JPH061981A - Method for predicting volume of produced gas in coke oven - Google Patents

Method for predicting volume of produced gas in coke oven

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Publication number
JPH061981A
JPH061981A JP18629492A JP18629492A JPH061981A JP H061981 A JPH061981 A JP H061981A JP 18629492 A JP18629492 A JP 18629492A JP 18629492 A JP18629492 A JP 18629492A JP H061981 A JPH061981 A JP H061981A
Authority
JP
Japan
Prior art keywords
time
volume
amount
coal
carbonization
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
JP18629492A
Other languages
Japanese (ja)
Inventor
Takafumi Sachi
佐地孝文
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
Sumitomo Metal Industries Ltd
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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP18629492A priority Critical patent/JPH061981A/en
Publication of JPH061981A publication Critical patent/JPH061981A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To accurately predict the volume of produced gases in fluctuation of an interval for block units in coke pushing operation of a coke oven according to a specific method. CONSTITUTION:The fluctuation in volume of produced gases with the elapse of time during a period from charging of coal to discharging of coke in respective carbonization chambers of a coke oven battery composed of the many carbonization chambers is initially computed and estimated from the amount of the charged coal, coal volatile content, holding time and dry distillation time. The volume of the produced gases in the coke oven battery is then predicted by utilizing the fluctuation in the volume of the produced gases with time. The computation of the fluctuation in the volume of the produced gases with time is carried out by utilizing the phenomenon that the fluctuation in the volume of the produced gases is proportional to the volatile content and amount of charged coal regardless of the elapsed time of dry distillation. When the holding time fluctuates from the reference value (HA) to (HB), the timing of the volume of the produced gases is horizontally displaced in proportion to the time of only carbonization. Furthermore, when the dry distillation time fluctuates from the reference value (KA) to (KB), the timing of the volume of the produced gases is preferably horizontally displaced in proportion to the time of only the carbonization and the volume of the produced gases is preferably made inversely proportional to the time of only carbonization (KB/KA).

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、多数の炭化室を有す
るコークス炉団のガス発生量を予測する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for predicting the gas generation amount of a coke oven cluster having a large number of carbonization chambers.

【0002】[0002]

【従来の技術】室炉式コークス炉は、蓄熱室の上部に炭
化室と燃焼室が交互に配置されており、炭化室に装入さ
れた装入炭は両側の燃焼室から炉壁を介して加熱乾留さ
れコークス化される。コークス炉は、数十ないし百余窯
程度で一炉団が形成され、炭化室からのコークスの排出
と、炭化室への装炭を行う窯出し作業はバッチである
が、通常はそのインターバルは稼働率に応じて大体一定
に定められており、燃焼用ガス量の総量は一定量となる
ような操業が実施されている。
2. Description of the Related Art In a chamber furnace type coke oven, a carbonization chamber and a combustion chamber are alternately arranged above a heat storage chamber, and the charging coal charged in the carbonization chamber is passed from the combustion chambers on both sides through a furnace wall. It is heated to dry distillation and coke. In the coke oven, one furnace group is formed in several tens to hundreds of kilns, and the discharge of coke from the carbonization chamber and the kiln removal work for carbonizing the carbonization chamber are batches, but the interval is usually It is set to be roughly constant according to the operating rate, and operations are carried out so that the total amount of combustion gas is constant.

【0003】上記コークス炉の炭化室の1室において石
炭装入から乾留終了までのガス発生量の経時変化は、数
多くの測定例が発表されているが、図6に示すようなパ
ターンとなり、ガス発生量は時間の経過と共にかなり大
幅に変動する。すなわち、装炭直後は、炭化室壁側の石
炭の急速な急速な乾留により多量のガスが発生し、ま
た、乾留後半の発生ガス温度700〜800℃で水素が
放出されるためのピークが表れる。しかしながら、コー
クス炉の窯出しインターバルは、稼働率に応じて大体一
定に定められているため、コークス炉団からのガス発生
総量は経時的にほぼ一定とみなすことができる。
A large number of measurement examples of the time-dependent change in the amount of gas generated from the charging of coal to the end of carbonization have been published in one of the carbonization chambers of the above coke oven. The amount generated fluctuates considerably over time. That is, immediately after carbonization, a large amount of gas is generated by the rapid and rapid carbonization of coal on the side of the carbonization chamber wall, and a peak appears because hydrogen is released at the generated gas temperature of 700 to 800 ° C. in the latter half of carbonization. . However, the firing interval of the coke oven is set to be approximately constant according to the operating rate, and therefore the total amount of gas generated from the coke oven cluster can be considered to be substantially constant over time.

【0004】一方、コークス炉の窯出し作業は、3直4
交替制で実施されているため、直の交替や、コークス炉
移動機械の故障修理、あるいはガス吸引系統の設備トラ
ブル等によって、前記窯出しインターバルが大幅に変動
することがしばしば発生する。コークス炉の窯出しイン
ターバルが大きく変動した場合は、コークス炉団からの
ガス発生量が経時的に大幅に変動し、後工程のガス精製
工程に不均一な負荷を与えるばかりでなく、コークス炉
ガスを燃料として使用している工場に多大の迷惑をかけ
ることとなる。しかしながら、このガス発生量の経時的
変動は、正確に把握することは非常に困難である。
On the other hand, the kiln removal work of the coke oven is 3 straight 4
Since the system is carried out by the shift system, the kiln discharge interval often changes greatly due to a direct shift, a trouble repair of the coke oven moving machine, a facility trouble of the gas suction system, or the like. When the firing interval of the coke oven fluctuates significantly, the amount of gas generated from the coke oven group fluctuates significantly over time, which not only gives a non-uniform load to the gas purification process in the subsequent process, but also the coke oven gas. This will cause a great deal of inconvenience to the factories that use fuel as fuel. However, it is very difficult to accurately grasp the variation with time of the gas generation amount.

【0005】上記コークス炉からのガス発生量を予測・
推定する方法としては、演算装置内に各炭化室における
石炭装入開始からコークス排出にいたる間のガス単位発
生量の経時的変化に基づいて求められるコークス炉団か
らのガス発生総量の経時的変化を現出し得る一連の計算
式を入力しておき、前記各炭化室における石炭の装入時
刻、今後の装入予定時刻およびコークス炉団からのガス
発生総量を検出・予測したい時刻を、前記演算装置に入
力することにより検出・予測希望時刻におけるコークス
炉団からのガス発生総量を演算させて出力させる(特開
昭57−121088号公報)、各炭化室に装入される
石炭量と、石炭装入からコークス排出に至る間のガス発
生量の経時的変化に基づいて求められるコークス炉団か
らのガス発生量を示す式と、過去のガス発生総量実績値
と過去のガス発生総量予測値に基づくガス発生総量予測
誤差を推定する式とによりガス発生総量を予測する都
度、新たな装入石炭量とガス発生総量測定値を前記各式
に加えて順次修正しながらガス発生総量を予測する(特
開平1−98693号公報)、あるいはガス発生パター
ンの近似式を、装炭から火落2時間前の第1段階と、火
落2時間前から火落までの第2段階と、火落から窯出し
までの第3段階の3つの式に要約し、かつガス発生量の
推定計算においては、石炭に含有される酸素量に応じた
補正を行う(特開平2−102292号公報)等が提案
されている。
Predict gas generation from the coke oven
As a method of estimation, the change over time in the total amount of gas generated from the coke oven cluster, which is calculated based on the change over time in the amount of gas generated from the start of coal charging in each carbonization chamber to the discharge of coke in the arithmetic unit, was used. By inputting a series of calculation formulas that can express the above, the calculation time of the coal charging time in each of the carbonization chambers, the expected charging time in the future, and the time when it is desired to detect and predict the total amount of gas generated from the coke oven cluster is calculated. By inputting into the device, the total amount of gas generated from the coke oven cluster at the desired detection / prediction time is calculated and output (Japanese Patent Laid-Open No. 57-121088). An equation showing the amount of gas generated from the coke furnace group, which is calculated based on the change over time in the amount of gas generated from the charging to the discharge of coke, and the actual total amount of gas generated in the past and the amount of gas generated in the past. Each time the total gas generation amount is predicted by the formula for estimating the total gas generation amount prediction error based on the amount prediction value, the new amount of coal charged and the total gas generation amount measurement value are added to each of the above formulas while sequentially correcting the total gas generation amount. (Japanese Patent Laid-Open No. Hei 1-98693), or an approximate expression of the gas generation pattern, a first stage 2 hours before the burn down from the coal charging, and a second stage 2 hours before the burn down to the burn down. , Is summarized in three equations in the third stage from the fall of the fire to the kiln removal, and in the estimation calculation of the gas generation amount, correction is made according to the amount of oxygen contained in the coal (Japanese Patent Laid-Open No. 2-102292). ) Etc. have been proposed.

【0006】[0006]

【発明が解決しようとする課題】上記特開昭57−12
1088号公報に開示の方法は、各炭化室における石炭
装入からコークス排出までの間のガス発生量の経時的変
化に基づいてコークス炉団からのガス発生総量の経時的
変化を現出し得る一連の計算式に、各炭化室への石炭装
入時刻、今後の装入予定時刻およびコークス炉団からの
ガス発生総量を検出・予測したい時刻を入力して演算さ
せており、操業条件の変動や装入石炭性状などの各種ガ
ス発生量に変動を及ぼす因子が加味されておらず、満足
な予測ができない。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
The method disclosed in Japanese Patent No. 1088 discloses a series of time-dependent changes in the total amount of gas generated from a coke oven cluster based on changes in the amount of gas generated from the charging of coal to the discharge of coke in each carbonization chamber. In the calculation formula, the coal charging time into each coking chamber, the expected charging time in the future, and the time at which it is desired to detect and predict the total amount of gas generated from the coke oven corps are input and calculated, and fluctuations in operating conditions and Satisfactory forecasts cannot be made because factors that affect the amount of various gases generated, such as the properties of charged coal, are not added.

【0007】また、特開平1−98693号公報に開示
の方法は、各炭化室に装入された石炭量と、石炭装入か
らコークス排出までの間のガス発生量の経時的変化に基
づいて求められるコークス炉団からのガス発生総量を、
過去の実績値と予測値の誤差を推定する式により予測
し、その都度新たな装入石炭量とガス発生総量測定値を
加えて順次修正するもので、操業条件の変動が加味され
ておらず、十分満足なガス発生総量の予測は困難であ
る。
Further, the method disclosed in JP-A-1-98693 is based on the amount of coal charged in each carbonization chamber and the change over time in the gas generation amount from the charging of coal to the discharge of coke. The total amount of gas generated from the coke oven group required
Prediction is performed using an equation that estimates the difference between the past actual value and the predicted value, and each time it is corrected by adding a new amount of coal charged and the measured value of the total amount of gas generated, no change in operating conditions is taken into consideration. However, it is difficult to predict a sufficiently satisfactory total gas generation amount.

【0008】さらに特開平2−102292号公報に開
示の方法は、ガス発生パターンの近似式を3つの式に要
約し、かつガス発生量の推定計算において石炭に含有さ
れる酸素量に応じた補正を行うもので、特開平1−98
693号公報に開示の方法と同様に操業条件の変動が加
味されておらず、十分満足なガス発生総量の予測は困難
である。
Further, the method disclosed in Japanese Patent Application Laid-Open No. 2-102292 summarizes the approximate formula of the gas generation pattern into three formulas, and corrects the estimated amount of gas generation according to the amount of oxygen contained in coal. The method described in JP-A-1-98
Similar to the method disclosed in Japanese Patent No. 693, fluctuations in operating conditions are not taken into consideration, and it is difficult to predict a sufficiently satisfactory total gas generation amount.

【0009】この発明の目的は、コークス炉の窯出し作
業におけるブロック単位内のインターバル変動時のガス
発生量を、ほぼ正確に短時間で行うことによって、コー
クス炉団のガス発生量を正確に予測できるガス発生量予
測方法を提供することにある。
An object of the present invention is to accurately predict the gas generation amount of a coke oven cluster by performing the gas generation amount during interval fluctuations within a block unit in the coke oven kiln removal work almost accurately in a short time. It is to provide a method of predicting the amount of gas generated.

【0010】[0010]

【課題を解決するための手段】本発明者らは、上記目的
を達成すべく鋭意試験研究を行った。その結果、各炭化
室からのガス発生量に影響を与える要因としては、装入
する石炭の揮発分、装炭量および乾留時間、置時間等の
乾留条件が考えられ、これら各要因の影響について種々
の条件下での実炉テストによって、石炭の揮発分、装炭
量の変動によるガス発生量の変動は、乾留経過時間に関
係なく揮発分、装炭量に比例し、置時間の変動によるガ
ス発生量の変動は、乾留経過時間におけるガス発生量の
タイミングを置時間に比例して水平移動すればよく、乾
留時間の変動によるガス発生量の変動は、乾留経過時間
におけるガス発生量のタイミングを火落時間に比例して
水平移動すると共に、ガス発生量を火落時間に比例させ
ればよいことを究明し、この発明に到達した。
[Means for Solving the Problems] The inventors of the present invention have conducted earnest research to achieve the above object. As a result, as factors affecting the amount of gas generated from each carbonization chamber, volatile matter of the coal to be charged, carbonization amount and carbonization time such as carbonization time, storage time, etc. are considered. According to the actual furnace test under various conditions, the fluctuation of the gas generation amount due to the fluctuation of the coal volatile matter and the coal charging amount is proportional to the volatile matter and the coal charging amount regardless of the dry distillation elapsed time, The fluctuation of the gas generation amount can be achieved by horizontally moving the timing of the gas generation amount during the dry distillation elapsed time in proportion to the standing time.The fluctuation of the gas generation amount due to the change of the dry distillation time depends on the timing of the gas generation amount during the dry distillation elapsed time. The present invention has been accomplished by moving horizontally along with the fire fall time and by making the gas generation amount proportional to the fire fall time.

【0011】すなわちこの発明は、多数の炭化室からな
るコークス炉団の各炭化室における石炭装入からコーク
ス排出までの間のガス発生量の経時的変動に基づいてコ
ークス炉団からのガス発生量を演算予測する方法におい
て、各炭化室のガス発生量の経時的変動を装炭量、石炭
揮発分、置時間ならびに乾留時間から演算推定し、この
推定した各炭化室のガス発生量の経時的変動を用いてコ
ークス炉団のガス発生量を予測するのである。
That is, according to the present invention, the amount of gas generated from the coke oven cluster is calculated based on the change over time in the amount of gas produced from the charging of coal to the discharge of coke in each carbonization chamber of the coke oven cluster consisting of a large number of carbonization chambers. In the method of calculating and predicting the above, the temporal change in the gas generation amount of each carbonization chamber is calculated and estimated from the coal charging amount, the coal volatile matter, the set time and the carbonization time, and the estimated gas generation amount of each carbonization chamber is changed over time. Fluctuations are used to predict the amount of gas produced by the coke oven cluster.

【0012】[0012]

【作用】コークス炉の窯出し作業は、通常5窯ピッチを
1つのブロックとするブロック単位で実施されており、
一般には各ブロック間のインターバルが大体一定になる
よう実施されている。このため、窯出し作業のインター
バルの変更は、各ブロック単位で行われることが多い
が、ブロック途中で変更される場合もあり、ガス発生量
の変動も大きい。この発明における各炭化室のガス発生
量の経時的変動を装炭量、石炭揮発分、置時間ならびに
乾留時間から演算するには、装炭量が例えば基準値Aか
らBに増加すると、図1に示すとおり、乾留経過時間
(i)におけるガス発生量は、ほぼ装炭量に比例してa
からbに増加する。また、石炭揮発分が例えば基準値V
AからVBに変動すると、図2に示すとおり、ほぼ揮発分
からのガス発生推定式(k1B+k2/k1A+k2、た
だしk1:揮発分の係数、k2:定数)に比例する。さら
に、置時間が例えば基準値HAからHBに延長すると、図
3に示すとおり、ガス発生量のタイミングを火落時間に
比例して水平移動すればよい。さらにまた、乾留時間が
例えば基準値KAからKBに延長すると、図4に示すとお
り、ガス発生量のタイミングを火落時間に比例して水平
移動すると共に、ガス発生量を火落時間KB/KAに反比
例させればよい。
[Operation] The coke oven kiln removal work is usually carried out in block units with 5 kiln pitches as one block,
Generally, the intervals between blocks are set to be almost constant. Therefore, the interval of the kiln removal work is often changed in each block, but it may be changed in the middle of the block, and the gas generation amount varies greatly. In order to calculate the temporal variation of the gas generation amount of each carbonization chamber in the present invention from the coal charging amount, the coal volatile matter, the set time and the carbonization time, when the coal charging amount is increased from the reference value A to B, for example, FIG. As shown in, the gas generation amount in the dry distillation elapsed time (i) is approximately a in proportion to the amount of coal charging.
To b. Further, the coal volatile matter is, for example, the reference value V.
When changing from A to V B , as shown in FIG. 2, a gas generation estimation formula (k 1 V B + k 2 / k 1 VA + k 2) , where k 1 is a coefficient of volatile matter and k 2 is a constant. ). Further, when the set time is extended from the reference value H A to H B , for example, the timing of the gas generation amount may be horizontally moved in proportion to the fire fall time, as shown in FIG. Furthermore, when the dry distillation time is extended from the reference value K A to K B , for example, as shown in FIG. 4, the timing of the gas generation amount is horizontally moved in proportion to the fire fall time, and the gas generation amount is changed to the fire fall time K. It should be inversely proportional to B / K A.

【0013】上記各炭化室の装炭量、石炭揮発分、置時
間ならびに乾留時間から演算推定したガス発生量の経時
的変動を合成することによって、装炭量、石炭揮発分、
置時間ならびに乾留時間の基準条件を決定すれば、種々
の条件下での任意乾留時間におけるガス発生量を正確に
予測することが可能となる。したがって、ブロック途中
での窯出しインターバルの変更によるガス発生量の経時
的変動は、窯出しブロック内の各炭化室のガス発生量を
演算推定することによって、全体として迅速かつ正確に
コークス炉団のガス発生量を予測することができる。
The coal charging amount, coal volatile matter, coal volatile matter, coal volatile matter, coal volatile matter, coal volatile matter, coal volatile matter
By determining the standard conditions for the standing time and the dry distillation time, it becomes possible to accurately predict the gas generation amount under the arbitrary dry distillation time under various conditions. Therefore, the time-dependent fluctuation of the gas generation rate due to the change of the kiln discharge interval in the middle of the block can be quickly and accurately determined as a whole by calculating and estimating the gas generation amount of each carbonization chamber in the kiln discharge block. The amount of gas generated can be predicted.

【0014】[0014]

【実施例】炉高7125mm、炉幅460mm、炉長1
6500mmの炭化室を72室有するコークス炉団にお
いて、火落時間20.9時間、置時間2.0時間での操
業における窯出しブロック途中で2時間の窯出し遅れの
インターバル変更を行った場合のガス発生量の経時的変
動を、各炭化室毎のガス発生量の経時的変動を演算推定
し、これに基づいてコークス炉団のガス発生量の経時的
変動を予測すると共に、実績値を測定した。その結果を
図5に示す。図5に示すとおり、この発明方法により予
測した破線で示すガス発生量は、実線で示す実績値とよ
く一致しており、ブロック途中での窯出しインターバル
の変更にも十分に対応している。
[Example] Furnace height 7125 mm, furnace width 460 mm, furnace length 1
In a coke oven cluster with 72 carbonization chambers of 6500 mm, when changing the interval of the firing delay of 2 hours in the firing block during the operation with the burn down time of 20.9 hours and the operating time of 2.0 hours, Estimate the time-dependent change of the gas generation amount of each coking chamber, and predict the time-dependent change of the gas generation amount of the coke furnace group based on this, and measure the actual value. did. The result is shown in FIG. As shown in FIG. 5, the gas generation amount shown by the broken line predicted by the method of the present invention agrees well with the actual value shown by the solid line, and sufficiently corresponds to the change of the kiln discharge interval in the middle of the block.

【0015】[0015]

【発明の効果】以上述べたとおり、この発明方法によれ
ば、各炭化室から発生するガス発生量の経時的変動を、
装炭量、装入する石炭揮発分、置時間ならびに乾留時間
に基づいて正確に演算推定することによって、窯出しブ
ロック途中での窯出しインターバルの変更に対するガス
発生量の経時的変動の予測を、迅速かつ高精度で実施す
ることができ、後工程のガス精製工程に不均一な負荷を
与えることが防止でき、コークス炉ガスを燃料として使
用している工場に多大の迷惑をかけることもない。
As described above, according to the method of the present invention, the variation with time of the gas generation amount generated from each carbonization chamber can be
By accurately calculating and estimating based on the coal loading amount, the coal volatile matter to be charged, the set time and the dry distillation time, it is possible to predict the change over time in the gas generation amount with respect to changes in the kiln discharge interval during the kiln discharge block, It can be carried out quickly and with high precision, can prevent uneven load from being applied to the gas purification process in the subsequent process, and does not cause much trouble to the factory that uses coke oven gas as fuel.

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

【図1】装炭量が増加した場合のガス発生量の経時的変
動を基準と比較して示すグラフである。
FIG. 1 is a graph showing a change over time in a gas generation amount when a coal charging amount is increased in comparison with a reference.

【図2】装入石炭の揮発分が増加した場合のガス発生量
の経時的変動を基準と比較して示すグラフである。
FIG. 2 is a graph showing changes over time in the gas generation amount when the volatile content of the charged coal increases, compared with a reference.

【図3】置時間が延長した場合のガス発生量の経時的変
動を基準と比較して示すグラフである。
FIG. 3 is a graph showing changes over time in the amount of gas generated when the standing time is extended, compared with a reference.

【図4】乾留時間が延長した場合のガス発生量の経時的
変動を基準と比較して示すグラフである。
FIG. 4 is a graph showing changes over time in the amount of gas generated when the dry distillation time is extended, in comparison with a reference.

【図5】実施例におけるコークス炉団のガス発生量の経
時的変動の実績と予測を示すグラフである。
FIG. 5 is a graph showing actual results and predictions of changes over time in the gas generation amount of the coke oven cluster in the example.

【図6】通常の炭化室におけるガス発生量の経時的変動
のパターンを示すグラフである。
FIG. 6 is a graph showing a variation pattern of a gas generation amount with time in a normal carbonization chamber.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 多数の炭化室からなるコークス炉団の各
炭化室における石炭装入からコークス排出までの間のガ
ス発生量の経時的変動に基づいてコークス炉団からのガ
ス発生量を演算予測する方法において、各炭化室のガス
発生量の経時的変動を装炭量、石炭揮発分、置時間なら
びに乾留時間から演算推定し、この推定した各炭化室の
ガス発生量の経時的変動を用いてコークス炉団のガス発
生量を予測することを特徴とするコークス炉のガス発生
量の予測方法。
1. A gas generation amount from a coke furnace group is calculated and predicted based on a temporal change in the gas generation amount from the charging of coal to the discharge of coke in each carbonization chamber of a coke furnace group consisting of a large number of carbonization chambers. In the method described above, the time-dependent fluctuation of the gas generation amount of each carbonization chamber is calculated and estimated from the coal charging amount, the coal volatile matter, the set time and the carbonization time, and the time-dependent change of the gas generation amount of each estimated carbonization chamber is used. A method for predicting gas generation in a coke oven, characterized by predicting gas generation in a coke oven cluster.
JP18629492A 1992-06-19 1992-06-19 Method for predicting volume of produced gas in coke oven Pending JPH061981A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18629492A JPH061981A (en) 1992-06-19 1992-06-19 Method for predicting volume of produced gas in coke oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18629492A JPH061981A (en) 1992-06-19 1992-06-19 Method for predicting volume of produced gas in coke oven

Publications (1)

Publication Number Publication Date
JPH061981A true JPH061981A (en) 1994-01-11

Family

ID=16185802

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18629492A Pending JPH061981A (en) 1992-06-19 1992-06-19 Method for predicting volume of produced gas in coke oven

Country Status (1)

Country Link
JP (1) JPH061981A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000041661A (en) * 1998-12-23 2000-07-15 이구택 Method for estimating total amount of generation of coke oven gas during periodic maintenance of coke furnace
KR20020052831A (en) * 2000-12-26 2002-07-04 신현준 Method for predicting COG production
KR101443505B1 (en) * 2013-02-28 2014-09-24 현대제철 주식회사 Method for forecasting generating quantity of coke oven gas
JP2016098282A (en) * 2014-11-20 2016-05-30 Jfeスチール株式会社 Coke oven gas recovery method and recovery apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000041661A (en) * 1998-12-23 2000-07-15 이구택 Method for estimating total amount of generation of coke oven gas during periodic maintenance of coke furnace
KR20020052831A (en) * 2000-12-26 2002-07-04 신현준 Method for predicting COG production
KR101443505B1 (en) * 2013-02-28 2014-09-24 현대제철 주식회사 Method for forecasting generating quantity of coke oven gas
JP2016098282A (en) * 2014-11-20 2016-05-30 Jfeスチール株式会社 Coke oven gas recovery method and recovery apparatus

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