EP4636099A1

EP4636099A1 - Method for measuring melt level inside blast furnace, device for measuring melt level inside blast furnace, and blast furnace operation method

Info

Publication number: EP4636099A1
Application number: EP23919837.7A
Authority: EP
Inventors: Taiki Iwanaga; Ryotaro Matsunaga
Original assignee: JFE Steel Corp
Current assignee: JFE Steel Corp
Priority date: 2023-01-30
Filing date: 2023-09-27
Publication date: 2025-10-22
Also published as: EP4636099A4; CN120569495A; KR20250129751A; JP7513226B1; JPWO2024161701A1

Abstract

A method for measuring a molten material level in a blast furnace according to the present invention includes: a measurement step of measuring a vibration frequency distribution in a height direction of a furnace body of the blast furnace by using a plurality of vibration meters arranged at predetermined intervals along the height direction of the furnace body; a vibration intensity calculation step of calculating a vibration intensity in a frequency range due to blast at each of measurement positions by performing Fourier transform on the vibration frequency distribution; a numerical analysis step of calculating a maximum vibration intensity distribution of a lower part of the blast furnace by using a numerical analysis model in which the molten material level and a blast amount in the blast furnace are variables; and a molten material level calculation step of calculating the molten material level at which a difference between the vibration intensity calculated in the vibration intensity calculation step and the maximum vibration intensity distribution calculated in the numerical analysis step is minimized, and determining the calculated molten material level as a position of the molten material level in the blast furnace.

Description

Field

The present invention relates to a method for measuring a molten material level in a blast furnace, a device for measuring the molten material level in the blast furnace, and a blast furnace operation method.

Background

In the iron and steel industry, a blast furnace is located in the most upstream process, and thus a technique for stabilizing the operation of the blast furnace is regarded as important. It is important to ensure good air permeability in the furnace for stable operation of the blast furnace. One of the factors inhibiting the air permeability in the furnace is an increase in liquid surface level of molten iron and molten slag (hereinafter, both are collectively referred to as molten material) accumulated in the packed bed in the lower part of the furnace. An increase in the liquid surface level of the molten material (hereinafter, abbreviated as molten material level) may cause a narrowing of a gas flow path in the furnace and may directly cause an increase in blast pressure. In addition, in the case where the molten material level reaches a blast tuyere level, erosion of the blast tuyere, and eventually, serious troubles such as clogging of the blast tuyere and slag return (a phenomenon in which the molten material flows back from the blast tuyere) may be caused. For this reason, in order to achieve a stable operation of the blast furnace, it should be surely avoided that the molten material level reaches the blast tuyere level.
From such a background, a method for evaluating the amount of the molten material accumulated in the furnace on the basis of the material balance from various operating parameters of the blast furnace has been proposed. Specifically, Patent Literature 1 describes a method for estimating an amount of a molten material accumulated in a furnace by obtaining a theoretical amount of the molten material discharged from the blast furnace using an actual volume value of a charge in the furnace and a theoretical volume value calculated from the operating parameters, and comparing the theoretical amount with the amount of the molten material actually discharged. In addition, Patent Literature 2 describes a method for estimating a molten material level in a furnace by solving variables measured by a plurality of strain gauges installed in the furnace body by giving parameters representing properties of constituent materials of the blast furnace including the molten material level to a general equation for continuous ambient strain.
In addition, Patent Literature 3 describes a method using so-called Bernoulli's principle in which a discharge speed of a molten material is calculated from a discharge distance, a discharge angle, and a discharge height of the molten material discharged from a taphole of a blast furnace, and a molten material level in the furnace is estimated using the discharge speed. The estimation accuracy of the present method depends on the calculation accuracy of the discharge speed of the molten material discharged from the taphole, and in the same method, the discharge speed is estimated by performing image analysis on an image captured by a camera. In addition, Patent Literature 4 describes a method in which vibration intensity of a furnace wall in a lower part of a furnace is measured and a molten material level in the furnace is estimated on the basis of a correspondence relationship between the vibration intensity of a specific frequency band obtained in advance and the molten material level.

Citation List

Patent Literature

Patent Literature 1: JP 2002-302709 A
Patent Literature 2: JP 2015-528905 A
Patent Literature 3: JP 7056813 B1
Patent Literature 4: WO 2022/201717 A

Summary

Technical Problem

However, the method described in Patent Literature 1 does not consider porosity of a packed bed in a lower part of the furnace and a shape of a solidified layer. Therefore, even if the amount of the molten material accumulated in the furnace can be estimated, there remains a problem in estimating a liquid surface level of the molten material, which is important for the stable operation of the blast furnace. In addition, since it is affected by various weighing errors, there is a concern that estimation errors accumulate in a blast furnace process in which a large mass is handled, and the estimation accuracy deteriorates over time.
In addition, the method described in Patent Literature 2 has the following problems. It is known that a refractory brick and a solidified layer in which a molten material in the furnace is cooled and solidified are present in the lower part of the furnace in addition to an iron shell and a cooling stave on a surface of the blast furnace. Then, the refractory brick deteriorates over time due to wear and thermal stress, and a range where the solidified layer exists changes daily according to thermal conditions of the lower part of the furnace. Therefore, it is extremely difficult to grasp a state of existence of these constituent materials. Therefore, in the method described in Patent Literature 2, it is substantially impossible to exclude unknown parameters other than the molten material level representing the constituent materials of the blast furnace from the general equation, and therefore, the accuracy of the molten material level estimated from the general equation is also far from satisfactory.
In addition, in the method described in Patent Literature 3, since a large amount of dust is generated along with discharge of a high-temperature molten material during tapping work, there is a low possibility that a clear discharge behavior of the molten material can be captured using a camera. In addition, the occurrence of an opening mistake represented by a lateral hole cannot be avoided in the tapping work, and this is also a cause contributing to a decrease in estimation frequency of the discharge behavior of the molten material. Furthermore, in association with this, since the opening shape is different for each tapping, it is difficult to quantify a frictional force received by the molten material in a path from the inside of the furnace to a discharge port. From the above, it can be said that it is extremely difficult to measure the molten material level with high accuracy by the method described in Patent Literature 3.
In addition, the method described in Patent Literature 4 has the following problems. Vibration intensity of the actual furnace body is affected by variations in blast amount and changes in the shape of structures such as a furnace packing material, a furnace bottom brick, and the solidified layer more strongly than the molten material level. For this reason, in the blast furnace process in which the operational situation changes from moment to moment, it is impossible to establish the correlation between the vibration intensity of the furnace body and the molten material level on a one-to-one basis. Therefore, the method described in Patent Literature 4 is effective only in an extremely ideal situation in which the conditions in the furnace other than the molten material level are in a steady state, and long-term and stable measurement of the molten material level is difficult.
The present invention has been made to solve the above mentioned problems, and an object of the present invention is to provide a method and a device for measuring a molten material level in a blast furnace capable of accurately measuring the molten material level in the blast furnace regardless of operation conditions of the blast furnace. In addition, another object of the present invention is to provide a blast furnace operation method in which eco-friendly blast furnace operation can be performed stably.

Solution to Problem

A method for measuring a molten material level in a blast furnace according to the present invention includes: a measurement step of measuring a vibration frequency distribution in a height direction of a furnace body of the blast furnace by using a plurality of vibration meters arranged at predetermined intervals along the height direction of the furnace body; a vibration intensity calculation step of calculating a vibration intensity in a frequency range due to blast at each of measurement positions by performing Fourier transform on the vibration frequency distribution; a numerical analysis step of calculating a maximum vibration intensity distribution of a lower part of the blast furnace by using a numerical analysis model in which the molten material level and a blast amount in the blast furnace are set as variables; and a molten material level calculation step of calculating the molten material level at which a difference between the vibration intensity calculated in the vibration intensity calculation step and the maximum vibration intensity distribution calculated in the numerical analysis step is minimized, and determining the calculated molten material level as a position of the molten material level in the blast furnace.
The vibration meter may be installed between a taphole level and a tuyere level of the furnace body.
The frequency range due to the blast may be in a range of 700 to 900 Hz.
A device for measuring a molten material level in a blast furnace according to the present invention includes: a plurality of vibration meters arranged at predetermined intervals along a height direction of a furnace body of the blast furnace and configured to measure a vibration frequency distribution in the height direction of the furnace body; and an information processing device configured to calculate a vibration intensity in a frequency range due to blast at each of measurement positions by performing Fourier transform on the vibration frequency distribution, calculate a maximum vibration intensity distribution in a lower part of the blast furnace using a numerical analysis model in which the molten material level and a blast amount in the blast furnace are set as variables, calculate the molten material level at which a difference between the vibration intensity and the maximum vibration intensity distribution is minimized, and determine the calculated molten material level as a position of the molten material level in the blast furnace.
A blast furnace operation method according to the present invention includes a step of operating a blast furnace according to a molten material level measured by using the method for measuring the molten material level in the blast furnace according to the present invention. Advantageous Effects of Invention
According to the method and the device for measuring the molten material level in the blast furnace of the present invention, the molten material level in the blast furnace can be measured with high accuracy regardless of operation conditions of the blast furnace. In addition, according to the blast furnace operation method of the present invention, eco-friendly blast furnace operation can be performed stably.

Brief Description of Drawings

[FIG. 1] FIG. 1 is a schematic cross-sectional view illustrating a configuration of a blast furnace to which a device for measuring a molten material level in the blast furnace according to an embodiment of the present invention is applied.
[FIG. 2] FIG. 2 is a diagram illustrating a calculation flow of a numerical analysis model for vibration.
[FIG. 3] FIG. 3 is a diagram illustrating a configuration of a computational grid.
[FIG. 4] FIG. 4 is a diagram illustrating an analysis example of a two-dimensional vibration model.
[FIG. 5] FIG. 5 is a diagram illustrating a result of plotting vibration intensities due to blast with respect to the height of a measurement position relative to a molten material level, the vibration intensities being measured by a plurality of vibration meters when the molten material level is changed.
[FIG. 6] FIG. 6 is a diagram illustrating a time-dependent change of a measurement value of the molten material level from an initial stage to an end stage of tapping.
[FIG. 7] FIG. 7 is a diagram illustrating a result of fitting vibration intensities measured by an actual machine to the maximum vibration intensities predicted using the numerical analysis model for each molten material level. Description of Embodiments

Hereinafter, a method for measuring a molten material level in a blast furnace, a device for measuring the molten material level in the blast furnace, and a blast furnace operation method according to an embodiment of the present invention will be described with reference to the drawings.

[Configuration]

First, a configuration of the device for measuring the molten material level in the blast furnace according to the embodiment of the present invention will be described with reference to FIG. 1.
FIG. 1 is a schematic cross-sectional view illustrating a configuration of the blast furnace to which the device for measuring the molten material level in the blast furnace according to the embodiment of the present invention is applied. As illustrated in FIG. 1, a blast furnace 1 according to the embodiment of the present invention includes a furnace body 2 having a substantially cylindrical shape, a blast tuyere (hereinafter, abbreviated as tuyere) 3 provided below the furnace body 2, and a taphole 4 provided in the furnace body 2 below the tuyere 3. Further, a furnace bottom portion of the blast furnace 1 is constituted by a furnace bottom brick 5 and a furnace wall brick 6, and an inner wall surface and an outer wall surface of the furnace wall brick 6 are covered with a cooling sleeve 7 and an iron shell 8, respectively.
In addition, the blast furnace 1 according to the embodiment of the present invention includes a plurality of vibration meters 9, a data logger 10, and an information processing device 11 as the device for measuring the molten material level in the blast furnace. The vibration meters 9 are perpendicular to a tangent in the circumferential direction of the furnace body 2 and are set at equal intervals along a straight line along the surface of the iron shell 8 from the height position of the taphole 4 to the height position of the tuyere 3. Each vibration meter 9 measures a vibration value of the furnace body 2 as a current value, and outputs an electrical signal indicating the measured current value to the data logger 10.
The data logger 10 converts the current value measured by each vibration meter 9 into the vibration value based on the electrical signal output from each vibration meter 9. The information processing device 11 calculates the vibration intensity of the furnace body 2 at the installation position of each vibration meter 9 by performing Fourier transform on time-dependent data of the vibration value at the installation position (measurement position) of each vibration meter 9 generated by the data logger 10. Then, the information processing device 11 calculates the molten material level in the blast furnace by executing the method for measuring the molten material level in the blast furnace described below using the calculated vibration intensity.
As a result of measurement with an actual machine, it has been confirmed that the vibration of the furnace body 2 has all vibration frequency bands, and the vibration having a particularly high peak value and a peak confirmed at all the measurement positions is in the frequency band of 700 to 900 Hz. Since it was confirmed that there is a rough tendency that the vibration in the frequency band of 700 to 900 Hz shows a high value at a position close to the tuyere 3, it is considered that the vibration is caused by a blast 23 from the tuyere 3 (vibration due to blast). Therefore, in the present invention, the molten material level is measured using the vibration intensity confirmed in the frequency range of 700 to 900 Hz corresponding to the vibration due to blast. Note that there is a possibility that the frequency band in which the vibration due to blast is confirmed varies depending on the shape of the furnace body 2, the ground influence, and the like, and there is no proof that the evaluation can be performed in every blast furnace with this frequency band. Therefore, when the present invention is developed for another blast furnace, it is desirable that basic analysis for the vibration frequency band is performed each time.
In the blast furnace 1 illustrated in FIG. 1, an iron ore 21 and a coke 22, which are raw materials, are charged in layers into the furnace body 2 from the top of the furnace, and are reduced by the blast (hot air) 23 pressure-fed from the tuyere 3 to become a molten material 24. Then, the molten material 24 is stored in the furnace bottom portion, and is discharged from the taphole 4 as the tapped molten iron slag 25 by boring the taphole 4 every predetermined time. The device for measuring the molten material level in the blast furnace according to the embodiment of the present invention measures a liquid surface level of the molten material 24 in the lower part of the furnace as the molten material level.

[Measurement Method]

Next, the method for measuring the molten material level in the blast furnace according to the embodiment of the present invention will be described with reference to FIGS. 2 to 5.
In the method for measuring the molten material level in the blast furnace according to the embodiment of the present invention, first, the information processing device 11 measures the vibration intensity in the height direction perpendicular to the tangent in the circumferential direction of the furnace body 2 and executes the numerical analysis model for the vibration to estimate the maximum vibration intensity distribution of the furnace body 2. The molten material level and the blast amount are required as input information of the numerical analysis model for the vibration. In the present embodiment, the former is treated as a variable for fitting actually measured data of vibration intensity distribution to a numerical analysis result, and as the latter, operational data of the blast furnace is sequentially imported. As a result, the molten material level can be obtained by fitting the actually measured data of the vibration intensity distribution to the numerical analysis result.
The numerical analysis model for the vibration will be described. The numerical analysis model for the vibration is a physical model for estimating the maximum vibration intensity distribution of the lower part of the furnace including an iron shell region and a packed bed region. FIG. 2 illustrates a calculation flow of the numerical analysis model for the vibration. As illustrated in FIG. 2, in the case where the numerical analysis model for the vibration is executed, first, a mesh condition necessary for setting the computational grid, an analysis time step, and a density and Young's modulus as the physical properties of the iron shell and the packed bed are set. In addition, the blast amount to the blast furnace 1 considered as a vibration source is input as an operating parameter (Step S1).
Next, as illustrated in FIG. 3, the information processing device 11 sets a computational grid by dividing a two-dimensional region 31 into a plurality of element regions 32. The two-dimensional region 31 is axial symmetry on a cross section in the lower part of the furnace of the blast furnace 1 including the iron shell and the packed bed, the cross section including one of the central axis of the furnace body 2 and the tuyeres 3 installed at a plurality of locations in the circumferential direction of the furnace body 2 and being perpendicular to the furnace bottom portion (step S2). In the present model, the element regions 32 are connected by a spring 33 and the dashpot 34, and the acceleration applied to a certain element region 32 is propagated to the peripheral element region 32 through the spring 33 and the dashpot 34. The spring 33 represents a restoring force describing a vibration phenomenon, and the dashpot 34 represents a damping force by which vibration energy is lost by various energy conversions in the process of propagation of vibration. In addition, in the present model, in consideration of the liquid surface (molten material level) L of the molten material, for the element region 32 having a center of gravity equal to or lower than the liquid surface L, a buoyancy force and a resistance force by the molten material are given to the movement of the element region 32.
Returning to FIG. 2, next, the information processing device 11 calculates a spring constant k of each element region 32 using Formula (1) shown below (Step S3). In Formula (1), E is the Young's modulus, A is the cross-sectional area of the element region 32 in the direction perpendicular to the spring 33, and L is the length of the element region 32 in the same direction as the spring 33. In the present embodiment, since the numerical analysis model is a two-dimensional analysis model, A is the square of the length of the element region 32 perpendicular to the spring 33. In addition, the spring constant k as the material property of each element region 32 is obtained, and an average value of the spring constants k of the two element regions 32 to be coupled is given as the spring constant of the spring 33 coupling the element regions 32.
[Formula 1] $k = EA / L$
Next, the information processing device 11 calculates a viscosity coefficient c of each element region 32 using Formula (2) shown below (Step S4). In Formula (2), m represents the mass of each element region 32. The volume of each element region 32 is given as a product of A and L. In addition, since the viscosity coefficient c is obtained as the material property of each element region 32, an average value of the viscosity coefficients c of the two element regions 32 to be coupled is given as the viscosity coefficient of the dashpot 34 coupling the element regions 32.
[Formula 2] $c = 2 \sqrt{mk}$
Next, using the processing results of Steps S2 and S3, the information processing device 11 formulates a vibration equation based on the vibration engineering theory for each element region 32 as in Formula (3) shown below (Step S5). In Formula (3), x represents displacement of each element region 32, t represents time, C_d represents a liquid resistance force, and F represents a buoyancy force and a blast external force. In addition, as illustrated in FIG. 3, the position in the radial direction of the two-dimensional region 31 is represented by a subscript I, and the position in the height direction is represented by a subscript J.
Formula (3) shown above is based on the Newton's equation of motion, and the inertia force of each element region 32 is taken into consideration on the left side, and the restoring force, the damping force, the liquid resistance force, the buoyancy force, and the blast external force acting on each element region 32 are taken into consideration on the right side. In addition, the formula is established on the assumption that the restoring force is proportional to the magnitude of displacement of each element region 32, and the damping force is proportional to the speed of each element region 32. In addition, the liquid resistance force C_d was calculated from Kozeny-Carman equation, and the blast external force was calculated as a product of the pressure loss in front of the tuyere calculated by the Ergun equation and the surface area of a raceway calculated from the depth estimation equation of the raceway.
It is known that the general solution of the differential equation of Formula (3) shown above is expressed by Formula (4) shown below. a represents a maximum acceleration of each element region 32, i represents an imaginary unit, and ω represents a vibration frequency.
Therefore, when the Formula (4) is substituted into Formula (3) and the formula is simplified for the maximum acceleration a, Formula (5) shown below is obtained.
Formula (5) shown above is an expression relating to the maximum acceleration of the element region 32 represented by the coordinates (I, J) of interest and the four element regions 32 around that element region 32. When Formula (5) is established for all the element regions 32, a simultaneous equation for the maximum acceleration a of all the element regions 32 is obtained. By solving this by the BiCG-Stab method, the maximum acceleration a of each element region 32 can be calculated. Therefore, the information processing device 11 calculates the maximum acceleration a of each element region 32, and calculates the maximum vibration intensity distribution of the furnace body 2 by substituting the calculated maximum acceleration a into Formula (4) (Step S6). Then, the information processing device 11 repeatedly executes the present processing until the maximum vibration intensity distribution of the furnace body 2 reaches a steady state (Step S7). In the present embodiment, 800 Hz, which is an average value of the actually measured vibration frequency of 700 to 900 Hz due to blast, is set as the vibration frequency ω.
As described above, the maximum vibration intensity distribution of the lower part of the furnace including the iron shell and the packed bed as components can be estimated based on the vibration engineering theory, but the molten material level remains as an unknown parameter. Since the range in which the liquid resistance force and the buoyancy force act in Formula (3) changes depending on the setting of the molten material level, the molten material level also affects the calculation result of the maximum vibration intensity distribution. Therefore, next, the information processing device 11 determines the molten material level as a variable so as to minimize a deviation of the maximum vibration intensity distribution estimated by the numerical analysis model from distribution of a plurality of vibration intensities measured in the height direction of the furnace body 2 when the molten material level is used. This makes it possible to accurately measure the molten material level in the blast furnace regardless of operation conditions of the blast furnace. In addition, by detecting an increase in the molten material level at an early stage and preventing an increase in reducing agent ratio caused by an increase in ventilation resistance due to an increase in the molten material level, it is possible to stably perform eco-friendly blast furnace operation.
In FIG. 4 , an analysis example of a two-dimensional vibration model is illustrated. As illustrated in FIG. 4 , it is possible to confirm a state in which blast vibration generated in a raceway space in which the coke is restrained and swirled by the blast pressure while vigorously burning in front of the tuyeres 3 gradually dissipates energy and is damped while being propagated to the periphery. In addition, in the analysis example illustrated in FIG. 4, the analysis has been performed on the assumption that the molten material surface exists in a region of 2/3 of the distance from the furnace bottom to the tuyeres 3, and it has been possible to confirm a state in which the vibration intensity is discontinuously damped at the interface. On the other hand, FIG. 5 illustrates a result of plotting vibration intensities due to blast with respect to the height of the measurement position of the vibration meter 9 relative to the molten material level (height of the vibration meter with respect to the liquid surface), the vibration intensities being measured by the plurality of vibration meters 9 when the molten material level is changed by using a cold model in which the lower part of the blast furnace 1 is simulated. As illustrated in FIG. 5, the vibration intensity due to blast changed discontinuously in the surface layer of the molten material, and the result has qualitatively coincided with the prediction result of the numerical analysis model illustrated in FIG. 4. In addition, this experiment included results obtained in a plurality of cases where simulation is performed in consideration of factors that can fluctuate in an actual blast furnace, such as physical properties of the molten material, a blast amount, a packed particle diameter, and particle size distribution of the packed particles, but none of the cases reversed the tendency illustrated in FIG. 5. Furthermore, also in an experiment in which simulation was performed in consideration of factors of vibration fluctuation that are assumed to occur due to disturbance, such as vibration at the time of raw material charging, a change in the total weight of the furnace packing material due to a change in the reducing agent ratio of the blast furnace, a structural change due to aging due to wear of the furnace bottom brick, and an installation situation of the furnace body, the tendency illustrated in FIG. 5 has been similarly confirmed. From the above, it is considered that the discontinuous variation in the vibration intensity on the surface of the molten material confirmed in FIG. 5 is an event that is uniformly confirmed under all operational conditions.

[Examples]

In this example, in a large blast furnace having a capacity of about 5000 m³, pulverized coal was blown from a tuyere using an ordinary charged raw material, vibration of the furnace body was measured using vibration meters installed at equal intervals on a line perpendicular to a tangent in a circumferential direction of the furnace body from a taphole level (height position 2 m) to a tuyere level, and a molten material level in the blast furnace was measured. Table 1 illustrates operation conditions of Example 1 and Example 2. A time-dependent change of a measurement value of the molten material level from an initial stage to an end stage of tapping is illustrated in FIG. 6. In addition, a result of fitting the vibration intensity measured by an actual machine to the maximum vibration intensity estimated using the numerical analysis model for each molten material level is illustrated in FIG. 7. As illustrated in FIG. 6, in both Examples 1 and 2, the molten material level is finally about the same as the taphole level. From this, according to the present invention, it was confirmed that the molten material level can be measured with high accuracy. In addition, as illustrated in FIG. 7(a), at the initial stage of the tapping, the difference between the actual value and the estimated value was minimized by setting the molten material level to about 4.0 m. In addition, as illustrated in FIG. 7(b), at the end stage of the tapping, the difference between the actual value and the estimated value was minimized by setting the residual molten iron slag level to about 2.0 m.

[Table 1]

Table 1

	Example 1	Example 2
Coke ratio (kg/t)	345	330
Pulverized coal ratio (kg/t)	220	235
Reducing agent ratio (kg/t)	565	565
Tapped molten iron amount (t/d)	9698	9712
Tapped molten iron temperature (°C)	1524	1526

Although the embodiments to which the invention made by the present inventors is applied have 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 embodiments. 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

According to the present invention, it is possible to provide a method and a device for measuring a molten material level in a blast furnace capable of accurately measuring the molten material level in the blast furnace regardless of operation conditions of the blast furnace. In addition, according to the present invention, it is possible to provide a blast furnace operation method in which eco-friendly blast furnace operation can be performed stably.

Reference Signs List

1: BLAST FURNACE
2: FURNACE BODY
3: BLAST TUYERE, TUYERE
4: TAPHOLE
5: FURNACE BOTTOM BRICK
6: FURNACE WALL BRICK
7: COOLING SLEEVE
8: IRON SHELL
9: VIBRATION METER
10: DATA LOGGER
11: INFORMATION PROCESSING DEVICE
21: IRON ORE
22: COKE
23: BLAST
24: MOLTEN MATERIAL
25: TAPPED MOLTEN IRON SLAG
31: TWO-DIMENSIONAL REGION
32: ELEMENT REGION
33: SPRING
34: DASHPOT

Claims

A method for measuring a molten material level in a blast furnace, the method comprising:
a measurement step of measuring a vibration frequency distribution in a height direction of a furnace body of the blast furnace by using a plurality of vibration meters arranged at predetermined intervals along the height direction of the furnace body;

a vibration intensity calculation step of calculating a vibration intensity in a frequency range due to blast at each of measurement positions by performing Fourier transform on the vibration frequency distribution;

a numerical analysis step of calculating a maximum vibration intensity distribution of a lower part of the blast furnace by using a numerical analysis model in which the molten material level and a blast amount in the blast furnace are set as variables; and

a molten material level calculation step of calculating the molten material level at which a difference between the vibration intensity calculated in the vibration intensity calculation step and the maximum vibration intensity distribution calculated in the numerical analysis step is minimized, and determining the calculated molten material level as a position of the molten material level in the blast furnace.
The method for measuring the molten material level in the blast furnace according to claim 1, wherein the vibration meter is installed between a taphole level and a tuyere level of the furnace body.
The method for measuring the molten material level in the blast furnace according to claim 1 or 2, wherein the frequency range due to the blast is in a range of 700 to 900 Hz.
A device for measuring a molten material level in a blast furnace, the device comprising:
a plurality of vibration meters arranged at predetermined intervals along a height direction of a furnace body of the blast furnace and configured to measure a vibration frequency distribution in the height direction of the furnace body; and

an information processing device configured to
calculate a vibration intensity in a frequency range due to blast at each of measurement positions by performing Fourier transform on the vibration frequency distribution,

calculate a maximum vibration intensity distribution in a lower part of the blast furnace using a numerical analysis model in which the molten material level and a blast amount in the blast furnace are set as variables,

calculate the molten material level at which a difference between the vibration intensity and the maximum vibration intensity distribution is minimized, and

determine the calculated molten material level as a position of the molten material level in the blast furnace.
A blast furnace operation method comprising
a step of operating a blast furnace according to a molten material level measured by using the method for measuring the molten material level in the blast furnace according to claim 1 or 2.