Field
[0001] The present invention relates to a nitrogen concentration prediction method, a nitrogen
concentration control method, a nitrogen concentration prediction apparatus, and a
nitrogen concentration control apparatus. Background
[0002] In general, molten steel processed in a converter or the like is conveyed to a secondary
refining step, and the nitrogen concentration thereof is controlled by vacuum degassing
process. Appropriate control of the nitrogen concentration in the molten steel contributes
to enhance functionality of the steel product, so that the control needs to be as
accurate as possible. Against the background, a lot of techniques for controlling
the nitrogen concentration in the molten steel in the vacuum degassing process have
been proposed. More specifically, Patent Literature 1 describes a method in which,
in the first half of the vacuum degassing process, the process is conducted so as
to control hydrogen concentration and oxygen concentration to predetermined levels
or below, during which the nitrogen concentration in the molten steel is analyzed,
then in the second half of the vacuum degassing process, process conditions are determined
according to an analysis value of the nitrogen concentration. According to the method
described in Patent Literature 1, the nitrogen concentration in the molten steel is
predicted in consideration of nitriding and denitriding reactions at the surface of
a molten steel bath in a vacuum chamber and at a bubble interface, nitriding reaction
due to incoming atmospheric air through a dip tube, and mixing of the molten steel
under circulation.
Citation List
Patent Literature
Non Patent Literature
[0004]
Non Patent Literature 1: T. Kuwabara, K. Umezawa, K. Mori, and H. Watanabe: Trans. Iron Steel Inst. Jpn., 28(1988),
305
Non Patent Literature 2: Recommended Equilibrium Values for Steelmaking Reaction, edited by 19th Committee
of Japan Society for the Promotion of Science, revised and enlarged: 1984
Non Patent Literature 3: T. Kitamura, K. Miyamoto, R. Tsujino, S. Mizoguchi, and K. Kato: ISIJ International,
36(1996), 395
Non Patent Literature 4: K. Harashima, S. Mizoguchi, H. Kajioka, and M. Sakakura: Tetsu-to-Hagane, 73(1987),
1559
Summary
Technical Problem
[0005] According to the method described in Patent Literature 1, the nitrogen concentration
in the molten steel is predicted without considering influences of differences in
the component and temperature for each molten steel to be processed, influences of
auxiliary material to be added to the molten steel on the components of the molten
steel or the vacuum degassing process, and influences of disturbance in process steps
other than the vacuum degassing process, the conveyance step, and the like. Therefore,
in the method described in Patent Literature 1, changes in the rate of change of nitrogen
concentration due to the aforementioned influences will increase a prediction error
of the nitrogen concentration, and this would make it difficult to accurately control
the nitrogen concentration in the molten steel.
[0006] The present invention has been made in view of the above problem, and an object thereof
is to provide a nitrogen concentration prediction method and a nitrogen concentration
prediction apparatus, capable of accurately predicting the nitrogen concentration
in the molten steel during the vacuum degassing process. Another object of the present
invention is to provide a nitrogen concentration control method and a nitrogen concentration
control apparatus, capable of accurately controlling the nitrogen concentration in
the molten steel during the vacuum degassing process.
Solution to Problem
[0007] A nitrogen concentration prediction method for predicting a nitrogen concentration
in molten steel in a vacuum degassing process, includes: a prediction step of calculating
a predicted value of the nitrogen concentration in the molten steel under an operating
condition to be predicted, by using a nitrogen concentration prediction model that
is a physical model that uses, as an input variable, a condition of the vacuum degassing
process, and uses, as an output variable, a predicted value of the nitrogen concentration
in the molten steel under the condition; and a correction step of correcting the predicted
value of the nitrogen concentration in the molten steel calculated in the prediction
step, by using a machine learning correction model that is a machine learning model
that uses, as an explanatory variable, the condition of the vacuum degassing process,
and uses, as a target variable, a prediction error which is a difference value between
the predicted value of the nitrogen concentration in the molten steel calculated under
the condition with use of the nitrogen concentration prediction model, and an actual
value.
[0008] The explanatory variable preferably includes a number of times of use of a facility
of the vacuum degassing apparatus.
[0009] The correction step is preferably conducted, upon acquisition of the actual value
of the nitrogen concentration in the molten steel.
[0010] A nitrogen concentration control method according to the present invention includes
a step of controlling a condition of the vacuum degassing process according to the
nitrogen concentration in the molten steel predicted by the nitrogen concentration
prediction method according to the present invention.
[0011] The nitrogen concentration prediction method is preferably applied to a vacuum degassing
process in which a flow rate of circulation gas per ton of the molten steel is in
a range of 4 to 20 NL/min·ton, and a degree of vacuum in a vacuum chamber is 12/76
(atm) or less.
[0012] The nitrogen concentration prediction method is preferably applied to a vacuum degassing
process in which a target value of the nitrogen concentration in the molten steel
is in a range of 30 to 100 ppm.
[0013] A nitrogen concentration prediction apparatus for predicting a nitrogen concentration
in molten steel in a vacuum degassing process, includes: a prediction means for calculating
a predicted value of the nitrogen concentration in the molten steel under an operating
condition to be predicted, by using a nitrogen concentration prediction model that
is a physical model that uses, as an input variable, a condition of the vacuum degassing
process, and uses, as an output variable, a predicted value of the nitrogen concentration
in the molten steel under the condition; and a correction means for correcting the
predicted value of the nitrogen concentration in the molten steel calculated by the
prediction means, by using a machine learning correction model that is a machine learning
model that uses, as an explanatory variable, the condition of the vacuum degassing
process, and uses, as a target variable, a prediction error which is a difference
value between the predicted value of the nitrogen concentration in the molten steel
calculated under the condition with use of the nitrogen concentration prediction model,
and an actual value.
[0014] A nitrogen concentration control apparatus includes a control means for controlling
a condition of a vacuum degassing process, according to the nitrogen concentration
in the molten steel predicted by the nitrogen concentration prediction apparatus according
to the present invention.
Advantageous Effects of Invention
[0015] According to the nitrogen concentration prediction method and the nitrogen concentration
prediction apparatus of the present invention, the nitrogen concentration in the molten
steel during the vacuum degassing process can be accurately predicted. According to
the nitrogen concentration control method and the nitrogen concentration control apparatus
of the present invention, the nitrogen concentration in the molten steel during the
vacuum degassing process can be accurately controlled.
Brief Description of Drawings
[0016]
[FIG. 1] FIG. 1 is a schematic diagram illustrating a structure of a vacuum degassing
apparatus according to an embodiment of the present invention.
[FIG. 2] FIG. 2 is a diagram illustrating a prediction image of a nitrogen concentration,
based on combination of a nitrogen concentration prediction model and a machine learning
correction model.
[FIG. 3] FIG. 3 is a flowchart illustrating a flow of a nitrogen concentration prediction
process according to an embodiment of the present invention.
Description of Embodiments
[0017] Hereinafter, a nitrogen concentration prediction method, a nitrogen concentration
control method, a nitrogen concentration prediction apparatus, and a nitrogen concentration
control apparatus according to an embodiment of the present invention will be described
in detail with reference to the drawings.
[Vacuum Degassing Apparatus]
[0018] First, a structure of a vacuum degassing apparatus according to an embodiment of
the present invention will be described with reference to FIG. 1.
[0019] FIG. 1 is a schematic diagram illustrating a structure of a vacuum degassing apparatus
according to an embodiment of the present invention. As illustrated in FIG. 1, a vacuum
degassing apparatus 1 according to an embodiment of the present invention has a ladle
2 in which molten steel S is accommodated, and a vacuum chamber 3 capable of controlling
the inside to a vacuum state. To a lower portion of the vacuum chamber 3, two dip
tubes 4 that communicate with the inside of the vacuum chamber 3 are provided, and
in one of the dip tubes 4, a blow-in port 5 through which a circulation gas G is blown
into the vacuum chamber 3 is formed. In the upper portion of the vacuum chamber 3,
there is formed an exhaust port 6 through which a gas generated by the vacuum degassing
process is discharged to the outside.
[0020] When conducting the vacuum degassing process with use of such a vacuum degassing
apparatus, first, the lower ends of the two dip tubes 4 are immersed in the molten
steel S accommodated in the ladle 2. Next, the inside of the vacuum chamber 3 is evacuated
while blowing therein the circulation gas G such as argon gas or nitrogen gas through
the blow-in port 5, thereby circulating the molten steel S between the ladle 2 and
the vacuum chamber 3 for degassing process. Since the molten steel S herein in the
vacuum chamber 3 is exposed to a reduced pressure atmosphere, a degassing reaction
vigorously proceeds, whereby mainly decarburization process, denitriding process,
dehydrogenation process, and the like are allowed to proceed. The gas generated by
the degassing reaction is discharged through the exhaust port 6 to the outside. Also
the components of the molten steel S are adjusted, by concurrently charging alloy,
auxiliary material, and the like into the molten steel S.
[0021] When the nitrogen concentration in the molten steel S needs to be controlled, the
nitrogen concentration in the molten steel S is controlled by changing operating conditions
such as switching of species of the circulation gas G, adjustment of flow rate of
circulation gas G, and adjustment of the degree of vacuum in the vacuum chamber 3.
For example, use of nitrogen gas as the circulation gas G will increase the rate of
nitriding. Meanwhile, by increasing the degree of vacuum in the vacuum chamber 3 to
further lower the pressure in the vacuum chamber 3, the rate of denitriding in the
vacuum chamber 3 will be increased. The nitrogen concentration in the molten steel
S is controllable by such operations.
[0022] This sort of control of the operating conditions of the vacuum degassing apparatus
1 is implemented by a control apparatus 10 constituted by an information processor
such as a computer. The control apparatus 10 controls the operating conditions of
the vacuum degassing apparatus 1, according to information that indicates an operating
state of the vacuum degassing apparatus 1 acquired from a sensor or the like attached
to the vacuum degassing apparatus 1. In addition in the present embodiment, the control
apparatus 10 functions as a nitrogen concentration prediction unit 11 and a correction
unit 12, as a result of execution of a computer program by an arithmetic processing
unit in the information processor. The nitrogen concentration prediction unit 11 uses
the nitrogen concentration prediction model to predict the nitrogen concentration
in the molten steel S, and controls the operating conditions of the vacuum degassing
apparatus 1 according to the thus predicted nitrogen concentration, thereby controlling
the nitrogen concentration in the molten steel S. The nitrogen concentration prediction
model herein is a physical model that uses the operating condition of the vacuum degassing
apparatus 1 as an input variable, and uses the predicted value of the nitrogen concentration
in the molten steel S as an output variable. The correction unit 12 is structured
to correct, with use of the machine learning correction model, the predicted value
of the nitrogen concentration calculated by the nitrogen concentration prediction
unit 11. The machine learning correction model herein is a machine learning model
that uses, as an explanatory variable, the operating condition of the vacuum degassing
apparatus 1, and uses, as a target variable, a prediction error which is a difference
value between the predicted value of the nitrogen concentration calculated by the
nitrogen concentration prediction unit 11 with use of the operating condition, and
an actual value. The nitrogen concentration prediction model and the machine learning
correction model will be detailed later.
[Nitrogen Concentration Prediction Model]
[0023] Next, the nitrogen concentration prediction model will be described.
[0024] Rates of change d[N]
L/dt and d[N]
v/dt of the nitrogen concentration in the molten steel S, in the ladle 2 and in the
vacuum chamber 3, may be given by expressions (1) and (2) below, assuming complete
mixing of the molten steel S. In expressions (1) and (2), t represents time (sec),
[N]
V represents the nitrogen concentration (mass%) in the molten steel S in the vacuum
chamber 3, V
V represents the volume (m
3) of the molten steel S in the vacuum chamber 3, Q represents the circulation volume
(m
3/sec) of the molten steel S, [N]
L represents the nitrogen concentration (mass%) in the molten steel S in the ladle
2, and V
L represents the volume (m
3) of the molten steel S in the ladle 2.
[Mathematical formula 1]

[Mathematical formula 2]

[0025] In expression (1), each term on the right side represents, in the order from the
first term, mixing of the molten steel S between the vacuum chamber 3 and the ladle
2 under circulation, the rate of change of the nitrogen concentration on the surface
of the molten steel bath in the vacuum chamber 3, and the rate of change of the nitrogen
concentration in the circulation gas at the bubble interface. On the other hand, expression
(2) considers mixing of the molten steel S between the vacuum chamber 3 and the ladle
2 under circulation.
[0026] Note that the circulation volume Q of the molten steel S in expressions (1) and (2)
may be calculated, with use of expression (3) below, with reference to the description
of Non Patent Literature 1. In expression (3), Q
g represents the flow rate of circulation gas (NM
3/min), D represents the diameter of dip tube 4 (m), and P
V represents the pressure (atm) in the vacuum chamber 3.
[Mathematical formula 3]

[0027] In the present embodiment, the rate of change in the nitrogen concentration at each
of the reaction sites for the nitriding and denitriding reactions assumes mixed rate
limiting by mass transfer on the molten steel side and the chemical reaction at the
gas-liquid interface, as given by expression (4) below. With this, expression (4)
is rearranged to give expression (5) below, as an expression that describes the reaction
rate of nitrogen in the molten steel S in the vacuum chamber 3. The nitrogen concentration
prediction model therefore calculates a predicted value of the nitrogen concentration
in the molten steel S, upon entry of necessary numerical values into expression (5)
below. In expressions (4) and (5), A represents a gas-liquid reaction interfacial
area (m
2), k
m represents a mass transfer coefficient of nitrogen on the molten steel side (m/sec),
k
r represents a rate constant of chemical reaction of nitrogen (m/sec·mass%), [N]
i represents the nitrogen concentration on the molten steel side of the gas-liquid
interface (mass%), and [N]
eq represents the nitrogen concentration in the molten steel under equilibrium with
nitrogen gas in the gas phase (equilibrium nitrogen concentration) (mass%).
[Mathematical formula 4]

[Mathematical formula 5]

[0028] The reaction sites where the rate of change of the nitrogen concentration is calculated
with use of expression (5) include the surface of the molten steel bath in the vacuum
chamber 3, and the bubble interface, wherein the difference lies in gas-liquid reaction
interfacial area A and equilibrium nitrogen concentration [N]
eq. Among these, the equilibrium nitrogen concentration [N]
eq may be calculated, with use of expression (6) below, with reference to the description
of Non Patent Literature 2. In expression (6), f
N represents an activity coefficient of nitrogen, P
N2 represents a partial pressure of nitrogen, R represents the gas constant (J/K·mol),
and T represents a temperature (K) of the molten steel S.
[Mathematical formula 6]

[0029] The activity coefficient f
N of nitrogen in expression (6) is calculated, while considering influences of C, Si,
Mn, and O as the main components. More specifically, the activity coefficient f
N of nitrogen is calculated by expression (7) below, with use of the values listed
in Table 1 below, as the first-order interaction coefficients between each of these
components and nitrogen described in Non Patent Literature 2. In expression (7), e
Nj represents the first-order interaction coefficient (j = C, Si, Mn, O) with nitrogen.
Note that the components listed above are examples, and it is obvious that the components
to be considered will actually increase or decrease depending on the component system
of the steel species to be processed.
[Table 1]
[0030]
(Table 1)
| |
j |
| C |
Si |
Mn |
O |
| N |
0.13 |
0.048 |
-0.02 |
-0.02 |
[Mathematical formula 7]

[0031] On the other hand, the mass transfer coefficient k
m of nitrogen on the molten steel side in expression (5) may be calculated, with use
of expressions (8) to (12) below, with reference to the description of Non Patent
Literature 3. In expressions (8) to (12), the mass transfer coefficient k
m of nitrogen on the molten steel side is determined, in consideration of the time
for replacement of the molten steel S around the bubble. In expressions (8) to (12),
θ represents a contact time (min) of the molten steel S with the bubble, D
N represents a diffusion coefficient (m
2/min) of nitrogen, d
B represents the diameter of blown bubble (m), U
B represents a rising speed of bubble (m/min), U
L represents a rising speed of molten steel (m/min), g represents the gravitational
acceleration (
m/s2), and L represents a height of the bath surface (m) in the vacuum chamber 3 above
a position where the circulation gas is blown.
[Mathematical formula 8]

[Mathematical formula 9]

[Mathematical formula 10]

[Mathematical formula 11]

[Mathematical formula 12]

[0032] Meanwhile, the rate constant k
r of chemical reaction of nitrogen in expression (5) may be calculated, with use of
expression (13) below, with reference to the description of Non Patent Literature
4. In expression (13), [O] represents oxygen concentration (mass%) in the molten steel
S, and [S] represents sulfur concentration (mass%) in the molten steel S.
[Mathematical formula 13]

[0033] When considering the reaction rate on the surface of the molten steel bath and the
reaction rate at the bubble interface, with respect to the gas-liquid reaction interfacial
area A in expression (5), the molten steel bath surface area, and the bubble interfacial
area respectively serve as such gas-liquid reaction interfacial area. Assuming now
that the molten steel bath surface area is proportional to 2/3 of the circulation
volume Q, and that the bubble interfacial area is proportional to the 2/3 power of
the flow rate of circulation gas Q
g, these areas may be estimated by expressions (14) and (15) below. In expressions
(14) and (15), α
S and α
B represent respective proportional constants. Another conceivable method for estimating
the gas-liquid reaction interfacial area may be a calculation method in consideration
of physical behaviors of the bubble or the surface area of the molten steel bath,
with use of the flow rate of circulation gas, the circulation gas species, the degree
of vacuum, and the like.
[Mathematical formula 14]

[Mathematical formula 15]

[0034] On the other hand, the reaction that occurs at the nitrogen bubble interface upon
blowing of nitrogen gas will be either a nitriding reaction or a denitriding reaction,
depending on magnitude relation between the nitrogen concentration in the molten steel
S, and the nitrogen concentration under equilibrium with the nitrogen partial pressure
in the nitrogen bubble. In addition, the blown nitrogen bubble will rise up in the
molten steel, so that the nitrogen partial pressure in the nitrogen bubble will decrease
due to change in the static pressure exerted from the molten steel. Accordingly, the
rate of reaction and the direction of reaction of the rising nitrogen bubble will
not be constant. The nitrogen concentration prediction model therefore employs expression
(16) below, in which these matters are taken into consideration, to calculate the
rate of change of the nitrogen concentration at the nitrogen bubble interface. [N]e
q(x) in expression (16) represents an equilibrium nitrogen concentration (mass%) in
the nitrogen bubble at a rising distance x from the blowing position of the circulation
gas, and may be calculated with use of expression (6) described previously.
[Mathematical formula 16]

[Machine Learning Correction Model]
[0035] Next, the machine learning correction model will be described.
[0036] The reason why the machine learning model is used to correct the predicted value
of the nitrogen concentration is to consider a difference in operating conditions
and influence of disturbance, which are difficult to consider only by prediction with
a physical model which can degrade the prediction accuracy of the nitrogen concentration.
Review of the process results of the vacuum degassing process revealed that some of
the results gave different rates of change in the nitrogen concentration, even under
almost the same circulation gas pattern, the degree of vacuum, and nitrogen concentration.
That is, there is a case where the variation in the change rate of the nitrogen concentration
cannot be explained only by simple vacuum degassing process conditions. In such a
case, prediction calculation of the nitrogen concentration with use of the physical
model will degrade the prediction accuracy of the nitrogen concentration. A plurality
of causes of different denitriding behaviors under substantially the same process
conditions are conceivable. Several causes will be exemplified below.
[0037] The first cause relates to influence of the molten steel components. Although influences
of C, Si, P, Mn, O, and S are considered also in the aforementioned nitrogen concentration
prediction model, the model takes only direct influences on changes in the nitrogen
concentration into account, while leaving the changes in the temperature and the change
in the slag composition, due to difference in these components or the component change
during the vacuum degassing process unconsidered.
[0038] The second cause relates to influences of alloy or auxiliary material to be added.
Besides the change in the components of the molten steel due to the addition of the
alloy or the auxiliary material, expected occurrence includes entry of impurity component,
change in the molten steel temperature, influence on molten steel flow, and changes
in the degree of vacuum and the atmosphere during the addition, which would affect
the change rate of the nitrogen concentration on occasion.
[0039] The third cause relates to influences outside the vacuum degassing process. Process
state in a converter, which is a process that precedes the vacuum degassing process,
or the time or environment before the molten steel is conveyed to the vacuum degassing
apparatus would change the state of the molten steel at the start of the process.
There may be a case where the molten steel is not analyzed at the start of the vacuum
degassing process, and instead, analysis values of the molten steel immediately after
the output from the converter are used as initial conditions of the molten steel including
the nitrogen concentration, due to constraints of process time and steps. The case
is, however, susceptible to influences outside the vacuum degassing process.
[0040] The denitriding behavior seems to change due to such causes. It is, however, difficult
to evaluate how these causes affect the rate of denitriding, and it is also very difficult
to separate the influences of the plurality of causes. Moreover, besides the aforementioned
causes, there may even be any influence that is not easily conceived. As a matter
of course, it is not easy to formulate these influences and reflect them in the physical
model, to improve the prediction accuracy.
[0041] From intensive studies on measures against such problems, it was found effective
to use machine learning with operating conditions as the feature. The machine learning
can evaluate complicated influences ascribed to an entered feature at a time, without
needing a logic describing how they affect, and is therefore useful as a solution
to the aforementioned problem.
[0042] The machine learning model created in the present invention is a regression prediction
model, structured to predict a target variable from an explanatory variable called
feature. Creation of the machine learning model therefore needs to set the target
variable, and to select an appropriate feature. From examination, deviation of the
predicted value of the nitrogen concentration based on the physical model was considered
to be an effective target variable. For a prediction model of a physical quantity
with use of the machine learning, a fitting parameter in reaction formula is often
used as the target variable. This is applicable when it is found, from the result
of examination of the reaction, that any unknown parameter which cannot be derived
from existing numerical values is obviously present. In other words, this is applicable
in a case where how the feature used in the machine learning contributes to a physical
reaction has been understood to some extent. For the aforementioned problem, it is,
however, difficult to understand just how the influences are exerted, and also a number
of influential factors present there would mutually interfere. Such technique is therefore
not applicable.
[0043] Therefore for the present embodiment, an error between the prediction result by the
physical model and the actual value was used as the target variable, rather than using
the parameters in the physical model as the target variable. This makes it possible
to separate the target variable from the calculation of the physical model, and to
isolate the machine learning model from the prediction in consideration of the reaction
theory by the physical model, whereby the machine learning is also applicable to the
aforementioned problem. Also the method is widely applicable regardless of calculation
technique by the physical model, which is a secondary benefit of this method. What
is required as learning data for the machine learning is a calculation result of the
physical model, so that accuracy improvement by the machine learning is expectable
regardless of accuracy or theory of the physical model itself. This means that the
machine learning is easily introduced, and is applicable not only to the vacuum degassing
process but also to many processes.
[0044] Other advantages are exemplified by simplicity of accuracy verification, remodeling,
and the like, since the physical model and the machine learning model are almost independent.
In the method of determining the parameters in the physical model by the machine learning
model, one prediction result is output. If the accuracy is poor, it is however not
always easy to determine which of the physical model or the machine learning model
has the accuracy problem. According to the present method, the prediction result by
the physical model, and the correction result by the machine learning model that corrects
the predicted result are separately obtainable, making it easy to separately evaluate
the accuracy of the individual models. Also verification and remodeling for improving
the prediction accuracy of the individual models are easy.
[0045] For selection of the feature, variables that can affect the denitriding behavior,
from among the operating conditions, were examined, and a machine learning model was
actually created to evaluate contribution of each feature to the accuracy. Therefore,
molten steel component, circulation gas pattern, the degree of vacuum, amounts of
addition of alloy and auxiliary material, conveyance time from a previous process,
and the like, which are generally considered to be influential, were selected as the
feature. Other than these, the number of times of use of the facility, such as the
number of times of use of the ladle, the number of times of use of the dip tube, and
the number of times of use of the vacuum chamber, were found to be largely influential
to the accuracy. In the steel refining process, a thermodynamic examination into the
reaction is a main issue. On the other hand in the vacuum degassing process, physical
behavior of the molten steel, centered round the gas-liquid reaction interfacial area,
is important. Accordingly, the refractory would change the shape depending on the
number of times of use of the facility, whereby the flow of molten steel during the
vacuum degassing process would change, and this presumably affects the denitriding
behavior. For this reason, largeness of the influence of the number of times of use
of the facility is considered to be a unique point in the vacuum degassing processing,
and to be important information that greatly affects the prediction accuracy.
[0046] The importance of the aforementioned number of times of use of the facility, as the
feature, does not depend on the type of the target variable. That is, in most cases
where the machine learning is used for implementing the prediction and control related
to the denitriding reaction of the vacuum degassing process, selection of the number
of times of use of the facility as the feature is understood to be highly effective.
Note, however, that this examination is considered to be well applicable to a process
conducted with a flow rate of circulation gas per ton of the molten steel of 4 to
20 (NL/min·ton), in the range of degree of vacuum in the vacuum chamber <12/76 (atm).
From a simulation of the molten steel flow by numerical analysis, it was found that
the flow of the molten steel becomes anomalous outside the aforementioned ranges,
so that the influence of the difference in the shape of the refractory, depending
on the number of times of use of the facility, will not be effectively considered.
More specifically, if the flow rate of circulation gas is extremely small, or if the
degree of vacuum in the vacuum chamber is small, the amount of circulation molten
steel will be very small. If the flow rate of circulation gas is extremely large,
agitation by the bubble will be large, and also the disturbance of the surface of
the molten steel bath will become large. In these cases, the influence of the refractory
at a location different from the refractory portion that affects the molten steel
in the normal process would become large, and this would make it unable to understand
the influence simply by the number of times of use of the facility. Therefore, the
accuracy of machine learning will degrade outside the aforementioned ranges. It is,
however, considered highly probable that the method of the present invention is effective
to improve the control accuracy even outside the aforementioned ranges of numerical
conditions, by modifying the physical model or optimizing the machine learning model,
assuming such ranges of process conditions.
[0047] An algorithm used for the machine learning is not particularly limited, for which
an appropriate algorithm is selected according to the situation of facility that differs
for each facility, and characteristics of the number of pieces of learning data. In
the embodiment of the present invention, a model was created with use of gradient
boosting based on a decision tree algorithm. It has, however, been confirmed that
comparable accuracy is also obtainable by many algorithms such as random forest and
neural network.
[0048] Next, a method of correcting the nitrogen concentration by the machine learning correction
model will be described. In the present embodiment, what is used as the target variable
by the machine learning correction model is an error [N]
Error (mass%) between the predicted value by the nitrogen concentration prediction model,
and an actual value, given by expression (17) below. In expression (17), [N]
Result represents the actual value (mass%) of the nitrogen concentration, and [N]
Phys-Calc represents a predicted value (mass%) of the nitrogen concentration with use of the
nitrogen concentration prediction model.
[Mathematical formula 17]

[0049] The machine learning correction model that uses the error [N]
Error as the target variable may be interpreted as being able to predict how the predicted
value by the nitrogen concentration prediction model deviates under a given operating
condition. Therefore as given by expression (18) below, the predicted value by the
nitrogen concentration prediction model may be corrected to a value closer to the
actual value, by using this predicted error. In expression (18), [N]
Prediction represents a final predicted value (mass%) of the nitrogen concentration, and [N]
prediction Error represents a prediction error (mass%) obtained from the machine learning correction
model.
[Mathematical formula 18]

[0050] A prediction image of the nitrogen concentration, based on combination of the nitrogen
concentration prediction model and the machine learning correction model, is illustrated
in FIG. 2. As illustrated in FIG. 2, the prediction by the nitrogen concentration
prediction model progresses from a process start point, during which the correction
takes place at process times (10 minutes, 20 minutes, and 30 minutes, in this example)
where the correction by the machine learning correction model is applicable. The prediction
by the nitrogen concentration prediction model proceeds again from the predicted value
of the nitrogen concentration thus corrected. Such flow is repeated also thereafter,
to predict the nitrogen concentration at the end of process. A necessary condition,
under which the machine learning correction model is applicable, is that past actual
values capable of serving as the learning data are available at a certain process
time. The correction in this case can take place only at the process time when the
analysis has taken place and the actual values of the nitrogen concentration have
been accumulated. For example in a process case where the actual value data has been
acquired by sampling at the process times of 10 minutes and 20 minutes, and at the
end of process, the predicted values by the nitrogen concentration prediction model
at these process times are correctable.
[0051] The higher the frequency of the correction by machine learning, the more the prediction
accuracy tends to improve. The machine learning correction is substantially enabled
at the time of intermediate analysis, so that a process pattern having a higher frequency
of intermediate analysis will be more expectable for improvement in the control accuracy
by the present invention. More specifically, higher control accuracy is expectable
for a process in which the machine learning correction takes place once or more times
per the process time of 15 minutes, or in which the machine learning takes place at
least once or more, within a period between the scheduled process end time and a point
in time 15 minutes before it. The value of 15 minutes was found out, while balancing
the accuracy of the nitrogen concentration prediction model, the charge frequency
of alloy and auxiliary material, the time required for melting and homogenization
of alloy and auxiliary material, the frequency of sample collection, the time required
for analysis, and the like.
[0052] When creating the machine learning correction model, the learning data volume is
preferably as large as possible. Therefore, for a case where a large volume of past
records of the nitrogen concentration control directed to similar steel species are
available, application of the present invention will give a distinct improvement in
the prediction accuracy. In many of the steel species in need of the nitrogen concentration
control to which the present invention is applied, the target nitrogen concentration
falls in the range of 30 to 100 ppm. Improvement in the prediction accuracy was confirmed
particularly in this range. In a case where a target nitrogen concentration of less
than 30 ppm is aimed at, the denitriding process will take place over a long duration
of time, although it depends on the nitrogen concentration value before the process.
Conversely, in a case where the target nitrogen concentration is larger than 100 ppm,
the nitriding process often takes place over a long duration of time.
[0053] In such a case, the nitrogen concentration control is different in nature from nitrogen
concentration control in which the nitriding process and the denitriding process are
switched, aiming at the control within a range between the upper and lower limits
on both sides of the target nitrogen concentration value, which is the main object
of the present invention. In addition, the obtainable actual data will lack diversity
of data, while being biased either towards the nitriding or denitriding process. Incorporation
of such extreme data into the learning data group would degrade the prediction accuracy.
Therefore, application to the steel species having the target nitrogen concentration
in the range from 30 to 100 ppm is preferred, in order to keep the prediction accuracy
at a high level. Note, the prediction per se is possible at higher accuracy than in
the prior art, even for the steel species out of the aforementioned range. In addition,
it is probable enough that a method, based on switching of the nitrogen concentration
prediction model and the machine learning correction model for each target nitrogen
concentration, is used to improve the prediction accuracy in different target nitrogen
concentration ranges.
[Nitrogen Concentration Prediction Process]
[0054] Lastly, a flow of the nitrogen concentration prediction process according to one
embodiment of the present invention will be described, with reference to FIG. 3.
[0055] FIG. 3 is a flowchart illustrating a flow of a nitrogen concentration prediction
process according to an embodiment of the present invention. The flowchart illustrated
in FIG. 3 starts at the time (step S1) the initial conditions are entered to the control
apparatus 10, and an execution command of the nitrogen concentration prediction process
is entered to the control apparatus 10. The nitrogen concentration prediction process
then advances to a process of step S2. Examples of the initial conditions entered
to the control apparatus 10 include the amount of molten steel, initial composition
of the molten steel, and conditions of the vacuum degassing process (degree of vacuum,
flow rate of circulation gas, circulation gas species, etc.).
[0056] In the process of step S2, the control apparatus 10 determines parameters used for
calculating the molten steel-side mass transfer coefficient of nitrogen, the chemical
reaction rate constant, the activity coefficient, and the like in the reaction formula
contained in the nitrogen concentration prediction model, the circulation volume,
and the reaction interfacial area. Upon this, the process of step S2 is completed,
and the nitrogen concentration prediction process then advances to processes of steps
S3 and S4.
[0057] In the process of step S3, the control apparatus 10 calculates the rate of change
of the nitrogen concentration at the bubble interface, with use of the nitrogen concentration
prediction model. Upon this, the process of step S3 is completed, and the nitrogen
concentration prediction process then advances to a process of step S5.
[0058] In the process of step S4, the control apparatus 10 calculates the rate of change
of the nitrogen concentration at the surface of the molten steel bath in the vacuum
chamber, with use of the nitrogen concentration prediction model. Upon this, the process
of step S4 is completed, and the nitrogen concentration prediction process then advances
to a process of step S5.
[0059] In the process of step S5, the control apparatus 10 calculates the amounts of change
Δ[N] of the nitrogen concentrations in the vacuum chamber and in the molten steel
in the ladle, with use of the rate of change of the nitrogen concentration at the
bubble interface calculated by the process of step S3, and the rate of change of the
nitrogen concentration on the surface of the molten steel bath in the vacuum chamber
calculated by the process of step S4. Upon this, the process of step S5 is completed,
and the nitrogen concentration prediction process then advances to a process of step
S6.
[0060] In the process of step S6, the control apparatus 10 calculates the nitrogen concentrations
[N]
V, [N]
L of the molten steel in the vacuum chamber and in the ladle, with use of the amounts
of change Δ[N] of the nitrogen concentrations in the molten steel in the vacuum chamber
and in the ladle calculated by the process of step S5. Upon this, the process of step
S6 is completed, and the nitrogen concentration prediction process then advances to
a process of step S7.
[0061] In the process of step S7, the control apparatus 10 determines whether or not the
current time is a time allowed for the machine learning correction. If the determination
teaches that the current time is not the time allowed for the machine learning correction
(step S7: No), the control apparatus 10 returns the nitrogen concentration prediction
process to the process of step S2. On the other hand, if the current time is the time
allowed for the machine learning correction (step S7: Yes), the control apparatus
10 advances the nitrogen concentration prediction process to the process of step S8.
[0062] In the process of step S8, the control apparatus 10 calculates the prediction error
of the nitrogen concentration prediction model, by entering the operating condition
of the vacuum degassing process to the machine learning correction model. The control
apparatus 10 then uses the thus calculated prediction error to correct the nitrogen
concentrations [N]
V and [N]
L of the molten steel in the vacuum chamber and in the ladle, calculated in the process
of step S6. Upon this, the process of step S8 is completed, and the nitrogen concentration
prediction process then advances to a process of step S9.
[0063] In the process of step S9, the control apparatus 10 determines whether or not the
calculated time for the vacuum degassing process exceeds a preset process time. If
the determination teaches that the calculated time for the vacuum degassing process
does not exceed the preset process time (step S9: No), the control apparatus 10 increases
the time for the vacuum degassing process by a predetermined duration, and then returns
the nitrogen concentration prediction process back to the process of step S2. On the
other hand, in a case where the calculated time for the vacuum degassing process exceeds
the preset process time (step S9: Yes), the control apparatus 10 ends a series of
nitrogen concentration prediction processes. Thereafter, the operator compares the
predicted value and the target value of the nitrogen concentration, and corrects the
process condition for adjusting the nitrogen concentration, according to the result
of comparison. Examples of the process conditions include circulation gas species,
flow rate of circulation gas, process time for vacuum degassing, and the degree of
vacuum.
[Examples]
[0064] In this Example, a plurality of steel types was subjected to the nitrogen concentration
control. The molten steel before the vacuum degassing process contains components
in the ranges of [C] < 0.1%, [P] < 0.01%, [S] < 0.01%, [Mn] = 0.02 to 1.2%, [Si] =
0.1 to 4.0%, and [Al] <0.1%. The target nitrogen concentration was 20 to 120 ppm,
the molten steel temperature was 1480 to 1630°C, and the process amount of molten
steel was 180 to 240 ton. Nitrogen gas or argon gas was used as the circulation gas,
wherein the flow rate of circulation gas was 1000 to 3000 (NL/min), the degree of
vacuum during stabilized process was 12/76 (atm) or below, and the circulation process
time was 30 minutes. During the process, the nitrogen concentration was analyzed at
a plurality of times of sampling, and recorded as actual values.
[0065] The control method was conducted by entering initial conditions at the start of process,
to determine the process conditions. The nitrogen concentration was predicted according
to the process conditions, wherein if the predicted nitrogen concentration at the
end of process and the target value differ by a certain value or more, the nitrogen
concentration was controlled by correcting the process conditions. Upon acquisition
of each actual value by the nitrogen concentration analysis during the process, the
nitrogen concentration was predicted again from the actual value, and the process
conditions were similarly corrected if necessary. A difference value between the predicted
value and the target value, which gives a criterion for the correction of process
conditions, needs to be appropriately determined according to change behavior of the
nitrogen concentration which will differ depending on the facility, the molten steel
components, and the molten steel conditions, and accuracy of the nitrogen concentration
prediction model, and was set to 2 ppm in Example. The control was conducted as described
above, and the control accuracy was evaluated from the result. Results of the evaluation
of control accuracy are summarized in Table 2. The evaluation was made for about hundred
charges per example, wherein the evaluation method employed standard deviation σ of
difference between the target value and the actual value at the end of process, and
percentage of deviation from target nitrogen concentration range ± 5 ppm.
[Table 2]
[0066]
(Table 2)
| |
Machine learning correction |
Feature regarding number of times of use of facility |
Characteristic of process condition |
Process completion time |
Process time allowed for analysis and machine learning correction |
σ of target value - actual value (ppm) |
Percentage of deviation from ±5 ppm |
Model evaluation |
| Example 1 |
Applied |
Applied |
- |
30 min |
12 min, 22 min, end of process |
1.82 |
0.9 |
○ |
| Example 2 |
Applied |
Not applied |
- |
12 min, 22 min, end of process |
2.02 |
1.4 |
○ |
| Example 3 |
Applied |
Applied |
- |
14 min, end of process |
2.26 |
2.8 |
○ |
| Example 4 |
Applied |
Applied |
- |
7 min, 14 min, end of process |
2.17 |
2.3 |
○ |
| Example 5 |
Applied |
Applied |
Target[N] < 30ppm |
12 min, 22 min, end of process |
2.47 |
4.2 |
○ |
| Example 6 |
Applied |
Applied |
Target[N] > 100ppm |
7 min, 19 min, end of process |
2.56 |
4.9 |
○ |
| Example 7 |
Applied |
Applied |
Flow rate of circulation gas > 20NL/min·ton |
10 min, 25 min, end of process |
2.69 |
6.1 |
○ |
| Comparative Example 1 |
Not applied |
- |
- |
- |
3.51 |
15.8 |
× |
[0067] As summarized in Table 2, great improvement in the control accuracy was found in
Examples 1 to 4, as compared with Comparative Example that employed a prior technique.
From comparison between Example 1 and Example 2, even Example 2 was found to demonstrate
higher accuracy as compared with Comparative Example. Usage of the number of times
of use of the facility as the feature was, however, found to more distinctively improve
the control accuracy. Examples 1, 3, and 4 employed different process timings for
the analysis and the machine learning correction, wherein low frequency of correction,
such as in Example 3, was found to degrade the accuracy. Example 4, whose number of
times of correction was the same as that in Example 1, was found to degrade the control
accuracy, since the correction is concentrated in the first half of the process, but
is absent in a duration close to the end of process. From the results, it was confirmed
that high control accuracy was obtainable by keeping a sufficient number of times
of correction as in Example 1, and by conducting the correction in a duration close
to the end of process.
[0068] Having described the embodiments to which the invention made by the present inventors
was applied, the present invention is, however, not limited by the description and
drawings that constitute a part of the disclosure of the present invention according
to the present embodiments. That is, all the other embodiments, Examples, operation
techniques, and the like, made by those skilled in the art while referring to the
present embodiment, are included in the scope of the present invention.
Industrial Applicability
[0069] According to the present invention, the nitrogen concentration prediction method
and the nitrogen concentration prediction apparatus, capable of accurately predicting
the nitrogen concentration in the molten steel during the vacuum degassing process,
may be provided. According to the present invention, also the nitrogen concentration
control method and the nitrogen concentration control apparatus, capable of accurately
controlling the nitrogen concentration in the molten steel during the vacuum degassing
process, may be provided.
Reference Signs List
[0070]
- 1
- VACUUM DEGASSING APPARATUS
- 2
- LADLE
- 3
- VACUUM CHAMBER
- 4
- DIP TUBE
- 5
- BLOW-IN PORT
- 6
- EXHAUST PORT
- 10
- CONTROL APPARATUS
- 11
- NITROGEN CONCENTRATION PREDICTION UNIT
- 12
- CORRECTION UNIT
- G
- CIRCULATION GAS
- S
- MOLTEN STEEL