SUPPLIED HEAT QUANTITY ESTIMATION METHOD, SUPPLIED HEAT QUANTITY ESTIMATION DEVICE, SUPPLIED HEAT QUANTITY ESTIMATION PROGRAM, AND BLAST FURNACE OPERATION METHOD

Abstract

A supplied heat quantity estimation method estimates a quantity of heat supplied to pig iron in a blast furnace from a quantity of heat supplied into the blast furnace and a production speed of molten iron in the blast furnace, and includes an estimation step of estimating a change in carried out sensible heat by in-furnace passing gas and a change in carried in sensible heat supplied by a raw material preheated by the in-furnace passing gas, and estimating the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated changes of the carried out sensible heat and the carried in sensible heat. The estimation step includes calculating an iron making speed and estimating a quantity of heat held in furnace core coke present in the blast furnace to estimate the quantity of heat supplied to pig iron.

Claims

1. A supplied heat quantity estimation method for estimating a quantity of heat supplied to pig iron in a blast furnace from a quantity of heat supplied into the blast furnace and a production speed of molten iron in the blast furnace, the supplied heat quantity estimation method comprising an estimation step of estimating a change in carried out sensible heat by in-furnace passing gas and a change in carried in sensible heat supplied by a raw material preheated by the in-furnace passing gas, and estimating the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated changes of the carried out sensible heat and the carried in sensible heat, wherein the estimation step includes a step of calculating an iron making speed using an amount of oxygen in blown air per unit time, an amount of carbon gasified in the blast furnace, and an amount of carbon required for heating and reducing iron content per predetermined unit amount in molten iron, and estimating the quantity of heat supplied to pig iron in the blast furnace using the calculated iron making speed, and a step of estimating a quantity of heat held in deadman coke present in the blast furnace, and estimating the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated quantity of heat held in deadman coke.

2. A supplied heat quantity estimation device for estimating a quantity of heat supplied to pig iron in a blast furnace from a quantity of heat supplied into the blast furnace and a production speed of molten iron in the blast furnace, the supplied heat quantity estimation device comprising an estimation unit configured to estimate a change in carried out sensible heat by in-furnace passing gas and a change in carried in sensible heat supplied by a raw material preheated by the in-furnace passing gas, and estimate the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated changes of the carried out sensible heat and the carried in sensible heat, wherein the estimation unit is configured to calculate an iron making speed using an amount of oxygen in blown air per unit time, an amount of carbon gasified in the blast furnace, and an amount of carbon required for heating and reducing iron content per predetermined unit amount in molten iron, estimate the quantity of heat supplied to pig iron in the blast furnace using the calculated iron making speed, estimate a quantity of heat held in deadman coke present in the blast furnace, and estimate the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated quantity of heat held in deadman coke.

3. (canceled)

4. A blast furnace operation method comprising a step of controlling a quantity of heat supplied into the blast furnace based on the quantity of heat supplied to pig iron in the blast furnace estimated by the supplied heat quantity estimation method according to claim 1.

5. A non-transitory computer-readable recording medium on which an executable program for estimating a quantity of heat supplied to pig iron in a blast furnace from a quantity of heat supplied into the blast furnace and a production speed of molten iron in the blast furnace, the program causing a processor of a computer to execute: an estimation step of estimating a change in carried out sensible heat by in-furnace passing gas and a change in carried in sensible heat supplied by a raw material preheated by the in-furnace passing gas; and estimating the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated changes of the carried out sensible heat and the carried in sensible heat, wherein the estimation step includes calculating an iron making speed using an amount of oxygen in blown air per unit time, an amount of carbon gasified in the blast furnace, and an amount of carbon required for heating and reducing iron content per predetermined unit amount in molten iron, and estimating the quantity of heat supplied to pig iron in the blast furnace using the calculated iron making speed, and estimating a quantity of heat held in furnace core coke present in the blast furnace, and estimating the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated quantity of heat held in furnace core coke.

Description

BRIEF DESCRIPTION OF DRAWINGS

[0013] FIG. 1 is a block diagram illustrating a configuration of a furnace heat control device according to one embodiment of the present invention.

[0014] FIG. 2 is a flowchart illustrating a flow of furnace heat control processing according to the one embodiment of the present invention.

[0015] FIG. 3 is a diagram illustrating an example of a relationship between a conventional index and a furnace heat index of the present invention, and a temperature difference from a reference molten iron temperature.

DESCRIPTION OF EMBODIMENTS

[0016] Hereinafter, a configuration and operation of a furnace heat control device according to one embodiment of the present invention to which a supplied heat quantity estimation method and a supplied heat quantity estimation device according to the present invention are applied will be described with reference to the drawings.

[Configuration]

[0017] First, a configuration of a furnace heat control device according to one embodiment of the present invention will be described with reference to FIG. 1. FIG. 1 is a block diagram illustrating a configuration of the furnace heat control device according to the one embodiment of the present invention. As illustrated in FIG. 1, a furnace heat control device 1 according to the one embodiment of the present invention includes an information processing device such as a computer, and controls the temperature of molten iron produced in a blast furnace 2 within a predetermined range by controlling the quantity of heat supplied to a melt in the blast furnace 2 from a tuyere disposed in a lower part of the blast furnace 2. The furnace heat control device 1 functions as a supplied heat quantity estimation device according to the present invention.

[0018] The furnace heat control device 1 having such a configuration, by executing furnace heat control processing described below, accurately estimates the quantity of heat supplied to pig iron in the blast furnace 2 when the operation rate of the blast furnace 2 greatly changes, particularly even in descending operation, and accurately controls the molten iron temperature within a predetermined range while appropriately maintaining the quantity of heat supplied to pig iron in the blast furnace 2 using the estimation result. Hereinafter, a flow of the furnace heat control processing according to the one embodiment of the present invention will be described with reference to FIG. 2.

[0019] Note that the operation of the furnace heat control device 1 described below is implemented by an arithmetic processing device such as a CPU in the information processing device included in the furnace heat control device 1 loading 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 provided by being recorded in a computer-readable recording medium such as a CD-ROM, a flexible disk, a CD-R, or a DVD as a file in an installable format or an executable format. The program 1a may be stored in a computer connected to a network such as a telecommunication 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 provided by being downloaded via the network.

[Furnace Heat Control Processing]

[0020] FIG. 2 is a flowchart illustrating a flow of furnace heat control processing according to the one embodiment of the present invention. The flowchart illustrated in FIG. 2 starts at a timing when an execution command of the furnace heat control processing is input to the furnace heat control device 1, and in the furnace heat control processing, processing of steps S2, S3, and S4 is performed in addition to processing of step S1 of estimating the quantity of heat supplied into the blast furnace by a reaction heat balance (heat of reaction generation, reaction endotherm) in the blast furnace, blown air sensible heat, heat loss (quantity of heat removed from the furnace body or the like), and the like, which has been conventionally performed, the processing is integrated, and then processing of step S5 of estimating the supplied heat quantity is proceeded to. The processing of step S1 of estimating the quantity of heat supplied into the blast furnace by the reaction heat balance (heat of reaction generation, reaction endotherm) in the blast furnace, blown air sensible heat, heat loss (quantity of heat removed from the furnace body or the like), and the like is conventionally performed, and the supplied heat quantity at this time is set as Q.sub.0. A preferred example of the processing in step S1 will be described below.

[0021] In the processing of step S2, the furnace heat control device 1 estimates sensible heat (gas carried out sensible heat) Q.sub.7 carried out to the upper part of the blast furnace 2 by the gas (in-furnace passing gas) passing from the lower part to the upper part of the blast furnace 2. Specifically, the gas carried out sensible heat Q.sub.7 (MJ/t-p: quantity of heat per ton of pig iron. Hereinafter, t-p represents pig iron tonnage) can be calculated by multiplying a temperature difference between an estimated temperature of gas combusted in front of the tuyere and a reference temperature representing a temperature of the upper end of the lower part of the blast furnace by the specific heat of the gas, and is expressed by the following Formula (1). As a result, the processing of step S2 is completed, and the processing proceeds to the processing of step S5.

[00001]$\begin{array}{cc}{Q}_7=?.Math.\left\{.Math.\left(C_i.Math.V_i\right)\right\}.Math.\left(\mathrm{TFT}-T_{\mathrm{base}}\right).Math.\frac{1}{\mathrm{Pig}}& \left(1\right)\end{array}$

[0022] Here, C.sub.i represents the specific heat (MJ/m.sup.3/? C.) of the gas species i (nitrogen, carbon monoxide, hydrogen), V.sub.i represents the flow rate (m.sup.3(s.t.p)/min) (m.sup.3(s.t.p):0? C., volume at 1 atm (atmospheric pressure)) of the gas species i in Bosch gas, TFT represents a theoretical combustion temperature (? C.), T.sub.base represents a reference temperature (? C.) (800 to 1200? C., preferably 900 to 1000? C.), Pig represents an iron making speed (t-p/min), and ? represents an influence coefficient changed by the blast furnace 2. These values can be acquired from a host computer 3 such as a process computer connected to the furnace heat control device 1 via a telecommunication line, for example.

[0023] In normal operation, a raw material is charged such that the height of the surface of the raw material in the blast furnace is kept constant. Therefore, the amount of molten iron produced per unit time can be estimated from the amount of iron in the raw material charged per unit time. Furthermore, since the oxidation degree of the raw material charged (ratio of the number of moles of oxygen to the number of moles of iron in the iron ore material) is known, the amount of molten iron produced per unit time can also be calculated from the balance between carbon and oxygen per unit time in the blast furnace. However, during descending operation in which the height of the raw material charging surface is gradually lowered, the raw material charging is not performed or the raw material charging is performed intermittently, and thus the amount of molten iron produced per unit time is difficult to be estimated from the amount of iron in the raw material charged per unit time. Furthermore, in a case where the height of the surface of the raw material greatly decreases due to no charging of the raw material, the reduction rate of the ore on the surface of the raw material increases, and thus the amount of molten iron is difficult to be accurately calculated from the balance of carbon and oxygen per unit time in the blast furnace.

[0024] Therefore, in the present embodiment, the amount of molten iron produced per unit time is estimated without being affected by the amount of iron charged per unit time and the degree of oxidation of the raw material on the surface of the raw material, using the amount of oxygen in blown air per unit time, the amount of carbon gasified in the blast furnace, and the amount of carbon required for heating and reducing 1 kmol of iron in the molten iron. Specifically, when a value obtained by rebating the amount of carbon gasified in a reaction of 2FeO+C.fwdarw.2Fe+CO.sub.2 to the amount per 1 kmol of Fe is y.sub.s1 (kmol-C/kmol-Fe), and a value obtained by rebating the amount of carbon gasified at the tuyere in a reaction of 2C+O.sub.2.fwdarw.2CO or C+H.sub.2O.fwdarw.CO+H.sub.2 by blown air oxygen and oxygen of blown air moisture to the amount per 1 kmol of Fe is y.sub.b (kmol-C/kmol-Fe), the amount of carbon X (kmol-C/kmol-Fe) required for heating and reducing per 1 kmol of iron content in the molten iron is represented by the following Formula (2). Here, since the ratio of a reducing material with which the blast furnace is filled is known, the amount of carbon X (kmol-C/kmol-Fe) required for heating and reducing iron per 1 kmol of iron content in the molten iron can be obtained by converting the amount of carbon into a molar quantity from the ratio of the reducing material and also converting the amount of iron contained in 1 t of molten iron of the denominator of the ratio of the reducing material into a molar quantity.

[00002]$\begin{array}{cc}X=y_{\mathrm{st}}+y_b& \left(2\right)\end{array}$

[0025] Furthermore, the amount of carbon A (kmol-C/min) consumed by a direct reduction per unit time can be measured as an increase amount of the amount of carbon while gas generated by combustion in front of the tuyere reacts in the blast furnace and is discharged from the upper part of the blast furnace, and thus can be obtained from the difference between a composition of blown air gas and a gas analysis value of the upper part of the blast furnace. When the amount of carbon contained in CO generated by oxygen contained in blown air and moisture in blown air is denoted by B (kmol-C/min), a relationship represented by the following Formula (3) is established between the above-mentioned y.sub.s1 and y.sub.b.

[00003]$\begin{array}{cc}A:B=y_{\mathrm{st}}:y_b& \left(3\right)\end{array}$

[0026] Therefore, the following Formulas (4) and (5) are obtained by solving the Formulas (2) and (3) for y.sub.b and y.sub.s1. Since the amount of oxygen in blown air (kmol-O/min) is known from air blowing conditions, the molar quantity of iron produced per unit time (iron making speed (kmol-Fe/min)) can be obtained by dividing the amount of oxygen in blown air by the y.sub.s1 value indicated in Formula (5). Here, by multiplying the calculated molar quantity of iron by a molar mass of iron and dividing the obtained value by a weight ratio of iron in the molten iron, the amount of molten iron produced per unit time can be obtained. As a result, the amount of molten iron produced per unit time can be accurately estimated even in descending operation. Note that, as the weight ratio of iron in the molten iron, an analysis value of a molten iron component is preferably used, and an immediately preceding analysis value is more preferably used.

[00004]$\begin{array}{cc}{y}_b=X\frac{B}{A+B}& \left(4\right)\end{array}$$\begin{array}{cc}{y}_{\mathrm{sl}}=X\frac{A}{A+B}& \left(5\right)\end{array}$

[0027] In the processing of step S3, the furnace heat control device 1 estimates sensible heat (raw material carried in sensible heat) Q.sub.8 carried in to 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. Specifically, the raw material carried in sensible heat Q.sub.8 (MJ/t-p) can be calculated by multiplying the temperature difference between the raw material temperature T.sub.1 (=1450 to 1500? C.) at the lower end of a fusion zone and the reference temperature T.sub.base by the specific heat of the raw material as indicated by the following Formula (6). As a result, the processing of step S3 is completed, and the processing proceeds to the processing of step S5.

[00005]$\begin{array}{cc}{Q}_8=?.Math.\left\{.Math.\left(C_j.Math.R_j\right)\right\}.Math.\left(T_1-T_{\mathrm{base}}\right)& \left(6\right)\end{array}$

[0028] Here. C.sub.j represents specific heat (MJ/kg/? C.) of a raw material j (coke, pig iron, slag), R.sub.j represents a basic unit (kg/t-p) of the raw material j, T.sub.1 represents a raw material temperature (? C.) at the lower end of the fusion zone, T.sub.base represents the reference temperature (? C.), and ? represents an influence coefficient changed by the blast furnace 2. These values can be acquired from, for example, the host computer 3.

[0029] In the processing of step S4, the furnace heat control device 1 estimates the quantity of heat (coke holding heat quantity) Q.sub.9 held in the deadman coke present in the lower part of the blast furnace 2. Specifically, the coke holding heat quantity Q.sub.9 (MJ/t-p) can be obtained by multiplying a value obtained by subtracting a combustion consumption amount and a carbon amount discharged as dust from a coke basic unit per 1 t of molten iron by a difference between a reference temperature and a theoretical combustion temperature and specific heat of coke C.sub.coke, and is expressed by the following Formula (7). As a result, the processing of step S4 is completed, and the processing proceeds to the processing of step S5. Note that the processing of step S4 may be omitted.

[00006]$\begin{array}{cc}{Q}_9=?.Math.C_{\mathrm{Coke}}.Math.\left(?.Math.\mathrm{TFT}-T_{\mathrm{base}}\right).Math.\left\{\mathrm{CR}-\frac{\left({\mathrm{CR}}_{\mathrm{burn}}-\mathrm{PCR}.Math.C_{\mathrm{inPC}}\right)+C_{\mathrm{sol}}+\mathrm{Dust}.Math.C_{\mathrm{indust}}}{0.88}\right\}& \left(7\right)\end{array}$

[0030] Here, C.sub.coke represents the specific heat of coke (MJ/kg/? C.), TFT represents the theoretical combustion temperature (? C.), T.sub.base represents the reference temperature (? C.), CR represents a coke ratio (kg/t-p), CR.sub.burn represents a pre-tuyere combustion carbon ratio (amount of oxygen consumed in front of the tuyere by blown air oxygen and humidity control) (kg/t-p), PCR represents a pulverized coal ratio (kg/t-p), C.sub.inPC represents a carbon ratio in pulverized coal, C.sub.sol represents a solution loss carbon ratio (kg/t-p), Dust represents a dust ratio (kg/t-p), C.sub.indust represents a carbon ratio in dust, and ? and ? represent influence coefficients changed by the blast furnace 2. These values can be acquired from, for example, the host computer 3.

[0031] In the processing of step S5, the furnace heat control device 1 estimates the quantity of heat supplied to pig iron in the blast furnace 2 using the supplied heat quantity Q.sub.0 estimated in the processing of step S1, the gas carried out sensible heat Q.sub.7, the raw material carried in sensible heat Q.sub.8, and the coke holding heat quantity Q.sub.9 that are estimated in the processing of steps S2 to S4. Specifically, the furnace heat control device 1 calculates a furnace heat index T.sub.Q (MJ/t-p) corresponding to the quantity of heat supplied to pig iron in the blast furnace 2 by substituting the supplied heat quantity Q.sub.0 estimated in step S1, the gas carried out sensible heat Q.sub.7, the raw material carried in sensible heat Q.sub.8, and the coke holding heat quantity Q.sub.9 that are estimated in the processing of steps S2 to S4 into the following Formula (8). As a result, the processing of step S5 is completed, and the processing proceeds to the processing of step S6. Note that, in a case where the processing of step S4 is omitted, the value of the coke holding heat quantity Q.sub.9 is set to zero.

[00007]$\begin{array}{cc}{T}_Q=Q_0-Q_7+Q_8-Q_9& \left(8\right)\end{array}$

[0032] Here, Q.sub.0 represents the quantity of heat supplied into the blast furnace by the reaction heat balance (heat of reaction generation, reaction endotherm) in the blast furnace, blown air sensible heat, heat loss (quantity of heat removed from the furnace body or the like), and the like, and an estimation method adopted in many cases in the conventional supplied heat quantity estimation can be applied, but as a preferable form, Formula (9) can be cited.

[00008]$\begin{array}{cc}{Q}_0=Q_1+Q_2-Q_3-Q_4-Q_5-Q_6& \left(9\right)\end{array}$

[0033] Here, Q.sub.1 represents combustion heat (MJ/t-p) of post-tuyere coke. The combustion heat Q.sub.1 can be calculated by dividing the calorific amount due to combustion of coke calculated from the amount of oxygen blown from the tuyere to the blast furnace per unit time by the amount of molten iron produced per unit time (iron making speed). The iron making speed can be accurately calculated even at the time of descending operation by the above-described method.

[0034] Furthermore, Q.sub.2 represents blown air sensible heat (MJ/t-p) input to the blast furnace by blown air from the tuyere. The blown air sensible heat Q.sub.2 can be calculated by obtaining the quantity of heat input to the blast furnace by blown air per unit time from the blown air amount per unit time and the measured value of the blown air temperature, and dividing this value by the amount of molten iron produced per unit time.

[0035] Furthermore, Q.sub.3 represents solution loss reaction heat (MJ/t-p). For this value, for example, as described in Patent Literature 1, the reaction heat can be calculated by obtaining the solution loss carbon amount from the furnace top gas component value. The solution loss reaction heat Q.sub.3 can be calculated by dividing the solution loss reaction heat by the amount of molten iron produced per unit time.

[0036] Furthermore, Q.sub.4 represents heat of decomposition (MJ/t-p) of moisture mainly contained in blown air. The heat of decomposition Q.sub.4 can be calculated by dividing heat of decomposition obtained from the measured value of the blown air moisture by the amount of molten iron produced per unit time.

[0037] Furthermore, Q.sub.5 represents heat loss from the furnace body (for example, quantity of heat removed by cooling water) (MJ/t-p). In a case where the quantity of heat removed by cooling water is calculated as the heat loss, the quantity of heat removed Q.sub.5 can be calculated by calculating the quantity of heat removed by the cooling water per unit time from the amount of the cooling water and the temperature difference between the inlet side and the outlet side of the cooling water of the furnace body of the blast furnace, and dividing the calculated quantity of heat removed by the amount of molten iron produced per unit time.

[0038] Furthermore, Q.sub.6 represents the heat of decomposition (MJ/t-p) of the reducing material blown from the tuyere per unit time. The heat of decomposition Q.sub.6 can be calculated by dividing the heat of decomposition by the amount of molten iron produced per unit time.

[0039] In the processing of step S6, the furnace heat control device 1 controls the quantity of heat supplied from the tuyere into the blast furnace 2 based on the quantity of heat supplied to pig iron in the blast furnace 2 estimated in the processing of step S5, thereby appropriately maintaining the quantity of heat supplied to the pig iron in the blast furnace 2 and controlling the molten iron temperature within a predetermined range. As a result, the processing of step S6 is completed, and a series of the furnace heat control processing ends.

[0040] As is apparent from the above description, in the furnace heat control processing according to the one embodiment of the present invention, the furnace heat control device 1 estimates a change in carried out sensible heat to the upper part of the blast furnace by in-furnace passing gas and a change in carried in sensible heat supplied to the lower part of the blast furnace by a raw material preheated by the in-furnace passing gas, and estimates the quantity of heat supplied to pig iron in the blast furnace in consideration of the estimated changes of the carried out sensible heat and the carried in sensible heat. Furthermore, the furnace heat control device 1 calculates the iron making speed using the amount of oxygen in blown air per unit time, the amount of carbon gasified in the blast furnace, and the amount of carbon required for heating and reducing the iron content per predetermined unit amount in molten iron, estimates the quantity of heat supplied to pig iron in the blast furnace using the calculated iron making speed, estimates the quantity of heat held in the deadman coke present in the blast furnace, and estimates the quantity of heat supplied to the pig iron in the blast furnace in consideration of the estimated quantity of heat held in the deadman coke. As a result, the quantity of heat supplied to the pig iron in the blast furnace can be accurately estimated when the operation rate such as the amount of air blown into the blast furnace greatly changes, particularly even in descending operation. As a result, the molten iron temperature can be accurately controlled within a predetermined range while the quantity of heat supplied to the pig iron in the blast furnace is appropriately maintained when the operation rate greatly changes, particularly even in descending operation.

Example

[0041] FIG. 4 indicates results of comparing a conventional furnace heat index (estimated by Q.sub.1 to Q.sub.6) and a furnace heat index (estimated by Q.sub.1 to Q.sub.9) of the present invention in descending operation with an actual molten iron temperature (difference from the reference molten iron temperature). As indicated in FIG. 4, in the furnace heat index of the present invention (present invention example), a certain correlation between the furnace heat index and the molten iron temperature (difference from the reference molten iron temperature) can be confirmed as compared with the conventional furnace heat index (comparative example). Furthermore, Table 1 indicates a summary of the standard deviation of the difference between the estimated molten iron temperature and the actual molten iron temperature when each factor is taken into consideration. It can be seen that the estimation accuracy was improved in the case of estimating the furnace heat index by Q.sub.1 to Q.sub.9 using the method of calculating the iron making speed of the present invention (present invention example) as compared with the case of estimating the furnace heat index using only Q.sub.1 to Q.sub.6 as the conventional furnace heat index (Comparative Example 1) and the case of estimating the furnace heat index using Q.sub.1 to Q.sub.9 without using the method of calculating the iron making speed of the present invention (Comparative Example 2). As a result, it can be seen that the molten iron temperature can be accurately controlled within a predetermined range while the quantity of heat supplied to the pig iron in the blast furnace is appropriately maintained when the operation rate greatly changes, particularly even in descending operation, using the furnace heat index of the present invention.

TABLE-US-00001 TABLE 1 Comparative Comparative Present invention Example 1 Example 2 example Considered indexes Q.sub.1 to Q.sub.6 Q.sub.1 to Q.sub.9 Q.sub.1 to Q.sub.9 Standard deviation of 127.1 110.3 14.3 actual molten iron temperature with respect to estimated molten iron temperature

[0042] Although the embodiment to which the invention made by the present inventors is applied has been described above, the present invention is not limited by the description and drawings constituting a part of the disclosure of the present invention according to the present embodiment. That is, other embodiments, examples, operation techniques, and the like made by those skilled in the art based on the present embodiment are all included in the scope of the present invention.

INDUSTRIAL APPLICABILITY

[0043] According to the present invention, a supplied heat quantity estimation method, a supplied heat quantity estimation device, and a supplied heat quantity estimation program capable of accurately estimating the quantity of heat supplied to pig iron in a blast furnace when the operation rate greatly changes, particularly even in descending operation can be provided. According to the present invention, a blast furnace operation method in which a molten iron temperature can be accurately controlled within a predetermined range while the quantity of heat supplied to pig iron in the blast furnace is appropriately maintained when the operation rate greatly changes, particularly even in descending operation can be provided.

REFERENCE SIGNS LIST

[0044] 1 FURNACE HEAT CONTROL DEVICE [0045] 1a PROGRAM [0046] 2 BLAST FURNACE [0047] 3 HOST COMPUTER