WO2023276356A1 - 供給熱量推定方法、供給熱量推定装置、供給熱量推定プログラム、及び高炉の操業方法 - Google Patents
供給熱量推定方法、供給熱量推定装置、供給熱量推定プログラム、及び高炉の操業方法 Download PDFInfo
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- WO2023276356A1 WO2023276356A1 PCT/JP2022/014486 JP2022014486W WO2023276356A1 WO 2023276356 A1 WO2023276356 A1 WO 2023276356A1 JP 2022014486 W JP2022014486 W JP 2022014486W WO 2023276356 A1 WO2023276356 A1 WO 2023276356A1
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- heat
- amount
- blast furnace
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- 238000000034 method Methods 0.000 title claims abstract description 61
- 229910000805 Pig iron Inorganic materials 0.000 claims abstract description 60
- 239000002994 raw material Substances 0.000 claims abstract description 33
- 239000000571 coke Substances 0.000 claims abstract description 29
- 238000007664 blowing Methods 0.000 claims abstract description 6
- 229910052751 metal Inorganic materials 0.000 claims description 36
- 239000002184 metal Substances 0.000 claims description 36
- 230000000717 retained effect Effects 0.000 claims description 16
- 238000004519 manufacturing process Methods 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 22
- 239000007789 gas Substances 0.000 description 18
- 238000006243 chemical reaction Methods 0.000 description 13
- 229910052742 iron Inorganic materials 0.000 description 11
- 238000012545 processing Methods 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 229910052799 carbon Inorganic materials 0.000 description 7
- 230000017525 heat dissipation Effects 0.000 description 7
- 239000000498 cooling water Substances 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000004891 communication Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000012937 correction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000010365 information processing Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000000284 resting effect Effects 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B7/00—Blast furnaces
- C21B7/24—Test rods or other checking devices
Definitions
- the present invention relates to a supplied heat amount estimation method for estimating the amount of heat supplied to pig iron in a blast furnace, a supplied heat amount estimation device, a supplied heat amount estimation program, and a blast furnace operating method.
- Patent Document 1 the current furnace heat index deviation from the furnace heat index reference level corresponding to the target hot metal temperature, and the current furnace top unloading speed reference level corresponding to the target hot metal temperature To sequentially estimate the molten iron temperature after a specific time from the unloading speed variation amount and the influence time of both variations on the molten iron temperature, and based on the estimation result, perform furnace heat control operation so as to reduce the molten iron temperature fluctuation.
- a furnace heat control method for a blast furnace characterized by In addition, in Patent Document 2, actual values of blast condition data including at least one of blast temperature, blast humidity, blast volume, pulverized coal injection volume, and oxygen enrichment volume, and at least solution loss carbon
- a blast furnace hot metal temperature prediction method for predicting future hot metal temperature based on operation data including actual values of disturbance factor data including quantity and actual values of hot metal temperature, the data accumulation step of accumulating operation data and a steady-state prediction model construction process for constructing a steady-state prediction model that predicts the molten iron temperature in a steady state from the operation data in a steady state accumulated in the data accumulation process, and a low-dimensional steady-state prediction model.
- a non-steady state prediction model construction step for constructing a non-steady state prediction model for predicting the hot metal temperature during the non-steady state from the operation data during the non-steady state accumulated in the data accumulation step; and a hot metal temperature prediction step of predicting the hot metal temperature from the state prediction model and the unsteady state prediction model.
- the amount of hot metal produced changes due to changes in the operating rate such as the air flow rate into the blast furnace, and the amount of pig iron is different from the amount of heat supplied to the blast furnace.
- the heat retained in the blast furnace is dissipated during a wind break in which the blowing of air to the blast furnace is temporarily stopped.
- the height of the surface of the raw materials charged into the blast furnace may be lowered, and when the blast furnace is started up after the wind break, the room temperature raw material may be refilled and operated. Thermal compensation of the raw material is also required.
- the present invention has been made in view of the above problems, and its object is to provide a heat quantity to be supplied to the pig iron in the blast furnace even when the operating rate changes greatly, especially when the blast furnace is started up after a wind break.
- a supplied heat amount estimation method a supplied heat amount estimation device, and a supplied heat amount estimation program capable of estimating accurately.
- Another object of the present invention is to maintain the amount of heat supplied to the pig iron in the blast furnace appropriately even when the operation rate changes greatly, especially when the blast furnace is started up after a wind break.
- a supplied heat amount estimation method is a supplied heat amount estimation method for estimating the amount of heat supplied to pig iron in a blast furnace from the amount of heat supplied to the blast furnace and the production rate of hot metal in the blast furnace. Estimate the change in the sensible heat brought out by the gas and the change in the sensible heat brought in by the raw material preheated by the gas passing through the furnace, and consider the estimated change in the sensible heat taken out and the sensible heat brought in.
- an estimating step of estimating the amount of heat supplied to the pig iron in the blast furnace includes estimating the amount of heat supplied to the pig iron in the blast furnace in consideration of the heat dissipated from the blast furnace during a wind break; estimating the amount of heat retained in the core coke present in the blast furnace, and estimating the amount of heat supplied to the pig iron in the blast furnace taking into account the estimated amount of heat retained in the core coke.
- the estimating step preferably includes a step of estimating the change in the brought-in sensible heat in consideration of the surface height of the raw material that is lowered during the wind break.
- a supplied heat amount estimating apparatus is a supplied heat amount estimating apparatus for estimating the amount of heat supplied to pig iron in a blast furnace from the amount of heat supplied to the blast furnace and the production rate of hot metal in the blast furnace. Estimate the change in the sensible heat brought out by the gas and the change in the sensible heat brought in by the raw material preheated by the gas passing through the furnace, and consider the estimated change in the sensible heat taken out and the sensible heat brought in.
- the estimating means for estimating the amount of heat supplied to the pig iron in the blast furnace, the estimating means estimating the amount of heat supplied to the pig iron in the blast furnace in consideration of the heat dissipated from the blast furnace during a wind break;
- the amount of heat retained in the core coke is estimated, and the amount of heat supplied to the pig iron in the blast furnace is estimated considering the estimated amount of heat retained in the core coke.
- the estimating means preferably estimates the change in the brought-in sensible heat in consideration of the surface height of the raw material that is lowered during the wind break.
- a supplied heat amount estimation program is a supplied heat amount estimation program that causes a computer to execute processing for estimating the amount of heat supplied to pig iron in a blast furnace from the amount of heat supplied to the blast furnace and the rate of production of hot metal in the blast furnace.
- the computer estimates a change in the sensible heat brought out by the gas passing through the furnace and a change in the sensible heat brought in by the raw material preheated by the gas passing through the furnace, and the estimated sensible heat taken out and
- An estimation process for estimating the amount of heat supplied to the pig iron in the blast furnace in consideration of the change in the sensible heat brought in is executed, and the estimation process is performed by taking into account the surface height of the raw material lowered during the wind break.
- the method for operating a blast furnace according to the present invention includes a step of controlling the amount of heat supplied to the blast furnace based on the amount of heat supplied to the pig iron in the blast furnace estimated by the method for estimating the amount of heat supplied according to the present invention.
- the supplied heat amount estimation method, the supplied heat amount estimation device, and the supplied heat amount estimation program according to the present invention when the operation rate changes greatly, especially when the blast furnace is started after the wind break, the pig iron in the blast furnace is supplied with It is possible to accurately estimate the amount of heat applied. Further, according to the method of operating a blast furnace according to the present invention, even when the operating rate changes greatly, especially when the blast furnace is started up after a wind break, the amount of heat supplied to the pig iron in the blast furnace can be appropriately maintained and the molten iron temperature can be adjusted. can be precisely controlled within a predetermined range.
- FIG. 1 is a block diagram showing the configuration of a furnace heat control system that is an embodiment of the present invention.
- FIG. 2 is a flow chart showing the flow of furnace heat control processing, which is an embodiment of the present invention.
- FIG. 3 is a diagram showing an example of the relationship between the conventional index, the furnace heat index of the present invention, and the temperature difference from the standard hot metal temperature.
- FIG. 1 is a block diagram showing the configuration of a furnace heat control system that is an embodiment of the present invention.
- a furnace heat control apparatus 1 which is an embodiment of the present invention, is configured by an information processing apparatus such as a computer.
- the furnace heat control device 1 functions as a supplied heat amount estimation device according to the present invention.
- the furnace heat control device 1 By executing the furnace heat control process described below, the furnace heat control device 1 having such a configuration can also The amount of heat supplied to the pig iron in the blast furnace 2 is accurately estimated, and the estimated result is used to appropriately maintain the amount of heat supplied to the pig iron in the blast furnace 2 and to precisely control the temperature of molten iron within a predetermined range.
- the flow of the furnace heat control process which is one embodiment of the present invention, will be described below with reference to FIG.
- the operation of the furnace heat control apparatus 1 described below is performed by an arithmetic processing unit such as a CPU in the information processing apparatus constituting the furnace heat control apparatus 1, which stores a program 1a from a storage unit such as a ROM to a temporary storage unit such as a RAM. and executing the loaded program 1a.
- the program 1a may be configured to be recorded in a computer-readable recording medium such as a CD-ROM, a flexible disk, a CD-R, and a DVD as a file in an installable format or an executable format and provided. .
- the program 1a is provided by being stored on a computer connected to a network such as an electric communication line such as the Internet, a telephone communication network such as a mobile phone, or a wireless communication network such as WiFi (registered trademark), and downloaded via the network. It may be configured to
- FIG. 2 is a flow chart showing the flow of furnace heat control processing, which is an embodiment of the present invention.
- the flowchart shown in FIG. 2 starts at the timing when an execution command for the furnace heat control process is input to the furnace heat control device 1, and the furnace heat control process is based on the conventional reaction heat balance (reaction heat balance) in the blast furnace.
- reaction heat balance reaction heat balance
- steps S2, S3, and S4 are additionally performed, and these are integrated to proceed to the processing of step S5 for estimating the amount of heat to be supplied.
- step S1 for estimating the amount of heat supplied to the blast furnace based on the reaction heat balance (heat generated by reaction, endothermic reaction), sensible heat from blown air, and heat loss (amount of heat removed from the furnace body, etc.) in the blast furnace has been conventionally performed.
- the amount of heat supplied at this time is assumed to be Q0 .
- a preferred example of the processing of step S1 will be described later.
- the furnace heat control device 1 estimates the sensible heat Q7 brought out to the upper part of the blast furnace 2 by the gas passing from the lower part to the upper part of the blast furnace 2 (furnace passing gas).
- the sensible heat Q 7 (MJ/tp: amount of heat per ton of pig iron; hereinafter, tp indicates pig iron tonnage) is It can be calculated by multiplying the temperature difference between the estimated temperature of the gas burned in front of the mouth and the reference temperature representing the temperature of the lower upper end of the blast furnace by the specific heat of the gas, and is expressed by the following formula (1).
- C i is the specific heat (MJ/m 3 /°C) of gas type i (nitrogen, carbon monoxide, hydrogen), and V i is the flow rate of gas type i in bosh gas (m 3 (stp )/min) (m 3 (s.t.p): volume at 0°C and 1 atm (atmospheric pressure)), TFT is the theoretical combustion temperature (°C), T base is the reference temperature (°C) (800 to 1200°C , preferably 900 to 1000° C.), Pig is the ironmaking speed (tp/min), and ⁇ is the influence factor changed by the blast furnace 2.
- a host computer 3 such as a process computer connected to the furnace heat control device 1 via an electric communication line, for example.
- the furnace heat control device 1 estimates the sensible heat Q8 brought into the lower part of the blast furnace 2 by the raw material supplied from the upper part to the lower part of the blast furnace 2 (raw material sensible heat brought in).
- the raw material temperature T1 is a function of the raw material surface height (reduced height) L initial that is lowered when the wind is not blowing, as shown in the following formula (3).
- step S3 it is possible to consider the heat compensation of the room temperature raw material when the room temperature raw material is refilled and operated when the blast furnace is started up after the wind break. It is possible to accurately evaluate that the amount of heat is reduced. This completes the process of step S3, and proceeds to the process of step S5.
- Cj is the specific heat (MJ/kg/°C) of raw material j (coke, pig iron, slag)
- Rj is the unit consumption of raw material j (kg / tp)
- T1 is the raw material at the lower end of the cohesive zone.
- T base is the reference temperature (° C.)
- ⁇ is the influence factor changed by the blast furnace 2 .
- the furnace heat control device 1 estimates the amount of heat retained in the core coke existing in the lower part of the blast furnace 2 (coke retention heat amount) Q9 .
- the coke retention heat quantity Q 9 (MJ/tp) is the value obtained by subtracting the combustion consumption and the amount of carbon discharged as dust from the coke consumption rate per 1 ton of hot metal, and the reference temperature and theoretical combustion It can be obtained by multiplying the difference from the temperature and the specific heat C coke of coke, and is expressed by the following formula (4).
- C coke is the specific heat of coke (MJ/kg/°C)
- TFT is the theoretical combustion temperature (°C)
- T base is the reference temperature (°C)
- CR is the coke ratio (kg/tp)
- CR burn is Pre-tuyere combustion carbon ratio (amount of oxygen consumed in front of tuyere by blast oxygen and humidity control) (kg/tp)
- PCR is pulverized coal ratio (kg/tp)
- C inPC is in pulverized coal
- C sol is solution loss carbon ratio (kg/t-p)
- Dust is dust ratio (kg/t-p)
- C indust is carbon ratio in dust
- ⁇ and ⁇ are changed by blast furnace 2 Indicates the influence coefficient.
- step S5 the furnace heat control device 1 estimates the heat dissipation Q10 due to the stop wind.
- the dissipated heat Q 10 (MJ/tp) due to the resting wind can be obtained by the following formula (5).
- the heat dissipation Q10 due to the resting wind it can be evaluated that part of the heat quantity supplied to the lower part of the blast furnace is used for heating the furnace body until the heat dissipation Q10 is eliminated. Thereby, the process of step S5 is completed, and the process proceeds to step S6.
- Q is the integrated value of the heat dissipation per unit time during the wind break (MJ / min)
- t 1 is the wind break time (min)
- t 2 is the elapsed time from the start of the blast furnace after the wind break ( min)
- a, b, and c are coefficients in consideration of the influence of the cooling equipment capacity of the blast furnace body.
- the furnace heat control device 1 controls the supply heat amount Q 0 estimated in the process of step S1, the gas carry-out sensible heat Q 7 estimated in the processes of steps S2 to S5, the raw material carry-in sensible heat Q 8 , coke retention heat Q 9 , and radiated heat Q 10 due to the rest wind, the heat quantity supplied to the pig iron in the blast furnace 2 is estimated. Specifically, the furnace heat control device 1 calculates the supply heat quantity Q 0 estimated in step S1, the gas take-out sensible heat Q 7 estimated in the processing of steps S2 to S5, and the raw material Furnace heat index T Q ( MJ/ tp ) is calculated. Thereby, the process of step S6 is completed, and it progresses to the process of step S7.
- Q0 represents the amount of heat supplied into the blast furnace due to the reaction heat balance (heat generated by reaction, endothermic reaction), sensible heat of blown air, and heat loss (amount of heat removed from the furnace body, etc.) in the blast furnace. Therefore, it is possible to apply an estimation method that has been adopted in many cases in the conventional estimation of the amount of heat supplied, but a preferred form is Equation (7).
- Q 1 indicates the combustion heat of tuyere tip coke (MJ/tp).
- Combustion heat Q1 can be calculated by dividing the amount of heat generated by coke combustion, which is calculated from the amount of oxygen blown from the tuyere into the blast furnace per unit time, by the amount of molten pig iron produced per unit time.
- Q 2 indicates the sensible heat of the air blown into the blast furnace (MJ/tp) by the air blown from the tuyeres.
- Blast sensible heat Q 2 is the amount of heat put into the blast furnace by the blast per unit time from the measured value of the blast volume and blast temperature per unit time, and this value is the amount of molten pig iron produced in that unit time. can be calculated by dividing
- Q3 indicates the heat of solution loss reaction (MJ/tp).
- the reaction heat can be calculated by obtaining the amount of solution loss carbon from the top gas component value as described in Patent Document 1.
- the solution loss reaction heat Q3 can be calculated by dividing this solution loss reaction heat by the amount of molten pig iron produced per unit time.
- Q 4 indicates the decomposition heat (MJ/tp) of moisture mainly contained in the blown air.
- the heat of decomposition Q4 can be calculated by dividing the heat of decomposition obtained from the measured value of the air humidity by the amount of hot metal produced per unit time.
- the amount of heat removed Q5 indicates the heat loss from the furnace body (for example, the amount of heat removed by cooling water) (MJ/tp).
- the amount of heat removed Q5 is the amount of heat removed per unit time by cooling water from the amount of cooling water and the temperature difference between the inlet and outlet sides of cooling water in the blast furnace body. can be calculated by dividing the calculated amount of heat removal by the amount of molten pig iron produced per unit time.
- Q6 indicates the decomposition heat (MJ/tp) of the reducing material blown from the tuyere per unit time.
- the heat of decomposition Q6 can be calculated by dividing the heat of decomposition by the amount of hot metal produced per unit time.
- step S7 the furnace heat control device 1 controls the amount of heat supplied from the tuyeres into the blast furnace 2 based on the amount of heat supplied to the pig iron in the blast furnace 2 estimated in the process of step S6. , the amount of heat supplied to the pig iron in the blast furnace 2 is properly maintained, and the molten pig iron temperature is controlled within a predetermined range. As a result, the processing of step S7 is completed, and the series of furnace heat control processing ends.
- the furnace heat control device 1 controls the change in the sensible heat carried out to the upper part of the blast furnace by the gas passing through the furnace and the gas passing through the furnace. Estimate the change in the sensible heat brought into the lower part of the blast furnace by the raw materials preheated by do. In addition, the furnace heat control device 1 estimates the amount of heat supplied to the pig iron in the blast furnace in consideration of the heat dissipated from the blast furnace during the wind break, estimates the amount of heat retained in the core coke present in the blast furnace, Considering the estimated amount of heat retained in the core coke, the amount of heat supplied to the pig iron in the blast furnace is estimated.
- Fig. 3 shows the conventional furnace heat index (estimated by Q 1 to Q 6 ) and the furnace heat index of the present invention (estimated by Q 1 to Q 10 ) at the start-up of the blast furnace after the wind break and the actual hot metal temperature (reference hot metal temperature). difference from temperature).
- the furnace heat index of the present invention invention example, compared with the conventional furnace heat index (comparative example), the difference between the furnace heat index and the hot metal temperature (difference from the reference hot metal temperature) A certain correlation can be confirmed between them.
- Table 1 summarizes the standard deviation of the difference between the estimated hot metal temperature and the actual hot metal temperature when considering each factor.
- the furnace heat index of the present invention even when the operation rate changes greatly, especially when starting up the blast furnace after the wind is stopped, the amount of heat supplied to the pig iron in the blast furnace can be appropriately maintained and the molten iron temperature can be adjusted. can be precisely controlled within a predetermined range.
- a supplied heat amount estimation method capable of accurately estimating the amount of heat supplied to pig iron in a blast furnace even when the operating rate changes significantly, especially when the blast furnace is started up after a wind break, and supplied heat amount estimation.
- a device and a supplied heat quantity estimation program can be provided.
- the amount of heat supplied to the pig iron in the blast furnace is properly maintained and the molten iron temperature is kept within a predetermined range.
- a well-controllable method of operating a blast furnace can be provided.
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Abstract
Description
まず、図1を参照して、本発明の一実施形態である炉熱制御装置の構成について説明する。図1は、本発明の一実施形態である炉熱制御装置の構成を示すブロック図である。図1に示すように、本発明の一実施形態である炉熱制御装置1は、コンピュータ等の情報処理装置によって構成され、高炉2の下部に設けられている羽口から高炉2内の融体に供給される熱量を制御することによって高炉2内で製造される溶銑の温度を所定範囲内に制御する。炉熱制御装置1は、本発明に係る供給熱量推定装置として機能する。
図2は、本発明の一実施形態である炉熱制御処理の流れを示すフローチャートである。図2に示すフローチャートは、炉熱制御処理の実行命令が炉熱制御装置1に入力されたタイミングで開始となり、炉熱制御処理は、従来から行われてきた高炉内での反応熱収支(反応生成熱、反応吸熱)、送風顕熱、及びヒートロス(炉体からの抜熱量等)等によって高炉内に供給される熱量を推定するステップS1の処理に加え、ステップS2、ステップS3、及びステップS4の処理を追加して行い、これらを統合して供給熱量を推定するステップS5の処理に進む。高炉内での反応熱収支(反応生成熱、反応吸熱)、送風顕熱、及びヒートロス(炉体からの抜熱量等)等によって高炉内に供給される熱量を推定するステップS1の処理は従来から行われており、この時の供給熱量をQ0とする。ステップS1の処理の好適な例については後述する。
図3に休風後の高炉立ち上げ時における従来の炉熱指数(Q1~Q6で推定)と本発明の炉熱指数(Q1~Q10で推定)を実際の溶銑温度(基準溶銑温度からの差)と対比した結果を示す。図3に示すように、本発明の炉熱指数(本発明例)では、従来の炉熱指数(比較例)と比較して、炉熱指数と溶銑温度(基準溶銑温度からの差)との間に一定の相関関係を確認できる。また、表1にそれぞれの因子を考慮した際の推定溶銑温度と実績溶銑温度の差の標準偏差をまとめたものを示す。従来の炉熱指数として、Q1~Q6のみを用いて炉熱指数を推定した場合(比較例1)や休風による減尺高さ及び放散熱を考慮しない場合(比較例2。Q1~Q9を用いて炉熱指数を推定。但し、減尺高さに応じたQ8の修正なし)と比較して、休風による減尺高さ及び放散熱を考慮した場合(本発明例1。Q1~Q10を用いて炉熱指数を推定。減尺高さに応じたQ8の修正あり)及び休風による放散熱のみを考慮した場合(本発明例2。Q1~Q10を用いて炉熱指数を推定。但し、減尺高さに応じたQ8の修正なし)により推定精度が向上していることがわかる。これにより、操業度が大きく変化した際、特に休風後の高炉の立ち上げの際にも本発明の炉熱指数を用いることにより、高炉内の銑鉄に供給される熱量を適正に保ち溶銑温度を所定範囲内に精度よく制御できることがわかる。
1a プログラム
2 高炉
3 上位コンピュータ
Claims (6)
- 高炉内に供給される熱量及び高炉内での溶銑の製造速度から高炉内の銑鉄に供給される熱量を推定する供給熱量推定方法であって、
炉内通過ガスによる持出顕熱の変化及び前記炉内通過ガスによって予熱される原料により供給される持ち込み顕熱の変化を推定し、推定された持出顕熱及び持ち込み顕熱の変化を考慮して高炉内の銑鉄に供給される熱量を推定する推定ステップを含み、
前記推定ステップは、休風時に高炉から放散する熱を考慮して高炉内の銑鉄に供給される熱量を推定するステップと、前記高炉に存在する炉芯コークスに保持される熱量を推定し、推定された炉芯コークスに保持される熱量を考慮して高炉内の銑鉄に供給される熱量を推定するステップと、を含む、
供給熱量推定方法。 - 前記推定ステップは、休風時に下げた原料の表面高さを考慮して前記持ち込み顕熱の変化を推定するステップを含む、請求項1に記載の供給熱量推定方法。
- 高炉内に供給される熱量及び高炉内での溶銑の製造速度から高炉内の銑鉄に供給される熱量を推定する供給熱量推定装置であって、
炉内通過ガスによる持出顕熱の変化及び前記炉内通過ガスによって予熱される原料により供給される持ち込み顕熱の変化を推定し、推定された持出顕熱及び持ち込み顕熱の変化を考慮して高炉内の銑鉄に供給される熱量を推定する推定手段を備え、
前記推定手段は、休風時に下げた原料の表面高さを考慮して前記持ち込み顕熱の変化を推定し、休風時に高炉から放散する熱を考慮して高炉内の銑鉄に供給される熱量を推定し、前記高炉に存在する炉芯コークスに保持される熱量を推定し、推定された炉芯コークスに保持される熱量を考慮して高炉内の銑鉄に供給される熱量を推定する、
供給熱量推定装置。 - 前記推定手段は、休風時に下げた原料の表面高さを考慮して前記持ち込み顕熱の変化を推定する、請求項3に記載の供給熱量推定装置。
- 高炉内に供給される熱量及び高炉内での溶銑の製造速度から高炉内の銑鉄に供給される熱量を推定する処理をコンピュータに実行させる供給熱量推定プログラムであって、
前記コンピュータに、炉内通過ガスによる持出顕熱の変化及び前記炉内通過ガスによって予熱される原料により供給される持ち込み顕熱の変化を推定し、推定された持出顕熱及び持ち込み顕熱の変化を考慮して高炉内の銑鉄に供給される熱量を推定する推定処理を実行させ、
前記推定処理は、休風時に下げた原料の表面高さを考慮して前記持ち込み顕熱の変化を推定し、休風時に高炉から放散する熱を考慮して高炉内の銑鉄に供給される熱量を推定し、前記高炉に存在する炉芯コークスに保持される熱量を推定し、推定された炉芯コークスに保持される熱量を考慮して高炉内の銑鉄に供給される熱量を推定する処理を含む、供給熱量推定プログラム。 - 請求項1又は2に記載の供給熱量推定方法によって推定された高炉内の銑鉄に供給される熱量に基づいて高炉内に供給される熱量を制御するステップを含む、高炉の操業方法。
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