JPS6383196A - Method of estimating and controlling coking time in coke oven - Google Patents
Method of estimating and controlling coking time in coke ovenInfo
- Publication number
- JPS6383196A JPS6383196A JP22798686A JP22798686A JPS6383196A JP S6383196 A JPS6383196 A JP S6383196A JP 22798686 A JP22798686 A JP 22798686A JP 22798686 A JP22798686 A JP 22798686A JP S6383196 A JPS6383196 A JP S6383196A
- Authority
- JP
- Japan
- Prior art keywords
- time
- fire
- coking time
- oven
- coke oven
- 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
Links
- 239000000571 coke Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims description 8
- 238000004939 coking Methods 0.000 title abstract 10
- 238000002485 combustion reaction Methods 0.000 claims abstract description 10
- 239000011449 brick Substances 0.000 claims abstract description 7
- 238000005192 partition Methods 0.000 claims abstract description 7
- 238000003763 carbonization Methods 0.000 claims description 12
- 239000003245 coal Substances 0.000 description 14
- 238000010586 diagram Methods 0.000 description 4
- 238000009529 body temperature measurement Methods 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000001514 detection method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Coke Industry (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、コークス炉火落時間の予測制御方法に関する
。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for predicting and controlling coke oven fire-off time.
(従来技術)
従来、燃焼室や燃焼小室間のヘアピン部に温度計を設置
し、この温度から石炭の乾留状況を検出している。しか
し石炭の温度は乾留中に20〜900℃変化するにもか
かわらずこの温度計の測温点では10〜20℃しか変化
せず、炭化室の温度変化を的確に反映しているとはいえ
ない。またコークス炉の時定数も4〜5時間と長いため
、石炭乾留状態を迅速に検出し、制御することも難しい
。また上記測温点は、燃焼室両側の石炭乾留のほか燃焼
状態(ガスカロリー、ガス流量、空気量)の影響を受け
るため、温度変化を的確に検出することが困難である。(Prior Art) Conventionally, a thermometer is installed in the combustion chamber or the hairpin section between combustion chambers, and the carbonization status of coal is detected from this temperature. However, although the temperature of the coal changes by 20 to 900 degrees Celsius during carbonization, the temperature measurement point of this thermometer only changes by 10 to 20 degrees Celsius, and although it does not accurately reflect the temperature change in the carbonization chamber. do not have. Furthermore, since the time constant of a coke oven is as long as 4 to 5 hours, it is difficult to quickly detect and control the state of coal carbonization. Furthermore, the temperature measurement point is affected by combustion conditions (gas calories, gas flow rate, air amount) as well as coal carbonization on both sides of the combustion chamber, making it difficult to accurately detect temperature changes.
このためこの温度変化を火落時間の予測制御に使用する
ことが困難である。Therefore, it is difficult to use this temperature change for predictive control of fire-off time.
そこで上昇管曲管部に温度計を設置して石炭乾留末期の
ピーク温度を検出し火落時間を予測することが考えられ
るが、このピーク温度を示す点は、欠落点の2〜3時間
前であり、コークス炉の時定数4〜5時間よりも短く、
火落時間の制御には使用できない。Therefore, it is possible to install a thermometer in the curved part of the riser pipe to detect the peak temperature at the end of coal carbonization and predict the fire-fall time, but the point showing this peak temperature is 2 to 3 hours before the missing point. , which is shorter than the time constant of a coke oven, which is 4 to 5 hours.
It cannot be used to control the fire fall time.
(発明が解決する技術的課題)
本発明は、コークス炉側々の窯の石炭乾留状況を的確に
検出して、火落時間を予測し、この予測値にもとずいて
供給熱量、空気量を調整して火落時間を制御することに
より、個々の窯の火落時間のバラツキを少なくすること
を目的とするコークス炉火落時間の予測制御方法を提供
する。(Technical Problem to be Solved by the Invention) The present invention accurately detects the coal carbonization status in the kilns on both sides of the coke oven, predicts the fire-off time, and based on this predicted value, supplies heat amount and air amount. Provided is a method for predicting and controlling a coke oven burn-off time, which aims to reduce variations in the burn-off time of individual ovens by adjusting the burn-off time.
(技術的課題を解決する手段)
本発明は、コークス炉の個々の窯に構成された炭化室と
燃焼室の間の仕切りレンガに温度計を装着し、この温度
計でフリュー温度を経時的に測定してこの温度が極小値
となる時間を検出し、この時間を基準として火落時間を
算出し、この算出火落時間と目標火落時間との偏差にも
とずいて個々の窯の供給熱量と空気流量を制御し、もっ
て火落時間が目標火落時間となるように制御することを
特徴とするコークス炉火落時間の予測制御方法である。(Means for Solving Technical Problems) The present invention provides a thermometer attached to a partition brick between a carbonization chamber and a combustion chamber configured in each individual kiln of a coke oven, and measures the flue temperature over time using this thermometer. Measure the temperature to detect the time when this temperature reaches its minimum value, calculate the fire-off time based on this time, and adjust the supply to each kiln based on the deviation between this calculated fire-off time and the target fire-off time. This is a method for predicting and controlling a coke oven burn-off time, which is characterized by controlling the amount of heat and air flow rate so that the burn-off time becomes a target burn-off time.
(発明の詳細な説明)
以下本発明を図面を参照して説明する。第1図はコーク
ス炉の概略図を示し、炭化室11と燃焼室12との間の
仕切りレンガ13に温度計14をそれぞれ設置している
。この温度計14の設置箇所は石炭の温度と燃焼室の温
度変化を均等に受け、石炭乾留状況の検出精度が良い。(Detailed Description of the Invention) The present invention will be described below with reference to the drawings. FIG. 1 shows a schematic diagram of a coke oven, in which thermometers 14 are installed in partition bricks 13 between a carbonization chamber 11 and a combustion chamber 12, respectively. The location where this thermometer 14 is installed receives changes in the temperature of the coal and the temperature of the combustion chamber equally, and the detection accuracy of the carbonization status of the coal is good.
この温度計14で検出する温度は、石炭装入から欠落ま
での間に、例えば第2図に示すように変化する。即ち、
石炭装入当初、900〜1000℃で蓄熱されているが
、常温の石炭装入により放熱され、2〜3時間後に約5
00℃に低下し、極小値を示した後石炭の温度の上昇と
ともに上昇しコークス窯出し時には元の温度900〜1
000℃に戻る。The temperature detected by this thermometer 14 changes as shown in FIG. 2, for example, from the time the coal is charged until the coal is dropped. That is,
When the coal is initially charged, heat is stored at 900 to 1000℃, but the heat is radiated by charging the coal at room temperature, and after 2 to 3 hours, the temperature is about 5℃.
The temperature drops to 00℃, shows a minimum value, then rises as the temperature of the coal rises, and returns to the original temperature of 900 to 1 when taken out of the coke oven.
Return to 000℃.
ここで検出したフリュー温度の変曲点a、C。Inflection points a and C of the flue temperature detected here.
極小値すを示す時間は、目標火落時間、置き時間と前回
実績火落時間、置き時間で決まる。本発明では極小値に
達する目標時間と実績時間の差を演算器15で算出し、
この値をもとにガスコック1Bの供給熱量とウェストバ
ルブ17の空気量を制御し、火落時間の修正制御を行う
。The time at which the minimum value is reached is determined by the target fire-off time, the setting time, the previous actual fire-off time, and the setting time. In the present invention, the difference between the target time and the actual time to reach the minimum value is calculated by the calculator 15,
Based on this value, the amount of heat supplied from the gas cock 1B and the amount of air from the waste valve 17 are controlled to correct the fire-off time.
以下演算器15内で行う具体的演算方法について述べる
。A specific calculation method performed within the calculator 15 will be described below.
[極小値を示す目標時間の計算] (1)式により、前回実績火落時間NCTa。[Calculation of target time showing minimum value] According to formula (1), the previous actual fire fall time NCTa.
置き時間STaをもとに仕切りレンガ内の蓄熱量を計算
する。ついで(2)式により、ここで得られた仕切りレ
ンガ内蓄熱量と目標火落時間N CT os S T
oをもとに極小値を示す時間T。The amount of heat stored in the partition brick is calculated based on the placement time STa. Next, using equation (2), the amount of heat storage in the partition brick obtained here and the target fire-off time N CT os S T
Time T that shows the minimum value based on o.
を計算する。Calculate.
Q = 1 / (N CT a + S T a )
x (al +a2 STa+a3 (STa)2
)・・・(1)
T+ −1/ (NCTo +STO)X (bo +
1/NCTO−1+b2 NCTO−2>・・・(2)
t)o −Q/ (NCTO+s”ro )x (Co
+c1NCTo−2+1/NCTo−3)al、al、
a3、bl、b2、Co5C!、C2:定数
火落時間の予測とNCT予測(NCToとするための制
御量)
極小値を示す時間の実績値をTaとすると火落時間の予
測値は(3)式となる。Q = 1 / (N CT a + S Ta)
x (al +a2 STa+a3 (STa)2
)...(1) T+ -1/ (NCTo +STO)X (bo +
1/NCTO-1+b2 NCTO-2>...(2) t)o -Q/ (NCTO+s"ro)x (Co
+c1NCTo-2+1/NCTo-3) al, al,
a3, bl, b2, Co5C! , C2: Prediction of constant fire-off time and NCT prediction (control amount for setting NCTo) If Ta is the actual value of the time showing the minimum value, the predicted value of the fire-off time is expressed by equation (3).
NCT−NCTO+1/NCT。NCT-NCTO+1/NCT.
X (dl十d2ΔT+d3Δ72)・・・(3)ΔT
−Tl−Ta、d1 、d2 、d3 ’定数またN
CT予測をNCToに一致させるためには偏差分だけ供
給熱量と空気量を調整する必要があり、(4)、(5)
式で決まる供給熱量の修正量をもとに(6)、(7)式
でガスフックとウェストバルブの開度調整量を計算する
。X (dl + d2 ΔT + d3 Δ72)...(3) ΔT
-Tl-Ta, d1, d2, d3' constant and N
In order to match the CT prediction with NCTo, it is necessary to adjust the supplied heat amount and air amount by the deviation, (4), (5)
Based on the correction amount of the supplied heat determined by the equation (6) and (7), the opening adjustment amount of the gas hook and waist valve is calculated using equations (6) and (7).
供給熱量修正量Δqの決定。Determination of supply heat amount correction amount Δq.
Δq t = K s X N CT o/ (N C
T o −T > )Xq (T’1−Ta)
・・・(4)ΔQ””K2 ΔQt−に3ΔQ
t−1に1、K2、Ks、定数、Δqt、Δqt−1:
今回及び前回偏差にもとすく調整量計算値ガスコック、
ウェストバルブ開度修正量ΔWc1ΔWaの決定。Δq t = K s X N CT o/ (N C
T o -T > )Xq (T'1-Ta)
...(4) ΔQ""K2 3ΔQ to ΔQt-
1 at t-1, K2, Ks, constant, Δqt, Δqt-1:
Calculated adjustment amount gas cock for this and previous deviations,
Determination of waist valve opening correction amount ΔWc1ΔWa.
ΔWc−に4Δq/q ・ (6)ΔW
a = K5 We ・” (7
)個々の窯の基準供給熱量、に、 、Ksは定数となる
。4Δq/q to ΔWc- (6) ΔW
a = K5 We ・” (7
) The standard supply heat amount of each kiln, , , Ks is a constant.
第3図は本発明制御方法の一例を示す。FIG. 3 shows an example of the control method of the present invention.
測定フリュー温度の極小値Taが出現する時間が、目標
フリュー温度の極小値T1が出現する時間よりも遅いと
フリュー温度の極小値を検出した時点でガスコックの開
度を大きくしてガス量を増加する。また同時にウェスト
バルブ開度を大きくして空気量を増加する。このように
して火落時間を目標とする時間に修正制御する。If the time at which the minimum value Ta of the measured flue temperature appears is later than the time at which the minimum value T1 of the target flue temperature appears, the opening degree of the gas cock is increased to increase the gas amount when the minimum value of the flue temperature is detected. do. At the same time, the opening of the waist valve is increased to increase the amount of air. In this way, the fire fall time is corrected and controlled to the target time.
第4図は極小値のバラツキと火落時間のバラツキとの関
係を示す。この図から極小値に達する時間の偏差ΔT−
T、−”raに比例して火落時間が早くなることがわか
る。FIG. 4 shows the relationship between the variation in minimum values and the variation in fire-off time. From this figure, the deviation of the time to reach the minimum value ΔT−
It can be seen that the fire-off time becomes faster in proportion to T, -"ra.
(発明の効果)
本発明によれば、火落時間と比例関係にある極小値に達
する時間をもとにして火落時間を制御するので、火落時
間を的確に修正してそのバラツキを大幅に減少すること
ができ、20〜30Kca1kg−coal程度の省エ
ネルギーを図れ、コークス品位が安定、向上した。(Effects of the Invention) According to the present invention, since the fire-off time is controlled based on the time to reach the minimum value which is proportional to the fire-off time, the fire-off time can be accurately corrected to greatly reduce the variation in the fire-off time. This resulted in energy savings of approximately 20 to 30 Kcal/kg-coal, and the coke quality was stabilized and improved.
第1図はコークス炉の要部の概略断面図、第2図は温度
計で測定したフリュー温度の経時的変化を示す図、第3
図は本発明の制御方法の一例を示す図、第4図はフリュ
ー温度の極小値に達した時間の偏差と火落時間の偏差と
の相関を示す説明図である。
11・・・炭化室、12・・・燃焼室、13・・・仕切
りレンガ、14・・・温度計、15・・・演算器、1G
・・・ガスコック、17・・・ウェストバルブ。
出願人代理人 弁理士 鈴江武彦
火冷吋関−偏差
ANCT= NCTa−NCT。
第4図
手続補正書
61,11.12
昭和 年 月 日
特許庁長官 黒 1)明 雄 殿
・1.事件の表示
特願昭61−227986号
2、発明の名称
コークス炉火落時間の予測制御方法
3、補正をする者
事件との関係 特許出願人
(412) 日本鋼管株式会社
4、代理人
東京都千代田区霞が関3丁目7番2号 UBEビル7、
補正の内容
(1) 明細書中箱5頁第7行に、
rX (a +a ST、a+a (STa)2
)Jl 2 3
とあるを
rX (a +a STa+a3 (STa)
)Jl2
と訂正する。
(2)同第6頁第12行〜第13行に、「ΔQ−に2
Δq −に3 Δqt−1K1、K2、K3、定数、
Δqt、Δqt−t:Jとあるを、
「Δq−・K2ΔQ −に3 Δqt−1K1%に2
、K3、定数、Δq 1Δq :」t 、、L
−、t
と訂正する。Figure 1 is a schematic cross-sectional view of the main parts of a coke oven, Figure 2 is a diagram showing changes in flue temperature over time measured with a thermometer, and Figure 3 is a diagram showing changes in flue temperature over time as measured by a thermometer.
The figure shows an example of the control method of the present invention, and FIG. 4 is an explanatory diagram showing the correlation between the deviation in the time when the flue temperature reaches the minimum value and the deviation in the fire-off time. 11... Carbonization chamber, 12... Combustion chamber, 13... Partition brick, 14... Thermometer, 15... Arithmetic unit, 1G
...Gas cock, 17...West valve. Applicant's agent: Patent attorney Takehiko Suzue - deviation ANCT = NCTa - NCT. Figure 4 Procedural Amendment 61, 11.12 Showa Year, Month, Date Commissioner of the Patent Office Black 1) Mr. Akio, 1. Display of the case Japanese Patent Application No. 61-227986 2, Title of the invention: Predictive control method for coke oven fire-down time 3, Person making the amendment Relationship to the case Patent applicant (412) Nippon Kokan Co., Ltd. 4, Agent Tokyo UBE Building 7, 3-7-2 Kasumigaseki, Chiyoda-ku,
Contents of amendment (1) In box 5, line 7 of the specification, rX (a +a ST, a+a (STa)2
) Jl 2 3 rX (a +a STa+a3 (STa)
) Jl2. (2) On page 6, lines 12 and 13, it is stated that “2
Δq-to 3 Δqt-1K1, K2, K3, constant,
Δqt, Δqt-t: J means 3 to Δq-・K2ΔQ-2 to Δqt-1K1%
, K3, constant, Δq 1Δq:”t ,,L
-, t.
Claims (1)
の仕切りレンガに温度計を装着し、この温度計でフリュ
ー温度を経時的に測定してこの温度が極小値となる時間
を検出し、この時間を基準として火落時間を算出し、こ
の算出火落時間と目標火落時間との偏差にもとずいて個
々の窯の供給熱量と空気流量を制御し、もって火落時間
が目標火落時間となるように制御するコークス炉火落時
間の予測制御方法。A thermometer is attached to the partition brick between the carbonization chamber and combustion chamber in each individual kiln of a coke oven, and this thermometer measures the flue temperature over time to detect the time when this temperature reaches its minimum value. Then, the fire-off time is calculated based on this time, and the amount of heat supplied to each kiln and the air flow rate are controlled based on the deviation between the calculated fire-off time and the target fire-off time, thereby reducing the fire-off time. A method for predicting and controlling a coke oven burn-off time to achieve a target burn-off time.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22798686A JPS6383196A (en) | 1986-09-29 | 1986-09-29 | Method of estimating and controlling coking time in coke oven |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22798686A JPS6383196A (en) | 1986-09-29 | 1986-09-29 | Method of estimating and controlling coking time in coke oven |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6383196A true JPS6383196A (en) | 1988-04-13 |
Family
ID=16869370
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22798686A Pending JPS6383196A (en) | 1986-09-29 | 1986-09-29 | Method of estimating and controlling coking time in coke oven |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6383196A (en) |
-
1986
- 1986-09-29 JP JP22798686A patent/JPS6383196A/en active Pending
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