Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS597751B2 - Method for predicting fire-down time of coke oven - Google Patents
[go: Go Back, main page]

JPS597751B2 - Method for predicting fire-down time of coke oven - Google Patents

Method for predicting fire-down time of coke oven

Info

Publication number
JPS597751B2
JPS597751B2 JP647279A JP647279A JPS597751B2 JP S597751 B2 JPS597751 B2 JP S597751B2 JP 647279 A JP647279 A JP 647279A JP 647279 A JP647279 A JP 647279A JP S597751 B2 JPS597751 B2 JP S597751B2
Authority
JP
Japan
Prior art keywords
temperature
time
generated gas
fire
maximum
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
Application number
JP647279A
Other languages
Japanese (ja)
Other versions
JPS5598280A (en
Inventor
春夫 山村
正久 小野
喜保 阪本
洋一 田村
俊行 山本
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 JP647279A priority Critical patent/JPS597751B2/en
Publication of JPS5598280A publication Critical patent/JPS5598280A/en
Publication of JPS597751B2 publication Critical patent/JPS597751B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Coke Industry (AREA)

Description

【発明の詳細な説明】 この発明は、コークス炉炭化室に装入した石炭の乾留が
完了する時刻(以下火落と称す)を予測するコークス炉
の火落時刻予測方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coke oven burn-off time prediction method for predicting the time when carbonization of coal charged in a coke oven carbonization chamber is completed (hereinafter referred to as burn-off time).

コークス炉において、従来の火落時刻の予測方法は、装
入炭の量、水分、粒度、揮発分などの装入炭諸元と装炭
から火落までの炭化室両側燃焼室の平均炉温から火落時
刻を予測する方法があるが、この方法では石炭乾留の進
行状況を表わす情報を何もとり入れていないために約2
0時間先の火落時刻を予測するには誤差が大きく不正確
であり、炭化室の火落予測方法としては、上記方法は実
用できなかった。
In a coke oven, the conventional method for predicting the burnout time is based on the characteristics of the charged coal, such as the amount of charged coal, moisture content, particle size, and volatile content, and the average furnace temperature of the combustion chambers on both sides of the coking chamber from coal loading to the burnout. There is a method of predicting the fire-fall time from
Predicting the firefall time 0 hours in advance involves large errors and is inaccurate, and the above method could not be put to practical use as a method for predicting firefall in the carbonization chamber.

又、他の方法では、火落時の発生ガス温度Yと、装炭か
ら火落までの経過時間Xとの相関関係を次式Y=aX十
b(a,bは定数)で求めておき、発生ガスを排出する
上昇管部の測温値と装炭からの経過時間が前紀相関関係
式を満す時を火落時刻と判定する方法があるが、これは
発生ガス温度の変化を常時測定し、しかも発生ガス温度
は実測値を用いているので、発生ガス中に含まれるター
ルなどが温度測定器に付着して検出温度が時間の経過と
共に不正確になっていた。
In addition, in another method, the correlation between the generated gas temperature Y at the time of fire-break and the elapsed time X from coal loading to fire-break is calculated using the following formula Y = a There is a method of determining the fire-break time when the measured temperature value of the riser pipe section that discharges generated gas and the elapsed time from coal loading satisfy the correlation equation, but this method is based on the change in the temperature of the generated gas. Since the temperature of the generated gas is constantly measured and actual measured values are used, tar contained in the generated gas adheres to the temperature measuring device, causing the detected temperature to become inaccurate over time.

又、温度測定位置や気温、雨天などの気候の状態によっ
ても発生ガス温度は変化するので、火落時刻を正確に予
測することができなかった。
In addition, the temperature of the generated gas changes depending on the temperature measurement location, air temperature, and climatic conditions such as rainy weather, making it impossible to accurately predict the time of fire.

以上の如く、従来の方法は火落時刻の予測が不正確であ
るから、乾留過剰による燃焼エネルギー損失や乾留不良
によるコークス品質のバラツキが大きいという問題があ
った。
As described above, the conventional method has problems in that the prediction of the fire-off time is inaccurate, resulting in large variations in coke quality due to combustion energy loss due to excessive carbonization and insufficient carbonization.

この発明は、上記の欠点を解消することを目的とするコ
ークス炉の火落時刻予測方法を提案するものである。
This invention proposes a method for predicting the fire-off time of a coke oven, which aims to eliminate the above-mentioned drawbacks.

以下、この発明を図面について説明する。The present invention will be explained below with reference to the drawings.

発明者は、第1図に示すように、コークス炉1の上昇管
2の屈曲部に熱電対3を挿入して炭化室4から排出され
る発生ガス温度を連続的に多数測定した結果、発生ガス
温度が最高値を示す時は、炭化室内の炭層が乾留過程中
である一定の状態に達していることが判明した。
As shown in FIG. 1, the inventor inserts a thermocouple 3 into the bent part of the riser pipe 2 of the coke oven 1 and continuously measures the temperature of the generated gas discharged from the carbonization chamber 4. It was found that when the gas temperature reached its maximum value, the coal bed in the carbonization chamber had reached a certain state during the carbonization process.

なお、5は発生ガス集合ダクトである。Note that 5 is a generated gas collection duct.

そして、前記状態になってから火落するまでに必要な石
炭乾留のための総熱量は、炉型式(通常炉型式が決まれ
ば装入炭量は一定である)が決まれば一意に決定される
The total amount of heat required for coal carbonization from the time the above condition is reached to the time of fire-off is uniquely determined once the furnace type (normally, once the furnace type is determined, the amount of charged coal is constant) .

一方、燃焼室への単位時間当りの投入熱量はコークス炉
の設備構造上測定不可能であるが、装炭時刻から発生ガ
ス最高温度に至るまでの燃焼室温度の平均値は同期間内
の単位時間当りの投入熱量により決定されるので、該平
均温度から単位時間当りの投入熱量が計算可能である。
On the other hand, the amount of heat input into the combustion chamber per unit time cannot be measured due to the equipment structure of the coke oven, but the average value of the combustion chamber temperature from the time of coal loading to the maximum temperature of the generated gas is measured per unit time during the same period. Since it is determined by the amount of heat input per unit time, the amount of heat input per unit time can be calculated from the average temperature.

故に、炉型式が同じなら火落ちまでに必要な総熱量は一
意に決定され、燃焼室温度が決まれば火落までに必要な
時間が決定できることを見い出した。
Therefore, it was discovered that if the furnace type is the same, the total amount of heat required until fire-off is uniquely determined, and once the combustion chamber temperature is determined, the time required until fire-off can be determined.

つまり、この発明はコークス炉の発生ガス温度を一定時
間ごとに測定し、この温度変化により発生ガス最高温度
に至る時刻を求め、装炭時刻より上記発生ガス温度が燃
焼開始時刻より最高温度に至るまでの時間の範囲で燃焼
室の平均温度を測定し、この平均温度により下記に示す
関係式のl成を介してコークス炉の火落時刻を予測する
ものである。
In other words, this invention measures the temperature of the generated gas in a coke oven at regular intervals, determines the time when the generated gas reaches its maximum temperature based on the temperature change, and the temperature of the generated gas reaches its maximum temperature from the time of coal loading and from the combustion start time. The average temperature of the combustion chamber is measured over a period of time, and the fire-off time of the coke oven is predicted using this average temperature through the relational expression shown below.

t:発生ガス最高温度の時刻より火落するまでの時間、 a1,a2:炉によって定まる係数、 TF二装炭時刻より発生ガス温度が最高温度に到達する
までの燃焼室の平均温度、 CI”過去のデータによって得られた1/’I’ Fの
平均値、 上記発生ガス温度は、一定温度値を越した後最高温度に
至るまでは単調に昇温し、最高温度付近では緩やかな変
化になり、その後は単調な降温過程になり、火落に至っ
ている。
t: Time from the time of the maximum temperature of the generated gas until it burns out, a1, a2: Coefficient determined by the furnace, Average temperature of the combustion chamber from the time of TF double coaling until the temperature of the generated gas reaches the maximum temperature, CI" The average value of 1/'I' F obtained from past data, the above generated gas temperature rises monotonically until reaching the maximum temperature after exceeding a certain temperature value, and changes slowly near the maximum temperature. After that, there was a monotonous cooling process, which led to the collapse of the flames.

このように、発生ガス温度は一定の温度変化過程を経る
ものであるから、発生ガス最高温度を求める際は、所定
時間ごとにこの発生ガス温度の差を順次連続して求める
ことにより、容易に発生ガス最高温度を求めることがで
きる。
In this way, the temperature of the generated gas undergoes a constant temperature change process, so when determining the maximum temperature of the generated gas, it is easy to find the maximum temperature of the generated gas by successively determining the difference in the temperature of the generated gas at predetermined intervals. The maximum temperature of generated gas can be determined.

又、上記燃焼室の平均温度TFを求める際は、測定温度
の合計をその測定回数で割ることにより容易に求まる。
Further, when determining the average temperature TF of the combustion chamber, it can be easily determined by dividing the sum of the measured temperatures by the number of measurements.

なお、上記発生ガス最高温度の時刻より火落するまでの
時間tは、火落時刻をt。
Note that the time t from the time of the maximum temperature of the generated gas to the end of the fire is t.

とおき、発生ガス最高温度時刻をtpとすると、t=t
c−tpで表わされ、発生ガス最高2温度の検出時刻が
分かると直ちに熱量の関係式の1)式から火落時刻が分
かる。
If the maximum temperature time of the generated gas is tp, then t=t
It is expressed as c-tp, and as soon as the detection time of the two highest temperatures of the generated gas is known, the fire-off time can be determined from equation 1) of the heat quantity relation.

上記1)式を用いた火落時刻予測方法において、上昇管
屈曲部で測定した発生ガス最高温度は、そのまま実測値
として使用するものでなく、発生ガスが最高温度に至っ
た時刻を求めるためのものであるから、温度測定器にタ
ールなどが付着して真の温度より低く検出したり、外気
温度の影響、温度計取り付け位置などにより発生ガス温
度が変動しても問題はない。
In the firebreak time prediction method using equation 1) above, the maximum temperature of the generated gas measured at the bend in the riser pipe is not used as an actual measurement value, but is used to determine the time when the generated gas reaches the maximum temperature. Therefore, there is no problem even if tar or the like adheres to the temperature measuring device and the temperature is lower than the true temperature, or if the temperature of the generated gas fluctuates due to the influence of outside air temperature, the position where the thermometer is installed, etc.

次に、この発明の火落時刻の予測について第2図のブロ
ック図を基に詳細に説明する。
Next, prediction of fire-fall time according to the present invention will be explained in detail based on the block diagram of FIG. 2.

コークス炉の各炭化室上方の上昇管屈曲部に発生ガス測
温装置6を設け、炭化室からの発生ガス温度を連続的に
測定する。
A generated gas temperature measuring device 6 is provided at the bend of the riser pipe above each carbonization chamber of the coke oven, and continuously measures the temperature of the generated gas from the carbonization chamber.

前記発生ガス測温装置6によって測定された測温値は、
最高温度算出装置7へ送信され、前記装置7内では一定
時間毎連続して、例えば15分毎に発生ガス測温装置6
からの受信値を順次連続して対比しながら最高温度を算
出し、すなわち、一定温度値(炉により定まる)を越し
た後に15分毎に(今回の値)と(前回の15分前の値
)との差を算出し、(今回の値)−(前回の値)≦0に
至った時刻を最高温度の時刻として、平均温度算出装置
9に送信する。
The temperature value measured by the generated gas temperature measuring device 6 is:
The generated gas temperature is transmitted to the maximum temperature calculation device 7, and within the device 7, the generated gas temperature measurement device 6
Calculate the maximum temperature by comparing the values received from ), and the time when (current value) - (previous value)≦0 is reached is set as the time of maximum temperature and transmitted to the average temperature calculation device 9.

一方燃焼室の上部に燃焼室の雰囲気温度を連続的に測定
するための燃焼室測温装置8を設け、前記燃焼室測温装
置8で測温された測温信号は平均温度算出装置9に送信
される。
On the other hand, a combustion chamber temperature measuring device 8 for continuously measuring the atmospheric temperature of the combustion chamber is installed in the upper part of the combustion chamber, and the temperature signal measured by the combustion chamber temperature measuring device 8 is sent to an average temperature calculating device 9. Sent.

前記平均温度算出装置9内では、装炭時刻より燃焼室測
温装置8からの測温信号により、一定時間毎、例えば2
分毎に順次測温値を加算すると同時に、加算頻度をも算
出し、最高温度算出装置7からの信号を受信した時点で
、前記加算測温値を加算頻度で除して、装炭時刻より発
生ガス温度が最高温度に到達するまでの燃焼室における
平均温度TFを算出し、演算装置11に送信される。
In the average temperature calculation device 9, temperature measurement is performed every fixed time, for example, 2 times, based on the temperature measurement signal from the combustion chamber temperature measurement device 8 from the coal loading time.
At the same time as adding temperature values sequentially every minute, the addition frequency is also calculated, and when the signal from the maximum temperature calculation device 7 is received, the added temperature value is divided by the addition frequency, and from the coal loading time. The average temperature TF in the combustion chamber until the generated gas temperature reaches the maximum temperature is calculated and transmitted to the calculation device 11.

演算装置11内には、予め火落時刻算出式を記憶してお
き、平均温度算出装置9からのTF値と、予め実測して
求めておいたa1,a2,c1の値が設定されている設
定器10からのa1,a2,C1の値からtの値、すな
わち火落までの時刻を算出し、前記算出火落時刻は表示
装置12により表示されると同時に、表示装置12に内
蔵されているタイマーによって、時刻の経過につれて火
落時刻までの時間も表示されるようになっている。
In the arithmetic device 11, a formula for calculating the fire-off time is stored in advance, and the TF value from the average temperature calculation device 9 and the values of a1, a2, and c1, which have been actually measured and determined in advance, are set. The value of t, that is, the time until the fire break is calculated from the values of a1, a2, and C1 from the setting device 10, and the calculated fire break time is displayed on the display device 12, and at the same time, a As the time passes, the timer will also display the time until the end of the fire.

前記本願発明法を実操業のコークス炉(炉長16500
mm、炉幅4507111,炉高7125mm)に適用
するために、予め同コークス炉の発生ガス温度、燃焼室
温度、実際に火落した時刻(石炭の温度を測定し950
℃に達した時刻を火落時刻とした)の測定実1験を繰返
し、発生ガス最高温度時刻から実際に火落するまでの経
過時間tと装炭から発生ガス最高温度時刻までの炭化室
両側の燃焼室の平均温度TFを求め、1/TFの平均値
C1を求めた後tと( 1/TF−C1) との一次
回帰式を七俵7し が得られた。
The method of the present invention was applied to a coke oven in actual operation (furnace length: 16,500 mm).
mm, oven width: 4507111 mm, oven height: 7125 mm), we measured the gas temperature of the coke oven, the combustion chamber temperature, and the actual time of fire (coal temperature was measured at 950 mm).
The measurement experiment (the time when the temperature reached ℃ was defined as the fire-off time) was repeated, and the elapsed time t from the time of the maximum temperature of the generated gas to the time of actual fire-off and the time from coal loading to the time of the maximum temperature of the generated gas on both sides of the carbonization chamber were repeated. After determining the average temperature TF of the combustion chamber and determining the average value C1 of 1/TF, a linear regression equation between t and (1/TF-C1) was obtained.

そして、同コークス炉の発生ガス温度と燃焼室温度を測
定し、装炭から発生ガス最高温度時刻までの炭化室両側
の燃焼室温度平均値TFを求め、予め決定したa1,a
2,C1の値を用いて、火落時刻算出式t−a1+a2
(1/lrF−C1)から火落までの時間tを求めた後
、tc=t+ip(tp・・・・・・発生ガス最高温度
時刻)より求めた火落時刻tcO値と、実際に火落した
時刻t。
Then, the generated gas temperature and combustion chamber temperature of the coke oven are measured, and the combustion chamber temperature average value TF on both sides of the coking chamber from coal loading to the maximum generated gas temperature time is determined, and predetermined a1, a
2. Using the value of C1, the fire fall time calculation formula t-a1+a2
After calculating the time t until the fire falls from (1/lrF-C1), the fire fall time tcO value obtained from tc = t + ip (tp...the time of maximum temperature of the generated gas) and the actual fire fall time. The time t.

0(石炭温度を測定し決定)との差t c − t o
oを第3図に示した。
0 (determined by measuring coal temperature) t c − t o
o is shown in Figure 3.

この結果から予測火落時刻は、実際の火落時刻に対し、
±20分以内にその90係のものが入ることが判明した
From this result, the predicted firefall time can be calculated as follows:
It turned out that the 90th class would arrive within ±20 minutes.

以上のごとく、この発明法によると、火落時刻の数時間
前に精度よく、火落時刻の予測が行なえるから、火落時
刻に対するコークス炉の諸調整操作が事前にできるので
、コークスの品質悪化や乾留熱源燃料エネルギーの損失
を防ぐことができる効果をもっている。
As described above, according to the method of the present invention, it is possible to predict the fire-off time with high accuracy several hours before the fire-off time, and various adjustments of the coke oven can be made in advance with respect to the fire-off time, thereby improving the quality of coke. It has the effect of preventing deterioration and loss of carbonization heat source fuel energy.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は発生ガス温度の測定位置を示すコークス炉上部
の縦断面図、第2図はこの発明を実施するためのブ白ツ
ク図、第3図はこの発明の火落時刻の予測値と実績値と
の誤差を示す図表である。 1・・・・・・コークス炉、2・・・・・・上昇管、3
・・・・・・熱電対、4・・・・・・炭化室、5・・・
・・・発生ガス集合ダクト、6・・・・・・発生ガス測
温装置、7・・・・・・最高温度算出装置、8・・・・
・・燃焼室測温装置、9・・・・・・平均温度算出装置
、10・・・・・・設定器、11・・・・・・演算装置
、12・・・・・・表示装置。
Fig. 1 is a vertical cross-sectional view of the upper part of the coke oven showing the measurement position of the generated gas temperature, Fig. 2 is a blank diagram for implementing the present invention, and Fig. 3 is the predicted value of the fire-off time of the present invention. It is a chart showing errors with actual values. 1... Coke oven, 2... Rising pipe, 3
...Thermocouple, 4...Carbonization chamber, 5...
... Generated gas collection duct, 6... Generated gas temperature measuring device, 7... Maximum temperature calculation device, 8...
... Combustion chamber temperature measurement device, 9 ... Average temperature calculation device, 10 ... Setting device, 11 ... Calculation device, 12 ... Display device.

Claims (1)

【特許請求の範囲】 1 コークス炉で発生する発生ガス温度及び燃焼室温度
を連続的に測定し、前記発生ガス測温値を連続的に対比
しながら発生ガス最高温度に達する時間を算出し、前記
最高温度に達するまでの時間における前記燃焼室温度の
所定時間ごとの加算値と加算頻度から、発生ガス最高温
度時刻における燃焼室温度の平均値TFを算出して、下
記算出式よりコークス炉の火落時刻を予測することを特
徴とするコークス炉の火落時刻予測方法。 t=al+a2(1/1F−Cl) t二発生ガス最高温度時刻から火落するまでの時間。 TF:装炭時刻より発生ガス温度が最高に達するまでの
炭化室両側の燃焼室の平均温度。 a1,a2:炉型式により定まる定数であり、予め同型
式炉での実験により求めておく。 C1:実験時の実績値1/TFの平均値。
[Claims] 1. Continuously measuring the temperature of the generated gas generated in a coke oven and the temperature of the combustion chamber, and calculating the time to reach the maximum temperature of the generated gas while continuously comparing the temperature values of the generated gas, The average value TF of the combustion chamber temperature at the maximum generated gas temperature time is calculated from the addition value of the combustion chamber temperature every predetermined time and the addition frequency during the time until the maximum temperature is reached, and the average value TF of the combustion chamber temperature at the time of the maximum temperature of the generated gas is calculated. A method for predicting fire-off time of a coke oven, characterized by predicting fire-off time. t=al+a2(1/1F-Cl) t2 Time from the maximum temperature of the generated gas to the end of the fire. TF: Average temperature of the combustion chambers on both sides of the carbonization chamber from the time of coal loading until the generated gas temperature reaches its maximum. a1, a2: Constants determined by the furnace type, and are determined in advance through experiments using the same type of furnace. C1: Average value of actual value 1/TF during experiment.
JP647279A 1979-01-22 1979-01-22 Method for predicting fire-down time of coke oven Expired JPS597751B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP647279A JPS597751B2 (en) 1979-01-22 1979-01-22 Method for predicting fire-down time of coke oven

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP647279A JPS597751B2 (en) 1979-01-22 1979-01-22 Method for predicting fire-down time of coke oven

Publications (2)

Publication Number Publication Date
JPS5598280A JPS5598280A (en) 1980-07-26
JPS597751B2 true JPS597751B2 (en) 1984-02-20

Family

ID=11639391

Family Applications (1)

Application Number Title Priority Date Filing Date
JP647279A Expired JPS597751B2 (en) 1979-01-22 1979-01-22 Method for predicting fire-down time of coke oven

Country Status (1)

Country Link
JP (1) JPS597751B2 (en)

Also Published As

Publication number Publication date
JPS5598280A (en) 1980-07-26

Similar Documents

Publication Publication Date Title
JPS597751B2 (en) Method for predicting fire-down time of coke oven
GB2039942A (en) Monitoring the heating of coke ovens
JP6241195B2 (en) Method for Estimating Carbonization Product Temperature in a Laboratory Coke Oven
JPS5835636B2 (en) How to measure the furnace temperature of a coke oven
JPH09302351A (en) Control method of input heat quantity for each kiln of coke oven
JPH061980A (en) Method for predicting volume of produced gas in coke oven
JPS5950196B2 (en) How to determine whether a coke oven has caught fire
US3959082A (en) Method of operating a battery of coke ovens
JPH06158050A (en) Method for controlling coke oven temperature
JPS5767830A (en) Method for estimating average temperature of section of cable
JPH0145511B2 (en)
JP2872343B2 (en) Prediction method of fire time of coke oven
TWI818869B (en) Method and device for evaluating an optimum transverse furnace temperature of a coke oven
JPH0153716B2 (en)
JPS59140287A (en) Prediction of net coking time of coke oven
JPS5441902A (en) Maintenance of furnace of coke oven
JP6724738B2 (en) Judging completion method for coke oven
JP2564496B2 (en) Judgment method of variation of fire time in coke oven
JPH026592A (en) Brick wall damage detection method in coke oven carbonization chamber
JP5954382B2 (en) How to detect a fire in a coke oven
JP4112758B2 (en) Coke oven furnace management method
JPH03157483A (en) Process for controlling combustion of coke oven
JPS62177090A (en) Control of combustion in coke oven
JPH0558476B2 (en)
JPH07126652A (en) Coke oven discharge coke temperature control method