JPH0711018B2 - Blow-through prevention method in blast furnace operation - Google Patents
Blow-through prevention method in blast furnace operationInfo
- Publication number
- JPH0711018B2 JPH0711018B2 JP29857390A JP29857390A JPH0711018B2 JP H0711018 B2 JPH0711018 B2 JP H0711018B2 JP 29857390 A JP29857390 A JP 29857390A JP 29857390 A JP29857390 A JP 29857390A JP H0711018 B2 JPH0711018 B2 JP H0711018B2
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- Prior art keywords
- furnace
- reference value
- blast furnace
- gas temperature
- temperature
- Prior art date
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- Manufacture Of Iron (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は高炉操業に関し、特に、高炉の吹抜け防止に関
する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to blast furnace operation, and more particularly to prevention of blow-through in a blast furnace.
高炉操業において炉内の圧力損失が局所的に増しこれが
装入物荷重と釣り合った状態になると装入物の局所的な
静止、いわゆる棚吊りが発生し、棚吊りの上側では装入
物の降下が止り、棚吊りの下方の炉内装入物の降下に伴
って棚吊りの下に空間を生ずる。この空洞がある程度大
きくなると棚吊りの外側の装入物が空洞に滑り込み(ス
リップ)これに伴ってこの局部的な棚吊りがくずれる。
棚吊りが大きくそのくずれが急激に起ると大量の装入物
の局所的な、比較的に速い移動により、炉内の圧力損失
が局所的に低下しそこから炉内ガスが上方に吹上げ、こ
のとき装入物が炉頂に吹き上げられる。このような吹き
上げはいわゆる吹抜けと呼ばれ、炉内温度分布,装入物
分布を乱して正常な熱交換還元が行われなくなり、溶銑
温度等を乱したり、ひどい場合には冷込みに到ることが
ある。しかも炉頂の温度が極端に上昇するので、高炉設
備の保全上も大きな問題となる。When the pressure loss in the furnace locally increases during blast furnace operation and this becomes in a state of being balanced with the load of the charge, local stoppage of the charge, so-called hanging, occurs, and the load drops on the upper side of the hanging. Stops and creates space under the hanging as the furnace interior contents fall below the hanging. When this cavity becomes large to some extent, the charge on the outside of the hanging system slips into the cavity, which causes the local hanging process to collapse.
If the shelving is large and the collapse occurs suddenly, a large amount of the charged material moves locally and relatively quickly, causing the pressure loss inside the furnace to decrease locally and blowing up the gas inside the furnace upward. , At this time, the charge is blown up to the top of the furnace. This type of blow-up is called so-called blow-through, which disturbs the temperature distribution in the furnace and the distribution of the charged materials so that normal heat exchange reduction cannot be performed, disturbs the hot metal temperature, and in severe cases leads to cooling. Sometimes. Moreover, the temperature at the top of the furnace rises extremely, which poses a serious problem in maintaining the blast furnace equipment.
特公平1−20203号公報には、高炉の高さ方向の複数位
置の炉壁内面部の静圧を測定し、これらの静圧から、各
測定位置から炉頂までの圧力損失を求め、一方、各測定
位置から炉項までの装入物荷重を求めて、求めた圧力損
失と装入物荷重の比に対応して炉内吹込み送風条件を調
整して上記棚吊り(およびそれによってもたらされるス
リップおよび吹抜け)を防止する技術が提示されてい
る。Japanese Examined Patent Publication No. 1-20203 discloses a static pressure on the inner surface of the furnace wall at a plurality of positions in the height direction of the blast furnace, and from these static pressures, a pressure loss from each measurement position to the top of the furnace is obtained. , The charge load from each measurement position to the furnace term is calculated, and the blowing air condition in the furnace is adjusted according to the ratio of the calculated pressure loss and the load of the furnace, and the above hanging (and the resulting Slip and blow-through) are proposed.
ところが高炉内装入物の荷重は、焼結鉱の性状(粒度,T
Fe,還元粉化性,強度等),コークスの性状(粒度,還
元粉化性,強度等)及び炉内状況(高炉炉壁の損耗:内
容積の変化,摩擦抵抗の変化)により変動し、炉内各点
の装入物荷重の算出(推定)精度が低く、したがって棚
吊り等の発生可能性の推定精度が低い。これにより、棚
吊り等の抑制の信頼性を高めるためには過度に送風量を
抑制することになり操業の安定性が乱される。送風量の
抑制を緩めると棚吊り等を起す可能性が高くなる。した
がって、より一層信頼性が高い吹抜け防止技術が望まれ
る。However, the load on the interior of the blast furnace depends on the properties of the sinter (grain size, T
Fe, reduction pulverization property, strength, etc., coke properties (grain size, reduction pulverization property, strength, etc.) and furnace conditions (blast furnace furnace wall wear: change in internal volume, change in friction resistance), The accuracy of the calculation (estimation) of the charge load at each point in the furnace is low, and therefore the accuracy of estimation of the possibility of rack hangings is low. As a result, in order to increase the reliability of restraint such as hanging from a shelf, the amount of air blow is excessively restrained and the stability of operation is disturbed. Loosening the control of the air flow increases the possibility of hanging on a shelf. Therefore, a more reliable blow-through prevention technique is desired.
本発明は、吹抜けの発生可能性の検出信頼性を高くして
高炉操業の安定性をより高くすることを目的とする。It is an object of the present invention to increase the reliability of detection of the possibility of occurrence of blow-through and further improve the stability of blast furnace operation.
本願の第1番の発明では、高炉内装入物の、炉周方向複
数点の上表面レベル(Lj)の差(ΔH)が基準値(ΔH
s)以上であるかを検出すると共に上表面レベル(Lj)
それぞれの位置の降下速度(dLj)が基準値(dLs)以上
であるかを検出し;高炉炉頂部の複数の上昇管Zjの炉頂
ガス温度(Tej)のそれぞれの所定時間間隔Tets(10se
c)の変化量(dTej)と所定時間間隔Tetl(60sec)の温
度勾配(Taj)を検出し;前記上表面レベルの差(Δ
H)が基準値(ΔHs)以上(DΔH=1)および表面レ
ベル(Lj)のそれぞれの降下速度(dLj)の少なくとも
一者が基準値(dLs)以上(DdL=1)で、前記複数の上
昇管の炉頂ガス温度(Tej)の変化勾配(Taj)少くとも
一者が基準値Vp以上(Tajmax≧Vp)および他の少くとも
一者が基準値Vm以下(Tajmin≦Vn)かつ前記炉頂ガス温
度の少くとも一者が基準値(dTe)以上の温度低下変化
を示したとき(DRd=1&DdT=1)に、高炉内への送風
量を低減する(第2b図の27〜29)。In the first invention of the present application, the difference (ΔH) between the upper surface levels (Lj) of the blast furnace interior charges at a plurality of points in the furnace circumferential direction is the reference value (ΔH).
s) or higher and detect upper surface level (Lj)
It is detected whether the descent rate (dLj) at each position is equal to or higher than the reference value (dLs); each predetermined time interval Tets (10se) of the top gas temperature (Tej) of the plurality of riser tubes Zj at the top of the blast furnace.
The change amount (dTej) in c) and the temperature gradient (Taj) at a predetermined time interval Tetl (60 sec) are detected;
H) is a reference value (ΔHs) or more (DΔH = 1) and at least one of the descent rates (dLj) of the surface level (Lj) is a reference value (dLs) or more (DdL = 1), and the above-mentioned plurality of increases Fluctuation gradient (Taj) of the gas temperature (Tej) at the top of the pipe At least one of them is above the reference value Vp (Tajmax ≧ Vp) and at least one is below the reference value Vm (Tajmin ≦ Vn) and the above-mentioned furnace top When at least one of the gas temperatures shows a temperature drop change above the reference value (dTe) (DRd = 1 & DdT = 1), the amount of air blown into the blast furnace is reduced (27-29 in Fig. 2b).
本願の第2番目の発明では、高炉炉頂部の複数の上昇管
Zjの炉頂ガス温度(Tej)のそれぞれの所定時間間隔Tet
s(10sec)の変化量(dTej)と所定間間隔Tetl(60se
c)の温度勾配(Taj)を検出し;高炉シャフト上部の装
入物表面レベルの直下(通常操業時における最低装入物
上表面レベルより0.5m〜1m下)の装入物内の高炉円周方
向複数点の炉内ガス温度(Tsj)のそれぞれを検出し;
前記複数の上昇管Zjの炉頂ガス温度(Tej)変化勾配(T
aj)の少くとも一者が基準値Vp以上(Tajmax≧Vp)およ
び他の少くとも一者が基準値Vm以下(Tajmin≦Vn)、か
つ少くとも一者が基準値(dTe)以上の温度低下し(DRd
=1&DdT=1)、高炉シャフト上部の装入物表面直下
の高炉円周方向複数点のいずれかの位置の炉内ガス温度
(Tsj)の所定時間内における温度変化が基準値(測定
位置における過去の通常操業状態での炉内ガス温度の管
理上限値)(ΔTs1〜ΔTs2)範囲内で前記複数点の少く
とも一者(Tsmax)が基準値(Tss)以上(DT=1)のと
きに、高炉内への送風量を低減する(第3b図の49−28−
29)。In the second invention of the present application, a plurality of risers at the top of the blast furnace
Zet top gas temperature (Tej) at each predetermined time interval Tet
Change amount (dTej) of s (10 sec) and predetermined interval Tetl (60se
The temperature gradient (Taj) in c) is detected; the blast furnace circle in the charge just below the charge surface level above the blast furnace shaft (0.5m-1m below the minimum charge upper surface level during normal operation). Detecting each of the in-furnace gas temperatures (Tsj) at multiple points in the circumferential direction;
Top gas temperature (Tej) change gradient (Tj) of the plurality of risers Zj
at least one of aj) is above the reference value Vp (Tajmax ≥ Vp) and at least one is below the reference value Vm (Tajmin ≤ Vn), and at least one is below the reference value (dTe) (DRd
= 1 & DdT = 1), the temperature change in the furnace gas temperature (Tsj) at any of several positions in the circumferential direction of the blast furnace just below the surface of the charge on the upper part of the blast furnace shaft is the reference value (the past at the measurement position) Control upper limit of furnace gas temperature under normal operating conditions) (ΔTs 1 to ΔTs 2 ) within the range of at least one of the multiple points (Tsmax) is greater than or equal to the reference value (Tss) (DT = 1) In addition, the amount of air blown into the blast furnace is reduced (Fig. 3b, 49-28-
29).
なお、カッコ内の記号は、以下の説明する本発明の実施
例の対応事項に付した記号等を示す。The symbols in parentheses indicate the symbols attached to the corresponding items of the embodiments of the present invention described below.
吹抜けの発生の前には、棚吊りなど該下り状態に異常を
生じ、装入物内に局所的な空洞が生ずる。このような状
態では高炉円周方向で装入物の降下速度の相違が大きく
なり、装入物上表面レベルLjの高低差が大きくなる。Prior to the occurrence of the blow-through, abnormalities are caused in the descending state such as hanging from a shelf, and a local cavity is generated in the charging material. In such a state, the difference in the descending speed of the charging material in the circumferential direction of the blast furnace becomes large, and the height difference of the upper surface level Lj of the charging material becomes large.
ところで、装入物内にかなりの大きさの空洞が発生する
と、高炉円周方向で炉頂ガス温度分布が乱れ、高炉円周
方向のある位置の炉頂ガス温度が低下傾向に他の位置の
炉頂ガス温度が上昇傾向となって円周方向の炉頂ガス温
度偏差が発生する。しかし、吹抜けに至るときには上記
とは逆に炉頂ガス温度の比較的高い状態の炉頂ガス温度
が大きく低下する。すなわち、空洞内に装入物が崩れ込
み始めると、空洞を流れる炉内ガス流が減少してその部
分の近傍の装入物表面より流出して該部分の上にある炉
頂上昇管に流入する炉内ガス温度が比較的に高い状態か
ら低下を始め、その他の位置を流れる炉内ガス流が増大
してその部分の装入物の表面より流出して該表面の上に
ある炉頂上昇管に流入しその炉内ガス温度は比較的低い
状態から上昇を始め吹抜けに至ると急激に上昇する。By the way, if a cavity with a large size is generated in the charging material, the temperature distribution of the furnace top gas in the circumferential direction of the blast furnace is disturbed, and the temperature of the furnace top gas at a certain position in the circumferential direction of the blast furnace tends to decrease. The furnace top gas temperature tends to rise, and a circumferential furnace top gas temperature deviation occurs. However, when the blow-through occurs, contrary to the above, the furnace top gas temperature in a state where the furnace top gas temperature is relatively high drops significantly. That is, when the charge begins to collapse into the cavity, the gas flow in the furnace flowing through the cavity decreases and flows out from the surface of the charge in the vicinity of that part and flows into the furnace top rising pipe above that part. The temperature inside the furnace begins to drop from a relatively high temperature, and the furnace gas flow flowing at other positions increases and flows out from the surface of the charging material at that part, and the furnace top rises above that surface. The temperature of the gas flowing into the pipe rises from a relatively low state and rises sharply when it blows through.
第1番目の発明ではこのような現象に着目して、高炉内
装入物の、炉周方向複数点位置間の上表面レベル(Lj)
の差(ΔH)が基準値(ΔHs)以上であるかを検出し、
かつ、表面レベル(lj)のそれぞれの位置における降下
速度(dLj)が基準値(dLs)以上であるかを検出し、更
に、高炉炉頂部の複数の上昇管の炉頂ガス温度(Tej)
のそれぞれの所定時間内の変化量(dTej)と温度変化勾
配を検出し、上表面レベル(Lj)の差(ΔH)が基準値
(ΔHs)以上および炉周方向複数点の上表面レベル(l
j)のそれぞれの降下速度(dLj)の少くとも一者が基準
値(dLs)以上、ならびに、複数の上昇管の炉頂ガス温
度(Tej)の温度変化勾配が少くとも一者が基準値Vp以
上(Tajmax≧Vp)、および他の少くとも一者が基準値Vn
以下(Tajmin≦Vn)、かつ少くとも一者が基準値(dT
e)以上の温度低下変化を示したとき(DRd=1&DdT=
1)に、高炉内への送風量を低減する(第2b図の27〜2
9)。すなわち、装入物上表面レベルLjの高低差が大き
くしかも装入物上表面Ljレベルの降下速度が高く、加え
て、高炉円周方向のある位置の炉頂ガス温度が急激に上
昇し他の位置の炉頂ガス温度が緩やかな上昇か又は低下
し、かつある位置の炉頂ガス温度が基準値以上の温度低
下変動を示したときに、送風量を低減する。In the 1st invention, paying attention to such a phenomenon, the upper surface level (Lj) of the blast furnace interior insert between the plural positions in the circumferential direction of the furnace
The difference (ΔH) is greater than or equal to the reference value (ΔHs),
Also, it is detected whether the descent rate (dLj) at each position of the surface level (lj) is higher than the reference value (dLs), and the gas temperature (Tej) at the top of the riser pipes at the top of the blast furnace is detected.
The change amount (dTej) within each predetermined time and the temperature change gradient are detected, and the difference (ΔH) in the upper surface level (Lj) is equal to or greater than the reference value (ΔHs) and the upper surface level (l
At least one of the descent rates (dLj) of j) is at least the reference value (dLs), and at least one of the temperature gradients of the top gas temperature (Tej) of the riser pipes is at the reference value Vp. Above (Tajmax ≥ Vp), and at least one other is the reference value Vn
Below (Tajmin ≦ Vn), and at least one of them is the reference value (dT
e) When the temperature drop change above is shown (DRd = 1 & DdT =
In 1), the amount of air blown into the blast furnace is reduced (27-2 in Fig. 2b).
9). That is, there is a large difference in height of the charge upper surface level Lj, and the rate of decrease of the charge upper surface Lj level is high.In addition, the furnace top gas temperature at a certain position in the blast furnace circumferential direction suddenly rises and other When the furnace top gas temperature at a position gradually rises or falls and the furnace top gas temperature at a certain position shows a temperature decrease fluctuation of a reference value or more, the air flow rate is reduced.
この第1番目の発明によれば、吹抜け予知の信頼性が高
く、操業の安定性が向上する。According to the first aspect of the present invention, the reliability of blowout prediction is high and the stability of operation is improved.
第2番目の発明でも上述の現象に着目して、高炉炉頂部
の複数の上昇管の炉頂ガス温度(Tej)のそれぞれの変
化量(dTej)と温度変化勾配を検出し、高炉シャフト上
部の装入物上表面ST直下の高炉円周方向複数点の炉内ガ
ス温度(Tsj)のそれぞれを検出すると共に、その検出
値から各位置における温度変化量を検出して、複数の上
昇管Zjの炉頂ガス温度(Tej)の少くとも一者が基準値V
p以上(dTmax≧Vp)、および他の少くとも一者が基準値
Vn以下(dTmin≧Vn)、かつ少くとも一者が基準値(dT
e)以上低下変化し(DRd=1&DdT=1)、加えて、高
炉円周方向複数点のいずれかの位置の炉内ガス温度(Ts
j)の所定時間内における温度変化が基準値(ΔTs1〜Δ
Ts2)範囲内で、前記複数点の少くとも一者(Tsmax)が
基準値(Tss)以上になった(DT=1)ときに、高炉内
への送風量を低減する(第2b図の49−28−29)。すなわ
ち、高炉円周方向のある位置の炉頂ガス温度が急激に低
下し、他の位置の炉頂ガス温度が緩やかに上昇し、又は
低下しかつ、ある位置の炉頂ガス温度が基準値以上の低
下変動を示し、加えて、スキンフローガス温度に経時的
変動を生じたときに送風量を低減する。Also in the second invention, paying attention to the above-mentioned phenomenon, the change amount (dTej) and the temperature change gradient of each of the furnace top gas temperatures (Tej) of the plurality of riser tubes at the blast furnace top are detected, and It detects each of the in-furnace gas temperatures (Tsj) at multiple points in the blast furnace circumferential direction immediately below the upper surface ST of the charge, and also detects the temperature change amount at each position from the detected values, At least one of the furnace top gas temperature (Tej) is the standard value V
p or more (dTmax ≥ Vp), and at least one other is the reference value
Vn or less (dTmin ≥ Vn), and at least one of them is the reference value (dT
e) More than a decrease (DRd = 1 & DdT = 1), and in addition, the furnace gas temperature (Ts
The temperature change of j) within a predetermined time is the reference value (ΔTs 1 ~ Δ
Within the range of Ts 2 ), when at least one of the plurality of points (Tsmax) exceeds the reference value (Tss) (DT = 1), the amount of air blown into the blast furnace is reduced (Fig. 2b). 49-28-29). That is, the temperature of the top gas at a certain position in the circumferential direction of the blast furnace sharply decreases, the temperature of the top gas at another position gradually increases or decreases, and the temperature of the top gas at a position is equal to or higher than the reference value. In addition, the air flow rate is reduced when the skin flow gas temperature fluctuates with time.
この第2番目の発明によれば、炉頂ガス温度およびスキ
ンフローガス温度の円周方向の経時的変化量の異変検出
の組合せで吹抜け予知を行なうのでその信頼性が高く、
操業の安定性が向上する。According to the second aspect of the present invention, since the blow-through prediction is performed by the combination of the abnormal change detection of the temporal change amount of the furnace top gas temperature and the skin flow gas temperature in the circumferential direction, the reliability thereof is high,
Operation stability is improved.
本発明の他の目的および特徴は、図面を参照した以下の
実施例の説明より明らかになろう。Other objects and features of the present invention will become apparent from the following description of embodiments with reference to the drawings.
〔第1番の発明の実施例〕 第1図に、本発明を実施する装置の概要を示す。この実
施例では、シャフト上段部の装入物表面ST直下の炉内ガ
ス温度Tejを検出する4個の温度計Tkj(スキンフロー温
度計)が、高炉円周方向に等間隔に設置されており、装
入物上表面レベルLj直下の炉内ガス温度Tsjを示す温度
検出信号を入出力インターフェイス(入,出力信号処理
回路)SPCに与える。シャフト部の上方にはサウンジン
グ装置Sが装備されており、これが装入物上表面の表面
レベル(高さ)Ljを円周方向で等間隔に定めた4点で検
出し、表面レベル信号を入出力インターフェイスSPCに
与える。高炉炉頂には4本の上昇管Zjがあり、これらに
もガス温度計Tzjが装備されており、これらが上昇管Zj
を上昇する炉頂ガス温度Tejを計測し炉頂ガス温度を示
す信号を入出力インターフェイスSPCに与える。[First Embodiment of the Invention] FIG. 1 shows an outline of an apparatus for carrying out the present invention. In this embodiment, four thermometers Tkj (skin flow thermometers) for detecting the in-furnace gas temperature Tej just below the charging surface ST at the upper stage of the shaft are installed at equal intervals in the circumferential direction of the blast furnace. , A temperature detection signal indicating the furnace gas temperature Tsj just below the upper surface level Lj of the charge is given to the input / output interface (input / output signal processing circuit) SPC. A sounding device S is installed above the shaft part, and this detects the surface level (height) Lj of the upper surface of the charge at four points that are set at equal intervals in the circumferential direction, and inputs the surface level signal. Give to the output interface SPC. At the top of the blast furnace, there are four rising pipes Zj, which are also equipped with gas thermometers Tzj. These are rising pipes Zj.
The temperature Tej of the furnace top gas that rises is measured, and a signal indicating the temperature of the furnace top gas is given to the input / output interface SPC.
各上昇管ZjにNo.1〜4の番号を付け、各上昇管Zjを上昇
する炉頂ガス温度Tejのjが上昇管No.数字(j=1〜
4)を示すものとすると、すなわち上昇管Zjの炉頂ガス
温度TejがNo.jの上昇管の炉頂ガス温度を示すものであ
るとすると、スキンフローガス温度Tsj測定位置(円周
方向j=1〜4),装入物上表面レベルLj測定位置(円
周方向j=1〜4)のそれぞれ(円周方向の位置j)
は、高炉の垂直軸心と各上昇管Zjの中心軸を含む各垂直
面上にある。Numbers 1 to 4 are assigned to the respective riser pipes Zj, and j of the furnace top gas temperature Tej that rises each riser pipe Zj is the riser pipe number number (j = 1 to 1).
4), that is, the furnace top gas temperature Tej of the rising pipe Zj indicates the furnace top gas temperature of the rising pipe of No. j, the skin flow gas temperature Tsj measurement position (circumferential direction j = 1 to 4), and each of the charging upper surface level Lj measurement positions (circumferential direction j = 1 to 4) (circumferential position j)
Is on each vertical plane that includes the vertical axis of the blast furnace and the central axis of each riser Zj.
すなわち、仮に炉内ガスが高炉軸心に関して全く対称に
上昇するとすると、Tsjは装入物表面直下の装入物内を
上昇管No.jに向って上昇するスキンフローガス温度、Lj
は上昇管No.jに最も近い装入物表面の表面レベル,Tejは
上昇管No.j内を流れる炉頂ガス温度である。That is, if the furnace gas rises symmetrically with respect to the blast furnace axis, Tsj is the skin flow gas temperature that rises toward the riser No. j in the charge immediately below the charge surface, Lj.
Is the surface level of the charging surface closest to the riser No.j, and Tej is the temperature of the top gas flowing in the riser No.j.
サウンジング装置Sは、円周方向4点の装入物上表面レ
ベルを測定して入出力インターフェイスSPCに入力して
そこに測定データを10secの周期でラッチする。スキン
フロー温度計Tkjおよび上昇管Zj内ガス温度を測定する
炉頂温度計Tzjは、それぞれ温度検出データを入出力イ
ンターフェイスSPCに入力してそこに2sec周期、5sec周
期でラッチする。The sounding device S measures the surface level on the charged material at four points in the circumferential direction and inputs it to the input / output interface SPC, and latches the measured data there at a cycle of 10 seconds. The skin flow thermometer Tkj and the furnace top thermometer Tzj for measuring the gas temperature in the rising pipe Zj respectively input the temperature detection data to the input / output interface SPC and latch it there at a cycle of 2 seconds and 5 seconds.
入出力インターフェイスSPCは、与えられた測定データ
の最新のものすべてを10sec周期で1セットのデータフ
レームに編集し保持しており、コンピュータCMRがデー
タを要求して来ると該1セットのデータフレームをコン
ピュータCMRに転送する。The input / output interface SPC edits and holds all the latest data of the given measurement data in a set of 10-second data frames, and when the computer CMR requests data, the set of data frames is stored. Transfer to computer CMR.
コンピュータCMRは、10sec周期で測定データを入出力イ
ンターフェイスSPCに要求し、1セットのデータフレー
ムを受信して、その中の所要のデータを摘出しそして後
述する吹抜け予知処理を実行して吹抜けの発生可能性を
判定し、判定結果に対応した送風制御データを作成し、
測定データを要求するとき転送指示信号と共に送風制御
データを入出力インターフェイスSPCに出力する。入出
力インターフェイスSPCは、コンピユータCMRからの送風
制御データは送風装置BRAに送出する。The computer CMR requests the measurement data from the input / output interface SPC at a cycle of 10 seconds, receives a set of data frames, extracts the required data from the data frames, and executes the blowout prediction process described later to generate blowouts. Judge the possibility, create the blow control data corresponding to the judgment result,
When requesting measurement data, the blow control data is output to the input / output interface SPC together with the transfer instruction signal. The input / output interface SPC sends the air blow control data from the computer CMR to the air blower BRA.
第2a図および第2b図に、コンピュータCMRの吹抜け予知
処理の内容を示す。2a and 2b show the contents of the blow-through prediction process of the computer CMR.
まず第2a図を参照すると、この処理を開始するときには
コンピユータCMRはまず10秒タイマをスタートし10秒の
経過を待つ。(ステップ1,2;以下カッコ内ではステップ
という語を省略し番号数字のみ記す)。10秒が経過する
と10秒タイマを再スタートし(3)、入出力インターフ
ェイスSPCより測定データを読込む(4)。First, referring to FIG. 2a, when starting this process, the computer CMR first starts a 10-second timer and waits for 10 seconds. (Steps 1 and 2; in parentheses, the word step is omitted and only numbers are shown). When 10 seconds have passed, the 10-second timer is restarted (3) and the measurement data is read from the input / output interface SPC (4).
コンピユータCMRは次に、読込んだ最新の測定データよ
り表面レベルデータLjを読出して(5)、表面レベルデ
ータLjの中の最大値Lmaxと最小値Lminを摘出し(6,
7)、最大値Lmaxと最小値Lminの偏差ΔHを算出し
(8)、偏差ΔHが基準値ΔHs(0.5m)以上であるかを
チエックして(9)、そうであると判定データレジスタ
DΔHに「1」を書込み(10)、そうでなければ判定デ
ータレジスタDΔHをクリアする(11)。Next, the computer CMR reads the surface level data Lj from the latest read measurement data (5) and extracts the maximum value Lmax and the minimum value Lmin from the surface level data Lj (6,
7) Calculate the deviation ΔH between the maximum value Lmax and the minimum value Lmin (8), check if the deviation ΔH is the reference value ΔHs (0.5m) or more (9), and judge that it is the determination data register DΔH "1" is written in (10), otherwise, the judgment data register DΔH is cleared (11).
次にコンピュータCMRは、最新の表面レベル測定値Ljと1
0sec前の表面レベル測定値(前回の入力値)を参照し
て、過去10secの間の表面レベル降下量dLjを算出する
(13)。そして、降下量dLjが基準値dLs(1.0m)以上で
あるかをチェックして(14)、そうであると判定データ
レジスタDdLに「1」を書込み(15)、そうでなれれば
判定データレジスタDdLをクリアする(16)。Computer CMR then updates the latest surface level readings Lj and 1
The surface level drop dLj for the past 10 seconds is calculated by referring to the surface level measurement value 0 seconds before (the previous input value) (13). Then, it is checked whether the amount dLj of drop is equal to or greater than the reference value dLs (1.0 m) (14), and if so, write "1" to the judgment data register DdL (15), and if not, the judgment data register Clear DdL (16).
次に第2b図を参照する。コンピュータCMRは次に、上昇
管Zjの炉頂ガス温度Tejを10sec間隔で測定データより読
出し(17)、今回より6回前までの読出しデータと共に
行レジスタMTRjに書込む(18)。一方、今回読出した炉
頂ガス温度Tejの測定データを前回読出した測定データ
により、10secの間の各炉頂ガス温度の低下変動量dTej
を算出する。そして、今回算出した温度低下変動量をdT
ejが基準値dTe(20℃)以上であるか(異常変動がある
か)をチェックする(19)。異常低下変動があると判定
レジスタDdTに「1」を書込み(20)、ないと判定レジ
スタDdTをクリアする(21)。Reference is now made to FIG. 2b. Next, the computer CMR reads the furnace top gas temperature Tej of the rising pipe Zj from the measurement data at intervals of 10 seconds (17), and writes it in the row register MTRj together with the read data six times before this time (18). On the other hand, based on the previously read measurement data of the furnace top gas temperature Tej that was read this time, the decrease fluctuation amount dTej of each furnace top gas temperature during 10 seconds
To calculate. Then, the calculated temperature drop fluctuation amount is calculated as dT
It is checked whether ej is equal to or higher than the reference value dTe (20 ° C) (whether there is an abnormal change) (19). If there is an abnormal change, "1" is written to the judgment register DdT (20), and if not, the judgment register DdT is cleared (21).
コンピュータCMRは次に、行うレジスタMTRjのデータ(6
0secの間の、10sec毎に入力した炉内ガス温度Tej)から
回帰式により高炉円周方向における各位置での温度変化
勾配(dTj)を算出し(22a)、この算出値の中の最高値
dTjmaxt最低値dTjminを摘出して(22,23)、最高値dTjm
axが基準値Vp(7℃/分)以上であるかをチェックしか
つ最低値dTjminが基準値Vn(3℃/分)以下であるかを
チェックして(24,25)、両者が共にあるとき(1つの
上昇管で炉頂ガス温度が急激に上昇しかつもう1つの上
昇管で炉頂ガス温度が緩やかに上昇又は低下)には、判
定レジスタDRdに「1」を書込み(26)、少なくとも一
方がないときには判定レジスタDRdをクリアする(2
7)。The computer CMR then performs the data (6
The temperature change gradient (dTj) at each position in the circumferential direction of the blast furnace was calculated from the furnace gas temperature (Tej) input every 10 seconds during 0 seconds by the regression equation (22a), and the highest value among the calculated values
dTjmaxt The lowest value dTjmin is extracted (22,23), and the highest value dTjm
Check if ax is greater than or equal to the reference value Vp (7 ° C / min) and if the lowest value dTjmin is less than or equal to the reference value Vn (3 ° C / min) (24,25). At this time (the furnace top gas temperature rises sharply in one riser pipe and the furnace top gas temperature rises or falls gently in the other riser pipe), "1" is written to the judgment register DRd (26), When at least one does not exist, the judgment register DRd is cleared (2
7).
コンピユータCMRは次に、判定レジスタDΔH,DdL,DdTお
よびDRdの内容をチェックして(28)、それらの内容が
すべて「1」であると吹抜けの可能性ありと判断する。
すなわち、装入物表面レベルの円周方向の差が基準値以
上、円周方向のある位置で表面レベル変動が基準値以
上、ある上昇管の炉頂ガス温度の低下変動が基準値以
上、および、上昇管の1つの炉頂ガス温度が上昇し、し
かも、もう1つのガス温度が低下、が同時に成立する
と、吹抜けの可能性があると判定する。Next, the computer CMR checks the contents of the judgment registers DΔH, DdL, DdT and DRd (28) and judges that there is a possibility of blow-through if the contents are all "1".
That is, the difference in the circumferential direction of the charge surface level is equal to or greater than the reference value, the surface level variation is equal to or greater than the reference value at a certain position in the circumferential direction, the decrease variation in the furnace top gas temperature of a certain riser is equal to or greater than the reference value, and , If the temperature of one furnace top gas in the riser rises and the temperature of the other gas falls simultaneously, it is determined that there is a possibility of blow-through.
吹抜けの可能性ありと判定するとコンピュータCMRは、
吹抜け防止用の風量減指示データを生成してこれを入出
力インターフェイスSPCを介して送風装置BRAに与え(2
9)、かつCRTディスプレイDISの表示を、現在の測定デ
ータ,判定データおよび送風装置の送風量データならび
に吹抜け注意を示すものに更新する(30)。If the computer CMR determines that there is a possibility of a void,
Generates air volume reduction instruction data for blow-through prevention and gives this to the blower BRA via the input / output interface SPC (2
9) In addition, the display on the CRT display DIS is updated to show the current measurement data, judgment data, air flow rate data of the air blower and cautions for blown air (30).
なお、上述のように吹抜けを予知したときには、吹抜け
限界指数F、 RIV:高炉の実効内容積, OC:ORE/COKE(−), ρc:COKE嵩密度(t/m3), ρo:ORE嵩密度(t/m3), BV:送風量(Nm3/min), TP:炉頂圧力(kg/cm2), S:炉内平均断面積(m2) に、吹抜け防止用の値を与え、逆算により送風量BVを算
出し、算出した送風量BVより更に安全度を高めるための
値を減算し、残値を示す送風量データを送風装置BRAに
与える(29)。When predicting the blow-through as described above, the blow-through limit index F, RIV: Effective internal volume of blast furnace, OC: ORE / COKE (-), ρc: COKE bulk density (t / m 3 ), ρo: ORE bulk density (t / m 3 ), BV: Air flow rate (Nm 3 / min) ), TP: Furnace top pressure (kg / cm 2 ), S: Furnace average cross-sectional area (m 2 ) with blow-through prevention values, and calculate the air flow rate BV by back-calculation. From the calculated air flow rate BV Further, the value for increasing the safety is subtracted, and the air flow rate data indicating the residual value is given to the air blower BRA (29).
吹抜け対処要と判定しなかったときには、現状態維持の
信号を送風装置BRAに与え(31)、CRTディスプレイDIS
の表示を、現在の測定データ,判定データおよび送風装
置の送風量データならびに吹抜けがないことを表示する
(32)。When it is not judged that the blow-through should be taken, a signal for maintaining the current state is given to the blower device BRA (31), and the CRT display DIS
The current measurement data, the judgment data, the air flow rate data of the air blower, and the absence of blow-through are displayed on the display (32).
〔第2番の発明の実施例〕 この実施例のコンピュータCMRの処理動作を第3a図およ
び第3c図に示す。この実施例では、10secの時間経過毎
にコンピュータCMRは以下の処理を行なう。[Second Embodiment of the Invention] The processing operation of the computer CMR of this embodiment is shown in FIGS. 3a and 3c. In this embodiment, the computer CMR performs the following processing every 10 seconds.
まず第3a図を参照する。コンピュータCMRはまず最新の
炉頂ガス温度Tejを10sec間隔で測定データより読出し
(1〜4)、今回より6回前までの読出しデータと共に
行レジスタMTRjに書込む(18)。一方、今回読出した炉
頂ガス温度Tejの測定データと前回読出した測定データ
により10secの間の各炉頂ガス温度の低下変動量dTejを
算出する。そして、今回算出した温度低下変動量dTejが
基準値dTe(20℃)以上であるか(異常変動があるか)
をチェックする(19)。異常低下変動があると判定レジ
スタDdTに「1」を書込み(20)、ないと判定レジスタD
dTをクリアする(21)。コンピュータCMRは次に、行レ
ジスタMTRjのデータ(60secの間の、10sec毎に入力した
炉頂ガス温度Tej)から回帰式により高炉円周方向にお
ける各位置での温度変化勾配(dTj)を算出し(22a)、
この算出値の中の最高値dTmaxと最低値dTminを摘出して
(22,23)、最高値dTjmaxが基準値Vp(7℃/分)以上
であるかをチェックしかつ最低値dTminが基準値Vn(3
℃/分)以下であるかをチェックして(24,25)、両者
が共にあるとき(1つの上昇管Zjで炉頂ガス温度が上昇
しかつもう1つの上昇管Zjで炉頂ガス温度が低下)に
は、判定レジスタDRdに「1」を書込み(26)、一方が
ないときには判定レジスタDRdをクリアする(27)。First, refer to FIG. 3a. The computer CMR first reads the latest furnace top gas temperature Tej from the measurement data at intervals of 10 seconds (1 to 4), and writes it in the row register MTRj together with the read data up to 6 times before this time (18). On the other hand, the decrease fluctuation amount dTej of each furnace top gas temperature during 10 seconds is calculated from the measurement data of the furnace top gas temperature Tej read this time and the measurement data read last time. And whether the calculated temperature drop variation dTej is more than the reference value dTe (20 ℃) (whether there is an abnormal variation)
Check (19). Write "1" to the judgment register DdT if there is an abnormal decrease fluctuation (20), and if there is not, judge the register D
Clear dT (21). The computer CMR then calculates the temperature change gradient (dTj) at each position in the circumferential direction of the blast furnace from the regression equation from the data in the row register MTRj (furnace gas temperature Tej input every 10 seconds during 60 seconds). (22a),
The maximum value dTmax and the minimum value dTmin among these calculated values are extracted (22,23), and it is checked whether the maximum value dTjmax is higher than the reference value Vp (7 ° C / min) and the lowest value dTmin is the reference value. Vn (3
(24 ° C / min) or less (24,25), and when both are present (one riser pipe Zj raises the top gas temperature and another riser Zj changes the top gas temperature To decrease), "1" is written in the judgment register DRd (26), and when there is no one, the judgment register DRd is cleared (27).
次に2sec間隔で入力したスキンフローガス温度をコンピ
ュータCMRは、10sec毎に該スキンフローガス温度データ
Tsjを読出す(41)。Next, the computer CMR displays the skin flow gas temperature input at 2 second intervals every 10 seconds.
Read Tsj (41).
次に第3b図を参照する。コンピュータCMRは、読出した
温度データTsj,j=1〜4別の各5個の測定データ中の
最高値Tsmaxと最低値Tsminを摘出して(42,43)それら
の温度差(温度変化量)ΔTsj=Tsjmax−Tsjminを算出
し(44)、温度差ΔTsjが基準値ΔTs1(10℃)〜ΔTs2
(20℃)の範囲内であるか(スキンフローガス温度に変
動があるか)、および、最高値Tsjmaxが基準値Tss(300
℃)以上であるかをチェックし(45,46)、そうである
と判定レジスタDTに「1」を書込み(47)、ないと判定
レジスタDTをクリアする(48)。Reference is now made to FIG. 3b. The computer CMR extracts the maximum value Tsmax and the minimum value Tsmin from each of the five measured data of the read temperature data Tsj, j = 1 to 4 (42,43), and their temperature difference (temperature change amount). ΔTsj = Tsjmax-Tsjmin is calculated (44), and the temperature difference ΔTsj is the reference value ΔTs 1 (10 ° C) to ΔTs 2
Within the range of (20 ℃) (whether the skin flow gas temperature fluctuates), and the maximum value Tsjmax is the reference value Tss (300
It is checked whether the temperature is higher than (° C) or not (45, 46), and if so, "1" is written in the judgment register DT (47), and if not, the judgment register DT is cleared (48).
コンピユータCMRは次に、判定レジスタDdT,DRdおよびDT
の内容をチェックして(49)、それらの内容がすべて
「1」であると吹抜けの可能性ありと判断する。すなわ
ち、ある上昇管Zjの炉頂ガス温度の低下変動が基準値以
上,上昇管Zjの1つの炉頂ガス温度の温度変化勾配が基
準値以上とし、しかも、もう1つの炉頂ガス温度の温度
変化勾配が基準値以下、および、スキンフローガス温度
Tsjの変化量円周方向いずれかの位置で異常で、しか
も、ある位置のスキンフローガス温度Tsjが異常に高
い、が同時に成立すると、吹抜けの可能性があると判定
する。The computer CMR then determines the decision registers DdT, DRd and DT.
Check the contents of (49), and if all of them are "1", it is judged that there is a possibility of a void. That is, the decrease fluctuation of the furnace top gas temperature of a certain rising pipe Zj is not less than the reference value, the temperature change gradient of one furnace top gas temperature of the rising pipe Zj is not less than the reference value, and the temperature of the other furnace top gas temperature is The change gradient is below the reference value and the skin flow gas temperature
Change amount of Tsj If abnormal at any position in the circumferential direction and the skin flow gas temperature Tsj at a certain position is abnormally high at the same time, it is determined that there is a possibility of blow-through.
吹抜けの可能性ありと判定するとコンピュータCMRは、
吹抜け防止用の風量減指示データを生成してこれを入出
力インターフェイスSPCを介して送風装置BRAに与え(2
9)、かつCRTディスプレイDISの表示を、現在の測定デ
ータ,判定データおよび送風装置の送風量データならび
に吹抜け注意を示すものに更新する。(30)。If the computer CMR determines that there is a possibility of a void,
Generates air volume reduction instruction data for blow-through prevention and gives this to the blower BRA via the input / output interface SPC (2
9) In addition, the display on the CRT display DIS is updated to show the current measurement data, judgment data, air flow rate data of the air blower, and cautions for blown air. (30).
吹抜けを予知しなかったときには、そのときの現状維持
信号を送風装置BRAに与え(31)、CRTディスプレイDIS
の表示を、現在の測定データ,判定データおよび送風装
置の送風量データならびに吹抜けのないことを表示する
(32)。When the blow-through is not predicted, the current status maintenance signal at that time is given to the blower device BRA (31), and the CRT display DIS
The current measurement data, the judgment data, the air flow rate data of the air blower, and the absence of blow-through are displayed (32).
第1番目の発明によれば、装入物表面レベル変動検出に
炉頂ガス温度の円周方向の異変検出をも加えて吹抜け予
知を行なうのでその信頼性が高く、操業の安定性が向上
する。According to the first aspect of the present invention, since the blow-through prediction is performed by adding the detection of the variation of the furnace top gas temperature in the circumferential direction in addition to the detection of the fluctuation of the charge surface level, the reliability is high and the operation stability is improved. .
第2番目の発明によれば、炉頂ガス温度の円周方向の異
変検出にスキンフローガス温度の円周方向の異変検出を
も加えて吹抜け予知を行なうのでその信頼性が高く、操
業の安定性が向上する。According to the second aspect of the present invention, since the blow-through prediction is performed by adding the circumferential variation of the furnace top gas temperature to the circumferential variation of the skin flow gas temperature, the reliability is high and the operation is stable. The property is improved.
第1図は、本願の発明を実施する装置の概要を示すブロ
ック図である。 第2a図および第2b図は、本願の第1実施例の、第1図に
示すコンピュータCMRの処理動作を示すフローチャート
である。 第3a図および第3b図は、本願の第2実施例の、コンピュ
ータCMRの処理動作を示すフローチャートである。FIG. 1 is a block diagram showing an outline of an apparatus for carrying out the invention of the present application. 2a and 2b are flowcharts showing the processing operation of the computer CMR shown in FIG. 1 according to the first embodiment of the present application. 3a and 3b are flowcharts showing the processing operation of the computer CMR according to the second embodiment of the present application.
Claims (2)
レベルの差が基準以上であるかを検出すると共に上表面
レベルをそれぞれの位置の降下速度が基準値以上である
かを検出し、 高炉炉頂部の複数の上昇管の炉頂ガス温度のそれぞれの
所定時間内の変化量と温度変化勾配を検出し、 炉周方向複数点の上表面レベル差が基準値以上および上
表面レベルそれぞれの降下速度の少くとも一者が基準値
以上で、前記複数の上昇管の炉頂ガス温度変化勾配の少
くとも一者が基準値以上で他の少くとも一者が基準以下
で、かつ、少くとも炉頂ガス温度の一者が基準値以上の
温度低下を示したとき、高炉内への送風量を低減する、
高炉操業における吹抜け防止方法。1. A method for detecting whether or not a difference between upper surface levels at a plurality of points in a furnace circumferential direction of an blast furnace interior charge is higher than a reference value and detecting whether the descending speed of each position of the upper surface level is a reference value or more. Detecting the amount of change and temperature change gradient of the furnace top gas temperature of multiple risers at the top of the blast furnace within a predetermined time, the upper surface level difference at multiple points in the furnace circumferential direction is above the reference value and the upper surface At least one of the descending speeds of each level is equal to or higher than the reference value, at least one of the furnace top gas temperature change gradients of the plurality of riser pipes is equal to or higher than the reference value, and at least one other is equal to or lower than the reference value, and , At least when one of the furnace top gas temperatures shows a temperature drop above the reference value, reduce the amount of air blown into the blast furnace,
Blow-through prevention method in blast furnace operation.
のそれぞれの所定時間の変化量と温度変化勾配を検出
し、 高炉シャフト上部の装入物表面直下の高炉円周方向複数
点の炉内ガス温度のそれぞれを検出し、 前記複数の上昇管の炉頂ガス温度変化勾配の少くとも一
者が基準値以上で、他の少くとも一者が基準値以下で、
かつ、少なくとも炉頂ガス温度の一者が基準値以上の温
度低下を示し、高炉シヤフト上部の装入物表面直下の高
炉円周方向複数点のいずれかの位置の炉内ガス温度の所
定時間内における温度変化が基準値範囲内で前記複数点
の少くとも一者が基準値以上のとき、高炉内への送風量
を低減する。、高炉操業における吹抜け防止方法。2. A plurality of points in the circumferential direction of the blast furnace just below the surface of the charge above the shaft of the blast furnace are detected by detecting the amount of change and the temperature change gradient of the furnace top gas temperature of a plurality of rising pipes at the top of the blast furnace. Detecting each of the furnace gas temperature, at least one of the furnace top gas temperature change gradient of the plurality of risers is a reference value or more, other at least one is below the reference value,
In addition, at least one of the furnace top gas temperatures shows a temperature drop above the reference value, and the gas temperature in the furnace at any of the multiple points in the circumferential direction of the blast furnace immediately below the surface of the charge at the upper part of the blast furnace is within the predetermined time. When the temperature change in is within the reference value range and at least one of the plurality of points is the reference value or more, the amount of air blown into the blast furnace is reduced. , Blow through prevention method in blast furnace operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29857390A JPH0711018B2 (en) | 1990-11-02 | 1990-11-02 | Blow-through prevention method in blast furnace operation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29857390A JPH0711018B2 (en) | 1990-11-02 | 1990-11-02 | Blow-through prevention method in blast furnace operation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04173909A JPH04173909A (en) | 1992-06-22 |
| JPH0711018B2 true JPH0711018B2 (en) | 1995-02-08 |
Family
ID=17861497
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29857390A Expired - Lifetime JPH0711018B2 (en) | 1990-11-02 | 1990-11-02 | Blow-through prevention method in blast furnace operation |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0711018B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101540248B1 (en) * | 2013-12-26 | 2015-07-29 | 주식회사 포스코 | Signs of blast furnace sensors and detection methods for channeling |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5256982B2 (en) * | 2008-10-09 | 2013-08-07 | 新日鐵住金株式会社 | Operation method of vertical melting furnace |
| JP6870694B2 (en) * | 2018-04-03 | 2021-05-12 | Jfeスチール株式会社 | Blast furnace condition condition determination device, blast furnace operation method, and blast furnace condition condition determination method |
| JP6870693B2 (en) * | 2018-04-03 | 2021-05-12 | Jfeスチール株式会社 | Blast furnace condition condition determination device, blast furnace operation method, and blast furnace condition condition determination method |
-
1990
- 1990-11-02 JP JP29857390A patent/JPH0711018B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101540248B1 (en) * | 2013-12-26 | 2015-07-29 | 주식회사 포스코 | Signs of blast furnace sensors and detection methods for channeling |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04173909A (en) | 1992-06-22 |
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