas temperature in the substantially horizontal temperature range is calculated based on the average gas temperature at the time of the fire. By calculating the gas temperature, it is possible to very easily and accurately predict the required time point of the fire after the completion of the coke generation.

〔実施例〕〔Example〕

以下、この発明に係るコークス炉の火落ち時間予測方
法の一実施例につき、第1図ないし第3図を参照して詳
細に説明する。
Hereinafter, an embodiment of a method for estimating a burn-out time of a coke oven according to the present invention will be described in detail with reference to FIGS. 1 to 3.

第1図はこの発明の一実施例を適用するコークス炉の
要部を模式的に示す断面構成図である。
FIG. 1 is a sectional view schematically showing a main part of a coke oven to which one embodiment of the present invention is applied.

この第1図に示すコークス炉の構成において、符号1
はコークス炉の乾留室、2は当該乾留室1内で発生する
ガスを取出すための上昇管を示し、上昇管2の頂部に
は、トップカバー3を開閉自在に被蓋させると共に、上
方側部にあつて、ベンド部4を配置してガス集合管5を
連通させてあり、この実施例の場合、当該ベンド部4内
に対して、上昇管2を通して得られる発生ガスの温度を
測定するための、例えば、熱電対などからなる温度測定
手段6を設けてある。
In the configuration of the coke oven shown in FIG.
Is a carbonization chamber of a coke oven, and 2 is a riser for taking out gas generated in the carbonization chamber 1. A top cover 3 is covered on the top of the riser 2 so as to be openable and closable. In order to measure the temperature of the generated gas obtained through the riser pipe 2 in the bend part 4, a bend part 4 is disposed so as to communicate with the gas collecting pipe 5. For example, a temperature measuring means 6 composed of a thermocouple or the like is provided.

なおこゝで、このようにベンド部4に温度測定手段6
を設ける理由は、発生ガスの温度測定を行なうのに、当
該ベンド部4の方が、上昇管2内よりもガス温度が安定
し、後述するガス温度の経時変化における実質的な水平
温度域をより一層高精度で把握できるからであるが、必
要に応じては上昇管2内に、温度測定手段6を設けるこ
とを妨げない。
Here, the temperature measuring means 6 is attached to the bend portion 4 in this manner.
The reason for providing is that when the temperature of the generated gas is measured, the bend portion 4 has a more stable gas temperature than that in the riser 2, and has a substantially horizontal temperature range in the time-dependent change of the gas temperature described later. This is because the temperature can be grasped with even higher accuracy, but the provision of the temperature measuring means 6 in the riser tube 2 is not prevented if necessary.

しかして、前記の第1図に示すコークス炉を用い、そ
の乾留室1内に原料石炭を装入した後、火落ち時点を過
ぎるまでの間に発生するガス温度を経時的に逐次に測定
すると、第2図に示すような温度変化を計測し得る。す
なわち、当該発生ガス温度は、コークス炉の乾留室1内
への原料石炭の装炭後、最初は、まず比較的短時間内に
急激な温度勾配で急速に昇温し、ついで温度勾配が次第
に緩やかになり、やがて殆んど温度上昇せずに、実質的
に水平かつ直線的な温度勾配部、つまりこゝでは、実質
的に平均化された温度Taによる水平温度域Aに達し
て、この水平温度域Aが比較的長時間に亘つて保持され
る。そして、この水平温度域Aを経過した時点で、発生
ガス温度は、再度やゝ急激に上昇して、比較的短時間内
に一旦温度Tbによる最高温度点Bに達した後、引き続
いて今度は急激かつ直線的に降温し初め、再度前記水平
温度域Aでの温度Ta点を経て下降するもので、当該直
線的な降温域における温度Ta点を経過した後の温度領
域部分にあつて、こゝでの目的である温度Tによる火落
ち時点Cが存在する。
Then, using the coke oven shown in FIG. 1 described above, after charging the raw coal into the dry distillation chamber 1, the gas temperature generated before the time of the burnout is measured sequentially with time. , A temperature change as shown in FIG. 2 can be measured. That is, the temperature of the generated gas first rises rapidly with a steep temperature gradient within a relatively short time after charging the raw coal into the carbonization chamber 1 of the coke oven, and then the temperature gradient gradually increases. With a gradual and short-term rise in temperature, the temperature reaches a substantially horizontal and linear temperature gradient, that is, a horizontal temperature range A due to a substantially averaged temperature Ta. This horizontal temperature range A is maintained for a relatively long time. Then, when the expiration of the horizontal temperature zone A, generated gas temperature rises again Yaゝrapidly, after once reaching a maximum temperature point B due to the temperature T b within a relatively short time, this time subsequently initially the temperature was lowered rapidly and linearly, in which descends through the temperature T a point again the horizontal temperature range a, filed in the temperature region portion after the lapse of the temperature T a point in the linear temperature lowering zone In this case, there is a time point C at which the fire falls due to the temperature T, which is the purpose of this procedure.

従つて、装炭された原料石炭の乾留操作中に、予め前
記の火落ち時点Cにおける発生ガス温度T,もしくは火落
ち時点Cでの装炭後の経過時間Yの何れかを確認できる
ものとすれば、当該原料石炭の乾留終了時点,ひいて
は、目的とするところのコークスの生成完了に該当する
火落ち時点Cを、そのコークスの生成完了の以前にあつ
て容易に予測できることになる。
Therefore, during the carbonization operation of the charged raw coal, any of the generated gas temperature T at the above-mentioned burn-down time point C or the elapsed time Y after coal-burning at the burn-out time point C can be confirmed in advance. Then, the time point at which the carbonization of the raw coal ends, and thus the time point C at which the intended coke generation is completed, can be easily predicted before the completion of the coke generation.

そしてまた、本発明者らによる鋭意研究の結果によれ
ば、乾留操作中での発生ガス温度の経時変化が、原料石
炭の装入時点での温度域から、実質的に平均化された温
度Taとなる水平温度域Aを経て、一旦最高温度Tbに達
した後、再度実質水平温度域Aに下降するまでの時間X
と、コークスの生成が完了する火落ち時間Yとの間にも
密接な関係があつて、こゝでは、関係式 Y=aX+b 式中、a,bは炉形式、操業温度および装入炭水分、装
入炭量などの装入条件によつて決定される定数 が成立することが判明した。
Further, according to the results of the earnest study by the present inventors, the change with time of the generated gas temperature during the carbonization operation is substantially equalized from the temperature range at the time of charging the raw coal to the temperature T. through the horizontal temperature zone a to be a, once after reaching the maximum temperature T b, until descends substantially horizontally temperature range a again time X
There is also a close relationship between the burn-off time Y and the completion of coke formation, where the relational expression Y = aX + b, where a and b are the furnace type, operating temperature and coal moisture It was found that the constants determined by the charging conditions such as the amount of coal charged were satisfied.

仍つてこのために、予備操業などによつて、予め前記
関係式の定数a,bを求めておけば、実際の操業時には、
実質水平温度域Aにおける平均ガス温度Taから、当該
操業での火落ち時点における発生ガス温度Tを簡単に算
出し得て、目的とする火落ち時点Cを極めて容易に予測
することができるのである。
For this reason, if the constants a and b of the above relational expression are obtained in advance by preliminary operation or the like, during actual operation,
From the average gas temperature T a at substantially horizontal temperature zone A, and obtained easily calculating the generated gas temperature T in the fire fall time in the operation, it is possible to predict the fire fall time C of interest very easily is there.

またこゝで、第3図には、実質水平温度域Aにおける
発生ガスの平均温度Taを基準にした前記各時間X,Yの関
係を示してあるが、同図から明らかなように、この実施
例方法の場合、実質水平温度域Aにおける平均ガス温度
aは、乾留初期から終期に近い比較的安定した状態の
領域での発生ガス温度であることから、温度のバラツキ
が非常に少なく、このために、より高精度による火落ち
時点の予測が可能になる。
In Matakoko, the third figure, as each time X relative to the average temperature T a of the generated gas in the substantially horizontal temperature range A, but are shown the relationship between Y, it is evident from the figure, in this embodiment method, the average gas temperature T a at substantially horizontal temperature range a, since a generated gas temperature in the region of relatively stable state close to the end of the dry distillation initial, variation in temperature is very low For this reason, it is possible to more accurately predict the time of a fire.

〔発明の効果〕〔The invention's effect〕

以上詳述したように、この発明方法によれば、コーク
スの生成に際して、原料石炭の乾留中に発生するガス温
度の経時変化が、装入時点での温度域から、実質的に平
均化された温度となる水平温度域を経て、一旦最高温度
に達した後、再度実質水平温度域に下降するまでの時間
Xと、コークスの生成が完了する火落ち時間Yとの間
に、関係式Y=aX+b(同式中、a,bは炉形式、操業温
度および装入炭水分、装入炭量などの装入条件によつて
決定される定数)が成立する点に鑑み、予め同式の定数
a,bを求めておき、乾留操作中にあつて、単に、発生ガ
スの温度を測定するだけの手段により、その実質水平温
度域における平均ガス温度から、コークスの生成完了に
先立つて、火落ち時点における発生ガス温度,ひいて
は、当該火落ち時点自体を簡単に算出することが可能に
なり、この結果、こゝでの所要の火落ち時点を極めて容
易に予測できるもので、従来のようにトップカバーを頻
繁に開放して発生ガスの色合を観察する手段とは異なつ
て、相応の熟練を必要としたり、発生ガスの放出に伴う
環境汚染とか、エネルギー損失がなく、生成コークスの
品質低下を招く惧れもないなどの利点を有し、併せて、
精度の高い予測が可能になるなどの優れた特長がある。
As described in detail above, according to the method of the present invention, during the production of coke, the change over time in the gas temperature generated during carbonization of the raw coal was substantially averaged from the temperature range at the time of charging. After the temperature reaches the maximum temperature once through the horizontal temperature range where the temperature reaches the maximum temperature and then falls to the substantially horizontal temperature range again, and the burn-out time Y when the coke generation is completed, the relational expression Y = In view of the fact that aX + b (where a and b are constants determined by the furnace type, operating temperature and charging conditions such as charged coal moisture and charged coal quantity) is satisfied, the constants of the same equation must be satisfied in advance.
a and b are determined, and during the carbonization operation, by means of simply measuring the temperature of the generated gas, the fire is dropped from the average gas temperature in the substantially horizontal temperature range before the completion of coke generation. It is possible to easily calculate the temperature of the generated gas at the time point and, consequently, the burn-out time itself. As a result, the required burn-out time can be predicted very easily. Unlike means for opening the cover frequently and observing the color of the generated gas, it requires appropriate skill, does not cause environmental pollution due to release of the generated gas, does not lose energy, and leads to deterioration in the quality of produced coke It has advantages such as fearless,
It has excellent features such as highly accurate prediction.

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

第1図はこの発明の一実施例を適用するコークス炉の要
部を模式的に示す断面構成図、第2図は装炭後の経過時
間と発生ガス温度との関係を示す説明図、第3図は装炭
後3時間〜9時間の発生ガス温度の平均に用いた火落ち
時間の予測を示すグラフである。 1……コークス炉の乾留室、2……上昇管、3……トッ
プカバー、4……ベンド部、5……ガス集合管、6……
温度測定手段(熱電対など)。 A……実質水平温度域、B……最高温度点、C……火落
ち時点。
FIG. 1 is a sectional view schematically showing a main part of a coke oven to which one embodiment of the present invention is applied, FIG. 2 is an explanatory view showing a relationship between an elapsed time after coal charging and a generated gas temperature. FIG. 3 is a graph showing the prediction of the burn-off time used for averaging the generated gas temperatures from 3 hours to 9 hours after coal charging. 1 ... carbonization chamber of coke oven, 2 ... riser pipe, 3 ... top cover, 4 ... bend section, 5 ... gas collecting pipe, 6 ...
Temperature measurement means (such as thermocouples). A: substantial horizontal temperature range, B: maximum temperature point, C: time of fire.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】石炭を乾留処理してコークスを生成するコ
ークス炉において、当該コークス炉の上昇管または上昇
管ベンド部に設けた温度測定手段により、原料石炭の乾
留操作中に発生するガス温度を測定して、予め当該発生
ガス温度の経時変化が、原料石炭の装入時点での温度域
から、実質的に平均化された温度となる水平温度域を経
て、最高温度に上昇した後、再度、平均温度域に下降す
るまでの時間Xと、コークスの生成が完了する火落ち時
間Yとの関係式 Y=aX+b 式中、a,bは炉形式、操業温度および装入炭水分、装入
炭量などの装入条件によつて決定される定数 を求めておき、前記温度測定手段により、乾留中の発生
ガス温度を逐次に測定して、前記実質水平温度域の平均
温度を算出し、当該算出温度から前記関係式に基づいて
火落ち時間を事前に予測し得るようにしたことを特徴と
するコークス炉の火落ち時間予測方法。
In a coke oven for producing coke by subjecting coal to carbonization, the temperature of gas generated during carbonization of raw coal is measured by temperature measuring means provided in a riser or a riser bend of the coke oven. Measured, the time-dependent change of the generated gas temperature in advance, from the temperature range at the time of charging the raw coal, through a horizontal temperature range that becomes substantially averaged temperature, to rise to the highest temperature, then again , A relational expression between the time X until the temperature falls to the average temperature range and the burn-out time Y at which the coke generation is completed Y = aX + b where a and b are the furnace type, operating temperature and charged coal moisture, and charged. A constant determined according to the charging conditions such as the amount of coal is determined in advance, and the temperature of the generated gas during the dry distillation is sequentially measured by the temperature measuring means to calculate an average temperature in the substantially horizontal temperature range. Based on the calculated temperature, Fire drop time prediction method of the coke oven, characterized in that it has adapted to predict Chi time in advance.
JP10892390A 1990-04-26 1990-04-26 Prediction method of fire time of coke oven Expired - Fee Related JP2872343B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10892390A JP2872343B2 (en) 1990-04-26 1990-04-26 Prediction method of fire time of coke oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10892390A JP2872343B2 (en) 1990-04-26 1990-04-26 Prediction method of fire time of coke oven

Publications (2)

Publication Number Publication Date
JPH048797A JPH048797A (en) 1992-01-13
JP2872343B2 true JP2872343B2 (en) 1999-03-17

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JP5954382B2 (en) * 2013-09-24 2016-07-20 Jfeスチール株式会社 How to detect a fire in a coke oven

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